NC0090174_Application_20220913

�d r .
ROY COOPER ul ��``�' !-
Governor „� 1`11
ELIZABETH S.BISER
Secretary
RICHARD E.ROGERS,JR. NORTH CAROLINA
Director Environmental Quality
September 15, 2022
Carolina Development Services, LLC
Attn: Matthew Kirchner, PE
2649 Brekonridge Centre Dr
Monroe, NC 28110
Subject: Permit Application
Application No. NC0090174
Codydowns-Glass
Union County
Dear Applicant:
The Water Quality Permitting Section acknowledges receipt of your application for a new NPDES WW permit, including
supporting documentation and your check number 31021 in the amount of$860.00 as payment of the application fee.
These items were received in our offices on September 13, 2022. Your application will be assigned to a permit writer
within the Section's NPDES WW permitting branch.The permit writer will contact you if additional information is required
to complete evaluation of your application. Your timely and direct response to any such request will help to expedite the
review process. Please note that acceptance of the application does not guarantee a NPDES permit will be issued for the
proposed activity. A permit will only be issued following a complete review of the application, concluding the proposed
discharge is allowable per applicable statutes and rules.
Information regarding the status of your renewal application can be found online using the Department of Environmental
Quality's Environmental Application Tracker at:
https://deq.nc.gov/permits-regulations/permit-guidance/environmental-application-tracker
If you have any additional questions about the permit, please contact the primary reviewer of the application using the
links available within the Application Tracker.
Sincerely,
34c,.
Wren T edford
Administrative Assistant
Water Quality Permitting Section
cc: Jonathan McCall, ORC
ec: WQPS Laserfiche File w/application
D E Qi North Caroliament of Quality I Div in f Watr R
1 Mooresville RegionalnaDep Officert 1670 EastEnvironmental Center Avenue,Suite is 3010 Io Mooresvillee .Northesources
Carolina 28115
�\ 704.663.1699

United States Office of Water EPA Form 3510-2A
Environmental Protection Agency Washington,D.C. Revised March 2019
Water Permits Division
: EPA Application Form 2A
New and Existing Publicly
Owned Treatment Works
NPDES Permitting Program
Note: Complete this form if your facility is a new or existing publicly owned treatment works.

Paperwork Reduc":ion Act Notice
The U.S. Environmental Protection Agency estimates the average burden to collect information and
complete Form 2A to average between 4.7 and 24.7 hours, depending on the number of sections the
applicant must complete. The estimate includes time for reviewing instructions, searching existing data
sources, gathering and maintaining the needed data, and completing and reviewing the collection of
information. Send comments about the burden estimate or any other aspect of this collection of
information to the Chief, Information Policy Branch (PM-223), U.S. Environmental Protection Agency,
1200 Pennsylvania Avenue,NW, Washington, DC 20460, and to the Office of Information and
Regulatory Affairs, Office of Management and Budget, 725 17th Street,NW, Washington, DC 20503,
marked "Attention: Desk Officer for EPA."

FORM 2A—GENERAL INSTRUCTIONS
Who Must Complete Form 2A? Form 2A. If you do not assert a claim of confidentiality at the time
All new and existing publicly owned treatment works(POTWs)and you submit your information to the NPDES permitting authority,
other dischargers designated by the National Pollutant Discharge EPA may make the information available to the public without
Elimination System(NPDES)permitting authority must complete further notice to you.EPA will handle claims of confidentiality in
Form 2A. Note that you may wish to consult the"General accordance with the Agency's business confidentiality regulations
Instructions"of NPDES Application Form 1 to determine if your at Part 2 of Title 4 of the Code of Federal Regulations(CFR).
treatment works is required to submit any additional NPDES Completion of Forms
application forms. Form 2A is divided into six major sections. It also contains five
At the state level,either the U.S. Environmental Protection Agency effluent monitoring tables(Tables A through E)and an industrial
(EPA)or an approved state agency administers the NPDES permit discharge information table(Table F),all located at the end of the
program. If you are located in a jurisdiction in which an EPA form.Note that not all applicants are required to complete each
regional office administers the NPDES permit program,you should section of the form or all of the tables.The questions on the form
use Form 2A and all other applicable forms described in these will direct you to the items and tables you must complete.
instructions. If you are located in a jurisdiction where a state Print or type in the specified areas only. If you do not have enough
administers the NPDES permit program,contact the state to space on the form to answer a question,you may continue on
determine the forms you should complete. States often develop additional sheets,as necessary,using a format consistent with the
their own application forms rather than use the federal forms.See form.
http://www.epa.gov/nodes/nodes-state-program-information for a
list of states that have approved NPDES permit programs and Provide your EPA Identification Number from the Facility Registry
those that do not. Service,NPDES permit number,and facility name at the top of
Exhibit 2A-1 (see end of this section)provides contact information each page of Form 2A and any attachments. If your facility is new
for each of EPA's 10 regional offices.Since the exhibit's content is (i.e.,not yet constructed),write or type"New Facility"in the space
subject to change,consult EPA's website for the latest information: provided for the EPA Identification Number and NPDES permit
http://www.epa.gov/aboutepa#regional. number.If you do not know your EPA Identification Number,
contact your NPDES permitting authority.See Exhibit 2A-1 for
Where to File Your Completed Form contact information.Additionally,for Tables A through E,provide
• If you are in a jurisdiction with an approved state NPDES the applicable outtall number at the top of each page.
permit program,file according to the instructions on the state Do not leave any response areas blank unless the form directs you
forms. to skip them. If the form directs respond you to and to an item that does
P
• If you are in a jurisdiction where EPA is the NPDES permitting not apply to your facility or activity,enter"NA"for"not applicable"to
authority(i.e.,the state is not an NPDES-authorized state), show that you considered the item and determined a response was
mail the completed application forms to the EPA regional office not necessary for your facility.
that covers the state in which your facility is located(see If you have previously submitted information that answers a specific
Exhibit 2A-1). question to EPA or an approved state NPDES agency,you may
When to File Your Completed Form either repeat the information in the space provided or attach a copy
of the previous submission.
Form 2A must be submitted at least 180 days before your present
NPDES permit expires or,if you are a new discharger,at least Note for New Dischargers
180 days before the date on which the discharge is to commence, Provide all information available to you at the time you
unless the NPDES permitting authority has granted permission for a complete Form 2A. If you do not have information to respond
later date. to an item because your facility has yet to discharge,write or
Fees type"data are not available"next to the item on the form.Note
that you are required to submit actual data no later than
EPA does not require applicants to pay a fee for applying for 24 months after your facility commences to discharge.
NPDES permits. However,states that administer the NPDES permit
program may charge fees.Consult with state officials for further The NPDES permitting authority will consider your application
information. complete when it and any supplementary material are received and
completed according to the authority's satisfaction.The NPDES
Public Availability of Submitted Information permitting authority will judge the completeness of any application
EPA will make information from NPDES permit application forms independently of the status of any other permit application or permit
available to the public for inspection and copying upon request.You for the same facility or activity.
may not claim any information on Form 2A(or related attachments) Definitions
as confidential.
The legal definitions of all key terms used in the various NPDES
You may make a claim of confidentiality for any information that you
application forms are included in the"Glossary"at the end of these
submit to EPA that goes beyond the information required by instructions.
2A-1

FORM 2A—GENERAL INSTRUCTIONS CONTINUED
Exhibit 2A-1.Addresses of EPA Regional Contacts and Covered States
REGION 1 REGION 6
U.S.Environmental Protection Agency,Region 1 U.S.Environmental Protection Agency,Region 6
5 Post Office Square,Suite 100,Boston,MA 02109-3912 1445 Ross Avenue,Suite 1200,Dallas,TX 75202-2733
Phone:[phone];toll free:[phone] Phone:[phone];toll free:[phone]
Fax:[phone] Fax:[phone]
Website:http://www.epa.gov/aboutepa/epa-region-1-new-enoland Website:http://www.epa.aov/aboutepa/epa-region-6-south-central
Covered states:Connecticut,Maine,Massachusetts,New Hampshire,Rhode Covered states:Arkansas,Louisiana,New Mexico,Oklahoma,and Texas
Island,and Vermont
REGION 2 REGION 7
U.S.Environmental Protection Agency,Region 2 U.S.Environmental Protection Agency,Region 7
290 Broadway,New York,NY 10007-1866 11201 Renner Boulevard,Lenexa,KS 66219
Phone:[phone];toll free:[phone] Phone:[phone];toll free:[phone]
Fax:[phone] Website:http://www.epa.gov/aboutepa/epa-region-7-midwest
Website:http://www.epa.00v/aboutepa/epa-region-2 Covered states:Iowa,Kansas,Missouri,and Nebraska
Covered states:New Jersey,New York,Virgin Islands,and Puerto Rico
REGION 3 REGION 8
U.S.Environmental Protection Agency,Region 3 U.S.Environmental Protection Agency,Region 8
1650 Arch Street,Philadelphia,PA 19103-2029 1595 Wynkoop Street,Denver,CO 80202-1129
Phone:[phone];toll free:[phone] Phone:[phone];toll free:[phone]
Fax:[phone] Fax:[phone]
Website:http://www.epa.gov/aboutepa/epa-region-3-mid-atlantic Website:http://www.epa.gov/aboutepa/epa-region-8-mountains-and-plains
Covered states:Delaware,District of Columbia,Maryland,Pennsylvania,Virginia, Covered states:Colorado,Montana,North Dakota,South Dakota,Utah,and
and West Virginia Wyoming
REGION 4 REGION 9
U.S.Environmental Protection Agency,Region 4 U.S.Environmental Protection Agency,Region 9
Sam Nunn Atlanta Federal Center 75 Hawthorne Street,San Francisco,CA 94105
61 Forsyth Street,SW,Atlanta,GA 30303-8960 Phone:[phone];toll free:(866)EPA-WEST
Phone:[phone];toll free:[phone] Fax:[phone]
Fax:[phone] Website:http://www.epa.gov/aboutepa/epa-reqion-9-pacific-southwest
Website:http://www.epa.qov/aboutepa/about-epa-region-4-southeast Covered states:Arizona,California,Hawaii,Nevada,Guam,American Samoa,
Covered states:Alabama,Florida,Georgia,Kentucky,Mississippi,North Carolina, and Trust Territories
South Carolina,and Tennessee
REGION 5 REGION 10
U.S.Environmental Protection Agency,Region 5 U.S.Environmental Protection Agency,Region 10
77 West Jackson Boulevard,Chicago,IL 60604-3507 1200 Sixth Avenue,Suite 900,Seattle,WA 98101
Phone:[phone];toll free:[phone] Phone:[phone];toll free:[phone]
Fax:[phone] Fax:[phone]
Website:http://www.epa.gov/aboutepa/epa-region-5 Website:http://www.epa.00v/aboutepa/epa-region-10-pacific-northwest
Covered states:Illinois,Indiana,Michigan,Minnesota,Ohio,and Wisconsin Covered states:Alaska,Idaho,Oregon,and Washington
2A-2

FORM 2A—LINE-BY-LINE INSTRUCTIONS
Section 1.Basic Application Information for All Applicants Discharge Points by Type
Facility Information Item 1.11.Provide the facility's total number of effluent discharge
Item 1.1.Enter the facility's official or legal name.Do not use a points to waters of the United States by type(e.g.,treated effluent,
colloquial name. Provide the mailing address of the facility.Next, untreated effluent,combined sewer overflows,bypasses, and
give the name(first and last),title,work telephone number,and constructed emergency overflows).
email address of the person who is thoroughly familiar with the Outfalls and Other Discharge or Disposal Methods
operation of the facility and with the facts reported in this Outfalls Other Than to Waters of the United States
application.
Item 1.12.Indicate whether the POTW discharges wastewater to
Include a complete location address for the facility if different from basins,ponds,or other surface impoundments that do not have
the mailing address. If the facility lacks a street name or route outlets for discharge to waters of the United States.If yes,continue
number,give the most accurate,alternative geographic information to Item 1.13. If no,skip to Item 1.14.
(e.g.,section number or quarter section number from county
records or"at intersection of Routes 425 and 22"). Item 1.13.Specify the location of each surface impoundment,the
average daily volume discharged to each surface impoundment in
Item 1.2.Indicate whether the application is for a facility that has gallons per day(gpd),and whether the discharge is continuous or
not yet commenced discharge. If yes,be advised that you are intermittent.
required to submit actual data no later than 24 months after your
facility commences to discharge. Item 1.14.Indicate if the facility applies wastewater to land. If yes,
continue to Item 1.15. If no,skip to Item 1.16.
Applicant Information
Item 1.3.Indicate if the applicant is different from the entity listed Item 1.15.Provide the location of each land application site;the
under Item 1.1. If so,specify the applicant name and address. size of each land application site(in acres);the average daily
Provide the name(first and last)of a contact,including his/her title, volume applied to each land application site(in gpd),and whether
telephone number,and email address. the land application is continuous or intermittent.
Item 1.4.Indicate if the applicant is the facility's owner,operator,or Item 1.16.Note whether the facility's effluent is transported to
both. another facility for treatment prior to discharge. If yes,continue to
Item 1.17. If no,skip to Item 1.21.
Item 1.5.Specify whether the NPDES permitting authority should Item 1.17.Describe the means by which the effluent is transported,
send correspondence to the facility or the applicant. such as by tank truck or pipe.
Existing Environmental Permits Item 1.18.Specify whether the facility's effluent is transported by a
Item 1.6.Indicate all environmental permits or construction party other than the applicant. If yes,continue to Item 1.19. If no,
approvals received or applied for(including dates)under the noted skip to Item 1.20.
programs. Print or type the corresponding permit number for each.
Item 1.19.Provide the name,mailing address,contact person,
Collection System and Population Served phone number,and email address of the entity that transports the
Item 1.7.Specify the municipalities served by the treatment works, discharge.
including unincorporated connector districts.For each municipality. Item 1.20.Provide the name,mailing address,contact person,
indicate the population served,the percentage of each collection phone number,email address,and NPDES permit number(if any)
system type if known(e.g.,separate sanitary or combined storm of the receiving facility.Also specify the average daily flow rate from
and sanitary),and collection system ownership status.Finally, the facility into the receiving facility in mgd.
indicate the total percentage of sewer line each type comprises.
Do not report privately owned collection systems discharging Item 1.21.Indicate if wastewater is disposed of in a manner other
industrial waste to the treatment works in Item 1.7.Those facilities than those already mentioned in Items 1.14 through 1.21 that do
must be reported on Table F. not have outlets to waters of the United States,such as
underground percolation and underground injections. If yes,
Indian Country continue to Item 1.22. If no,skip to Item 1.23.
Item 1.8.Indicate if the POTW is located in Indian Country. Item 1.22.Provide a description of the disposal method,including
Item 1.9.Note whether the treatment works discharges to a the location and size of each disposal site;the annual average daily
receiving stream that flows through Indian Country. discharge volume(in gpd),and whether disposal through this
Design and Actual Flow Rates method is continuous or intermittent.
Item 1.10.Provide the facility's design flow rate in million gallons Variance Requests
per day(mgd). Next,specify the facility's actual annual average Item 1.23.If known at the time of application,check all of the
daily flow rate and maximum daily flow rate for each of the previous authorized variances that you plan to request or renew. Note that
three years(in mgd). you are not being asked to submit any other information at this
time.Contact your NPDES permitting authority to determine the
2A-3

FORM 2A—LINE-BY-LINE INSTRUCTIONS CONTINUED
specifics of what you should provide and when.The ability to website at htto://nationalmap.gov/.(For a map from this site, use
request a variance is not limited to the time of application,and an the traditional 7.5-minute quadrangle format. If none is available,
applicant may request a variance consistent with statutory and use a USGS 15-minute series map.)You may also use a plat or
regulatory requirements. other appropriate map.Briefly describe land uses in the map area
Contractor Information (e.g.,residential,commercial).An example of an acceptable
Item 1.24.Indicate if any of the operational or maintenance location map is shown as Exhibit 2A-2 at the end of these
activities associated with wastewater treatment and effluent quality instructions. Note: Exhibit 2A-2 is provided for illustration only;it
of the POTW are the responsibility of a contractor. If yes,continue does not show an actual facility. Note that you have completed your
to Item 1.25. If no,skip to Section 2. topographic map and attached it to the application.
Item 1.25.Provide a listing of all contractors(by company name). Flow Diagram
For each,specify the mailing address,a contact name,telephone Item 2.4.Provide a process flow diagram or schematic showing the
number,and email address.Also summarize the operational and processes of the treatment plant, including all bypass piping and all
maintenance responsibilities of each contractor. backup power sources or redundancy in the system.This includes
a water balance showing all treatment units, including disinfection
Section 2.Additional Information (e.g.,chlorination and dechlorination),and showing daily average
Outfalls to Waters of the United States flow rates at influent and discharge points,and approximate daily
Design Flow flow rates between treatment units.Also provide a narrative
Item 2.1.Indicate whether the treatment works has a design flow description of the diagram/schematic.Answer"Yes"to Item 2.4
greater than or equal to 0.1 mgd. If yes,continue to Item 2.2. If no, appe you have completed and attached your diagram to the
application.
skip to Section 3.
Inflow and Infiltration Scheduled Improvements and Schedules of Implementation
Item 2.2.Specify the POTW's current average daily volume of Item 2.5.Indicate whether any improvements to the facility are
inflow and infiltration(in gpd)and steps the facility is taking to scheduled. If yes,list and briefly describe each scheduled
minimize inflow and infiltration. improvement and continue to Item 2.6. If no,skip to Section 3.
Topographic Map Item 2.6.For each scheduled improvement,indicate the outfall
number of each outfall affected and the scheduled or actual dates
Item 2.3.Prepare a topographic map(or other map if a topographic of completion for the following: (1)commencement of construction,
map is unavailable)extending at least one mile beyond property (2)completion of construction,(3)commencement of discharge,
boundaries of the treatment plant,including all unit processes and and(4)attainment of operational level.
showing the following:(1)treatment plant area and unit processes;
(2)major pipes or other structures through which wastewater enters Item 2.7.Note whether the appropriate permits/clearances
the treatment plant and the pipes or other structures through which concerning other federal/state requirements have been obtained
treated wastewater is discharged from the treatment plant(include and briefly explain your response.
outfalls from bypass piping,if applicable); (3)each well where fluids Section 3.Information on Effluent Discharges
from the treatment plant are injected underground;(4)wells, Description of Outfalls
springs,and other surface water bodies listed in public records or
otherwise known to the applicant within 1/4 mile of the treatment Item 3.1.Provide a description of each of the POTW's wastewater
works'property boundaries;(5)sewage sludge management discharge outfalls.The application form provides reporting space
facilities(including onsite treatment,storage,and disposal sites); for three outfalls. If your facility has more than this number,attach
and(6)location at which waste classified as hazardous under the additional sheets as necessary.
Resource Conservation and Recovery Act(RCRA)enters the For each outfall,provide the outfall number. Indicate the state,
treatment plant by truck,rail,or dedicated pipe. county,and city or town where each outfall is located. Note the
On each map,include the map scale,a meridian arrow showing distance from shore in feet and the depth below the surface in feet.
north,and latitude and longitude to the nearest second.Latitude Specify the average daily flow rate through the outfall in mgd.Also
and longitude coordinates may be obtained in a variety of ways, specify the latitude and longitude of each outfall to the nearest
including use of hand held devices(e.g.,a GPS enabled second. Latitude and longitude coordinates may be obtained in a
smartphone),internet mapping tools(e.g., variety of ways,including use of hand held devices(e.g.,a GPS
https://mvnasadata.larc.nasa.gov/latitudelongitude-finder/), enabled smartphone),internet mapping tools(e.g.,
geographic information systems(e.g.,ArcView),or paper maps https://mvnasadata.larc.nasa.gov/latitudelongitude-finder/),
from trusted sources(e.g.,U.S.Geological Survey or USGS). geographic information systems(e.g.,ArcView),or paper maps
from trusted sources(e.g.,USGS).The location of each outfall(i.e.,
On all maps of rivers,show the direction of the current. In tidal where the coordinates are collected)shall be the point where the
waters,show the directions of ebb and flow tides. discharge is released into a water of the United States. For further
You may develop your map by going to USGS's National Map guidance,refer to http://www.epa.gov/geosoatial/latitudelongitude-
data-standard.
2A-4

FORM 2A—LINE-BY-LINE INSTRUCTIONS CONTINUED
Seasonal or Periodic Discharge Data completing Items 3.10 to 3.26 and Tables A through E.
Item 3.2.Indicate whether any of the outfalls described under Item 3.10 and Table A.All applicants that discharge wastewater to
Item 3.1 have seasonal or periodic discharges.If yes,continue to waters of the United States must provide effluent data for Table A
Item 3.3.If no,skip to Item 3.4. parameters. Respond"Yes"to Item 3.10 when you have completed
Item 3.3.Specify the following for each applicable outfall: Table A and attached it to your application.
(1)number of times per year discharge occurs,(2)average duration Item 3.11.Answer whether the POTW has conducted any whole
of each discharge,(3)average flow of each discharge in mgd,and effluent toxicity(WET)tests during the 4.5 years prior to the date of
(4)months in which discharge occurs. the application on any of the facility's discharges or on any
Diffuser Type receiving water near the discharge points. If yes,continue to Item
Item 3.4.Note whether any of the outfalls listed under Item 3.1 are 3.12. If no,skip to Item 3.13.
equipped with a diffuser. If yes,continue to Item 3.5. If no,skip to Item 3.12.For each applicable outfall,note the number of acute
Item 3.6. and chronic WET tests conducted since the last permit reissuance
Item 3.5.Briefly describe the diffuser type at each applicable of the facility's discharges or of the receiving water near the
outfall. discharge points.
Waters of the United States Item 3.13.Note whether the POTW has a design flow greater than
Item 3.6.Note whether the POTW discharges or plans to discharge or equal to 0.1 mgd. If yes,continue to Item 3.14. If no,skip to Item
wastewater to waters of the United States from one or more 3.16.
discharge points. If yes,continue to Item 3.7. If no,skip to Item 3.14 and Table B.Answer whether the treatment works uses
Section 6. chlorine for disinfection,uses it elsewhere in the treatment process,
Receiving Water Description or otherwise has reasonable potential to discharge chlorine in its
Item 3.7.Provide receiving water and related information in the effluent. If yes,complete Table B including chlorine. If no,complete
table provided on the form(if known):(1)name of receiving water, Table B,omitting chlorine.
(2)name of watershed/river/stream system and U.S.Soil Item 3.15.Answer"Yes"when you have completed monitoring for
Conservation Service 14-digit watershed code,(3)name of state all applicable Table B parameters and attached the results to your
management/river basin and U.S.Geological Survey(USGS)8-digit application.
hydrologic unit code,(4)acute and chronic critical low flow in cubic
feet per second(cfs)and total hardness of receiving stream at Item 3.16 and Screen for Tables C through E.Indicate whether
critical low flow,in milligrams per liter(mg/L)of calcium carbonate, one or more of the conditions apply to your POTW. If yes,continue
if applicable. to Item 3.17. If no,skip to Section 4.
Treatment Description Item 3.17 and Table C.Answer"Yes"to indicate you have
completed monitoring for all applicable Table C pollutants and
Item 3.8.Specify the highest level of treatment provided for attached the results to your application package.
discharges from each outfall(e.g.,primary,equivalent to
secondary,secondary,or advanced).Also indicate the following Item 3.18 and Table D.Answer"Yes"to indicate you have
design removals(in percent)for the following parameters for each completed monitoring for applicable Table D pollutants required by
outfall:(1)biochemical oxygen demand(BODsor CBOD5),(2)total your NPDES permitting authority and attached the results to your
suspended solids(TSS),(3)phosphorus(if applicable),(4)nitrogen application package,or"No"if the NPDES permitting authority has
(if applicable),and(5)any other removals that an advanced not required additional sampling for the pollutants in Table D.
treatment system is designed to achieve. Item 3.19 and Additional Screen for Table E.Answer whether the
Item 3.9.Provide a description of the type(s)of disinfection used for POTW conducted either(1)a minimum of four quarterly WET tests
wastewater discharged through each outfall.Indicate the seasons for one year preceding this permit application or(2)at least four
the disinfection type is used.Note whether the POTW dechlorinates annual WET tests in the past 4.5 years. If yes,continue to Item
if disinfection is accomplished through chlorination.Otherwise, 3.20. If no,complete tests and Table E and then skip to Item 3.26.
check"Not Applicable." Item 3.20 and Additional Screen for Table E.Report whether you
Effluent Testing Data and Tables A through E have previously submitted the results of the WET tests indicated in
Items 3.10 to 3.26.These items require you to collect and report Item 3.19 to your NPDES permitting authority.If yes,continue to
data for the parameters and pollutants listed in Tables A through E, Item 3.21. If no,provide the results in Table E and skip to Item 3.26.
located at the end of Form 2A.The instructions for completing the Item 3.21.Report the dates the testing data were submitted to your
tables are table-specific,as are the criteria for determining who NPDES permitting authority and provide a summary of the results.
should complete them. Item 3.22.Regardless of how you may have provided the results of
Important note:Read the"General Instructions for Reporting, previously conducted WET analyses to your NPDES permitting
Sampling,and Analysis"later in these instructions before authority,indicate if any of the tests resulted in toxicity.If yes,
2A-5

FORM 2A—LINE-BY-LINE INSTRUCTIONS CONTINUED
continue to Item 3.23. If no,skip to Item 3.26. pretreatment program,which is defined at 40 CFR 403.3 as a
Item 3.23.Describe the cause(s)of toxicity. program administered by a POTW that meets the criteria
established in 40 CFR 403.8 and 403.9 and that has been
Item 3.24.Indicate if the POTW has conducted a toxicity reduction approved by the NPDES permitting authority.
evaluation. If yes,continue to Item 3.25. If no,skip to Item 3.26.
Item 4.4.Answer whether you have submitted either of the
Item 3.25.Provide details of any toxicity reduction evaluations following to the NPDES permitting authority that contains
performed. information substantially identical to that required in Table F:(1)a
Item 3.26.Answer"Yes"when you have completed Table E for all pretreatment program annual report submitted within one year of
applicable outfalls and attached the results to the application the application or(2)a pretreatment program. If yes,continue to
package,or answer"No"if the item is not applicable because you Item 4.5. If no,skip to Item 4.6.
previously submitted WET data to your NPDES permitting authority. Item 4.5.Identify the title and date of the pretreatment program
Section 4.Industrial Discharges,Table F,and Hazardous annual report or pretreatment program referenced in Item 4.4 and
Wastes skip to Item 4.7.
Item 4.1.Indicate if the POTW receives discharges from significant Item 4.6 and Table F.Complete Table F by providing the following
industrial users(SlUs)or non-significant categorical industrial users information for each SIU that discharges to the POTW:(1)name
(NSCIUs),including SlUs and NSCIUs that truck or haul waste. If and mailing address;(2)description of all industrial processes that
yes,continue to Item 4.2. If no,skip to Item 4.7. affect or contribute to each SIU's discharge; (3)a list of the principal
1. SlUs are defined as: products and raw materials that affect or contribute to the SIU's
discharge;(4)average daily volume of wastewater discharged by
a. All industrial users subject to categorical pretreatment each SIU,indicating the amount attributable to process flow and
standards under 40 CFR 403.6 and 40 CFR Chapter I, non-process flow;(5)whether the SIU is subject to local limits;
Subchapter N(ClUs);and (6)whether the SIU is subject to categorical standards and the
b. Any other industrial user per 40 CFR 403.3 that: categories/subcategories under which the SIU is subject;and
(7)whether any problems(e.g.,upsets, pass-through interference)
i. Discharges an average of 25,000 gpd or more of have occurred at the POTW that can be attributed to the SIU in the
process wastewater to the treatment works(with past 4.5 years.Answer"Yes"to Item 4.6 when you have completed
certain exclusions);or and attached Table F to the application package.
ii. Contributes a process wastestream that makes up
5 percent or more of the average dry weather Note:Sills include users that truck or haul industrial waste to the
hydraulic or organic capacity of the treatment plant; POTW. Information for these users must be provided in Table F.
or Item 4.7.Indicate if the POTW receives or has been notified that it
iii. Is designated as an SIU by the control authority. will receive by truck,rail,or dedicated pipe any wastes that are
2. The control authority may determine that an Industrial User regulated as RCRA hazardous wastes pursuant to 40 CFR 261.If
Yes,continue to Item 4.8. If no,skip to Item 4.9.
subject to categorical Pretreatment Standards under 40 CFR
403.6 and 40 CFR Chapter I,Subchapter N is a NSCIU rather Item 4.8.For each hazardous waste received,provide the
than a SIU on a finding that the Industrial User never hazardous waste number,the method by which the waste is
discharges more than 100 gpd of total categorical wastewater received(e.g.,by truck,dedicated pipe,rail,etc.),and the amount
(excluding sanitary, non-contact cooling and boiler blowdown of waste received annually(specify units).
wastewater, unless specifically included in the Pretreatment Item 4.9.Answer whether the POTW receives,or has been notified
Standard)and the following conditions are met: that it will receive,wastewaters that originate from remedial
a. The Industrial User,prior to the control authority's finding, activities,including those undertaken pursuant to Comprehensive
has consistently complied with all applicable categorical Environmental Response,Compensation,and Liability Act
Pretreatment Standards and Requirements; (CERCLA)and Sections 3004(u)or 3008(h)of RCRA. If yes,
b. The Industrial User annually submits the certification
continue to Item 4.10. If no,skip to Section 5.
statement required in 40 CFR 403.12(q)together with any Item 4.10.Answer whether the POTW receives(or expects to
additional information necessary to support the receive)less than 15 kilograms per month of non-acute hazardous
certification statement;and wastes as specified at 40 CFR 261.30(d)and 261.33(e). If yes,skip
c. The Industrial User never discharges any untreated to Section 5.If no,continue to Item 4.11.
concentrated wastewater. Item 4.11.In an attachment to the application,provide an
Item 4.2.Indicate the number of SIUs and NSCIUs that discharge identification and description of the site(s)or facility(ies)at which
to the POTW. the wastewater originates;the identities of the wastewater's
hazardous constituents,as listed in Appendix VII of 40 CFR 261,if
Item 4.3.Answer whether the POTW has an approved known;and the extent of treatment,if any,the wastewater receives
2A-6

General Instructions for Reporting,Sampling,and Analysis
Important note:Read these instructions before completing • The method ML is above the water quality criterion,but the
Tables A through E and Section 3 of Form 2A. amount of the pollutant or pollutant parameter in the facility's
General Items discharge is high enough that the method detects and
quantifies the level of the pollutant or pollutant parameter in
Complete the applicable tables for each outfall at your facility. Be the discharge.
sure to note the EPA Identification Number,NPDES permit • The method has the lowest ML of the analytical methods
number,facility name,and applicable outfall number at the top of
each page of the tables and any associated attachments. approved under 40 CFR 136 or required under 40 CFR
chapter I,subchapter N or 0,for the measured pollutant or
You may report some or all of the required data by attaching pollutant parameter.
separate sheets of paper instead of completing Tables A through
E for each of your outfalls,so long as the sheets contain all of the Consistent with 40 CFR 136,you may provide matrix or sample
required information and are similar in format to Tables A through specific MLs rather than the published levels.Further,where you
E.For example,you may be able to print a report in a compatible can demonstrate that,despite a good faith effort to use a method
format from the data system used in your analysis of metals that would otherwise meet the definition of"sufficiently sensitive,"
completed under Table C. the analytical results are not consistent with the quality assurance
(QA)/quality control(QC)specifications for that method,then the
Note for new dischargers.Provide all information available to NPDES permitting authority may determine that the method is not
you at the time you complete Form 2A. If you do not have performing adequately and the NPDES permitting authority should
information to respond to an item because your facility has yet to select a different method from the remaining EPA-approved
discharge,write or type"data are not available"next to the item methods that is sufficiently sensitive consistent with 40 CFR
on the form. Note that you are required to submit actual data no 122.21(e)(3)(i).Where no other EPA-approved methods exist,you
later than 24 months after your facility commences discharge. must select a method consistent with 40 CFR 122.21(e)(3)(ii).
Reporting of Effluent Data When there is no analytical method that has been approved under
Where effluent data are requested,do not provide information on 40 CFR 136;required under 40 CFR chapter I,subchapter N or 0,
CSOs.The latter information is requested instead under Section 5 and is not otherwise required by the NPDES permitting authority,
of Form 2A. you may use any suitable method but shall provide a description
Provide data for each outfall through which effluent is discharged. of the method.When selecting a suitable method,other factors
When an applicant has two or more outfalls with substantially such as a method's precision,accuracy,or resolution,may be
identical effluents,the NPDES permitting authority may allow the considered when assessing the performance of the method.
applicant to test only one outfall and report that quantitative data Effluent monitoring data must comply with the QA/QC
as applying to the substantially identical outfall. If the permitting requirements of 40 CFR 136(and other appropriate QA/QC
authority grants your request,attach a separate sheet to the requirements for standard methods for analytes not addressed by
application form identifying the outfall tested and describing why 40 CFR 136).
the other outfall(s)are substantially identical. Clearly specify the units of measure on Tables A through E for
At a minimum,effluent testing data must be based on at least each parameter/pollutant analyzed.Values should be reported as
three samples taken within 4.5 years prior to the date of the concentration or mass,except for flow,temperature,pH,color,
permit application. Samples must be representative of the and fecal coliform organisms,unless otherwise requested or
seasonal variation in the discharge from each outfall.Existing required by the NPDES permitting authority.Flow,temperature,
data may be used,if available,in lieu of sampling done solely for pH,color,and fecal coliform organisms must be reported as mgd,
the purpose of this application. degrees Celsius(°C),standard units,color units,and most
All existing data for pollutants specified in Tables A through D that probable number per 100 milliliters(MPN/100 mL),respectively.
is collected within 4.5 years of the application must be included in Use the following abbreviations in the columns requiring"units"in
the pollutant data summary that you submit.If,however,you Tables A through D.
sampled for a specific pollutant on a monthly or more frequent Concentration Mass
basis,it is only necessary,for such pollutant,to summarize all ppm=parts per million lbs=pounds
data collected within 1 year of the application. mg/L=milligrams per liter ton=tons(English tons)
Except as specified below,all required quantitative data shall be ppb=parts per billion mg=milligrams
collected in accordance with sufficiently sensitive analytical Ng/L=micrograms per liter g=grams
methods approved under 40 CFR 136 or required under 40 CFR
chapter I,subchapter N or 0.A method is"sufficiently sensitive" MPN=most probable number kg=kilograms
per 100 milliliters T=tonnes(metric tons)
when:
• The method minimum level(ML)is at or below the level of
the applicable water quality criterion for the measured
pollutant or pollutant parameter.
2A-7

General Instructions for Reporting,Sampling,and Analysis Continued
Grab samples must be used for pH,temperature,cyanide,total times,and the collection of duplicate samples—must be followed.
phenols,residual chlorine,oil and grease,fecal coliform(including The time when you sample should be representative of your normal
E.coh),and volatile organic compounds.For all other pollutants, operation,to the extent feasible,with your treatment system
24-hour composite samples must be used. For a composite operating properly with no system upsets.Collect samples from the
sample,only one analysis of the composite of aliquots is required. center of the flow channel,where turbulence is at a maximum,at a
The effluent monitoring data provided must include at least the site specified in your present NPDES permit,or at any site
following for each parameter:(1)the maximum daily discharge adequate for the collection of a representative sample.
based upon actual sample values,(2)average daily discharge for Further Requirements for Table E,Whole Effluent Toxicity
all samples,expressed as concentration or mass,and the number Testing
of samples used to obtain this value,(3)the analytical method Each applicant required to perform WET testing must provide
used,and(4)the threshold level(i.e.,method detection limit, results of a minimum of four quarterly tests for a year,from the year
minimum level,or other designated method endpoints)for the preceding the permit application,or the results from four tests
analytical method used. performed at least annually in the 4.5-year period prior to the
Metals must be reported as"total recoverable metal,"unless all application,provided the results show no appreciable toxicity using
approved analytical methods for the metal inherently measure only a safety factor determined by the NPDES permitting authority.
its dissolved form(e.g.,hexavalent chromium)or otherwise directed Applicants must conduct tests with multiple species(no less than
by the NPDES permitting authority. two species;e.g.,fish,invertebrate,plant)and test for acute or
Sampling chronic toxicity,depending on the range of receiving water dilution.
The collection of samples for the reported analyses should be See 40 CFR 122.21(j)(5)(v)for further details.
supervised by a person experienced in performing sampling of WET testing must be conducted using methods approved under
domestic wastewater.You may contact your NPDES permitting 40 CFR 136.West coast facilities in Washington,Oregon,
authority for detailed guidance on sampling techniques and for California,Alaska, Hawaii,and the Pacific Territories are exempted
answers to specific questions. See Exhibit 2A-1 for contact from 40 CFR 136 chronic methods and must use alternative
information.Any specific requirements in the analytical methods— guidance as directed by the NPDES permitting authority.
for example,for sample containers,sample preservation,holding
2A-8

FORM 2A—LINE-BY-LINE INSTRUCTIONS CONTINUED
or will receive before entering the POTW.Answer"Yes"to Item watershed(14-digit)code,if known;(3)name of the state
4.11 when you have completed and attached the information to the management/river basin and the USGS 8-digit hydrologic
application package. cataloging unit code,if known;and(4)a description of any known
Section 5.Combined Sewer Overflows water quality impacts on the receiving water caused by the CSO
CSO Map and Diagram (e.g.,permanent or intermittent beach closings,permanent or
intermittent shellfish bed closings,fish kills,fish advisories,other
Item 5.1.Indicate if the treatment works has a combined sewer recreational loss,or exceedance of any applicable state water
system. If yes,continue to Item 5.2. If no,skip to Section 6. quality standard).
Item 5.2.Attach a CSO system map to the application.The map Section 6.Checklist and Certification Statement
should indicate:(1)all CSO discharge points,(2)sensitive use Item 6.1.Review the checklist provided. In Column 1,mark the
areas potentially affected by CSOs(e.g.,beaches,drinking water sections of Form 2A that you have completed and are submitting
supplies,shellfish beds,sensitive aquatic ecosystems,and with your application. In Column 2,indicate for each section
outstanding national resource waters),and(3)waters supporting whether you are submitting attachments.
threatened and endangered species potentially affected by CSOs.
Answer"Yes"to Item 5.2 when you have completed the map and Item 6.2.The Clean Water Act provides for severe penalties for
attached it to the application package. submitting false information on this application form. CWA Section
Item 5.3.Prepare a diagram of the CSO collection system.The 309(c)(2)provides that"Any person who knowingly makes any false
diagram should show the following:(1)the location of major sewer statement,representation,or certification in any application, ...shall
trunk lines, both combined and separate sanitary;(2)the locations upon conviction,be punished by a fine of no more than$10,000 or
of points where separate sanitary sewers feed into the combined by imprisonment for not more than six months,or both."
sewer system;(3)in-line and off-line storage structures;(4)the FEDERAL REGULATIONS AT 40 CFR 122.22 REQUIRE THIS
locations of flow-regulating devices;and(5)the locations of pump APPLICATION TO BE SIGNED AS FOLLOWS:
stations.Answer"Yes"to Item 5.3 when you have completed the A. For a corporation, by a responsible corporate officer.For the
diagram and attached it to the application package. purpose of this section,a responsible corporate officer means:
CSO Outfall Description (1)a president,secretary,treasurer,or vice-president of the
Item 5.4.Provide the following information for each CSO outfall: corporation in charge of a principal business function,or any
(1)outfall number;(2)state,county,city or town and ZIP code in other person who performs similar policy-or decision-making
which the outfall is located;(3)latitude and longitude of the outfall, functions for the corporation,or(2)the manager of one or
to the nearest second,(4)distance of the outfall from shore and more manufacturing,production,or operating facilities,
depth of the outfall below water surface.Latitude and longitude provided the manager is authorized to make management
coordinates may be obtained in a variety of ways,including use of decisions which govern the operation of the regulated facility
hand held devices(e.g.,a GPS enabled smartphone),Internet including having the explicit or implicit duty of making major
mapping tools(e.g., capital investment recommendations,and initiating and
https://mynasadata.larc.nasa.gov/latitudelonoitude-finder/), directing other comprehensive measures to assure long term
information systemss environmental compliance with environmental laws and
geographic a( 'g"ArcView)'oraer ma paper p regulations;the manager can ensure that the necessary
from trusted sources(e.g.,USGS).The location of each CSO systems are established or actions taken to gather complete
outfall(i.e.,where the coordinates are collected)shall be the point and accurate information for permit application requirements;
where the discharge is released into a water of the United States. and where authority to sign documents has been assigned or
CSO Monitoring delegated to the manager in accordance with corporate
Item 5.5.Indicate whether the POTW has monitored any of the procedures.
following items in the past year for each of its CSO outtalls: B. For a partnership or sole proprietorship,by a general partner
(1)rainfall,(2)CSO flow volume,(3)CSO pollutant concentrations; or the proprietor,respectively.
(4)receiving water quality,(5)CSO frequency,and(6)number of C. For a municipality,state,federal,or other public facility,by
storm events. either a principal executive officer or ranking elected official.
CSO Events in Past Year For purposes of this section,a principal executive officer of a
Item 5.6.For each CSO outfall,record(1)the number of CSO federal agency includes:(1)The chief executive officer of the
events in the past year,(2)the average duration in hours per event, agency,or(2)a senior executive officer having responsibility
(3)the average volume per CSO event in million gallons,and for the overall operations of a principal geographic unit of the
(4)the minimum rainfall that caused a CSO event in inches of agency(e.g., Regional Administrators of EPA).
rainfall in the past year. Note whether your responses for sub-items END
(2)through(4)above are based on actual or estimated data. Submit your completed Form 2A and
CSO Receiving Waters all associated attachments
Item 5.7.For each CSO outfall,record the following receiving water (and any other required NPDES application forms)
information:(1)name of receiving water;(2)name of to your NPDES permitting authority.
watershed/stream system and the U.S.Soil Conservation Service
2A-9

Exhibit 2A-2.Example Topographic Map
III USGS U. CCPtilT.O.OfX4 WMfY[MCP
tUSTopo ,...11„„331IS
J
ti ; \
•
Mi.
ire 1y.� r
•
....f..
_ . ♦ t ..
•
r i
r - ..•°"'-- 1 '7. n
CENTRAL PROCESSING CO.
.. -. - • 001 —Aquatint- de Creek
.4.
Intake .. " .
4 ` t. "002 Waste Area
inieclim
CENTRALthY • /'
waste Ater mow!. �„`.-.-' / .,"
. y
;
I.
J
AMLLKpI1J11Y� _-lam• - •\ 1 .. _
_'•N.Mc71LeLL� ,�I p t /s
J t J,
i fps
ewe,wa N -y ,, , v v M ,Yr ".. \ m+r
■rrP4w.r�lr Owrr�LMr • Val 114 ea
timxisaa94sr.._.... .._4... ..,.»...=..W.,.. Location hap
...._ .-..«.._.-`».,,17.• �. Centra Proceeemg Co
..... ..,.......... .. ».�..,..«...�.....�... Contra;City.Cha
2A-10

FORM 2A—GLOSSARY
Note:This glossary includes terms used in the various NPDES application forms,including Form 2A.The definitions are from the NPDES
regulations at 40 CFR 122.2 unless otherwise specified. If you have any questions concerning the meaning of any of these terms,contact
your NPDES permitting authority.
ANIMAL FEEDING OPERATION(defined at§ 122.23)means a lot or facility(other than an aquatic animal production facility)where the
following conditions are met;
• Animals(other than aquatic animals)have been,are,or will be stabled or confined and fed or maintained for a total of 45 days or
more in any 12-month period;and
• Crops,vegetation,forage growth,or post-harvest residues are not sustained in the normal growing season over any portion of the lot
or facility.
APPLICATION means the EPA standard national forms for applying for a permit,including any additions,revisions,or modifications to the
forms;or forms approved by EPA for use in approved states,including any approved modifications or revisions.
APPROVED PROGRAM or APPROVED STATE means a State or interstate program which has been approved or authorized by EPA
under part 123.
AQUACULTURE PROJECT(defined at§122.25)means a defined managed water area which uses discharges of pollutants into that
designated area for the maintenance or production of harvestable freshwater,estuarine,or marine plants or animals.DESIGNATED
PROJECT AREA means the portions of the waters of the United States within which the permittee or permit applicant plans to confine the
cultivated species,using a method or plan or operation(including,but not limited to,physical confinement)which,on the basis of reliable
scientific evidence, is expected to ensure that specific individual organisms comprising an aquaculture crop will enjoy increased growth
attributable to the discharge of pollutants,and be harvested within a defined geographic area.
AVERAGE MONTHLY DISCHARGE LIMITATION means the highest allowable average of daily discharges over a calendar month,
calculated as the sum of all daily discharges measured during that month divided by the number of daily discharges measured during that
month.
AVERAGE WEEKLY DISCHARGE LIMITATION means the highest allowable average of daily discharges over a calendar week,
calculated as the sum of all daily discharges measured during a calendar week divided by the number of daily discharges measured during
that week.
BEST MANAGEMENT PRACTICES(BMPs)means schedules of activities,prohibitions of practices,maintenance procedures,and other
management practices to prevent or reduce the pollution of waters of the United States. BMPs include treatment requirements,operation
procedures,and practices to control plant site runoff,spillage or leaks,sludge or waste disposal,or drainage from raw material storage.
BIOSOLIDS(see sewage sludge).
BYPASS(defined at§122.41(m))means the intentional diversion of waste streams from any portion of a treatment facility.
COMBINED SEWER OVERFLOW(CSO)means a discharge from a combined sewer system(CSS)at a point prior to the Publicly Owned
Treatment Works(POTW)Treatment Plant(defined at§403.3(r)).
COMBINED SEWER SYSTEM(CSS)means a wastewater collection system owned by a State or municipality(as defined by section
502(4)of the CWA)which conveys sanitary wastewaters(domestic,commercial and industrial wastewaters)and storm water through a
single-pipe system to a Publicly Owned Treatment Works(POTW)Treatment Plant(as defined at§403.3(r)).
CONCENTRATED ANIMAL FEEDING OPERATION(defined at§ 122.23)means an animal feeding operation that is defined as a Large
CAFO or as a Medium CAFO by the terms of(A)or(B)below,or that is designated as a CAFO in accordance with 40 CFR 122.23(c).Two
or more AFOs under common ownership are considered to be a single AFO for the purposes of determining the number of animals at an
operation,if they adjoin each other or if they use a common area or system for the disposal of wastes.
A. LARGE CONCENTRATED ANIMAL FEEDING OPERATION(LARGE CAFO)means an AFO that stables or confines as many as or
more than the numbers of animals specified in any of the following categories:
1. 700 mature dairy cows,whether milked or dry;
2. 1,000 veal calves;
3. 1,000 cattle other than mature dairy cows or veal calves.Cattle includes but is not limited to heifers,steers,bulls and cow/calf
pairs;
4. 2,500 swine each weighing 55 pounds or more;
5. 10,000 swine each weighing less than 55 pounds;
6. 500 horses;
7. 10,000 sheep or lambs;
2A-11

FORM 2A—GLOSSARY CONTINUED
8. 55,000 turkeys;
9. 30,000 laying hens or broilers,if the AFO uses a liquid manure handling system;
10. 125,000 chickens(other than laying hens),if the AFO uses other than a liquid manure handling system;
11. 82,000 laying hens,if the AFO uses other than a liquid manure handling system;
12. 30,000 ducks(if the AFO uses other than a liquid manure handling system);or
13. 5,000 ducks(if the AFO uses a liquid manure handling system).
B. MEDIUM CONCENTRATED ANIMAL FEEDING OPERATION(MEDIUM CAFO)means any AFO with the type and number of
animals that fall within any of the ranges listed below and which has been defined or designated as a CAFO.An AFO is defined as a
Medium CAFO if:
1. The type and number of animals that it stables and confines falls within any of the following ranges:
a. 200 to 699 mature dairy cows,whether milked or dry;
b. 300 to 999 veal calves;
c. 300 to 999 cattle other than mature dairy cows or veal calves. Cattle includes but is not limited to heifers,steers,bulls and
cow/calf pairs;
d. 750 to 2,499 swine each weighing 55 pounds or more;
e. 3,000 to 9,999 swine each weighing less than 55 pounds:
f. 150 to 499 horses;
g. 3,000 to 9,999 sheep or lambs;
h. 16,500 to 54,999 turkeys;
i. 9,000 to 29,999 laying hens or broilers,if the AFO uses a liquid manure handling system;
j. 37,500 to 124,999 chickens(other than laying hens),if the AFO uses other than a liquid manure handling system;
k. 25,000 to 81,999 laying hens, if the AFO uses other than a liquid manure handling system;
I. 10,000 to 29,999 ducks(if the AFO uses other than a liquid manure handling system);ore
m. 1,500 to 4,999 ducks(if the AFO uses a liquid manure handling system);and
2. Either one of the following conditions are met:
a. Pollutants are discharged into waters of the United States through a man-made ditch,flushing system,or other similar man-
made device;or
b. Pollutants are discharged directly into waters of the United States which originate outside of and pass over,across,or
through the facility or otherwise come into direct contact with animals confined in the operation.
CONCENTRATED AQUATIC ANIMAL PRODUCTION FACILITY(defined at§122.24)means a hatchery,fish farm,or other facility which
contains,grows,or holds aquatic animals in either of the following categories,or which the Director designates as such on a case-by-case
basis:
A. Cold water fish species or other cold water aquatic animals including,but not limited to,the Salmonidae family of fish(e.g.,trout and
salmon)in ponds,raceways,or other similar structures which discharge at least 30 days per year but does not include:
1. Facilities which produce less than 9,090 harvest weight kilograms(approximately 20,000 pounds)of aquatic animals per year;
and
2. Facilities which feed less than 2,272 kilograms(approximately 5,000 pounds)of food during the calendar month of maximum
feeding.
B. Warm water fish species or other warm water aquatic animals including,but not limited to,the Ameiuridae, Cetrarchiclae,and
Cyprinidae families of fish(e.g.,respectively,catfish,sunfish,and minnows)in ponds,raceways,or other similar structures which
discharge at least 30 days per year,but does not include;
1. Closed ponds which discharge only during periods of excess runoff;or
2. Facilities which produce less than 45,454 harvest weight kilograms(approximately 100,000 pounds)of aquatic animals per year.
CWA means the Clean Water Act(formerly referred to as the Federal Water Pollution Control Act or Federal Water Pollution Control Act
Amendments of 1972)Public Law 92-500,as amended by Public Law 95-217,Public Law 95-576,Public Law 96-483 and Public Law
97-117,33 U.S.C. 1251 et seq.
CWA AND REGULATIONS means the Clean Water Act(CWA)and applicable regulations promulgated thereunder. In the case of an
approved State program,it includes State program requirements.
2A-12

FORM 2A—GLOSSARY CONTINUED
DAILY DISCHARGE means the"discharge of a pollutant"measured during a calendar day or any 24-hour period that reasonably
represents the calendar day for purposes of sampling.For pollutants with limitations expressed in units of mass,the"daily discharge"is
calculated as the total mass of the pollutant discharged over the day. For pollutants with limitations expressed in other units of
measurement,the"daily discharge"is calculated as the average measurement of the pollutant over the day.
DIRECT DISCHARGE means the"discharge of a pollutant."
DIRECTOR means the Regional Administrator or the State Director,as the context requires,or an authorized representative.When there
is no"approved State program,"and there is an EPA administered program,"Director"means the Regional Administrator.When there is
an approved State program,"Director"normally means the State Director. In some circumstances,however, EPA retains the authority to
take certain actions even when there is an approved State program.(For example,when EPA has issued an NPDES permit prior to the
approval of a State program,EPA may retain jurisdiction over that permit after program approval,see§123.1.)In such cases,the term
"Director"means the Regional Administrator and not the State Director.
DISCHARGE(OF A POLLUTANT)means:
• Any addition of any pollutant or combination of pollutants to waters of the United States from any point source;or
• Any addition of any pollutant or combination of pollutants to the waters of the contiguous zone or the ocean from any point source
other than a vessel or other floating craft which is being used as a means of transportation.
This definition includes discharges into waters of the United States from:surface runoff which is collected or channelled by man;
discharges through pipes,sewers,or other conveyances owned by a State,municipality,or other person which do not lead to a treatment
works;and discharges through pipes,sewers,or other conveyances,leading into privately owned treatment works.This term does not
include an addition of pollutants by any"indirect discharger".
DISCHARGE MONITORING REPORT means the EPA uniform national form,including any subsequent additions,revisions,or
modifications for the reporting of self-monitoring results by permittees.DMRs must be used by"approved States"as well as by EPA. EPA
will supply DMRs to any approved State upon request.The EPA national forms may be modified to substitute the state agency name,
address,logo,and other similar information,as appropriate,in place of EPA's.
DRAFT PERMIT means a document prepared under§ 124.6 indicating the Director's tentative decision to issue or deny,modify,revoke
and reissue,terminate,or reissue a"permit."A notice of intent to terminate a permit,and a notice of intent to deny a permit,as discussed
in§124.5,are types of"draft permits."A denial of a request for modification,revocation and reissuance,or termination,as discussed in
§124.5,is not a"draft permit."A"proposed permit"is not a"draft permit."
EFFLUENT LIMITATION means any restriction imposed by the Director on quantities,discharge rates,and concentrations of"pollutants"
which are"discharged"from"point sources"into"waters of the United States,"the waters of the"contiguous zone,"or the ocean.
EFFLUENT LIMITATIONS GUIDELINES means a regulation published by the Administrator under section 304(b)of the CWA to adopt or
revise"effluent limitations."
ENVIRONMENTAL PROTECTION AGENCY(EPA)means the United States Environmental Protection Agency.
FACILITY or ACTIVITY means any NPDES"point source"or any other facility or activity(including land or appurtenances thereto)that is
subject to regulation under the NPDES program.
GENERAL PERMIT means an NPDES"permit"issued under§122.28 authorizing a category of discharges under the CWA within a
geographical area.
HAZARDOUS SUBSTANCE means any substance designated under 40 CFR part 116 pursuant to section 311 of the CWA.
INDIAN COUNTRY(or INDAN LANDS)means:
• All land within the limits of any Indian reservation under the jurisdiction of the United States Government,notwithstanding the
issuance of any patent,and,including rights-of-way running through the reservation;
• All dependent Indian communities with the borders of the United States whether within the originally or subsequently acquired territory
thereof,and whether within or without the limits of a state;and
• All Indian allotments,the Indian titles to which have not been extinguished,including rights-of-way running through the same.
INDIAN TRIBE means any Indian Tribe,band,group,or community recognized by the Secretary of the Interior and exercising
governmental authority over a Federal Indian reservation.
INDIRECT DISCHARGE means a nondomestic discharger introducing"pollutants"to a"publicly owned treatment works."
2A-13

FORM 2A—GLOSSARY CONTINUED
LARGE MUNICIPAL SEPARATE STORM SEWER SYSTEM(defined at§122.26(b)(4))means all municipal separate storm sewers that
are either:
(i)Located in an incorporated place with a population of 250,000 or more as determined by the 1990 Decennial Census by the Bureau of
the Census(Appendix F of 40 CFR 122);or
(ii)Located in the counties listed in appendix H of 40 CFR 122,except municipal separate storm sewers that are located in the
incorporated places,townships or towns within such counties;or
(iii)Owned or operated by a municipality other than those described in paragraphs(i)or(ii)and that are designated by the Director as part
of the large or medium municipal separate storm sewer system due to the interrelationship between the discharges of the designated
storm sewer and the discharges from municipal separate storm sewers described under paragraphs(i)or(ii). In making this determination
the Director may consider the following factors:
(A)Physical interconnections between the municipal separate storm sewers;
(B)The location of discharges from the designated municipal separate storm sewer relative to discharges from municipal separate storm
sewers described in paragraph(i);
(C)The quantity and nature of pollutants discharged to waters of the United States;
(D)The nature of the receiving waters;and
(E)Other relevant factors;or
(iv)The Director may, upon petition,designate as a large municipal separate storm sewer system,municipal separate storm sewers
located within the boundaries of a region defined by a storm water management regional authority based on a jurisdictional,watershed,or
other appropriate basis that includes one or more of the systems described in paragraphs(i),(ii),(iii).
LOG SORTING AND LOG STORAGE FACILITIES(defined at§122.27)means facilities whose discharges result from the holding of
unprocessed wood,for example,logs or roundwood with bark or after removal of bark held in self-contained bodies of water(mill ponds or
log ponds)or stored on land where water is applied intentionally on the logs(wet decking).(See 40 CFR 429,subpart I,including the
effluent limitations guidelines.)
MAJOR FACILITY means any NPDES"facility or activity"classified as such by the Regional Administrator,or,in the case of"approved
State programs,"the Regional Administrator in conjunction with the State Director.
MAXIMUM DAILY DISCHARGE LIMITATION means the highest allowable"daily discharge."
MEDIUM MUNICIPAL SEPARATE STORM SEWER SYSTEM(defined at§ 122.26(b)(7))means all municipal separate storm sewers that
are either:
(i)Located in an incorporated place with a population of 100,000 or more but less than 250,000,as determined by the 1990 Decennial
Census by the Bureau of the Census(appendix G of 40 CFR 122);or
(ii)Located in the counties listed in appendix I of 40 CFR 122,except municipal separate storm sewers that are located in the incorporated
places,townships or towns within such counties;or
(iii)Owned or operated by a municipality other than those described in paragraph(i)or(ii)and that are designated by the Director as part
of the large or medium municipal separate storm sewer system due to the interrelationship between the discharges of the designated
storm sewer and the discharges from municipal separate storm sewers described under paragraph(i)or(ii).In making this determination
the Director may consider the following factors:
(A)Physical interconnections between the municipal separate storm sewers;
(B)The location of discharges from the designated municipal separate storm sewer relative to discharges from municipal separate storm
sewers described in paragraph(i);
(C)The quantity and nature of pollutants discharged to waters of the United States;
(D)The nature of the receiving waters;or
(E)Other relevant factors;or
(iv)The Director may,upon petition,designate as a medium municipal separate storm sewer system,municipal separate storm sewers
located within the boundaries of a region defined by a storm water management regional authority based on a jurisdictional,watershed,or
other appropriate basis that includes one or more of the systems described in paragraphs(i),(ii),(iii)of this section.
2A-14

FORM 2A—GLOSSARY CONTINUED
MUNICIPALITY means a city,town,borough,county,parish,district,association,or other public body created by or under State law and
having jurisdiction over disposal of sewage,industrial wastes,or other wastes,or an Indian tribe or an authorized Indian tribal organization,
or a designated and approved management agency under section 208 of the CWA.
MUNICIPAL SEPARATE STORM SEWER(defined at§122.26(b)(8))means a conveyance or system of conveyances(including roads
with drainage systems,municipal streets,catch basins,curbs,gutters,ditches,man-made channels,or storm drains):
• Owned or operated by a State,city,town,borough,county,parish,district,association,or other public body(created by or pursuant to
State law)having jurisdiction over disposal of sewage, industrial wastes,stormwater,or other wastes,including special districts under
State law such as a sewer district,flood control district or drainage district,or similar entity,or an Indian tribe or an authorized Indian
tribal organization,or a designated and approved management agency under section 208 of the CWA that discharges to waters of the
United States.
• Designed or used for collecting or conveying stormwater.
• Which is not a combined sewer;and
• Which is not part of a POTW as defined at 40 CFR 122.2.
MUNICIPAL SLUDGE(see sewage sludge)
NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM(NPDES)means the national program for issuing,modifying, revoking
and reissuing,terminating,monitoring and enforcing permits,and imposing and enforcing pretreatment requirements,under sections 307,
402,318,and 405 of the CWA.The term includes an"approved program."
NEW DISCHARGER means any building,structure,facility,or installation:
• From which there is or may be a"discharge of pollutants;"
• That did not commence the"discharge of pollutants"at a particular"site"prior to August 13, 1979;
• Which is not a"new source;"and
• Which has never received a finally effective NPDES permit for discharges at that"site."
This definition includes an"indirect discharger"which commences discharging into"waters of the United States"after August 13, 1979. It
also means any existing mobile point source(other than an offshore or coastal oil and gas exploratory drilling rig or a coastal oil and gas
developmental drilling rig)such as a seafood processing rig,seafood processing vessel,or aggregate plant,that begins discharging at a
"site"for which it does not have a permit;and any offshore or coastal mobile oil and gas exploratory drilling rig or coastal mobile oil and gas
developmental drilling rig that commences the discharge of pollutants after August 13, 1979,at a"site"under EPA's permitting jurisdiction
for which it is not covered by an individual or general permit and which is located in an area determined by the Regional Administrator in
the issuance of a final permit to be an area of biological concern. In determining whether an area is an area of biological concern,the
Regional Administrator shall consider the factors specified in 40 CFR 125.122(a)(1)through(10).
An offshore or coastal mobile exploratory drilling rig or coastal mobile developmental drilling rig will be considered a"new discharger"only
for the duration of its discharge in an area of biological concern.
NEW SOURCE means any building,structure,facility,or installation from which there is or may be a"discharge of pollutants,"the
construction of which commenced:
• After promulgation of standards of performance under section 306 of the CWA which are applicable to such source,or
• After proposal of standards of performance in accordance with section 306 of the CWA which are applicable to such source,but only
if the standards are promulgated in accordance with section 306 within 120 days of their proposal.
OWNER OR OPERATOR means the owner or operator of any"facility or activity"subject to regulation under the NPDES program.
PERMIT means an authorization, license,or equivalent control document issued by EPA or an"approved State"to implement the
requirements of this part and parts 123 and 124."Permit"includes an NPDES"general permit"(§122.28).Permit does not include any
permit which has not yet been the subject of final agency action,such as a"draft permit"or a"proposed permit."
PESTICIDE DISCHARGES TO WATERS OF THE UNITED STATES FROM PESTICIDE APPLICATION means the application of
biological pesticides,and the application of chemical pesticides that leave a residue,from point sources to waters of the United States. In
the context of this definition of pesticide discharges to waters of the United States from pesticide application,this does not include
agricultural storm water discharges and return flows from irrigated agriculture,which are excluded by law(33 U.S.C. 1342(1);33 U.S.C.
1362(14)).
PESTICIDE RESIDUE for the purpose of determining whether a NPDES permit is needed for discharges to waters of the United States
from pesticide application,means that portion of a pesticide application that is discharged from a point source to waters of the United
States and no longer provides pesticidal benefits. It also includes any degradates of the pesticide.
2A-15

FORM 2A—GLOSSARY CONTINUED
POINT SOURCE means any discernible,confined,and discrete conveyance,including but not limited to,any pipe,ditch,channel,tunnel,
conduit,well,discrete fissure,container,rolling stock,concentrated animal feeding operation, landfill leachate collection system,vessel or
other floating craft from which pollutants are or may be discharged.This term does not include return flows from irrigated agriculture or
agricultural stormwater runoff.(See§ 122.3).
POLLUTANT means dredged spoil,solid waste,incinerator residue,filter backwash,sewage,garbage,sewage sludge,munitions,
chemical wastes, biological materials,radioactive materials(except those regulated under the Atomic Energy Act of 1954,as amended(42
U.S.C.2011 et seq.)), heat,wrecked or discarded equipment,rock,sand,cellar dirt and industrial,municipal,and agricultural waste
discharged into water. It does not mean:
• Sewage from vessels;or
• Water,gas,or other material which is injected into a well to facilitate production of oil or gas,or water derived in association with oil
and gas production and disposed of in a well,if the well used either to facilitate production or for disposal purposes is approved by
authority of the State in which the well is located,and if the State determines that the injection or disposal will not result in the
degradation of ground or surface water resources. Note:Radioactive materials covered by the Atomic Energy Act are those
encompassed in its definition of source,byproduct,or special nuclear materials. Examples of materials not covered include radium
and accelerator-produced isotopes.See Train v. Colorado Public Interest Research Group, Inc.,426 U.S. 1 (1976).
PRIMARY INDUSTRY CATEGORY means any industry category listed in the NRDC settlement agreement(Natural Resources Defense
Council et al.v. Train, 8 E.R.C.2120(D.D.C. 1976),modified 12 E.R.C. 1833(D.D.C. 1979));also listed in appendix A of part 122.
PRIVATELY OWNED TREATMENT WORKS means any device or system which is(1)used to treat wastes from any facility whose
operator is not the operator of the treatment works and(2)not a"POTW."
PROCESS WASTEWATER means any water which,during manufacturing or processing,comes into direct contact with or results from the
production or use of any raw material, intermediate product,finished product,byproduct,or waste product.
PROPOSED PERMIT means a state NPDES"permit"prepared after the close of the public comment period(and,when applicable,any
public hearing and administrative appeals)which is sent to EPA for review before final issuance by the State.A"proposed permit"is not a
"draft permit."
PUBLICLY OWNED TREATMENT WORKS or POTW(defined at§403.3)means a treatment works as defined by CWA Section 212,
which is owned by a state or municipality(as defined by CWA Section 502(4)).This definition includes any devices or systems used in the
storage,treatment,recycling,and reclamation)of municipal sewage or industrial wastes of a liquid nature.This definition also includes
sewers,pipes,and other conveyances only if they convey wastewater to a POTW.The term also means the municipality as defined in
CWA Section 502(4),which has jurisdiction over the indirect discharges to and the discharges from such a treatment works.
REGIONAL ADMINISTRATOR means the Regional Administrator of the appropriate Regional Office of the Environmental Protection
Agency or the authorized representative of the Regional Administrator.
ROCK CRUSHING AND GRAVEL WASHING FACILITIES(defined at§ 122.27)means facilities which process crushed and broken
stone,gravel,and riprap(See 40 CFR 436,subpart B,including the effluent limitations guidelines).
SCHEDULE OF COMPLIANCE means a schedule of remedial measures included in a"permit",including an enforceable sequence of
interim requirements(for example,actions,operations,or milestone events)leading to compliance with the CWA and regulations.
SECONDARY INDUSTRY CATEGORY means any industry category which is not a primary industry category.
SEWAGE FROM VESSELS means human body wastes and the wastes from toilets and other receptacles intended to receive or retain
body wastes that are discharged from vessels and regulated under section 312 of the CWA,except that with respect to commercial
vessels on the Great Lakes this term includes graywater. For the purposes of this definition,"graywater"means galley,bath,and shower
water.
SEWAGE SLUDGE means any solid,semi-solid,or liquid residue removed during the treatment of municipal waste water or domestic
sewage. Sewage sludge includes, but is not limited to,solids removed during primary,secondary,or advanced waste water treatment,
scum,septage, portable toilet pumpings,type III marine sanitation device pumpings(33 CFR 159),and sewage sludge products.Sewage
sludge does not include grit or screenings,or ash generated during the incineration of sewage sludge.
SILVICULTURAL POINT SOURCE(defined at§122.27)means any discernible,confined,and discrete conveyance related to rock
crushing,gravel washing,log sorting,or log storage facilities which are operated in connection with silvicultural activities and from which
pollutants are discharged into waters of the United States.This term does not include non-point source silvicultural activities such as
nursery operations,site preparation,reforestation and subsequent cultural treatment,thinning,prescribed burning,pest and fire control,
harvesting operations,surface drainage,or road construction and maintenance from which there is natural runoff.However,some of these
activities(such as stream crossing for roads)may involve point source discharges of dredged or fill material which may require a CWA
Section 404 permit(see 33 CFR 209.120 and part 233).
2A-16

FORM 2A—GLOSSARY CONTINUED
SITE means the land or water area where any"facility or activity"is physically located or conducted,including adjacent land used in
connection with the facility or activity.
SLUDGE-ONLY FACILITY means any"treatment works treating domestic sewage"whose methods of sewage sludge use or disposal are
subject to regulations promulgated pursuant to section 405(d)of the CWA and is required to obtain a permit under§122.1(b)(2).
STANDARDS FOR SEWAGE SLUDGE USE OR DISPOSAL means the regulations promulgated pursuant to section 405(d)of the CWA
which govern minimum requirements for sludge quality,management practices,and monitoring and reporting applicable to sewage sludge
or the use or disposal of sewage sludge by any person.
STATE means any of the 50 States,the District of Columbia,Guam,the Commonwealth of Puerto Rico,the Virgin Islands,American
Samoa,the Commonwealth of the Northern Mariana Islands,the Trust Territory of the Pacific Islands,or an Indian Tribe as defined in
these regulations which meets the requirements of§123.31 of this chapter.
STATE DIRECTOR means the chief administrative officer of any State or interstate agency operating an"approved program,"or the
delegated representative of the State Director.If responsibility is divided among two or more State or interstate agencies,"State Director"
means the chief administrative officer of the State or interstate agency authorized to perform the particular procedure or function to which
reference is made.
STORMWATER(or STORM WATER)(defined at§122.26(b)(13))means stormwater runoff,snow melt runoff,and surface runoff and
drainage.
STORMWATER DISCHARGE ASSOCIATED WITH INDUSTRIAL ACTIVITY(defined at§122.26(b)(14))means the discharge from any
conveyance that is used for collecting and conveying stormwater and that is directly related to manufacturing,processing or raw materials
storage areas at an industrial plant.The term does not include discharges from facilities or activities excluded from the NPDES program
under this part 122. For the categories of industries identified in this section,the term includes,but is not limited to,stormwater discharges
from industrial plant yards;immediate access roads and rail lines used or traveled by carriers of raw materials, manufactured products,
waste material,or by-products used or created by the facility;material handling sites;refuse sites;sites used for the application or disposal
of process waste waters(as defined at 40 CFR 401);sites used for the storage and maintenance of material handling equipment;sites
used for residual treatment,storage,or disposal;shipping and receiving areas;manufacturing buildings;storage areas(including tank
farms)for raw materials,and intermediate and final products;and areas where industrial activity has taken place in the past and significant
materials remain and are exposed to stormwater.For the purposes of this paragraph,material handling activities include storage,loading
and unloading,transportation,or conveyance of any raw material, intermediate product,final product,by-product or waste product.The
term excludes areas located on plant lands separate from the plant's industrial activities,such as office buildings and accompanying
parking lots as long as the drainage from the excluded areas is not mixed with stormwater drained from the above described areas.
Industrial facilities(including industrial facilities that are federally,State,or municipally owned or operated that meet the description of the
facilities listed in paragraphs 1 through 14 below)include those facilities designated under the provisions of 40 CFR 122.26(a)(1)(v).The
following categories of facilities are considered to be engaging in"industrial activity"for purposes of 40 CFR 122.26(b)(14):
1. Facilities subject to stormwater effluent limitations guidelines,new source performance standards,or toxic pollutant effluent standards
under 40 CFR Subchapter N(except facilities with toxic pollutant effluent standards which are exempted under paragraph 11 below);
2. Facilities classified as Standard Industrial Classification 24,Industry Group 241 that are rock crushing,gravel washing,log sorting,or
log storage facilities operated in connection with silvicultural activities defined in 40 CFR 122.27(b)(2)—(3)and Industry Groups 242
through 249;26(except 265 and 267),28(except 283),29,311,32(except 323),33,3441,373;(not included are all other types of
silvicultural facilities);
3. Facilities classified as Standard Industrial Classifications 10 through 14(mineral industry)including active or inactive mining
operations(except for areas of coal mining operations no longer meeting the definition of a reclamation area under 40 CFR 434.11(1)
because the performance bond issued to the facility by the appropriate SMCRA authority has been released,or except for areas of
non—coal mining operations which have been released from applicable State or Federal reclamation requirements after
December 17, 1990)and oil and gas exploration,production,processing,or treatment operations,or transmission facilities that
discharge stormwater contaminated by contact with or that has come into contact with,any overburden,raw material,intermediate
products,finished products,byproducts or waste products located on the site of such operations;(inactive mining operations are
mining sites that are not being actively mined,but which have an identifiable owner/operator;inactive mining sites do not include sites
where mining claims are being maintained prior to disturbances associated with the extraction,beneficiation,or processing of mined
materials,nor sites where minimal activities are undertaken for the sole purpose of maintaining a mining claim);
4. Hazardous waste treatment,storage,or disposal facilities,including those that are operating under interim status or a permit under
subtitle C of RCRA;
5. Landfills,land application sites,and open dumps that receive or have received any industrial wastes(waste that is received from any
of the facilities described under this subsection)including those that are subject to regulation under subtitle D of RCRA;
6. Facilities involved in the recycling of materials,including metal scrapyards,battery reclaimers,salvage yards,and automobile
junkyards,including but limited to those classified as Standard Industrial Classification 5015 and 5093;
2A-17

FORM 2A-GLOSSARY CONTINUED
7. Steam electric power generating facilities,including coal handling sites;
8. Transportation facilities classified as Standard Industrial Classifications 40,41,42(except 4221-25),43,44,45,and 5171 which have
vehicle maintenance shops,equipment cleaning operations,or airport deicing operations.Only those portions of the facility that are
either involved in vehicle maintenance(including vehicle rehabilitation,mechanical repairs,painting,fueling,and lubrication),
equipment cleaning operations,airport deicing operations,or which are otherwise identified under paragraphs 1-7 or 9-11 are
associated with industrial activity;
9. Treatment works treating domestic sewage or any other sewage sludge or wastewater treatment device or system,used in the
storage treatment,recycling,and reclamation of municipal or domestic sewage,including land dedicated to the disposal of sewage
sludge that are located within the confines of the facility,with a design flow of 1.0 mgd or more,or required to have an approved
pretreatment program under 40 CFR 403.Not included are farm lands,domestic gardens or lands used for sludge management
where sludge is beneficially reused and which are not physically located in the confines of the facility,or areas that are in compliance
with section 405 of the CWA;
10. Construction activity including clearing,grading and excavation,except operations that result in the disturbance of less than five acres
of total land area.Construction activity also includes the disturbance of less than five acres of total land area that is a part of a larger
common plan of development or sale if the larger common plan will ultimately disturb five acres or more;
11. Facilities under Standard Industrial Classifications 20,21,22,23,2434,25,265,267,27,283,285,30,31 (except 311),323,34
(except 3441),35,36,37(except 373),38,39,and 4221-25.
TOXIC POLLUTANT means any pollutant listed as toxic under section 307(a)(1)or,in the case of"sludge use or disposal practices,"any
pollutant identified in regulations implementing section 405(d)of the CWA.
TREATMENT WORKS TREATING DOMESTIC SEWAGE(TWTDS)means a POTW or any other sewage sludge or waste water
treatment devices or systems,regardless of ownership(including federal facilities),used in the storage,treatment,recycling,and
reclamation of municipal or domestic sewage,including land dedicated for the disposal of sewage sludge.This definition does not include
septic tanks or similar devices. For purposes of this definition,"domestic sewage"includes waste and waste water from humans or
household operations that are discharged to or otherwise enter a treatment works.In States where there is no approved State sludge
management program under section 405(f)of the CWA,the Regional Administrator may designate any person subject to the standards for
sewage sludge use and disposal in 40 CFR 503 as a"treatment works treating domestic sewage,"where he or she finds that there is a
potential for adverse effects on public health and the environment from poor sludge quality or poor sludge handling,use or disposal
practices,or where he or she finds that such designation is necessary to ensure that such person is in compliance with 40 CFR 503.
UPSET(defined at§ 122.41(n))means an exceptional incident in which there is unintentional and temporary noncompliance with
technology based permit effluent limitations because of factors beyond the reasonable control of the permittee.An upset does not include
noncompliance to the extent caused by operational error, improperly designed treatment facilities, inadequate treatment facilities,lack of
preventive maintenance,or careless or improper operation.
VARIANCE means any mechanism or provision under section 301 or 316 of the CWA or under 40 CFR 125,or in the applicable"effluent
limitations guidelines"which allows modification to or waiver of the generally applicable effluent limitation requirements or time deadlines of
the CWA.This includes provisions which allow the establishment of alternative limitations based on fundamentally different factors or on
sections 301(c),301(g),301(h),301(i),or 316(a)of the CWA.
WATERS OF THE UNITED STATES as defined at§122.2.
WHOLE EFFLUENT TOXICITY(WET)means the aggregate toxic effect of an effluent measured directly by a toxicity test.
2A-18

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
Form U.S.Environmental Protection Agency
2A a EPA Application for NPDES Permit to Discharge Wastewater
NPDES NEW AND EXISTING PUBLICLY OWNED TREATMENT WORKS
SECTION 1.BASIC APPLICATION INFORMATION FOR ALL APPLICANTS(40 CFR 122.21(j)(1)and(9))
1.1 Facility name
Codydowns-Glass
Mailing address(street or P.O.box)
2627 Beckonridge Centre Drive
City or town State ZIP code
o Monroe NC 28112
Contact name(first and last) Title Phone number Email address
O Jonathan McCall Owner/Operator [phone] [e-mail]
Location address(street,route number,or other specific identifier) ❑ Same as mailing address
1214 Helms Shortcut Rd
u_ City or town State ZIP code
Monroe NC 28112
1.2 Is this application for a facility that has yet to commence discharge?
✓❑ Yes 4 See instructions on data submission ❑ No
requirements for new dischargers.
1.3 Is applicant different from entity listed under Item 1.1 above?
❑✓ Yes ❑ No 4 SKIP to Item 1.4.
Applicant name
Carolina Development Services
Applicant address(street or P.O.box)
2627 Beckonridge Centre Drive
City or town State ZIP code
Monroe NC 28112
Contact name(first and last) Title Phone number Email address
c. Matthew C.Kirchner P.E. [phone] [e-mail]
n
1.4 Is the applicant the facility's owner,operator,or both?(Check only one response.)
❑ Owner ❑ Operator ElBoth
1.5 To which entity should the NPDES permitting authority send correspondence?(Check only one response.)
El Facility El Applicant ❑ Facility and applicant
(they are one and the same)
1.6 Indicate below any existing environmental permits.(Check all that apply and print or type the corresponding permit
number for each.)
Existing Environmental Permits
o ❑ NPDES(discharges to surface ❑ RCRA(hazardous waste) ❑ UIC(underground injection
water) control)
m
E
❑ PSD(air emissions) ❑ Nonattainment program(CM) ❑ NESHAPs(CM)
cn
❑ Ocean dumping(MPRSA) 0 Dredge or fill(CWA Section ❑ Other(specify)
404)
EPA Form 3510-2A(Revised 3-19) Page 1

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
1.7 Provide the collection system information requested below for the treatment works.
Municipality Population Collection System Type Ownership Status
Served Served (indicate percentage)
100 %separate sanitary sewer 0 Own El Maintain
„ 1,260 %combined storm and sanitary sewer 0 Own 0 Maintain
a) 0 Unknown 0 Own 0 Maintain
c %separate sanitary sewer 0 Own 0 Maintain
%combined storm and sanitary sewer ❑ Own 0 Maintain
fa
c 0 Unknown 0 Own 0 Maintain
0.
a %separate sanitary sewer ❑ Own 0 Maintain
c %combined storm and sanitary sewer 0 Own 0 Maintain
E 0 Unknown 0 Own 0 Maintain
43 %separate sanitary sewer 0 Own 0 Maintain
�+ %combined storm and sanitary sewer 0 Own 0 Maintain
co
c 0 Unknown 0 Own 0 Maintain
y Total
°' Population 1,260
o Served
Separate Sanitary Sewer System Combined Storm and
Sanitary Sewer
Total percentage of each type of
sewer line(in miles) 100 % 0
1.8 Is the treatment works located in Indian Country?
c
0 0 Yes ✓❑ No
U
c 1.9 Does the facility discharge to a receiving water that flows through Indian Country?
ca
c ❑ Yes ❑✓ No
1.10 Provide design and actual flow rates in the designated spaces. Design Flow Rate
0.12657 mgd
�a
w ai Annual Average Flow Rates(Actual)
Two Years Ago Last Year This Year
c
c o mgd mgd mgd
o cn LL
Maximum L.aily Flow Rates(Actual)
Two Years Ago Last Year This Year
mgd mgd mgd
H 1.11 Provide the total number of effluent discharge points to waters of the United States by type.
.o Total Number of Effluent Discharge Points by Type
CL Constructed
el- Treated Effluent Untreated Effluent Combined Sewer Bypasses E
R T Overflows yp Emergency
y
hOverflows
0 2 0 0 0 0
EPA Form 3510-2A(Revised 3-19) Page 2

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
Outfalls Other Than to Waters of the United States
1.12 Does the POTW discharge wastewater to basins,ponds,or other surface impoundments that do not have outlets for
discharge to waters of the United States?
❑ Yes ❑✓ No 4 SKIP to Item 1.14.
1.13 Provide the location of each surface impoundment and associated discharge information in the table below.
Surface Impoundment Location and Discharge Data
Average Daily Volume Continuous or Intermittent
Location Discharged to Surface (check one)
Impoundment
❑ Continuous
gpd ❑ Intermittent
❑ Continuous
gpd ❑ Intermittent
❑ Continuous
gpd ❑ Intermittent
.2 1.14 Is wastewater applied to land?
❑ Yes ❑✓ No 4 SKIP to Item 1.16.
0 1.15 Provide the land application site and discharge data requested below.
13. Land Application Site and Discharge Data
Continuous or
Location Size Average Daily Volume Intermittent
Applied (check one)
acres d
0 0 Continuous
cn
5 gp ❑ Intermittent
acres gpd 0 Continuous
0 Intermittent
0 Continuous
acres gpd ❑ Intermittent
A 1.16 Is effluent transported to another facility for treatment prior to discharge?
❑ Yes m No 4 SKIP to Item 1.21.
1.17 Describe the means by which the effluent is transported(e.g.,tank truck,pipe).
1.18 Is the effluent transported by a party other than the applicant?
❑ Yes ❑ No 4 SKIP to Item 1.20.
1.19 Provide information on the transporter below.
Transporter Data
Entity name Mailing address(street or P.O.box)
City or town State ZIP code
Contact name(first and last) Title
Phone number Email address
EPA Form 3510-2A(Revised 3-19) Page 3

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
1.20 In the table below,indicate the name,address,contact information,NPDES number,and average daily flow rate of the
receiving facility.
Receiving Facility Data
Facility name Mailing address(street or P.O.box)
CD
City or town State ZIP code
0
v
o Contact name(first and last) Title
0
s
Phone number Email address
Cl) NPDES number of receiving facility(if any) ❑ None Average daily flow rate mgd
to
0 1.21 Is the wastewater disposed of in a manner other than those already mentioned in Items 1.14 through 1.21 that do not
a have outlets to waters of the United States(e.g.,underground percolation,underground injection)?
m 0 Yes ❑✓ No 4 SKIP to Item 1.23.
0
0 1.22 Provide information in the table below on these other disposal methods.
s Information on Other Disposal Methods
6 Disposal Annual Average
o Method Location of Size of Daily Discharge Continuous or Intermittent
Description Disposal Site Disposal Site Volume (check one)
w —
7a 0 Continuous
= acres gpd ❑ Intermittent
❑ Continuous
acres gpd 0 Intermittent
0 Continuous
acres gpd 0 Intermittent
1 23 Do you intend to request or renew one or more of the variances authorized at 40 CFR 122.21(n)?(Check all that apply.
0 to Consult with your NPDES permitting authority to determine what information needs to be submitted and when.)
o . ❑ Discharges into marine waters(CWA ❑✓ Water quality related effluent limitation(CWA Section
Section 301(h)) 302(b)(2))
❑ Not applicable
1.24 Are any operational or maintenance aspects(related to wastewater treatment and effluent quality)of the treatment works
the responsibility of a contractor?
✓❑ Yes ❑ No 4SKIP to Section 2.
1.25 Provide location and contact information for each contractor in addition to a description of the contractor's operational
and maintenance responsibilities.
Contractor Information
Contractor 1 Contractor 2 Contractor 3
c Contractor name
m (company name) Carolina Development Services
oMailing address
c (street or P.O.box)
2627 Beckonridge Centre Dr
o City,state,and ZIP
code Monroe,NC,28110
e Contact name(first and Jonathan McCall
o last)
Phone number [phone]
Email address [e-mail]
Operational and bnry re,p�,,bdier wuum,ndnd aprnperp bren,ed
pperaror ro anentl ro nw sy,rem on,M1equenrinumber or oar.
maintenance wek hour perdy and dur,fb ba is ba etlpn N[
requirements.peco!tl me processed Hnwlepml.OppmVl,pH.00
responsibilities of m„,..p ,p�.p rm, y,tprer,rernmmendata r ae
pmoe:a wr,metera,re ter m the av+tem uper,ane emrienw w
contractor tlnipn 6ultlelim.Add 4p silty,th opeam snuld muap
EPA Form 3510-2A(Revised 3-19) Page 4

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
SECTION 2.ADDITIONAL INFORMATION(40 CFR 122.21(j)(1)tnd(2))
c Outfalis to Waters of the United States
c 2.1 Does the treatment works have a design flow greater than or equal to 0.1 mgd?
o ✓❑ Yes ❑ No 4 SKIP to Section 3.
c 2.2 Provide the treatment works'current average daily volume of inflow Average Daily Volume of Inflow and Infiltration
and infiltration.
152,000 gpd
Indicate the steps the facility is taking to minimize inflow and infiltration.
R The overall System is an above ground Package plant configuration,that is not subject to groundwater or storm-water
infiltration.There is no tying into any other type of feed such as storm-water.
c
2.3 Have you attached a topographic map to this application that contains all the required information?(See instructions for
• a specific requirements.)
0)
O z
o ❑ Yes ❑✓ No
E 2.4 Have you attached a process flow diagram or schematic to this application that contains all the required information?
o (See instructions for specific requirements.)
L.T. o ❑ Yes ❑✓ No
2.5 Are improvements to the facility scheduled?
❑ Yes ❑✓ No 4 SKIP to Section 3.
Briefly list and describe the scheduled improvements.
0
1.
c
E
2.
0
3.
a
w
U,
4.
-0
0 2.6 Provide scheduled or actual dates of completion for improvements.
Scheduled or Actual Dates of Completion for Improvements
E Affected Attainment of
Scheduled Outfalls begin End Begin Operational
2 Improvement Construction Construction Discharge
(from above) (list outfalt (MM/DD/YYYY) (MM/DD/YYYY) (MM/DD/YYYY) Level
number) (MM/DD/YYYY)
1
2
cn
3.
4.
2.7 Have appropriate permits/clearances concerning other federal/state requirements been obtained?Briefly explain your
response.
❑ Yes ❑ No ❑ None required or applicable
Explanation:
EPA Form 3510-2A(Revised 3-19) Page 5

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
SECTION 3.INFORMATION ON EFFLUENT DISCHARGES(40 CFR 122.21(j)(3)to(5))
3.1 Provide the following information for each outfall.(Attach additional sheets if you have more than three outfalls.)
Outfall Number 1 Outfall Number 2 Outfall Number
State North Carolina North Carolina
to
711
County Union Union
U
3
0 City or town Monroe Monroe
15
c
to
O Distance from shore 95 ft. 95 ft. ft.
a
d Depth below surface 1 ft. 1 ft. ft.
0
Average daily flow rate 0.075 mgd 0.075 mgd mgd
Latitude 34° 56' 43.40" N 34° 56' 43.40" N °
Longitude 80° 33' 35.79" W 80° 33' 35.79" W "
3.2 Do any of the outfalls described under Item 3.1 have seasonal or periodic discharges?
-11
G ✓❑ Yes 0 No 4 SKIP to Item 3.4.
d
1 E 3.3 If so,provide the following information for each applicable outfall.
r
to Outfall Number 1 Outfall Number 2 Outfall Number
0
o Number of times per year
o discharge occurs 365 365
a Average duration of each
`o discharge(specify units) Continuous Continuous
TO
ao discharge ow of each 0.075 mgd 0.075 mgd mgd
A
41)co
Months in which discharge 12 12
occurs
3.4 Are any of the outfalls listed under Item 3.1 equipped with a diffuser?
❑ Yes ❑✓ No 4 SKIP to Item 3.6.
3.5 Briefly describe the diffuser type at each applicable outfall.
0.
1- Outfall Number Outfall Number Outfall Number
d
w
3
c
o Does the treatment works discharge or plan to discharge wastewater to waters of the United States from one or more
d = 3.6 discharge points?
.1 d
3 w ✓❑ Yes 0 No+SKIP to Section 6.
EPA Form 3510-2A(Revised 3-19) Page 6

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
3.7 Provide the receiving water and related information(if known)for each outfall.
Outfall Number 1 Outfall Number 2 Outfall Number
Receiving water name Beaverdam Creek Beaverdam Creek
Name of watershed, river,
0 or stream system Yadkin Peedee Yadkin Peedee
a U.S.Soil Conservation .
d Service 14-digit watershed 030401050504 030401050504
o code
Name of state management/river basin North Carolina North Carolina
rn
c U.S.Geological Survey
4) 8-digit hydrologic 03040105 03040105
cc cataloging unit code
Critical low flow(acute) cfs cfs cfs
Critical low flow(chronic) cfs cfs cfs
Total hardness at critical mg/L of mg/L of mg/L of
low flow CaCO3 CaCO3 CaCO3
3.8 Provide the following information describing the treatment provided for discharges from each outfall.
Outfall Number 1 Outfall Number 2 Outfall Number
Highest Level of 0 Primary 0 Primary 0 Primary
Treatment(check all that 0 Equivalent to 0 Equivalent to 0 Equivalent to
apply per outfall) secondary secondary secondary
O Secondary 0 Secondary 0 Secondary
O Advanced 0 Advanced 0 Advanced
❑ Other(specify) 0 Other(specify) 0 Other(specify)
c
0
a Design Removal Rates by
•c Outfall
i
o BOD5 or CBOD5 <20 % <20 %
c
v
g TSS <10 % <10 % %
H
❑Not applicable 0 Not applicable ❑ Not applicable
Phosphorus <1 % <1 % ok
0 Not applicable 0 Not applicable 0 Not applicable
Nitrogen <5 % <5 %
Other(specify) 0 Not applicable 0 Not applicable 0 Not applicable
pH 6-9 % 6-9 % %
EPA Form 3510-2A(Revised 3-19) Page 7

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
3.9 Describe the type of disinfection used for the effluent from each outfall in the table below. If disinfection varies by
season,describe below.
micitlal ulsraviolel lamps produurrg uM1ravrolet wavekngtM1 al 35a nm.
� •M1e w,ter emery tM1e skmkas creel arakknwe rM1amxr ane nowa km lbe awce between
tM1e puartz sleeves andcNmber wall wM1ere suspendetl mkroxppic or{arwsms are eapaxdm
3 in s<slnrtwave{ermwidal uhravwlet rays.
C anskcent algbt port and M1ont panel lntlkatpr llgM1tl mtibwnl prwitle Dosivae indlcatwn
MI of germaldal lamp operasion.
Qwiper syskmfxllrta srounre cleaning of vuartz skeves wuM1pul disassembly or
v
Outfall Number 1 Outfall Number 2 Outfall Number
Disinfection type
H UV System UV System
a/
Seasons used
All Seasons All Seasons
Dechlorination used? ❑ Not applicable 0 Not applicable ❑ Not applicable
O Yes ❑ Yes ❑ Yes
✓❑ No ✓❑ No ❑ No
3.10 Have you completed monitoring for all Table A parameters and attached the results to the application package?
❑ Yes ✓❑ No
3.11 Have you conducted any WET tests during the 4.5 years prior to the date of the application on any of the facility's
discharges or on any receiving water near the discharge points?
❑ Yes © No 4 SKIP to Item 3.13.
3.12 Indicate the number of acute and chronic WET tests conducted since the last permit reissuance of the facility's
discharges by outfall number or of the receiving water near the discharge points.
Outfall Number Outfall Number Outfall Number
Acute Chronic Acute Chronic Acute Chronic
Number of tests of discharge
water
Number of tests of receiving
water
3.13 Does the treatment works have a design flow greater than or equal to 0.1 mgd?
co ❑✓ Yes ❑ No 4 SKIP to Item 3.16.
3.14 Does the POTW use chlorine for disinfection,use chlorine elsewhere in the treatment process,or otherwise have
reasonable potential to discharge chlorine in its effluent?
alElYes 4 Complete Table B,including chlorine. ElNo 4 Complete Table B,omitting chlorine.
3.15 Have you completed monitoring for all applicable Table B pollutants and attached the results to this application
package?
❑ Yes ✓❑ No
3.16 Does one or more of the following conditions apply?
• The facility has a design flow greater than or equal to 1 mgd.
• The POTW has an approved pretreatment program or is required to develop such a program.
• The NPDES permitting authority has informed the POTW that it must sample for the parameters in Table C,must
sample other additional parameters(Table D),or submit the results of WET tests for acute or chronic toxicity for
each of its discharge outfalls(Table E).
ElYes 4 Complete Tables C, D,and E as
applicable. ElNo 4 SKIP to Section 4.
3.17 Have you completed monitoring for all applicable Table C pollutants and attached the results to this application
package?
❑ Yes 0 No
3.18 Have you completed monitoring for all applicable Table D pollutants required by your NPDES permitting authority and
attached the results to this application package?
❑
No additional sampling required by NPDES Yes permitting authority.
EPA Form 3510-2A(Revised 3-19) Page 8

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
3.19 Has the POTW conducted either(1)minimum of four quarterly WET tests for one year preceding this permit application
or(2)at least four annual WET tests in the past 4.5 years?
❑ Yes ❑ No 4 Complete tests and Table E and SKIP to
Item 3.26.
3.20 Have you previously submitted the results of the above tests to your NPDES permitting authority?
❑ Yes ❑ No 4 Provide results in Table E and SKIP to
Item 3.26.
3.21 Indicate the dates the data were submitted to your NPDES permitting authority and provide a summary of the results.
Date(s)Submitted Summary of Results
(
MM/DD/YYYY)
c
c
w 3.22 Regardless of how you provided your WET testing data to the NPDES permitting authority,did any of the tests result in
toxicity?
Ck
❑ Yes ❑ No 4 SKIP to Item 3.26.
3.23 Describe the cause(s)of the toxicity:
c
d
� I
w
3.24 Has the treatment works conducted a toxicity reduction evaluation?
❑ Yes ❑ No 4 SKIP to Item 3.26.
3.25 Provide details of any toxicity reduction evaluations conducted.
3.26 Have you completed Table E for all applicable outfalls and attached the results to the application package?
❑ Yes Not applicable because previously submitted
information to the NPDES .ermittin• authorit .
SECTION 4.INDUSTRIAL DISCHARGES AND HAZARDOUS WASTES(40 CFR 122.21(j)(6)and(7))
4.1 Does the POTW receive discharges from SIUs or NSCIUs?
❑ Yes ❑✓ No SKIP to Item 4.7.
4.2 Indicate the number of SIUs and NSCIUs that discharge to the POTW.
Number of SIUs Number of NSCIUs
U)
0
A 4.3 Does the POTW have an approved pretreatment program?
_ ❑ Yes ❑ No
4.4 Have you submitted either of the following to the NPDES permitting authority that contains information substantially
identical to that required in Table F:(1)a pretreatment program annual report submitted within one year of the
P application or(2)a pretreatment program?
N ❑ Yes ❑ No 4 SKIP to Item 4.6.
0
o 4.5 Identify the title and date of the annual report or pretreatment program referenced in Item 4.4.SKIP to Item 4.7.
4.6 Have you completed and attached Table F to this application package?
❑ Yes ❑ No
EPA Form 3510-2A(Revised 3-19) Page 9

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
4.7 Does the POTW receive,or has it been notified that it will receive, by truck,rail,or dedicated pipe,any wastes that are
regulated as RCRA hazardous wastes pursuant to 40 CFR 261?
❑ Yes ❑✓ No 3 SKIP to Item 4.9.
4.8 If yes,provide the following information:
Annual
Hazardous Waste Waste Transport Method Amount of
Number (check all that apply) Waste Units
Received
❑ Truck ❑ Rail
❑ Dedicated pipe ❑ Other(specify)
0
❑ Truck ❑ Rail
3 ❑ Dedicated pipe ❑ Other(specify)
to
❑ Truck ❑ Rail
_ ❑ Dedicated pipe ❑ Other(specify)
o 4.9 Does the POTW receive,or has it been notified that it will receive,wastewaters that originate from remedial activities,
including those undertaken pursuant to CERCLA and Sections 3004(7)or 3008(h)of RCRA?
❑ Yes ❑✓ No 3 SKIP to Section 5.
4.10 Does the POTW receive(or expect to receive)less than 15 kilograms per month of non-acute hazardous wastes as
specified in 40 CFR 261.30(d)and 261.33(e)?
❑ Yes 3 SKIP to Section 5. ❑ No
4.11 Have you reported the following information in an attachment to this application:identification and description of the
site(s)or facility(ies)at which the wastewater originates;the identities of the wastewater's hazardous constituents;and
the extent of treatment,if any,the wastewater receives or will receive before entering the POTW?
❑ Yes ❑ No
SECTION 5.COMBINED SEWER OVERFLOWS(40 CFR 122.21(j)(8))
5.1 Does the treatment works have a combined sewer system?
❑ Yes ❑✓ No+SKIP to Section 6.
v 5.2 Have you attached a CSO system map to this application?(See instructions for map requirements.)
1° ❑ Yes
to 0 No
m
5.3 Have you attached a CSO system diagram to this application?(See instructions for diagram requirements.)
❑ Yes 0 No
EPA Form 3510-2A(Revised 3-19) Page 10

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
5.4 For each CSO outfall,provide the following information.(Attach additional sheets as necessary.)
CSO Outfall Number CSO Outfall Number CSO Outfall Number
City or town
0
::.
.a State and ZIP code
U
Yl
c) County
Ta
0
Latitude °
0
c) Longitude ° ° ° I
Distance from shore ft. ft. ft.
Depth below surface ft. ft. ft.
5.5 Did the POTW monitor any of the following items in the past year for its CSO outfalls?
CSO Outfall Numer CSO Outfall Number CSO Outfall Number
Rainfall ❑ Yes ❑ No ❑ Yes ❑ No 0 Yes ❑ No
am
c
00 CSO flow volume El Yes ❑ No El Yes 0 No ❑ Yes ❑ No
c
0 CSO pollutant
m 0 Yes ❑ No ❑ Yes ❑ No ❑ Yes ❑ No
0 concentrations
co
0 Receiving water quality ❑ Yes 0 No ❑ Yes 0 No ❑ Yes ❑ No
CSO frequency 0 Yes 0 No ❑ Yes ❑ No ❑ Yes ❑ No
Number of storm events ❑ Yes 0 No ❑ Yes ❑ No ❑ Yes ❑ No
I 5.6 Provide the following information for each of your CSO outfalls.
CSO Outfall Number CSO Outfall Number CSO Outfall Number
Number of CSO events in
- the past year events events events
03
a
c Average duration per hours hours hours
c event ❑Actual or❑Estimated 0 Actual or 0 Estimated 0 Actual or 0 Estimated
a)
w million gallons million gallons million gallons
o Average volume per event
� 0 Actual or 0 Estimated ❑Actual or 0 Estimated ❑Actual or 0 Estimated
Minimum rainfall causing inches of rainfall inches of rainfall inches of rainfall
a CSO event in last year 0 Actual or 0 Estimated 0 Actual or 0 Estimated 0 Actual or 0 Estimated
EPA Form 3510-2A(Revised 3-19) Page 11

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
5.7 Provide the information in the table below for each of your CSO outfalls.
CSO Outfall Number CSO Outfall Number CSO Outfa! Number
Receiving water name
Name of watershed/
stream system
a; U.S.Soil Conservation 0 Unknown 0 Unknown ❑ Unknown
co
Service 14-digit
watershed code
> (if known)
Name of state
management/river basin
U.S.Geological Survey 0 Unknown 0 Unknown 0 Unknown
8-Digit Hydrologic Unit
Code(if known)
Description of known
water quality impacts on
receiving stream by CSO
(see instructions for
exam iles
SECTION 6.CHECKLIST AND CERTIFICATION STATEMENT(40 CFR 172.22(a)and(d))
6.1 In Column 1 below,mark the sections of Form 2A that you have completed and are submitting with your application.For
each section,specify in Column 2 any attachments that you are enclosing to alert the permitting authority.Note that not
all applicants are required to provide attachments.
Column 1 Column 2
• Section 1: Basic Application
Information for All Applicants ❑ w/variance request(s) ❑✓ w/additional attachments
❑ Section 2:Additional ❑ wl topographic map ❑ w/process flow diagram
Information ✓❑ w/additional attachments
❑ w/Table A ❑ w/Table D
❑ Section 3: Information on ❑ w/Table B ❑ w/Table E
Effluent Discharges
E ❑ w/Table C ❑ wl additional attachments
to
Section 4: Industrial ❑ w/SIU and NSCIU attachments ❑ w/Table F
❑ Discharges and Hazardous
Wastes ❑ w/additional attachments
Section 5:Combined Sewer ❑ w/CSO map ❑ w/additional attachments
- ❑ Overflows
❑ w/CSO system diagram
✓❑ Section 6: Checklist and El w/attachments
to Certification Statement
N
.m 6.2 Certification Statement
I certify under penalty of law that this document and all attachments were prepared under my direction or supervision in
accordance with a system designed to assure that qualified personnel properly gather and evaluate the information
submitted.Based on my inquiry of the person or persons who manage the system,or those persons directly responsible
for gathering the information,the information submitted is,to the best of my knowledge and belief,true,accurate,and
complete.I am aware that there are significant penalties for submitting false information,including the possibility of fine
and imprisonment for knowing violations.
Name(print or type first and last name) Official title
Matthew C.Kirchner P.E.
Signature�� �i. / Date signed
/z�:Q,�Ut.Wui- C /11/LC-11.4 - 09/08/2022
EPA Form 3510-2A(Revised 3-19) Page 12

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE A.EFFLUENT PARAMETERS FOR ALL POTWS
Maximum Daily Discharge Average Daily Discharge
Pollutant Analytical ML or MDL
Value Units Value Units Number of Nethodl (include units)
Samples
Biochemical oxygen demand
❑ML
0 BODE or o CBOD5 ❑MDL
(report one)
Fecal coliform ❑ML
❑MDL
Design flow rate
pH(minimum) I }
pH(maximum) 1I
Temperature(winter)
Temperature(summer)
Li L
Total suspended solids(TSS) ❑MDL
1 Sampling shall be conducted according to sufficiently sensitive test procedures(i.e.,methods)approved under 40 CFR 136 for the analysis of pollutants or pollutant parameters or
required under 40 CFR chapter I,subchapter N or 0.See instructions and 40 CFR 122.21(e)(3).
EPA Form 3510-2A(Revised 3-19) Page 13

This page intentionally left blank.

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE B.EFFLUENT PARAMETERS FOR ALL POTWS WITH A FLOW EQUAL TO OR GREATER THAN 0.1 MGD
Maximum Daily Discharge Average Daily Discharge
Pollutant Analytical ML or MDL
Value Units Value Units Number of Method' (include units)
Samples
Ammonia(as N) ❑ML
❑MDL
Chlorine
❑ML
(total residual,TRC)2 ❑MDL
Dissolved oxygen ❑ML
❑MDL
Nitrate/nitrite ❑ML
❑MDL
Kjeldahl nitrogen ❑ML
❑MDL
Oil and grease ❑ML
❑MDL
Phosphorus CI ML
❑MDL
Total dissolved solids ❑ML
❑MDL
1 Sampling shall be conducted according to sufficiently sensitive test procedures(i.e.,methods)approved under 40 CFR 136 for the analysis of pollutants or pollutant parameters or
required under 40 CFR chapter I,subchapter N or 0.See instructions and 40 CFR 122.21(e)(3).
2 Facilities that do not use chlorine for disinfection,do not use chlorine elsewhere in the treatment process,and have no reasonable potential to discharge chlorine in their effluent are not
required to report data for chlorine.
EPA Form 3510-2A(Revised 3-19) Page 15

This page intentionally left blank.

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-G lass OMB No.2040-0004
TABLE C.EFFLUENT PARAMETERS FOR SELECTED POTWS
Maximum Daily Discharge Average Daily Discharge Analytical ML or MDL
Pollutant Number of Method' (include units)
Value Units Value Units Samples
Metals,Cyanide,and Total Phenols
❑ML
Hardness(as CaCO3) ❑MDL
Antimony,total recoverable CI ML
❑MDL
❑ML
Arsenic,total recoverable ❑MDL
Beryllium,total recoverable CI ML
❑MDL
Cadmium,total recoverable CI ML
Cl MDL
Chromium,total recoverable CI ML
❑MDL
Copper,total recoverable ❑ML
❑MDL
Lead,total recoverable ❑ML
❑MDL
Mercury,total recoverable ❑ML
❑MDL
Nickel,total recoverable ❑ML
❑MDL
Selenium,total recoverable ❑ML
❑MDL
Silver,total recoverable ❑ML
❑MDL
Thallium,total recoverable ❑ML
❑MDL
Zinc,total recoverable CI ML
❑MDL
Cyanide ❑ML
0 MDL
Total phenolic compounds ❑ML
❑MDL
Volatile Organic Compounds
Acrolein CI ML
__ _ ❑MDL
Acrylonitrile ❑ML
0 MDL
Benzene ❑ML
❑MDL
Bromoform CI ML
Cl MDL
EPA Form 3510-2A(Revised 3-19) Page 17

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE C.EFFLUENT PARAMETERS FOR SELECTED POTWS
Maximum Daily Discharge Average Daily Discharge Analytical ML or MDL
Pollutant
Value Units Value Units Number of Methods (include units)
samples _
Carbon tetrachloride ❑ML
❑MDL
Chlorobenzene ❑ML
❑MDL
Chlorodibromomethane ❑ML
❑MDL
Chloroethane ❑ML
❑MDL
2-chloroethylvinyl ether ❑ML
❑MDL
Chloroform ❑ML
❑MDL
Dichlorobromomethane ❑ML
❑MDL
1,1-dichloroethane ❑ML
❑MDL
1,2-dichloroethane ❑ML
❑MDL
trans-1,2-dichloroethylene ❑ML
❑MDL
1,1-dichloroethylene 0 ML
❑MDL
1,2-dichloropropane ❑ML
❑MDL
1,3-dichloropropylene ❑ML
❑MDL
Ethylbenzene ❑ML
❑MDL
Methyl bromide ❑ML
❑MDL
Methyl chloride ❑ML
❑MDL
Methylene chloride ❑ML
❑MDL
1,1,2,2-tetrachloroethane ❑ML
❑MDL
Tetrachloroethylene ❑ML
❑MDL
Toluene ❑ML
❑MDL
1,1,1-trichloroethane ❑ML
❑MDL
1,1,2-trichloroethane ❑ML
❑MDL
EPA Form 3510-2A(Revised 3-19) Page 18

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-G lass OMB No.2040-0004
Maximum Daily Discharge Average Daily Discharge Analytical ML or MDL
Pollutant Number of Method (include units)
Value Units Value Units Samples
Trichloroethylene ❑ML
El MDL
Vinyl chloride ❑ML
❑MDL
Acid-Extractable Compounds
p-chloro-m-cresol ❑ML
❑MDL
2-chlorophenol ❑ML
El MDL
2,4-dichlorophenol ❑ML
El MDL
2,4-dimethylphenol ❑ML
El MDL
El ML
4,6-dinitro-o-cresol ❑MDL
2,4-dinitrophenol El ML
❑MDL
2-nitrophenol El ML
El MDL
El ML
4-nitrophenol ❑MDL
Pentachlorophenol ❑ML
El MDL
Phenol El ML
❑MDL
2,4,6-trichlorophenol El ML
El MDL
Base-Neutral Compounds
Acenaphthene El ML
❑MDL
Acenaphthylene ❑ML
El MDL
Anthracene El ML
El MDL
Benzidine El ML
El MDL
Benzo(a)anthracene El ML
El MDL
Benzo(a)pyrene ❑ML
❑MDL
3,4-benzofluoranthene El ML
❑MDL
EPA Form 3510-2A(Revised 3-19) Page 19

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE C.EFFLUENT PARAMETERS FOR SELECTED POTWS
Maximum Daily Discharge Average Daily Discharge Analytical ML or MDL
Pollutant
Value Units Value Units 1- Number of Method' (include units)
Sam les
Benzo(ghi)perylene ❑ML
❑MDL
ID ML
Benzo(k)fluoranthene 0 MDL
❑ML
Bis(2-chloroethoxy)methane 0 MDL
❑ML
Bis(2-chloroethyl)ether ❑MDL_
❑ML
Bis(2-chloroisopropyl)ether ❑MDL
Bis(2-ethylhexyl)phthalate ❑ML
❑MDL
0 ML
4-bromophenyl phenyl ether 0 MDL
0 ML
Butyl benzyl phthalate 0 MDL
2-chloronaphthalene ❑ML
❑MDL
0 ML
4-chlorophenyl phenyl ether ❑MDL
0 ML
Chrysene 0 MDL
0 ML
di-n-butyl phthalate ❑MDL
di-n-octyl phthalate ❑ML
❑MDL
O ML
Dibenzo(a,h)anthracene _ ❑MDL
1,2-dichlorobenzene ❑ML
❑MDL
1,3-dichlorobenzene ❑ML
❑MDL
1,4-dichlorobenzene ❑ML
❑MDL
3,3-dichlorobenzidine ❑ML
❑MDL
0 ML
Diethyl phthalate 0 MDL
0 ML
Dimethyl phthalate ❑MDL
2,4-dinitrotoluene ❑ML
❑MDL
2,6-dinitrotoluene ❑ML
❑MDL
EPA Form 3510-2A(Revised 3-19) Page 20

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE C.EFFLUENT PARAMETERS FOR SELECTED POTWS
Maximum Daily Discharge Average Daily Discharge Analytical ML or MDL
Pollutant I Number of Method1 (include units)
Value Units Value Units Samples
1,2-diphenylhydrazine CI ML
❑MDL
Fluoranthene CI ML
❑MDL
Fluorene CI ML
❑MDL
Hexachlorobenzene CI ML
❑MDL
Hexachlorobutadiene ❑ML
❑MDL
Hexachlorocyclo-pentadiene ❑ML
❑MDL
Hexachloroethane ❑ML
❑MDL
Indeno(1,2,3-cd)pyrene ❑ML
❑MDL
Isophorone CI ML
❑MDl
0 ML
Naphthalene ❑MDL
Nitrobenzene CI ML
❑MDL
N-nitrosodi-n-propylamine CI ML
❑MDL
N-nitrosodimethylamine Cl ML
❑MDL
N-nitrosodiphenylamine CI ML
❑MDL
Phenanthrene CI ML
❑MDL
Pyrene CI ML
❑MDL
1,2,4-trichlorobenzene 0 ML
❑MDL
1 Sampling shall be conducted according to sufficiently sensitive test procedures(i.e.,methods)approved under 40 CFR 136 for the analysis of pollutants or pollutant parameters or
required under 40 CFR Chapter I,Subchapter N or 0.See instructions and 40 CFR 122.21(e)(3).
EPA Form 3510-2A(Revised 3-19) Page 21

This page intentionally left blank.

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE D.ADDITIONAL POLLUTANTS AS REQUIRED BY NPDES PERMITTING AUTHORITY
Maximum Daily Discharge Average Daily Dischar e
Pollutant Analytical ML or MDL
(list) Value Units Value Units Number of Method, (include units)
Samples
❑ No additional sampling is required by NPDES permitting authority.
El ML
❑MDL
❑ML
El MDL
❑ML
El MDL
❑ML
❑MDL
❑ML
❑MDL
❑ML
0 MDL
❑ML
❑MDL
❑ML
❑MDL
El ML
El MDL
El ML
❑MDL
El ML
❑MDL
❑ML
❑MDL
❑ML
❑MDL
0 ML
❑MDL
❑ML
❑MDL
❑ML
❑MDL
❑ML
❑MDL
Sampling shall be conducted according to sufficiently sensitive test procedures(i.e.,methods)approved under 40 CFR 136 for the analysis of pollutants or pollutant parameters or required
under 40 CFR chapter I,subchapter N or 0. See instructions and 40 CFR 122.21(e)(3).
EPA Form 3510-2A(Revised 3-19) Page 23

This page intentionally left blank.

EPA Identification Number NPDES Permit Number Name Facility Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE E.EFFLUENT MONITORING FOR WHOLE EFFLUENT TOXICITY
The table provides response space for one whole effluent toxicity sample. Copy the table to report additional test results.
Test Information
Test Number Test Number Test Number
Test species
Age at initiation of test
Outfall number
Date sample collected
Date test started
Duration
Toxicity Test Methods
Test method number
Manual title
Edition number and year of publication
Page number(s)
Sample Type
Check one: ❑ Grab ❑ Grab ❑ Grab
❑ 24-hour composite 0 24-hour composite ❑ 24-hour composite
Sample Location
Check one: El Before Disinfection ❑ Before Disinfection ❑ Before disinfection
❑After Disinfection ❑After Disinfection ❑After disinfection
❑ After Dechlorination ❑ After Dechlorination ❑ After dechlorination
Point in Treatment Process
Describe the point in the treatment process
at which the sample was collected for each
test.
Toxicity Type
Indicate for each test whether the test was ❑Acute ❑Acute ❑Acute
performed to asses acute or chronic toxicity,
or both.(Check one response.) ❑Chronic ❑ Chronic ❑ Chronic
❑ Both ❑ Both ❑ Both
EPA Form 3510-2A(Revised 3-19) Page 25

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE E.EFFLUENT MONITORING FOR WHOLE EFFLUENT TOXICITY
The table provides response space for one whole effluent toxicity sample.Copy the table to report additional test results.
Test Number Test Number Test Number
Test Type
Indicate the type of test performed.(Check one ❑ Static ❑ Static ❑ Static
response.)
❑ Static-renewal ❑ Static-renewal ❑ Static-renewal
❑ Flow-through ❑ Flow-through ❑ Flow-through
Source of Dilution Water
Indicate the source of dilution water.(Check ❑ Laboratory water ❑ Laboratory water ❑ Laboratory water
one response.)
❑ Receiving water ❑ Receiving water ❑ Receiving water
If laboratory water,specify type.
If receiving water,specify source.
Type of Dilution Water
Indicate the type of dilution water. If salt ❑ Fresh water ❑ Fresh water ❑ Fresh water
water, specify"natural"or type of artificial
sea salts or brine used. ❑ Salt water(specify) ElSalt water(specify) ElSalt water(specify)
Percentage Effluent Used
Specify the percentage effluent used for all
concentrations in the test series.
Parameters Tested
Check the parameters tested. ❑ pH ❑ Ammonia ❑ pH ❑ Ammonia ❑ pH ❑ Ammonia
❑ Salinity ❑ Dissolved oxygen ❑ Salinity ❑ Dissolved oxygen ❑ Salinity ❑ Dissolved oxygen
❑ Temperature ❑ Temperature ❑ Temperature
Acute Test Results
Percent survival in 100%effluent % % %
LCso
95%confidence interval
Control percent survival
EPA Form 3510-2A(Revised 3-19) Page 26

EPA Identification Number NPDES Permit Number Facility Name Outfall Number Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE E.EFFLUENT MONITORING FOR WHOLE EFFLUENT TOXICITY
The table provides response space for one whole effluent toxicity sample.Copy the table to report additional test results.
Test Number Test Number-- Test Number
Acute Test Results Continued
Other(describe)
Chronic Test Results
NOEC
IC25
Control percent survival
Other(describe)
Quality ControllQuality Assurance
Is reference toxicant data available? ❑ Yes El No ❑ Yes 0 No ❑ Yes ❑ No
Was reference toxicant test within ❑ Yes ❑ No ❑ Yes ❑ No ❑ Yes ❑ No
acceptable bounds?
What date was reference toxicant test run
(MM/DD/YYYY)?
Other(describe)
EPA Form 3510-2A(Revised 3-19) Page 27

This page intentionally left blank.

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE F.INDUSTRIAL DISCHARGE INFORMATION
Response space is provided for three SIUs. Copy the table to report information for additional Sills.
SIU SIU SIU
Name of SIU
Mailing address(street or P.O.box)
City,state,and ZIP code
Description of all industrial processes that affect
or contribute to the discharge.
List the principal products and raw materials that
affect or contribute to the SIU's discharge.
Indicate the average daily volume of wastewater
discharged by the SIU. gpd gpd gpd
How much of the average daily volume is
attributable to process flow? gpd gpd gpd
How much of the average daily volume is
attributable to non-process flow? gpd gpd gpd
Is the SIU subject to local limits?
❑ Yes ❑ No ❑ Yes ❑ No ❑ Yes ❑ No
Is the SIU subject to categorical standards?
❑ Yes ❑ No ❑ Yes ❑ No ❑ Yes ❑ No
EPA Form 3510-2A(Revised 3-19) Page 29

EPA Identification Number NPDES Permit Number Facility Name Form Approved 03/05/19
Codydowns-Glass OMB No.2040-0004
TABLE F.INDUSTRIAL DISCHARGE INFORMATION
Response space is provided for three SIUs.Copy the table to report information for additional Sills.
SIU SIU SIU
Under what categories and subcategories is the
SIU subject?
Has the POTW experienced problems(e.g.,
upsets,pass-through interferences)in the past 4.5 ❑ Yes ❑ No ❑ Yes ❑ No El Yes ❑ No
years that are attributable to the SIU?
If yes,describe.
EPA Form 3510-2A(Revised 3-19) Page 30

From: Weaver.John G
To: travis.brown a(�eagleonline.net
Cc: Albertin.Klaus P;Weaver.John G
Subject: Fw: USGS response to DWR USGS Low Rows request#2022-222(dated 2022/08/23)for Beaverdam Creek
Union County...Re: [EXTERNAL]Low-flow request approval
Date: Wednesday,August 31,2022 3:42:20 PM
Mr. Brown,
Forwarded below is a response I just sent a few minutes ago concerning the low-flow request
you recently submitted for Beaverdam Creek. Somehow your email address was inadvertently
incorrect, and I didn't catch it before the email was sent.
Curtis Weaver
J. Curtis Weaver, Hydrologist, PE Email:icweaverOusas.aov
USGS South Atlantic Water Science Center Online:httos://www.usgs.aov/centers/sa-water
North Carolina-South Carolina-Georgia
3916 Sunset Ridge Road
Raleigh, NC 27607
Phone:[phone] // Fax:[phone]
From: Weaver,John C<[e-mail]>
Sent:Wednesday, August 31, 2022 3:36 PM
To:[e-mail] <[e-mail]>; 'Matt Kirchner'
<[e-mail]>
Cc: [e-mail]<[e-mail]>; Montebello, Michael J
<[e-mail]>; Dowden, Doug<[e-mail]>; Litzenberger,
Kristin S<[e-mail]>; Denard, Derek<[e-mail]>; Albertin,
Klaus P<[e-mail]>; 'Haley Hardin' <[e-mail]>; Weaver,John
C<[e-mail]>
Subject: USGS response to DWR USGS Low Flows request#2022-222 (dated 2022/08/23) for
Beaverdam Creek Union County...Re: [EXTERNAL] Low-flow request approval
Mr. Brown and Mr. Kirchner,
In response to your inquiry about the low-flow characteristics for a location on Beaverdam Creek at
NC Secondary Road 2139 (Griffith Road) near Monroe in southern central Union County,the
following information is provided:
For the record: Initial location coordinates (34.9440460, -80.5682010) provided with the request
submission placed the point of interest on an unnamed tributary to Beaverdam Creek but with a
different drainage area determined when the low-flow request was initially pre-scoped. Via email

correspondence dated 08/23/2022 with the requestor,the actual point of interest was identified as
being just upstream from another small unnamed tributary that enters Beaverdam Creek also just
upstream from Griffith Road. Correspondence with the regrestor resulted in the final point of
interest being on the mainstem Beaverdam Creek where it crosses underneath NC Secondary Road
2139 (Griffith Road).
A check of the low-flow files here at the USGS South Atlantic Water Science Center (Raleigh
office) does not indicate a previous low-flow determination for the specific point of interest,
identified by the lat/long coordinates (34.94522, -80.55996) verified via email dated
08/23/2022 with the requestor following request submission to the DWR USGS Low Flows
portal.
No USGS discharge records are known to exist for the point of interest.
In the absence of site-specific discharge records sufficient for a low-flow analysis, estimates of low-
flow characteristics at ungaged locations are determined by assessing a range in the low-flow yields
(expressed as flow per square mile drainage area,or cfsm) at nearby index sites where estimates
have previously been determined.
A basin delineation completed using the online USGS StreamStats application for North Carolina
(https://streamstats.usgs.gov/ss/) indicates the drainage area for the point of interest (StreamStats
adjusted coordinates 34.94502, -80.55976 NAD83) is 14.0 sqmi.
For streams in Union County, low-flow characteristics published by the USGS are provided in the
following reports:
(1) The first is a statewide report completed in the early 1990's. It is USGS Water-Supply Paper 2403,
"Low-flow characteristics of streams in North Carolina" (Giese and Mason, 1993). An online version
of the report is available at http://pubs.usgs.gov/wsy/2403/report.pdf. The report provides the low-
flow characteristics (based on data through 1988) via regional relations and at-site values for sites
with drainage basins between 1 and 400 sqmi and not considered or known to be affected by
regulation and/or diversions.
(2)The second is a basin-wide report for the Rocky River basin published in 2003. It is USGS Water-
Resources Investigations Report 03-4147, "Low-Flow Characteristics and Profiles for the Rocky River
in the Yadkin-Pee Dee River Basin, North Carolina,through 2002" (Weaver and Fine, 2003). An
online version of the report is available through)1ttp://pubs.usgs.gov/wri/wri034147/. The report
provides the low-flow characteristics (based on data through 2002)for continuous-record gaging
stations and partial-record sites within the Rocky River basin. The report also provides low-flow
discharge profiles (7Q10, 30Q2, winter 7Q10, and 7Q2)for the Rocky River from its headwaters in
Mecklenburg County to its mouth.
(3)The third is a statewide report published in March 2015. It is USGS Scientific Investigations
Report 2015-5001, "Low-flow characteristics and flow-duration statistics for
selected USGS continuous-record streamgaging stations in North Carolina through 2012" (Weaver,

2015). The report is available online at http://pubs.usgs.gov/sir/2015/5001/. The report provides
updated low-flow characteristics and flow-duration statistics for 266 active (as of 2012 water year)
and discontinued streamgages across the state where a minimum of 10 climatic years discharge
records were available for flow analyses.
Low-flow characteristics estimated for point of interest:
Inspection of the above reports indicates the presence of nine (9) nearby selected USGS partial-
record sites (8) and continuous-record streamgages (1) across southern Union County in the general
vicinity of the point of interest where low-flow characteristics were published. Ranges for the low-
flow yields among these 9 index sites are shown below for the indicated flow statistics. Among
these 9 index sites,the low-flow discharge yields for the indicated flow statistics are as follows:
Annual 7010 low-flow yields==>from 0 to 0.0055 cfsm (average about 0.00071 cfsm, median about
0 cfsm) (zero flow at 7 of 9 index sites)
Annual 30Q2 low-flow yields ==>from 0 to 0.035 cfsm (average about 0.0079 cfsm, median
about 0.0051 cfsm) (zero flow at 4 of 9 index sites)
Winter 7Q10 low-flow yields ==>from 0 to 0.016 cfsm (average about 0.0046 cfsm, median
about 0.0018 cfsm) (zero flow at 4 of 9 index sites)
Annual 7Q2 low-flow yields ==>from 0 to 0.016 cfsm (average about 0.004 cfsm, median
about 0 cfsm) (zero flow at 5 of 9 index sites)
Average annual discharge yields ==>from 0.9 to 0.95 cfsm (average about 0.91 cfsm, median
about 0.9 cfsm)
Application of the above range in yields to the drainage area (14.0 sqmi)for the point of interest
results in the following estimated low-flow discharges:
Annual 7Q10 low-flow discharges==>from 0 to 0.077 cfs (average about 0.0099 cfs, median about 0
cfs) 3 zero flow
Annual 30Q2 low-flow discharges ==>from 0 to 0.49 cfs (average about 0.11 cfs, median
about 0.071 cfs) 4 use median value of 0.07 cfs
Winter 7Q10 low-flow discharges ==>from 0 to 0.22 cfs (average about 0.064 cfs, median
about 0.025 cfs) 4 rounded down to zero flow
Annual 7Q2 low-flow discharges==>from 0 to 0.22 cfs (average about 0.056 cfs, median
about 0 cfs) 4 zero flow
Average annual discharge discharges ==>from 12.6 to 13.3 cfs (average about 12.7 cfs,
median about 12.6 cfs)
Please note:

(1) The estimated flows are provided in units of cubic feet per second (cfs).
(2) The low-flow yields provided above are rounded to 2 significant figures. Estimated low-flow
discharges less than 1 cfs are rounded to 2 significant figures. If between 1 and 100 cfs, then
rounded to 1 decimal place; if greater than 100, then rounded to the nearest whole number(zero
decimal places).
(3)The information provided in this message is based on a preliminary assessment and considered
provisional, subject to revision pending collection of future data and further analyses.
These provisional streamflow statistics are provided via the DWR USGS Low Flows cooperative
agreement between the USGS and the N.C. Department of Environmental Quality, Division of Water
Resources.
Hope this information is helpful.
Thank you.
Curtis Weaver
J. Curtis Weaver, Hydrologist, PE Email:jcweaver(thusgs.aov
USGS South Atlantic Water Science Center Online:bttos://www.usgs.gov/centers/sa-water
North Carolina-South Carolina-Georgia
3916 Sunset Ridge Road
Raleigh, NC 27607
Phone:[phone] // Fax:[phone]
From: Albertin, Klaus P<[e-mail]>
Sent:Tuesday,August 23, 2022 10:45 AM
To:[e-mail] <[e-mail]>
Cc: Albertin, Klaus P<[e-mail]>; [e-mail]
<[e-mail]>; Weaver,John C<[e-mail]>; Montebello, Michael J
<[e-mail]>; Dowden, Doug<[e-mail]>; Litzenberger,
Kristin S<[e-mail]>; Denard, Derek<[e-mail]>
Subject: [EXTERNAL] Low-flow request approval
This email has been received from outside of DOI -Use caution before clicking on
links,opening attachments,or responding.
Your request has been approved and will be forwarded to USGS. A response from USGS
usually takes 7 - 10 business days.

Request Flow Statistic Approval
Request ID: 222
Requestor: Travis H. Brown
Requestor e-mail: [e-mail]
Requestor Phone: [phone]
Local Government:
Public Water Supply:
Consultant:
Contact:
Reason: Water Supply Water Availability/Safe Yield
River/Stream: Beavercreek damn WS-IV
Drainage Area(sq. mi.): 0.43
Latitude: 34.9440460
Longitude: 80.5682010
Other Information: Location is revised to a new location coordinates (34.94522, -80.55996)
per the requestor. The new point of interest is on the mainstem Beaverdam Creek(as opposed
to the initial unnamed tributary)just upstream from another small unnamed tributary. The
analysis will use the location where Beaverdam Creek crosses underneath Griffith Road(DA
= 14 sqmi).
Statististics: ["7Q 10","7Q 10 - Winter]
Approved by: Albertin, Klaus P

NORTH CAROLINA 2022 303(D) LIST
Rocky Yadkin-Pee Dee River Basin
AU Name AU Number Classification AU_LengthArea AU_Units
AU ID Description
Lanes Creek 13-17-40-(12 C 27.1 FW Miles
2352 From Marshville Water Supply Dam (located 0 ' mile downstream of Beaverdam Creek)to Rocky River
PARAMETER IR CATEGORY CRITERIA E:ATUS REASON FOR RATING 303D YEAR
Benthos(Nar,AL, FW) Exceeding Criteria Fair, Poor or Severe Bioclassification 1998
Beaverdam Creek 13-11-40-11 WS-V 12.1 W Miles
2354 From source to Lanes Creek
PARAMETER IR CATEGORY CRITERIA S TATUS REASON FOR RATING 303D YEAR
Copper(7 µg/I,AL, F'.V) 5 Exceedin Criteria Legacy Category 5 Total Metals 2008
Assessment
Hardy Creek 11, / 42 C 9.0 FW Miles
2385 From source to Rocky River
PARAMETER IR CATEGORY CRITERIA STATUS REASON FOR RATING 303D YEAR
Fish Community(Nar,AL, FW) 'a Exceeding Criteria Fair, Poor or Severe Bioclassification 2020
Clarks Creek 13-17-5-2 C 4.4 FW Miles
2399 From source to Mallard Creek
PARAMETER IR CATEGORY CRITERIA S:ATUS REASON FOR RATING 303D YEAR
Benthos(Nar,AL, FW) 5 Exceeding Criteria Fair, Poor or Severe Bioclassification C)i,
Doby Creek 13-17-5-3 C 4.1 FW Miles
2400 From source to Mallard Creek
PARAMETER IR CATEGORY CRITERIA STATUS REASON FOR RATING 303D YEAR
Benthos(Nar,AL, FW) 5 Exceeding Criteria Fair, Poor or Severe Bioclassification 2008
Toby Creek "13-17-5-4 C 4.4 FW Miles
2401 From source to Mallard Creek
PARAMETER IR CATEGORY CRITERIA SCATUS REASON FOR RATING 303D YEAR
Benthos(Nar,AL, RN) Exceeding Criteria Fair, Poor or Severe Bioclassification
Stony Creek 13-17-5-5 ; :i 'W Miles
2402 From source to Mallard Creek
PARAMETER IR CATEGORY CRITERIA S:ATUS REASON FOR RATING 303D YEAR
, r, Exceeding Criteria Fair, Poor or Severe Bioclassification 2008
6/7/2022 NC 2022 303d List-Approved by EPA 4/30/2022 Page 188 of 192

WATER
K,4...1 TREATMENT
A Division of Galene
CCS — 150I
Project Submittal
Eagle Engineering
For
Carolina Development Services LLC— Cody Glass CCS WTP
Questions relative to this proposal should be directed to: Abel Castineyra
Tel: [phone]
E: [e-mail]

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Contents
I. INTRODUCTION 2
II. DESIGN PARAMETERS 4
III. LAYOUT 5
IV. CALCULATION 1
1. PRE-TREATMENT 1
COARSE SCREEN 1
EQUALIZATION TANK 1
2. BIOLOGICAL TREATMENT 2
CLARIFIER 7
CLEAR WATER TANK 9
AEROBIC DIGESTER 9
3. TERTIARY TREATMENT 10
FILTRATION SYSTEM 10
DISINFECTION 12
DISINFECTION SYSTEM 13
UV SYSTEM 13
V. EQUIPMENTS 14
PRE-TREATMENT/SLUDGE TANK 14
SECONDARY TREATMENT 16
TERTIARY TREATMENT 19
APPENDIX 1-SUBMITTAL DRAWINGS 23
APPENDIX 2-CUT SHEETS 23
1

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
I. INTRODUCTION
The following document is a description of the packaged wastewater treatment plant
to be supplied by G Water for the 31 5-unit,Carolina Development Services LLC - Cody
Glass private residential development, located in the city of Monroe,North Carolina. The
treated effluent will be directed to the nearby Richardson Creek, which ultimately flows
into nearby Lake Lee.
The designed CCS unit is a biological treatment system that uses the Modified
Ludzack-Ettinger(MLE)process in the extended aeration mode with IFAS integration to
treat up to 152K GPD ADF of residential sewage. The system is a manufactured biological
treatment facility in a packaged plant delivery modal. Factory ready packaged plants,
operating in the extended aeration mode, are preferred over alternative designs for their
ease of installation, best in class odor control, operational efficiency, small footprint and
can be easily landscaped.
The extended aeration, activated sludge process has been employed extensively
throughout US and the world in its conventional form and in its modified form, such as
integrating fixed film (IFAS), to reliably meet secondary effluent treatment limits for
surface discharge.
The main sequence of operations includes: Equalization -Anoxic Zone—Aeration
Zones and Post anoxic cycles—Clarification—Tertiary filtration-UV disinfection-Sludge
Retention and Concentration.
The raw wastewater will be pumped from the equalization tank to a splitter box where
the flow to be discharged into the anoxic tanks will be controlled by means of V weirs. The
excess flow will be returned to the equalization tank.
The water level in the equalization tank will be controlled by four float switches,configured
for Stop pump level (low water level), Start pump level (continuous work) and High level
(start second pump) and High critical level (alarm).
The anoxic zone is designed to starve the biology and denitrify the sewage(biological
denitrification). In this tank the influent wastewater, and nitrate-rich mixed liquor pumped
from the effluent end of the aeration tanks are mixed. The influent wastewater serves as the
carbon source for bacteria,and the anoxic recycle pumps provide nitrate as an oxygen source.
2

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
The aeration reactors use IFAS technology. IFAS combines the treatment benefits
of activated sludge with the inherent stability and ease of operation of attached growth film
systems, increasing capacity and/or level of treatment. An increase in system stability is
also realized due to the significantly higher concentration of attached biology within IFAS
modules that can absorb variations or minor shocks in influent parameters.
The aeration reactors with Wavtex modules will be operated with a cycling
oxic/anoxic environment by alternating the aeration of each module. This creates transient
anoxic zones within the aerated tank for further denitrification.
A Dissolved Oxygen (DO) sensor will sense the oxygen level in the aeration tanks
and control the blower motor operation by means of VFD's.
An ORP sensor device will be inserted into anoxic tanks to measure electrical
charges (expressed as millivolts) to control anoxic conditions, assuring an efficient
denitrification process. Based on ORP sensor sign the flow for the MLSS recirculation
pump will be adjusted by means of a VFD controlled from the PLC.
Phosphate removal will be achieved by chemical means and precipitation. Alum
sulphate will be injected prior to the clarifier and will be used as coagulant. Phosphates will
be precipitated in clarifier. The chemical injection will be activated based on equalization
pumps operation.
Following the aeration basin, the mixed liquor enters the clarification zone where
biological solids agglomerate and develop floc size particles with excellent settling
characteristics. This floc mass then settles by gravity in the clarifiers and is further
concentrated in the hopper sections. Clean and fully treated water overflows from the
clarification zone is directed to a clear water tank. To assure minimal laminar velocity, and
prevent floating material to pass, a weir and baffle is included in the clarifier.
Water from the clear water tank will be pumped to the AMF Zeo filters for further
tertiary polishing and through a UV system for disinfection. The water will be with an
approximate 20 PSI residual pressure for further disposal.
The multimedia filters, in zeolite form,will enhance the particle removal efficiency
resulting in higher final water quality.
3

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
ADVANTAGES—CCS SYSTEM
✓ US and local Rep office for quick deployment of accredited service personnel.
✓ Completely retrievable equipment, eliminating the need for draining tanks for service.
✓ Low energy consumption due to the high efficiency obtained by retractable
course fine bubble diffusers.
✓ Factory assembled equipment,tested prior to deployment to site.
✓ Lowest interconnecting tie-points in peer group. Rapid deployment requiring only a
slab and utility connection and minor inter tankage connections.
✓ Stable wastewater treatment with extended air and increased surge tank withstanding
hydraulic shocks.
✓ High flexibility for operation.
✓ Fast stabilization under extreme conditions.
✓ Highly adaptable system, with flexible configurations that includes
Denitrification and Phosphorus reduction (if required).
✓ Low excess sludge production
II. DESIGN PARAMETERS
The following is the design parameters used for the Cody Glass Waste Water
Treatment Plant design base.
Table 1. Flow characterization
Average Daily Flow gpd 152,000
Maximum Day factor 2.0
Home units 315
Design population habitant 1,260
Peak Hour Factor* 3.73
18+ 1.26_
*Peak Hour Factor= 4+ 1.z6 3.73
4

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Table 2. Wastewater characterization (influent and effluent concentrations)
pH S.U. 6-9 6-9
BOD5 mg/L 250 <20
TSS mg/L 200 max < 10
TN mg/L 40 max <5
TP mg/L 20 <
Note:
1. All design parameters are based on min water temperature of 10°C.
2. Design assumes no inhibiting substances in water that will alter biological growth
with only domestic sewage water characteristics considered.
III. LAYOUT
The layout includes two upfront surge/equalization(EQ)tanks with integral sludge
holding compartments followed by four parallel trains with a capacity of '/4 of 152,000
GPD or 38K GPD/train.
Each single train includes an anoxic chamber (AN), an aeration zone (AE), two
hopper clarification zone (CLF) and final clear water tank.
After each parallel package plant scope, we have included our AMF-ZEO-200, a
duplex multi-media sand filter skid, in Zeolite form, to serve each dual train for tertiary
treatment required when achieving high suspended solids reduction.
The layout as proposed,will allow isolation or ramp up in approximately 38K GPD
increments of in- service vs out of service trains or a phase in approach to meet the
development's treatment needs.
Tanks will be installed above ground and is based on a steel structure. All G Water
supplied Units will require a slab not included in this scope. Any soil, civil or site
preparation work, if required,will be by others.
Note: See Appendix 1 for complete submittal drawings.
5

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
6

Eagle Engineering for Carolina Development Services LLC
Cody Gloss Residential Development, Monroe, NC
N'-T 1,r l+.T
C
15AKEEE 2ARNIGAL YWRIGAI 15.FO0R.1
ECWRRA11011 -. F!)IIAI.1101J
4
.. ,: ANt .E- V f I 1. ,.. •-, 7-, -, ------7-- - -,-i -..1 --- 6*----r 1' t1N -,r a_-_±. ..E1N4B( ',. ? '
11
1
J t V
�1 p -I amr, itl. t'�, 'r .
111 11 i
-- 1 5 1 - T
it
V . NOONC TANK •:4 �I IF ANOPC IANN *NOW TANK r • 1' NONE TMK
l
1
c _ 'r. ...c �,
+. I91'.' 1 II.F 11,40 ��I 1 0 `, 1` i` p
1 ! l - 1 I� 1■ l Him' /IA• ■IMINI I I I
1111iu111111111A; IIilnll■I■I■ I 11CCr 11 1 II
�,IutI111Al iu■ ■1■I■, I lq I' 11 I
1. l' "uIrn � ITt" " • 1 !3,*ie. 11r` Il ak-, 1.641
1111111IlINlllll+.' 'I �Ii1111 1■1■ I 1 I I I I II
II IIII1�IIIHIIIIN [IEIII�11■I■..: I 1 11 1
IIII11IIIllhlIlIN I ■1�111�11■I■ I ' II 1 I� III I I
IA11ll1lIllIl >N° I �n•AIIIIUI■I _ I II I I' 1
l
CUNFER ..1. Q
1
CI ARE ARIFER I CLMEER
1 lit I :-- I t
-I-
CIAMFER CLARE ER CLARIFIER CLAVIER
CLEAR NANA CLEAR WATER CLEARWATER T -p- rCLEARWATER
1AM1.. till TANK FANS N TANK
12 0 ._ .-- --_
—n I' 'I A 4,1
o 0
e0
ANFZE07ID MRff0-7ID
General Layout WWTP
1

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
IV. CALCULATION
1. PRE-TREATMENT
COARSE SCREEN
The CCS system includes an automated bar screen to assure no big solids are introduced
into the equalization (surge)tank. The bar screen is built into a channel located above the
tank, making the clean out very simple,reducing maintenance complexity.
Bar span: 5mm.
EQUALIZATION TANK
The equalization tank will have a hydraulic retention time of 8 hours for Average Daily
Flow.
Design Flow for each Equalization tank= 1/2 of 152,000 GPD
Q (Hourly Flow for Average daily flow) 3,167 GPH
HRT(at ADF) 8 hours
Volume (V)= Q (m3/hour) * HRT(hour)
Volume Equalization tank 25,336 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 340 in
Equalizer mixing:
Specific Airflow rate for mixing: 0.20 SCFM/ft2, (EDI design summary)
Bottom Area= 340.0 ft2
Airflow rate= 0.20 SCFM/ft2
Required airflow 68 SCFM
It will be aerated and mixed by means of three complete ballast based coarse bubble air

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
diffuser systems, completely retrievable for ease of maintenance and replacement.
Equalizer pumping rate:
The equalized flow will be pumped to the anoxic zone using a duplex (lead/lag) set of
submersible non-clog pumps installed within the EQ chamber.
The flow is pumped to a splitter box that ensures the ADF into the anoxic basins and the
excess is returned to the EQ chamber. This will reduce any peek flow events, and will
increase system stability.
The two upfront EQ tanks are tied on the top for overflow protection,as well as on the bottom
to assure equal flows run into each tank. Sectioningeach EQtank will be done byvalves on
the tank connecting points as well as in the discharge point followed by the bar screen. To
separate pipes, controlled by valves will direct the flows into either tank depending on
operator requirement
Submersible pumps
Semi open-single vane impellers.
Flow= 52.8GPM
TDH= 14.80 feet
Each pump will have a PVC ball valve and a check valve.
2. BIOLOGICAL TREATMENT
ANOXIC TANK
An anoxic chamber located before the Aeration tank, will be provided for denitrification. In
this chamber influent wastewater, return sludge from the clarifier and nitrate rich mixed
liquor from the aeration tank are mixed together by means of a mixer. Further denitrification

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
will be achieved in the aerobic tank having on-off aeration cycles in the Wavtex modules.
Denitrification in Anoxic Tank
1. Active biomass concentration (based on heterotrofic biomass, AB volume and 9c )
Xb =° 919.21 rng/I
2. Internal recycle Irratio using the Nox and desired effluent NO3-N concentration
IR = Nox/Ne - 1 - R
Ne = 7 mg/I (7mg/I in order to meet a standard of 15mgTN/L)
IR = 2.9
3. Amount of nitrate fed to anoxic tank
Flow = IRQ + RQ
Flow = 567.8 m3/d
104.2 GPM
NOx fed = Flow x Ne
NOx fed = 3.97 kg/d
4. Anoxic Volume and configuration
HRT= 3 h Define HRT
Vanox = 17.98 m3
4749.48 gal
Single stage
5. F/Mb calculation based on 1.
F/Mb = 2.18 g/g d
SDNR = 0.29 Using Curves for SDNRb
SDNRt = 0.26 Correction for T and IR
6. Amount of nitrate removed in the anoxic basin
Nor = Vanox * SDNR * MLVSS
Nor = 4.26 kg/d vs 4.0 kg/d to be reduced

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe,NC
Volume Anoxic tank 4,750 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 64 in
Mixing for the anoxic zone
The mixing system will be designed based on the thrust value. The performance of a
submersible mixer is measured by the total amount of the installed thrust(N/Newtons)
produced,position and orientation of the mixer.
Wet area=347ft2+64 ft2 =411 ft2 =38.20m2
Thrust=3 N/m2 * 38.2m2 Thrust=115 N
AEROBIC TANK (Entex Technology Design Memo)
An Integrated Fixed-film Activated Sludge (IFAS) WavTex system, it provides several key
advantages. The microbiology present on the media allows for increased treatment capacity
with a reduced footprint and shorter HRT. In addition, the inherently long SRT of the fixed
biology on the EnTextile media sheets translates to less sludge being produced compared to
activated sludge only.
The WavTex design for Cody Glass was based on the empirical removal rates of BOD,
ammonia, and nitrate.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
BOD Removal
Influent BOD=250 mg/L, or 78.2 ppd per train
40%of the treatment occurs in the mixed liquor,based on the MLSS concentration of 2,500
mg/L. Therefore, 60%of the treatment will occur on the WavTex modules.
78.2 ppd * 60%=46.91 ppd BOD removal required via WavTex per train.
BOD Removal Rate at 10°C=0.1175 ppd/ft2 of EnTextile media(gross)46.91 ppd/0.1175
ppd/ft2 =399.3 ft2
One WavTex module at 10' SWD=4,551 ft2
399.3 ft2/4,554 ft2 = 0.09 modules per train
NH3 Removal
Influent NH3 =40 mg/L, or 12.5 ppd per train
40%of the treatment occurs in the mixed liquor,based on the MLSS concentration of 2,500
mg/L. Therefore, 60%of the treatment will occur on the WavTex modules.
12.5 ppd * 60%= 7.51 ppd NH3 removal required via WavTex per train.
NH3 Removal Rate at 10 °C =0.0052 ppd/ft2 of EnTextile media(gross) 7.51 ppd/0.0052
ppd/ft2 = 1,443 ft2
One WavTex module at 10' SWD = 4,551 ft2 1,443 ft2/4,554 ft2 =0.32 modules per train
required

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
NO3 Removal
Influent NO3=40 mg/L,or 12.5 ppd per train(assume all NH3 is converted to NO3)Assume
that the pre-anoxic tank will reduce the NO3 to 15 mg/L or 4.69 ppd NO3 as presented above.
NH3 Removal Rate at 10 °C = 0.0052 ppd/ft2 of EnTextile media (gross). Note that the
denitrification rate equals that of the nitrification rate in the cyclic aeration approach. This is
because nitrification is the rate limiting step.
4.69 ppd/0.0052 ppd/ft2 =902 ft2
One WavTex module at 10' SWD = 4,551 ft2 902 ft2 / 4,554 ft2 = 0.20 modules per train
required
It was concluded that one (1) aerated WavTex module per train would provide sufficient
microbiology necessary for treatment of both BOD and ammonia. One (1) additional
WavTex module per train can be added in order to meet TN limit of< 5 mg/L. Though the
calculations yielded less than one module for both aerated treatment and denitrification, a
quantity of two (2) per train or eight (8) total was chosen for conservatism. This allows for
process flexibility within the MLSS concentration. Additionally, by having two (2)modules
per train, this ensures that one module will be in aerobic operation while the second is in
anoxic operation at all times. This is essential for creating the transient aerobic and anoxic
zones required to consistently meet the TN limit.
Aeration Requirements
Each WavTex module will have an integrated coarse bubble aeration grid that will run at
approximately 122scfm per train which is sufficient for scouring of the unit, mixing, and
biotreatment.
Hydraulic Retention Time
IFAS systems for municipal waste which adhere to these standard loading values can achieve
full nitrification with HRTs of 8 hours at temperatures above 10 deg C.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Volume Aerobic tank 12,667 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length* 191 in
Additional length is considered for recirculation pump installation.
CLARIFIER
A 2- hopper type clarifier each with a Q ADF capacity is included for each train. All pumps
in the clarifier will be based on Air Lift pumps and will include the RAS, the WAS and a
skimmer. Flow into the clarifiers are through a and baffle structure, reducing velocity and
assuring the minimal turbulence in the tank, for best settling conditions.
Design of the clarifier is based on following max design parameters:
Weir overflow rate < 5000 GPD per lineal foot for ADF
<20,000 GPD per lineal foot at PHF
Surface Loading rate (SLR) <900 GPD/SF based on influent, at PHF and considering
Activated Sludge with chemical addition to Mixed Liquor for
Phosphorus removal.
Solids Loading rate 35 ppd/SF at peak solids loading rate, calculated based on the
design maximum day flow rate plus the design maximum
return sludge rate requirement and the design MLSS under
aeration.
HRT Above 3 hours

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
Clarifier
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 215 in
Area 215 sf
Calculated Surface Loading Rate per train (each train '/ ADF = 38,000GPD)
PHF=ADF * Peak Factor
From Table 1, Peak Factor=3.73
PHF =38,000 gpd * 3.73 = 141,740 GPD
SLR= 141,740GPD 660 gpd/sf < 900 gpd/sf(at PHF)
215sf
Solids Loading Capacity
MDF=2 * ADF
MDF= 76,000 GPD (287.6m3/d)per train
IRt= IR ras+ IR anox=3.9
Clarifier area=215sf(20m2)
287.6m3/d*zsoomg*(1+3.9)
Solids load= 20m2*(1000) 176.15Kg-d/m2= 35.9 lb-d/sf
Hydraulic Retention Time (HRT)
Sludge hopper angle 0 60
H pyramid truncada 1/3 in 27.6
Major area in2 14,770
Minor area in2 144
1/3 Hopper volume gal 652.1
Cube volume gal 2,499.6

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Total volume per hopper gal 3,151.6
#hoppers ea 2.0
Total clarifier volume gal 6,303.2
Total clarifier Volurne(gal) 6,303.20
HRT = = 3.98hours
Q( gal ) 1,583.3
hour
CLEAR WATER TANK
One clear water tank will be provided for each train, each one with 15 minutes of Hydraulic
retention time for PHF (1.1 hrs for ADF). The clear water tanks will supply the filtration
system the required flow for final polishing prior to discharge.
Clear water tank 1,800 gal
Dimensions
Maximum Water Level 108 in
Width 144 in
Length 27 in
AEROBIC DIGESTER
Excess sludge from the clarifiers will be stabilized in an aerobic digester, aerated and mixed
by means of fine bubble diffusers. Stabilized sludge can be further dried to reduce volume
or otherwise disposed at an estimated 1.5% - 2% solid concentration, responsibility of the
client.
Px,tss=46.2 Kg
Sludge mass * (Kg)
Sludge tank Voume = Concentration (�/o * days
Sludge tank Voume = 4?o% * 20days =52.00m3 = 13,738ga1

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
Sludge tank 15,000 gal
Dimensions
Maximum Water Level 120 in
Width 144 in
Length 200 in
Sludge tank aeration/mixing:
Specific Airflow rate for mixing: 0.45 SCFM/ft2, (EDI design summary)
Bottom Area= 200.0 ft2
Airflow rate = 0.45 SCFM/ft2
Required airflow 90 SCFM
It will be aerated and mixed by means of three complete ballast based fine bubble air diffuser
systems, completely retrievable for ease of maintenance and replacement.
3. TERTIARY TREATMENT
FILTRATION SYSTEM
Two multimedia pressure filtration system one in operation and one in standby (Lead/Lag)
for redundancy purposes will be provided. Each having the capacity to filter the complete
flow of the plant.
During ADF operation one pump will send the water from the clean water tank to the
filtration system. The pumps will be controlled by three float switches, configures for Stop
pump level (low water level), Start pump level (continuous work) and High level (start
second pump).
The water flows into the top of the filter in a down-flow configuration. During this process,
the media removes the particles and impurities based on its design criteria.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
The filter includes two operating modes, a filtration mode and a cleaning (backwash) mode.
In filtration mode,the filtration media gradually accumulates impurities present in the water,
forming a layer of impurities. The accumulated impurities create a flow obstruction forming
a pressure differential between the inlet and the outlet.
In order to eliminate the obstruction and compensate the pressure differential, the filtration
system includes a backwash mode, achieving a complete filtration media wash. During the
process, an even lift up of the media is created by introducing clean water in a up-flow
process, discharging the dirty water through the drain (backwash line).
The backwash mode is activated automatically, when the inlet pressure and outlet pressure
switches sense a pressure differential of 7-10 psi (can be configured), or manually by the
operator. During backwash, clean water will be used from the second clean filter, assuring
clean water is used, and no additional pumps required.
Effluent from backwashing will be sent to the equalization tanks,
The schematic below shows the filter in operation and backwash mode. The G Water AMF
series filter vessel provides the industry's leading uniform distribution created by the unique
pattern of nozzle placement and disbursal on a specially designed lower plate configuration.
In the backwash mode,this pattern creates an even up flow of the media,reducing the particle
entrapment.
The pressure filter vessels will be designed with double flooring to assure high filtration
efficiency, reduction on backwash time, and reduction of"preferred channeling" effect on
the media.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
Zeolite Design Parameters:
Filtration Rate (ADF) 12-20 GPM/SF for Zeolite
Backwash Rate 15-20 GPM/SF for Zeolite(30%bed expansion)
Media Gravel/Zeolite
Pressure loss 5-7 PSI
PHF= 196.9GPM
Each AMF-ZEO-200 includes:
Two 48"- diameter tanks (one for redundancy)
Area per tank= 12.56sf
Media: Gravel/Zeolite
Feed pumps= 100GPM @ 30PSI (One pump in operation and second in standby for PHF or
backwash requirement)
Calculation for PHF
Backwash
MODEL Flow Tank diameter Area rate* Backwash
PHF Tanks Qty Filtration rate flow
GPM (pig) (m) (m2) (sf) # gpmlft2 gpm/ft2 (gpm)
AMF-Z-200 196.94 48 1.219 1.167 12.57 1 15.68 16.38 205
*for 30%bed expansion
FILTERING PROCESS BACK FLUSHING PROCESS
•
II----_� Filtering
�f/ ��\► Jrf/\ f`\1\v., Media
111111111 ttttttttt
;:r'vz z itrY��' '«.;1a4'}.:';r;.y�:
'n�.r s7 ,4 rS r. Filtering Elements
�i.° ,;,,, ''v? . ,y`,,�,r#r. S�.� r• t t t t t t t t t (Nozzle)
Mh+ik Zito z.lxitp
__ -- Lower Dispersing Plate
‘ti ti 1 1 ! l r r i
4
DISINFECTION

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
DISINFECTION SYSTEM
UV SYSTEM
Two Ultraviolet systems are provided using 4 lamps/each for single pass disinfection of the
treated wastewater prior to discharging from the plant. Each dual train will be disinfected
using UV 254nm, installed after the MMF-Zeolite step.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
V. EQUIPMENTS
PRE-TREATMENT/SLUDGE TANK
1. Bar Screen-Automatic:
Model Tsurumi KW 5038 Flow up to 113m3/hr
Bar span: 5mm.
Slope 60°
Material: 304 Stainless Steel
Motor 0.09kW
Quantity: 1 unit.
2. Submersible Pumps in Equalization tank:
Submersible pumps shall be supplied for feeding the water to the splitter box.
Semi-open, single vane impeller. Solids handling 0.79"/20mm
Each pump shall be able to handle I00GPM @ 30PSI
Model Tsurumi TOS 50B2.75HS
Suction/Discharge: 2", flanged
Motor 1 HP / 115 V/l ph
Casing, motor frame in Cast Iron, shaft stainless steel, on guide rail system for ease of
maintenance and replacement.
Each pump will have a PVC ball valve and a check valve.
Quantity: 4 units, 2 in operation and 2 in standby.
3. Level control:
Float switch, mechanically activated, wide angle.
Model SJE Pump Master WPS.
Electric: 120/230V
Quantity: 8 units (4 per tank)

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
4. Blowers for Equalization and Sludge tanks:
Model Gardner& Denver/IQ Positive displacement model IQ4LDSL
Blower Capacity required 160SCFM @ 6PSI each one(part of the air will be used for the
sludge stabilization tank)
Motor 7.5HP/240V/60Hz/3ph
Includes inlet an outlet filter, check valve,pressure relief valve, ball valve and pressure
gauge connected to a stainless steel pipe.
Each Equalization +Sludge tank requires one Blower
Quantity: 2 units
5. Air diffusers:
Sludge tank
Model EDI 88S, Retrieval units. Fine bubble flexible membrane diffuser,
FlexAirTM MagnumTM high oxygen transfer efficiency.
Hose feeder airline, SS hose clamps, and concrete ballast.
Quantity: 6 units (3 per tank)
Equalization tank
Model EDI Max Air duplex, Retrieval units. Coarse bubble PVC diffuser,
Hose feeder airline, SS hose clamps, and concrete ballast.
Quantity: 6 units (3 per tank)
Air valves: each diffuser will have a ball valve for isolation.
Material: Stainless steel 304
Model 20SSTH Matco Norca
6. Sludge evacuation:
Includes a stand pipe with a quick coupling (Banjo) connection, 3" in diameter.
7. Airlift Decanter:
Model Airlift type, SCH80 pipe, 2", with air hose pipe, and throttling ball valve.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
SECONDARY TREATMENT
1. Mixer for anoxic tank:
Submersible mixer type ABS XRW
Model 2121 60Hz Motor 2.4HP
Propeller diameter 210mm
Speed 1735 1/min
Thrust ISO 21630 255N
Installation Wall mounted on adjustable bracket
Quantity: 4 units (1 per train)
2. Blowers:
Model Gardner& Denver/IQ Positive displacement model IQ4LDSL.
Blower Capacity required 160SCFM @ 6PSI each one
Motor 7.5HP/240V/60Hz/3ph with VFD
Includes inlet an outlet filter, check valve, pressure relief valve, ball valve and pressure
gauge connected to a stainless steel 304 pipe.
Each Aeration basin('/a of ADF) requires one Blower
Standby units installed will also serve as a Standby option for the EQ/SHT
Quantity: 6 (1 per train and 2 in standby)
3. Wavtex Modules:
Textiles media for Integrated Fixed Film Activated Sludge IFAS system is produced from a
g g Y
woven, three- dimensional fabric, has a specific surface area of 4,551ft2 approximately.
Dimensions l Ofeet long by 6 feet wide, by 9.5 feet tall.
Quantity: 8 units (2 per train)
4. Air diffusers:
(1 per Wavtex module)Coarse bubble aeration grid that run at 122scfm for scouring of the
unit,mixing and biotreatment.
Material: PVC
Ball valve per grid, diameter 3"Material: Stainless steel 304 Model 20SSTH Matco Norca

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
5. Sensors DO and ORP:
FDO, luminescence optical DO sensor, for continuous monitoring.
Model YSI IQFDO700 with sensor cap factory calibrated(or similar)
Measurement range: Oxygen concentration 0 to 20
mg/I
I
Parameters measured: Dissolved oxygen and Temperature
Power consumption: 0.7 watts
Sensor Material: Housing- VA steel 1.4571; Sensor Cap and Locking Cap—POM
(Polyoxmethylene), PVS, silicone, PMMA
Rating: IP-68; waterproof
Quantity: 4 units
ORP sensor
Model YSI IQSensoLyt(or similar)
Probe w/amplifier for stationary measurement for anoxic chamber to control anoxic
conditions.
Power Consumption: 0.2W
Housing: V4A Stainless Steel 1.4571 (SW version POM (Polyoxmethylene)),
protection cap PVC
Quantity: 4 units
6. RAS and WAS:
Model Airlift type,SCH80 pipe,2",with air hose pipe,solenoid and ball valve to be operated
automatically or manually. Automatic recirculation programmed in the control panel.
Quantity: 8 units (1 per clarifier)
7. Skimmer:
Model Airlift type,SCH80 pipe,2",with air hose pipe,solenoid and ball valve to be operated
automatically or manually. Automatic recirculation programmed in the control panel.
Quantity: 8 units (1 per clarifier)

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
8. Mixed liquor recirculation pump:
Submersible pumps shall be supplied for MLSS recirculation from Aeration basin to Anoxic
tank.
Semi-open, single vane impeller. Solids handling 0.79"/20mm
Each pump shall be able to handle up to 105GPM @ 14PSI
Model Tsurumi TOS 80B21.5; Motor 2.0HP/240V/3ph with VFD
Suction/Discharge: 3", flanged
Casing, motor frame in Cast Iron, shaft stainless steel, on guide rail system for ease of
maintenance and replacement.
The pump will have a PVC ball valve and true union check valve.
Quantity: 4 units(1 per train)
9. Dosing pump for coagulant:
Electronic Metering Pumps
Model PULSAtron Series A Plus LBC4 (or similar)
Capacity 7.6LPH Max pressure 50PSI
Piping 'A"FNPT
SPM 125
Power 115VAC/60Hz/lph 0.6Amps
Quantity: 4 units
Each pump includes chemical tank for coagulant preparation
10. Control Panel:
The control panel is equipped with a PLC and consists of an interface through the HMI screen
for visualizations and configurations of the equipment.
Factory build, Unitronics PLC prewired and programmed.
One main control panel (MCP)
Enclosure: NEMA 4 weatherproof
Electrical hardware inside MCP: I/O cards, CPU, back up battery, magnetic starters, relays,
VFD's, and protections.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
The HMI interface consists of access screens for:
Surge tank pumps
Blowers with VFD and DO sensor
Airlift WAS.
Airlift RAS.
MLSS Recirculation pump with VFD
Dosing pump
Filtration pumps.
Filter backwash.
Skimmer.
UV System
TERTIARY TREATMENT
1. Filtration vessels
Material of Construction:
All filters installed in the filtration systems are manufactured from robust carbon steel
ASTM-A570-GR36. They ensure long lasting system operating life.
Protective Coating:
The coating process provides products with maximum anti-corrosion protection.
For filters up to 60" (included)the coating process is performed in seven stages, as follows:
1st stage: Automated shot blast cleaning of products to a level of SA 2.5 as per
international standard ISO 8501.
2nd stage: Phosphatization.
3rd stage: Rinsing.
4th stage: Sealing.
5th stage: Drying.
6th stage: Epoxy phenolic 120 micron.
7th stage: Oven curing.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
This process creates a perfectly coated product with a protective layer of 120 micron.
Vessels internal distribution:
The filter vessels use a unique design of a double chamber, divided by a welded reinforced
steel plate. The upper chamber contains the media; the lower chamber is empty and collects
the filtered water. The plate is covered by"mushroom"type diffusers which are PP, slotted
conical units. They disperse the water uniformly, using the whole media volume effectively,
avoiding the occurrence of channeling or caking when operated correctly.
Size: 48"diameter
Quantity: 4 units (2 in standby)
2. Media:
The vessels are filled with garnet as support media and Zeolite as filtration media.
Zeolite physical properties:
• Color: Light tan to near white
•Dry Bulk Density: 50 lbs/cu.ft
• Specific Gravity: 2.2 g/cc
•Mesh Size: 14x30
•Effective Size: 0.55mm
• Uniformity Coefficient: 1.8
• Hardness: 4-5 (Mohs Scale)
Design criteria:
•Bed Depth: 24-36 inches
• Freeboard: 50%of bed depth
•Backwash Flow Rate: 15-20 gpm/sq.ft.
•Backwash Bed Expansion: 30-40%of bed depth
• Service Flow Rate: 12-20 gpm/sq.ft.
•A gravel support bed is required
3. Feed Pump:

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
Two pumps per filtration skid will be supplied for feeding the water to the vessels.
Each pump shall be able to handle 100GPM @ 30PSI; Motor 5HP.
Suction/Discharge: 2", flanged
The pump shall be centrifugal type, Webtrol, Model FC (or similar).
Casing, Impeller Shaft Stainless Steel
Quantity: 4 units (2 per filtration skid)
4. Control Valves:
Solenoid controlled valve, opens and closes drip-tight in response to an electrical signal.
Material: Body, cover and plug Polyamid 6 & 30%GF
Diaphragm: NBR
Seals: NBR
Spring: Stainless Steel
Cover bolts: Stainless Steel
Tubing and fittings: Plastic
Solenoid voltage range: 24 VAC, 24 VDC
Quantity: 8 units (4 per filtration skid)
5. Woltman Turbine Water meter:
Magnetic drive register, Dry, IP68, NEMA 6P sealed register
"Reed switch" sensor allow one or two pulse outputs option
Body, cover: ductile iron
End Connections- Flanged: ANSI Class 150
Model: Turbo BAR-M,4"
Quantity: 1 unit.
6. Pressure Gauges:
Liquid filled pressure gauges with 4-1/2" diameter dials, and bronze bourdon tubes shall be
furnished for each vessel inlet and outlet.Each pressure gauge shall be furnished with manual
isolating valves.

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development,Monroe,NC
Quantity: 8 units(4 per skid)
7. UV system:
Germicidal ultraviolet lamps producing ultraviolet wavelength at 254 nm.
The water enters the stainless steel disinfection chamber and flows into the space between
the quartz sleeves and chamber wall where suspended microscopic organisms are exposed to
intense shortwave germicidal ultraviolet rays.
Translucent sight port and front panel indicator lights(not shown)provide positive indication
of germicidal lamp operation.
Manual wiper system facilitates routine cleaning of quartz sleeves without disassembly or
shutdown of disinfection systems.
Model Megatron M50
Nominal lamp length 1554mm
Power consumption 75 watts
Ultraviolet output 33 watts
Inlet/Outlet 2"NPT
Number of lamps 4
Power 120V
Dimensions 105 7/8" x 18 1/8" x 15 1/8"
Quantity: 2

Eagle Engineering for Carolina Development Services LLC
Cody Glass Residential Development, Monroe, NC
APPENDIX 1 - SUBMITTAL DRAWINGS
APPENDIX 2 - CUT SHEETS

',I WADE H.GRIFFIN
'' BK.6624-665
DONNIE B 8 BETTY A JORDAN NOW OR FORMERLY
DB 3057,PG 079 TAX PIN:09247012A
NOW OR FORMERLY ZONED:R-20
• TAX PIN:09-247-012B
ZONED:R-20
DONNIE B. BETTY JORDAN
D.1291,PG 122
\ N. OR FORMERLY
PININ:09-247-012
ZONED:R-20
li
wWrP
WIL/JAMANDREW& 1 -- -
MILDRED MCNEISH -• -- "
PLAT 6,PG 80 E I F 3
LOT - --
NOW OR FORMERLY
T f-9
ZONED:R 20
Description I September 3W,2022
Rook 010[0. N.IAZO _ -Toe Galene CCS-150 w/IFAS
Electrical PV.GUEZADA- Eagle Engineeringfor Carolina Development Services LLC
Drawing V.GOWU E� 9 eCodyGlass
pmt-Glass Residential Development NMlTP
WWTPLOCATION re'S WATER D9wo GENERAL EAYOUT Sleet No Sneer Sze I REV.NO.
SCALE 1:>'sg
`,.. 7 TREATMENT FOR REFERENCE OM, 01 Al 1 1
A Division of Galene TM m.pet ben pedisirl�..rre.y.m'ee�'mmt bLL/31k.�w....m�R.eem,we.mee
e e�wemm..Mumco.case amen e.ieewnmeee usew any car poem mm M eeap ewe

w-r 1r-r w-r
lea I 2T-11' 2T-11' I 1ea
16,000 gal 25,000GAL 25,0000AL 15,000 pal
�. TANK �' M� EQUALIZATION ,� ':• I , a Yj EOUALLWATION ll
s swoge
Iff 1.7 IT
" lj�
e e ,,,e Lc a. .1 .'�1'. , - I - - ---
•
4 „ ANOXIC TANK ANOXIC TANK y I I _ _ _ _ . ANDAG TANK •Ile.. I'..• A3OAG TAW y
e ti•i A1_u. WI Viil as u�. L.uA '
a- as u^ as C'
til a0 �0 0. ` 0` e,` p
r����111� tl u� III II�; 111111
!I11.41111 " I II ., . I; I '1 �l,
•rt
i■ui■ii' 1l 1!III�ii - 11
-
iiiinis"Ill , ; !viI
. rEl
1 'a
I
JCLARtRER -I• CLARFER'-, CIAIIFER - CLARIFIER
_._ -.
...".
, .
I, ,
..
_.., _. ,
..
CIARF101 c2.AIVfR cL.AIVER CLARFER
7 CLEAR WATER!- 'CLEARMT91 CLEAR WATER7 ,CLEAR MTER
41.
17 ■■
WO. 170
as
0 (1j...)
o ..0,
ANT-ZOO-ON ALi,SEO-No
Deavipaon I Septsmber 2nd,2022
sorbs-Procne -N.LAZO rue Galena CCS-150 a/IFAS
Swat P.GUEZADA
PLAN VIEW IRaainy V.GGNTAI FT Eagle Enyneedng for Carolina Development Services LLC
Cody Glees Reeideneel Development-EOVJTP
SCALE 1:5e D ng Sheet No slag see REV.NO.
��'^'''�� WATER GENERAL IAT REFIRENCE OUT
tD/TREATMENT Gatene
tlMaaraly g eeu...e....11:."'"tlL WAlln tnI I
A Division of Gate ems.oeaswa.....,.....e-a,w.`".aioe. •.w.a.wa.ar�r.aea.aowm+,....a.1e,..s.
a a.n.n.,y ra.el.d w.0ne rto,T.*oa uc.

k
I _� ",....I',O En.51.00E
B1 i
I
IMRE_; r�
e i;nian nl.•I STAND BY
, i . ' 'I ill
MIIII.—n,....11d
iu Ce=
I I
-- 111111
i
CLARIFIER- `.CLARIFIER
F ( —Cis____ III
I u = _ �s�� f� II I
lir`: R = M ■■■■ .i= it
i in !' rilii,
AMF,ZEO' O
_ INLrr_ =I�mz'rver+a i.t �- _ _ _ _ l ff
I_ i IIIIIII III III - Y ��� _-1 W.' •
. .—._ IEEE B£g ill 1g__ ._._._._. _._._F ---_ Rd ERNE SEW III — ,- dillAk
_._ _ _. - �_
ill WI EMI 4 : :I
==miil
r ---- ==mi il CLARIFIER CLARIFIER,
Y-,ts SA' WA' rS
I i
I i
PLAN VIEW
WALE 1:Y I
Description I September 2nd.2022
L. .1 Scab Process N.LAZO Trite -.—
—
Galene CCS-1 wilFAS
Electrical P.GUEZADn
Drawing V.GOWAI E� Ease Engineering for Carolina Do Developmeolopmo
nt Services LLC
Cody Gloss Residential Development-YUNrP
Ewan ROM =o»umm» RUM TAM •rOMr.ra eDEam»Tna MM.OIAareEia=w wens maw WATER GENERALLAYOUT Sheet No SI *See I IREV.NO.
ONLY
0375.1F05 nAR se.. ss000 o,=l idol=l ssw .Deal : u TREATMENT heserrses..`.. ...i.e.meF.„. caere.wee..,1T_sa
A Division of Galene
..4•euk.nal.N 0048E WNW n.....at

HAND RAIL HAND RAIL
1 r LARORM _leic H OP o:.11 _law PLATF00.M
y�
oYaaPw_71: - - - �- -
L
AMFZE0-100
ANO70C TANK 1 I
• CLARIFIER CLARIFIER
•
- s / _ -a WAVTEX MODULE 4 WAVTEX MODULE Z/I
/ \
.ri
u
G M
,n<uarA D 1c
r r , , , t f F iI I_'4,��
SECTION A
SCALE 1:n
HAND RAIL HAND RAIL
It _
o
I... _ PLATFORM LI'D PLATFORM VVVV
A.IlEOetlti AR REMtl-1 WC. A£Mtl-qy. MMO R S O
Nlibk
la ACCESS
STAIRWAY
.1116,
4 ..ec. 25,000GAL 5,000GAL -1116A wow.
FOUALIZATION " aP SLUDGE m
TANK i TANK \
to . Ni
II lik•
Ala w4 er say 'ilb&
i kl.c. 'ilL
K-1 t SECTION B
SCALE 1:to
1- 24 Z1 ,a1 0
iiiiI 1-0
SSI I 1 ,.,v ` I v+ei
_ 1EMI11111111111111P_ - I '1L���
P 41_�_ § _1e e!I U 0-� •F. WEIR V NOTCH DETAIL
M1 `1R.______ e .�k-7 SCALE 1:10
JAI
EEMEMEMI
•' '�n ' EZADA Description I September bM,ton
Miiiiiiiisale Prvutl N.LAZOElect rnr Galene CCS-150 w'IFAS
_ Doming
V.COW.F
_ vna v-v a,v1 Dravnrq V.GON7Ai F2 Eagle Engineering for Carolina Development nt Services LLC
o,v v iv I I � a Cody Glass Residential Development-WNVTR
IS: Dravon0 GENERAL LAYOUT Sheet No Shut Sim REV.NO.
°" SECTION 1 SECTION2 /� WATER FOR .OM, C1.1 A,
PLAN VIEW v P SCALE 1:u SCALE 1:N PLATE \.,,,/TREATMENT1,� 1
SPLITTER BOX DETAIL • No, 7 �'"7,:r" tl� T
SCALE 1:H A Division of Galene e.leW .°..—mr.a• ea.a�...MwIkIn�e:.a..
SCALE 1:15 r.w.=*No Wu;copy,rmn.m....m r,..v=u,.we�a�Mrrwn
- .�Y.AvR Hn++..M ou[r.[.'a'Tn.en.n uc.

E4, 4-MP NM Of Ss D11
I ,ar 1.- zr., I I
L
r '
Ir r - I r
. I LL-L 1 -I:µ.z °"
9 9 9
ea.,
SAAC CEO V PLATFORM - PLATFORM I APE e.
I 1
DNA NN m ss - 1-.m PIK M.ss. 1-MAA w Ss 1 f-MAAeM•• a--M.APE ae SS ' N
M4F
-v r v -AL:,
C oF.uer LFF.Ea ooaue. 3] PRISM osruel I �000GAL u,,,.. / C
AP,- .— —.—.—{_— 5,000GAL DECANTER.1. I
�' , a G • TANK G 41
SLUDGE M,) : 1 I • S
I; TANK - _ __
l: Tim iI5 _ I R. l k
��Q� j I1
Ii rl am ': i! il'ela <
ii 1 I„Ill IAM4WM ti
I I €
- 5 - t 7 7
PLAN VIEW • •
- •
-
SCALE 1:30 PM-li., -al. •. -:�.
1° o °I O 'll'0 10
AEI+ AB+
CLAR-2 CLAR-1 STAND BY EQ a SLUDGE
Dssenpeon I September 2M,2022
scarp Process -N.IPZO Tine Galene CCS-150 w/IFAS
Draing P.GOWNPEZADA Eagle En neenn Development Drawing V.GOWN F2 Bi 0 for sardine Devela Tit Services LLC
Cody Glass Residential Development-NWTP
WATER DowerQ GENERAL LAYOPT Sleet No Sheet S. REV.NO.
• J TREATMENT RIP Wine.MIT
0l "b. . 1 ,1111
T.dm Nis tral keen p.1111.0,041 and is Me sae pope*A Division of Galene

NANO RAIL NANO RAIL
•
C.
j PLATFORM PLATFORM •O
•
•
ACCESS
NNY
STAIR
• 16,1000AL PL a,000ML V
6/ SLUDGE EQUALIZATION
TANK TANK
AV
A
Ar
P.r ER MA I
SECTION C T 1—»4w
MALE is a
NANO RAIL HAND RAL INTO RAL
•
•
a.aepQAL
IL
�UOOE CLEARTANK WATER iILk1
TANK
Derria
SECTION D SECTION E SECTION G
KIWI I:a SOALR t:a SCALE 0:a
Descriptor 1 September bW.75771
rye-Promo N.LAZO ,Title Fledrn P.ODEIAD A Gllene CCS-150 AIFAS
Drawing V.GOWAIFZ Eagle Engineering for Carolina Development
to t Services LLC
Cody Gass Residential Development-VJJJTP WATER Df5N""0 Sheet No Sw.1 See REV.NO.
GE REFERINCE NERAL LAYOUT I
'TREATMENT ;� _ .,.�.•.•. : A' 1
ilt
A Division of Galena �.a.•..a•r.,w.,w'•r a Wafer
v..
R.....s .•.Pmw*MO M GREBE w.arTAW.uA

tl *k TE7 'O.I
EO.SLUDGE
NI
Ma1
n:1 N MIMIO.
STAND BY
r[J:, [):l.11.MiI O
AB•CLAR-1
n
1r j=rifoAmMi010
an—. +CLAR4 I 1 H41 G4
i i i i
�`Jrt`E 1 7- fi 1 It `u° l ``
I i I
I d I() II
:1' CLAIR%� CLARIFIER /%
a I trji ¢
ANOXIC TANK
I V 1 t.i a1
I I y{ ttI I
I f iI t I
ti I � ___. �. i .r. Ii .r I
!S s ill ��...tl 1 1� 1 .�', L •nf t., . ,
z=
Ec - -- . - - 1 -- t
- , in&owl
II
1 f aIl •f ..1.e•r . 1.1
Is I klt46, 1-. ANOXIC TANK __ __ Fes° I .—.—.— ; a f
L 11 I
_- ' CLARIFIER CLARIFR'. • I
• ° I I I i
I y l _ I l;
A I A . i A I I I / De.cnpSen I September ad.mzz
s;:. IS,1 +r-„ I rs I swb Ec ca kl P.oDF JAOA Tree Galene CCS-150 w/IFAS
4 H4 G4 Dt.wlnp V.GONZALEZ Eagle Err neennp for Caroline Development Services LLC
Cody Glass ReaidmEal Development-WWIP
��+ �IENE rAY� Sheet IN ...see I REV.NO.
PLANSCALE 1:SI VIEW CV TREATMENT ,N........e..10+CE011• i l,1
A Division of Galene +.^....+•^ae-e.,............e...r.
.e....wY..M rwBE V..,T.n.t MC

HAND RAIL HAND RAIL
PLATFORM- _
Ti
I• I I I
II
--- ) r r aL_ _ —I ._ . I I I 1_PI— r '. ;
• • q _ 1 1IIuI
FD Ff LEVEL 7 F1CR CAPoFlERAd -6 to--- } }
ii-•
• Y4 WAVTEX MODULE . WAVTEX MODULE
zz,
II
ANOXIC TANK • • I
A � ri
SECTION F SECTION H
SCALE 1:■ SCALE 1:II
HAND PAIL HAND RAIL
rni- pUTPOyRM (1 �1
Al 1 ,19Egr I J y .�=. :II in+l I1
# ' - — — — — —�' — — — �� 11 — — — rl E_" — —
i
i
e' ri
R e.
_ WAVIEXNOCLE e . ANOXIC TANK ANOXICTANK
IIIY—
ION
GLOeEV W er--G OII--C vORE VALVE SOMA won
r rC o .
e
f
SECTION I SECTION J
SCALE 1:SS SCALE 1:U
D.ecdptiDn I Septemberaw,nm
Sc.'.IEIEl P.LAZGuE Teel.ADA Gaiene CCS-150 vVIFAS
dewing V.GONZ
OrswinS V.GONZALEZ Eagle Endneedny for Carotins Development Services LLC
Cody Glass Residential Development-WWTP
WATER Drawlq GENERALENLAYOUT Sleet No She.See REV.NO.
CTREATMENT 06
Al 11 11 1 1
A Division of Galena M ~lanow mei`•nrN c.N.I wean..I"'"tlrer.°".��e e�Treeenm..mode nve
e:s.a.rrws.Ar.e weenie,,wr`. .smo•%solo,wyeen P.w-aerew,•.,wren

13-6.5"
A
48 INCH TANK 48 INCH TANK
m r1 48 INCH TANK 48 INCH TANK poi7
Y ma
AIIIIMIIII
elI V 1
i At R�al� �Iw!a:: ��I
I 0
in
im �.o,�E] 10 _-i PUMPS 1MI:;•l1.11l I e e
. UV SYSTEM II II
0 Ill
lb I" ' 11-2"
J FRONT VIEW
FILTRATION SYSTEM DETAIL (PLANT VIEW) SCALE 70
SCALE 1:15
48 INCH TANK
INLET 03" •iIIII■'J ,III.
BACKWASH ' i''
OUT 04"
1111
BACKWASH 11 I.it
IN 04' ■
OUTLET 04" ;�Illl■amll■
FROM CLEAR_ MI y j I■' IIIIIIII
WATER TANK (�iml li
I I
Deacripbon I September hnQ 2022
SECTION "A" sale Process N.LAZo Title Galene CCS 150 w IFAS
Electrical P. ofgADA
SCALE 1:15 Dnwina V.GON7ai F7 EadeCody Glom Ree Engineering tidential Development-Carolina Development Services LLC
�� WATER [Pawing Sleet No sham am. REV.NO.
w'''''acu°°UT � I
'( J TREATMENT ,ha.•.e�....r.•..r.m....N.•.e•.�+ow "t t LE I I I
A Division of Galene •••w..•.•e.+..a.�.•..•,••••....

..- Efficient.Elimination of Floating.Solid Matters in Sewage
Pi .' �1 scan resistance
�'' Tsurumi bar screens are pre-treatment equipment that enables smooth water treatment in post-processes.
") Front Screen Type Applications
KE/KS/K►�j •Primary treatment of general industrial wastewater
1 re of Screen(Example of Front Screen) Rear Screen Type •Treatment of wastewater from food processing factories
1 KM/KMA/KMS •Treatment of kitchen wastewater from hotels,factories.hospitals,etc.
When installed in a ditch,the screen "
Motor •Combined sewage treatment tanks(Johkasou/septic tank)
catches solid matters contained in •Village wastewater treatment facilities
the sewage and allows water to pass. � �� Residue
The solid matters caught by the screen Screen \ '� •rate Collecting •Small-scale sewage treatment facilities
is raised with rakes,and collected I, 1 ",*Co Basket
in the residue collecting basket. Y•r
���
L:y
Rake 7. L Lt.i
i i. •LLLL
.
��.10 � _1.7. LL -i Application in situations
r r( . / ' "" with water level fluctuations
C
• •The bar screen is compact and lightweight,making it easy to install in
, ___ ,,, / //,, ,4* ,
'�-'� U-shaped ditches,etc.With sealing rubber attached to the sides of the
y, s,. frame,the screen snugly fits any width of waterway.
s .,".r 4-c.
" •During operation,the rakes always move through the slits of the screen. E'x
- preventing the screen from being clogged with solids matter. 4y�1 , �./ The wetted metal parts are made of 304 stainless steel which exhibits
/ //
excellent durability even in harsh environments e.g.,outdoors,;,^v continuously operated day and night,etc•Maintenance is easy.Initial and running costs are low rat, •The KS-series screens are equipped with an eccentric roll mechanism a
" ,
that prevents retraction and clogging of the screen bar front edge caused
Sealing Rubber by residue. KE
�? •The KW-series screens incorporate a safety device that can stop the gear
motor immediately in the event of abnormal operation.
`' _. 0 0 /�Major Parts'Materials
lil, *r Screen Bars 304 Stainless Steel
t./ `:,ih 7 w°^..::4z Rake 304 Stainless Steel
Chain and Sprocket 304 Stainless Steel
�� �� Frame 304 Stainless Steel' Application in situations
°.'y'.- 'Frame material of KS-2002 is 430•tainlesc steal. Application
without water level fluctuations
Concrete Block for Fixing the Screen •The bar screen is compact and lightweight,making it easy to install in74'
U-shaped ditches,etc.With sealing rubber attached to the sides of the
Used for combined sewage treatment tank(Johkasou/septic tank)and small-scale sewage treatment facilities,etc. frame,the screen snugly fits any width of waterway. I,
• •Since the rake chain(dry chain)is not in contact with liquid,dirt and ,
n - - t"` . residue will not adhere to it.Therefore,it needs almost no maintenance. of „,,
NV
,�, . I " „'f •The wetted metal parts are made of 304 stainless steel,which exhibits "r+c
r` t. excellent durability even in harsh environments,e.g,outdoors, "'
nuously
erated day
N'I
,,/ p$y •r r !•••M`~ The barscreen can be directly night,ailed in a U-shaped
1
lif
—aa „uk
` ,' • ` "mt ditch to eliminate
\ -- I k •dirt from the bottom of the ditch.It provides excellent treatment effect,and KM
�,�`���'\ ...rrvrrvvvAAdl■MMk " ( -I-
. is advantageous both in terms of initial cost and running costs.
ll
�t
t
•, a
UAlI .Yr71➢„ +e• ?4 a� TSURUMI PUMP I 02

•
D
C $S J ? d O 7 = d d fD S
c '0 7c F 7c 7e 7e 7c 7c 7c 7c 7c 7c O c
,3 H fn N ; N . ' N N 1� N N.N m In m N N N fp a fit
' e .7'41" 1 N P $ $ PifiP ' N8i88o1888S n o^ < ? � x
a i (7 a m J a J tO 0 J r N < < N r ; N 0 N O N `
...‘:
Q d fD 7 d = N C�C
4 O N S CD y G
b x 7 y 4 C N
o 0 0 R N $ o 0 0 0 0 0 0 0 o f R m 5' m m N
R i 3 N
Z�Q@ _ N n. p� 0 10 to• N
5 N d O 1 IO ci O� O� O N 10 .Ni V N YNi J W tN0 OI I I I - J 'i (D W
•33-I J N C m m t0 A n
3 p J N N m N• , m
S s V 3 3 n. O pp P t�0 N 001 In t0 N ONE O O� �O OI ONI ;T �/i 3 N
4 1pY2. NSj 6f 3 F3 5 c° `°
Aag y 3 = o d
U
to c 3 3 1 m $ o J °. IN.1 O. N A tail m -. T m 2 g V 3 to J 3 I ,. .� c• m m 3 *_
= 3 d
N Wm � N t � I a
tr tv m a W O O m m "! 0 0 N O y
� t o
• a � a A t/)
oos : tiEti � gti � oo § goo � Uo dSt2tpp y N 'I
c m m n y 1 M
c ip < m
1 LI uo o f 8 8 8 8 8 0^ 0^ o^ o o tg § 8 o 8 8 8 II F m E ( a 2
o
8S8 R 88g888888888 § 88888 Js *
p� to g
A A tT O. Ol O 4 0 0 4 4 t., ti tan $ $ $ o 0 0 it
(M5 c o f
C
m 3 m a %
> CO N d -
RI N J a 1st Woto � VJmN 2 N J T. t u N O7 N V 13 al a F. -.
d fD
�
tD
a
o
'2 x x x E fx x x x x x x x x x x m m m ; u La An.,
n m1:.1 m m I
9 $ m 5 J tslm j g ; 1 1 1 g 8 g 1 1 �m� - o g E E — i. S I E
" A N A 14+ N s I
d ^m> o
R mN t�f� N
t0 iO us
iO Iv
cc co I CO to m to co co t0 CO > 5^ ..
m N
O F
r V V ,
Q A N IV O O O us N N N N NJ ,p E
3 m m m m m m a rn m to J e a V.' T. A a 35 .-• < <
u
N N O N N A A A a A A A 1 \.
N N N m a m N o 0 o m m m m mA f1 r \`•
O O O /- \
m a m to to to a s A a a a o u u W W o 0 1?; I _
O O O O O O O 0 O O O o 0 0 0
1 '4„
memo
N A w El ""2m N 41
-� . to -. tali tO -,I t El `12 alc t0 O O O O o 0 0 o O m I'
a
. 7C 7C "' _ N N N
11111
N A b 8 N tO N N r2O 8 0 0 0 0 0 tml� N O T a= ® ,Ii _øF
I 1 I II x x 7C mow
�— o
N in, o I't N m tOn "t $ o o m °1 0 o G)fa
f f E �i ssmrlRI
N m w N O ao O o 0 0 0 o a m �o f t f I I
"''a . .IijIN' 1114
O x X
0 o AA a o as a o a o 0 0 0 T.
o o 0 0 — V. 7C m F E F f E <
1 FEE
F � _
Y N m A 2. 0 J N m '4 r Yb O 0 1
A a a a o 0 0 3 S' I!twf'
3
\ O
I
r P�
IIMMII
�

APR.00 BE-BLPI
TSURUMI PUMP IES
SEWAIGE&WASTEWATER PUMPS SPECIFICATIONS
■ FEATURES
1. Semi-open, Single vane,(1 HP-5 (2Hp.and above.), and
Hp.),impellers with field adjustable further protected by an
/replaceable shear plate and, exclusionary oil seal(s),
Enclosed Multi-vane,(71/2- provides for the most durable
300 Hp.), impellers,with field seal design available.
adjustable/replaceable wear
plate provides for high wear 5. Double shielded, permanently i, r
l .
•
resistance and enhanced solids lubricated, high temperature ti,
handling capability. C3 ball bearings rated for a / °
2. Highly efficient, continuous duty B 10 life of 60,000 hours }
provide for extended
air filled, copper wound motor operational life.
with class E, B, F insulation •
minimizes the cost of operation.
PPL iCATIONIS
3. Built in thermal protection
prevents motor failure due to 1.Commercial, Industrial IMPELLER
overloading,accidental run-dry sewage,wastewater,or r
and single phasing in three effluent transfer.
phase units.
2. Decorative fountains andmoo
-
4. Double inside mechanical seals aquiculture .
with silicon carbide faces, running SHEAR PLATE
in an oil filled chamber, equipped 3. Raw water supply from rivers (2"-4") Q
with an oil lifter,- or lakes. Li
EQUIPPED
II SPECIFICATIONS Q STAIVOARD ■ OPTIONS
Discharge Size 2"-32" (50-800 mm) Dry-Pit
Horsepower Range 1 Hp.-300 Hp. (.75 kW-220 kW)
Performance Range, Capacity 25-33,000 G.P.M. (.09-125 m3/min)
Head 6.6 Ft.-278 Ft. (2-84.7m)
Maximum water temperature 104°F. (40°C.)
Materials of Construction
Casing Cast Iron,ASTM 48 Class 35 304/316 SS(BQ-Series)
Impeller Cast Iron,ASTM 48 Class 35 304/316 SS(BQ-Series)
Shaft 403,420 Stainless Steel 304/316 SS(BQ-Series)
Motor Frame Cast Iron, ASTM 48 Class 30 304/316 SS(BQ-Series)
Fasteners 304 Stainless Steel 304/316 SS (BQ-Series)
Mechanical Seal
Upper Seal Silicon Carbide/Silicon Carbide
Lower Seal - Silicon Carbide/Silicon Carbide
Elastomers NBR(Nitril Buna Rubber) Viton(BQ-Series)
Impeller Type Semi-open, Enclosed,solids handling.
Solids Handling Capability up to 6"non compressible
Bearings Pre-lubricated, Double Shielded
Motor Nomenclature
Type,Speed, Hz. I Air Filled, 3600, 1800,1200, 900, 600, Nema 3R inverter available for
514, &400 Rpm,60 Hz. 230 V.,1 Ph.operation from 2-5
Voltage, Phase 115 or 230 1 Phase(1 Hp) Hp.
208/230 or 460 V., 3 Phase
Insulation Class E, B, F
Accessories Submersible Power Cable 32'(10 m) Length as required.
TO/TOS Slide Rail System
Operational Mode Manual Automatic or Alternating
(1-5 Hp.)

Oct 00
60-PC-B-01
B-SERIES PERFORMANCE
AO TSURUMI PUMP SEWAGE&WASTEWATER PUMPS CURVE
MODEL BORE HP KW RPM SOLIDS DIA LIQUID SG. VISCOSITY TEMP.
(TOS)50B2.75HS 2"/50mm 1 0.75 3600 0.79"/20mm Water 1.0 1.81 CST 60°F
PUMP TYPE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
Sewage&Wastewater Pump Single 115/230 10.8/5.7 60 Capacitor-Start E
CURVE No. DATE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
EFF. TOTAL HD. I REMARKS:
% M. Ft
55 .
16-
100- 50
14-
90• 45
80- 12 - 40
Ty Q
70- 35 '
10- - - -- - - — - -
60- . 30 -
8-
50• 25 - "
40- 6- 20 _ ,I
30 - 15
4-
20- . 10 - — " — -
2-
10 - 5
—0 -0-0
US GPM 0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90
CAPACITY
M'/min. 0.00 0.05 0.10 0.15 0.20 0.25 0.30
SHAFT POWER
KW BHP -
I R:::
095 SNPF POWE 090- .
. 0.85 -
—0.60 --080 iii I iii

Oct 00 60-PC-B-04 I
L-7 TSURUMI PUMP E-SERIES PERFORMANCE
SEWA":E&WASTEWATER PUMPS CURVE
MODEL BORE HP KW RPM SOLIDS DIA LIQUID SG. VISCOSITY TEMP.
(TOS)801321.5 3"/80mm 2 1.5 3485 1.38'735mm Water 1.0 1.81 CST 60°F
PUMP TYPE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
Sewage&Wastewater Pump 3 208/230/460 6.3/6.3/3.1 60 Direct On Line E
CURVE No. DATE PHASE VOLTAGE AMPERAGE HZ STARTING METHOD INS.CLASS
EFF. TOTAL HD. I REMARKS:
M. Ft.
55
16-
100 50
90 14- 45
80 12- 40 i
ry
70 35
10-
60 . 30
8-
50 25
40 6- 20
30 15
4-
20 10
2
10 5
—0 0-0 ,
US GPM 0 25 50 75 100 125 150 175 200 225 250
CAPACITY r . . . . .
M'/min. 0.0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9
SHAFT POWER
KW BHP
1.50 - 2.0 .
1.45 -
9
1.40 SHAFT POWER
1.35 - 1.8
1.30 -
1.7
1.25 -
1.20 - 1.6
1.15 - }
— — 1.5 i i i I

24/9/2020
Scan.Order.Done. PUMPS
Details on page Al. Float Switches
Float
Switches tiltleGLINT. V --
•Normally closed.pump up •Normally open:pump down \
for filling applications for dewatering applicationsfill t
tether Float Pumping Float Max. No.
Length Switch Wire flange Switch Mould Ilem 3VA90 No. t
VM
Voltalcalgye Amps Mtn.-Max.Cord length Gauge Min./Max. Contact Form Temp Brand No. 1 APP4 e e
`1, it ,Mil lint i•aly Open i4 r11 r t, 10A1en
11..VA( 'lA I.On 16 ilnC No,molly Otal 14'I"! I.� 104170 4
14 - 0011 16 I to 6 Normally Open 14111F i't,r 10A171q1111.01
4A - 1911 IC tl 75 to6u Nrima14 Open t255F U,;,.a,n 3VA90
DNa• ohnyn •
Oh flit 111 5 Nrimlly Open T ant•i-,,t IP353
0A - tl ft 18 15 Not molly riper 120'1 Ir .r1 48L50
aA -- 15 ft 14 10 Normally Open 110'i :I r C mn 3*Y20
T,rMs
ar,„ 3A 3'to 13' 56Ott lb '10 2A Normally Openi - 110"I tinier 6PNV7
5A 1 m Is' 20 h 11 7lit 28 Normally ripen 1.105f baytof 104174 -
nA n to t: 10 r la 7In 28 Ottrnally 1Aos 1 1405r ---Dayton 38774 t
hA 3 t.i7' 15f le 7 in 25 Normally Jos.d 1-10q Daps 38775 yF
3A toll' in l lb 7 to 28 Norntally(lobed 1401 Baylor 38178IIIP
3A 3`ui 1A In i 16 710 26 Nonitally Open 40°F D3ytot 6PNU9
71 1 tit iO' la if; "Ito 28 Normally Open 140`F`-"- Uaytor 6P141/6 No. No. No.
i.,,,Ai. ,A A h i8' f 16 710 2A Murmally Opel) 14(Pr _. Dayton ONUS eaJV93 55E60 45JZne
lA o 1.iA' 101 1r lot 28 NnlmalpY Closed 1404---__Daly to 38Y80
:IA 1 to Ile 20 r 16 7 to 2A Nornudly Open 140.'F' ,TNaylor 6PNU7 Auto control pumps in sump/sewage and nonpotable
101 16 1to2e Nomullyr)peu t40T (Saylor 6PNV1
";A to 18- 50 h. Id l0$8 Nµmlally Open fanTf—,-:begun 6PNU9 water applications.All except diaphragm switches
ra In' 20 h II i it 23 Normally Open 1401. Tioyt01 6PNV3 include an adjustable mounting strap.
'A -I 18' GU 5 14 to 28 Nomad,'Open id Daylor 6PNV4
7 I III 15I le, J to 23 Normally Oran _Dayi 6PNU6 Nrle.Mae only with hgwna menonphle watt wit141 nest I ox.
'A s, IN' Io ll ii 7 m 23 Normally'Closed 1, Daytoi 38785
PoN 3A `t 18. 19 ii I� to 28 Nulnially Diet T Daytu, 6PNU8 Vertical—Weal for use In limited space.Na 3VA90 can
3A 9 to 18' 30 tl IC 7to28 Won*Open 44 • . -Diyloi 6PNV2 be wired for 230V
5A 3 to 18' 20 n 11 7 to 2P Normally Open 1401" _ -Dayton 6PNV0
Tether,Twit Nor.5d i t. n' 'torI II 7 to 28 Norniol y Open 1.i0°F.�- pay1m 6PNV5 Diaphragm—Water-pressure activated.Control pumps
li v I;,A 3 to IN' :;Lei I 12hoCO Nor pe @D'F Daytor 1E4175 up dz 10' HPal120VAC
A,, t,/ ti in' 'Intl i 12 inLO Nor!,.. 141PF-- - Devil, 10A176
Tether,Mob Ta,a t,I
aafun
!I .At ayTether,Daytona Normal Closed—Switches turn
- n I'i ft 'u,7:1 Nmmelly Opau 271'F - Oa t0A173 � Normally
.,,1to17 %i h 16 .to?I Nntmady open 186°F Days° 38781 on(close)when the float drops 45'below horizontal.
Tether,Che lcatAasstart
, 'aA to 15 1511 16 ;In 31 Normally Open 14111 Dayton 3BYe2 signaling a low level,and turn off(open)when the float
1JC to 18' 301i- It 1 to 31 Normally Open 140°r wytpt 38783 rises 45'above horizontal.
to-At' t'A 3 w 1111 15 II i i Ic 34 Normally Open 140°F Daylut 3BY94
ts.Tee Control Panel/Mat gate, Tether,Chemical-Resistant—Mechanical blue
,A ,i 3 to 18 'o o 16 - Normally Open 140'F Playiot 104172
n: In 1 e' ,ii II la • NormuBy open 1.40'F 0a4101 3BY79 switches have ABS float and 115V or 220V series plugs.
Deal Mk+areed r _. Nine'Use nun waft cnendellle cnmpahlie w1111 s'wdldl construction
14 Adjustable Normally Olen-"- t-pr Dayton IAPPd
e I",I 111 A 1lmsia5ir Normally of n 101°r PRCil P 9 scrim 380718
SR PunaMast9f WIN Mxls Tether Control Panel/Pilot Duty—No.10A1 72 is
ill t to 24 11t ft 16 7 to 36 Not molly(Nursed 140°r SSJFnhnmi;a, 45J246 mechanically-activated with tether clamp.No.3BY79 is
34 I `to 24 ft C /in 36 Not Molly Open 140'F SJr-ohm ins 45JI09
t? I,rl/n A 3 'to 24 20 a tO /ei116 Nototally.ten I lilT Sir Q61311,46 454210 mercury-activated with preset tether length.
34 1i to 24 2;ft it 7 to36 Norn,aally Closed ImWt- et CO mot,,a 45J742
5
z 1 to 21 11 a 161 in 36 Nu, Open tao"F-- ,t on, i, 4oJI11 SJE PumpMastere—Wide-angle pump switches are
3ASi' toga 15 it- 16 7 is 36 Not Closet) 1401"-sA r ni i I, 45JZ24 mechanidally-activated and can automatically control
34 to;1 I_;h 16 7 to 36 Normally Open 1.401--" 511-rittantno 45JY91
9t 'ta 7.1 11 li lb 'to 36 Normal! clwan till 5.4 Into I-I 45JI25 pumps lip to'4•HP all20 VAC and 1 HP at 230 VAC.
12ovN; 31 1 to 21' 15 n IF to 3r No11nzll Open 14O'F r S .w I.. 45JY92
iA I '1n24 20h 16 7b1136 NoimellyCltsA 1401- S11-Rol. -n, 453226 SJE PumpMasteroPlus—These rnechanlcally-acil-
94 n a I1 2,5 It 16 7to 36 Not molly Open 1a0°F-- 6a6ttmom=n 45JY93 voted.pump SWdcheS can automatically control pumps
1' to 2I. r t, IC 7 tole SIMmall Closed 140'F $JFRiimmtias 45J221
13 i,-Ir•2i 20 r I6 7 to 36 Normally Open 140"F SJF-nbpmlio, 45J794 up to 41 HP aft 20 VAC and 2 HP at 230 VAC
STE PantPMer ,'Poe Wide Angle
15A 9t to 21 10 I I i 7 to 36,' %Smelly Closed WIt"F ` SJC lI u,fws 45J244 SJE AmpMaster4'Plus—Mechanically-activated
3 to 24 151 14 7 ei 36 Normal!-Closed 140°F—SJC-Rhos Itus 45JZ45
B" I.,24 1st ++ h106 Namely Open WO°T '-3,IFnhomh¢ 45J213 Pump switches roan automatically control pumps up in
t2W23lVAC` 1 ,2.1 20 t 14 7.o 36 Nonnal!y Closed uo'C B.IF-Rht,rohi.. 451246 1 I/>HP at 125 VAC and 3 HP at 250 VAC.
_ �3' ii 74 70 f 14 710 36 Not
yy r I e t 140.7�—SJF-Rod mnu> 45JZ14
4/7 to 24' 301 14 7 to to 33lf Normally Closed
110 `A'1C-Nth b,c 45J147 Control Switches,SJE SignalMastesi'—These
se
Y P SJC'Rhoolhms 45JI15
T Ni* -24`' 01 14 r to 36 Normally Open 140"F SIFRnn t us 45JY95 mechanically-activated,control switches are designed
12UVAC 15 tl 1 t m i6 N I"nalttyyiyt�iN,Iseed ui•f' S it-tNii otI i us esaisu to activate pump control panels and alarms.Normally
-i - 14 io 3r Normally 01 140'6 Sit.RIto n os. 45J497 open thigh level)switches turn on(close)when the that
fe 4, — IJ /i9 36 Normally Open t4n°r Sir.Oh,moos 45JY98 tips slightly above horizontal signaling a high level,turn
736VAe i 'AP to f4' 30 n m 3i Normally rile t-SOF SJF-Rhnmhuc 45JZo7 g g g
e4E AalpfasAs•►Ma Tarts oft(open)when float drops below horizontal.Normally
20A 'to d^' v 7 to 24 No malty f p r 120'F SJF Mannino SAEPO closed pow level)switches turn on(close)when the
12Si25UVAc 20A J to 21 Nr mall✓ 1 120'F S.ir vi .bus 54EP1
n
.7aA 9 to 2�1 Nt +oily nj 110°i S1F-Fitmin l! 54EP2 float tips slightly below horizontal signaling a low level.
A 1 9 ro 21 NI m Maley nl,E i79' S,IF-Rbf nhu, 5AEP3 turn oft(open)when float drops above horizontal.
Ziirili 1 {jE$ignalM sit No r.Angle
1 ndlly nt e 1401 itiOntioot., 45JZ76 Control differential is 1'r'above or below horizontal.
_ al) nn,Ml I lo°r sir-Rico D u 45Ju8
128,25ov- `"+" ""'""" oro,,Y tlmet 19 , B iF.04/ Nt,. 45J719 SJE PtanpMastees WPS,Potable Water—
s Nr nail l e 14041 s t imnbus 45JI ,a Mechanically-activated control switch can control
a +_"""" 7 n 11!" - Non Ianj a{en 17n"i Jt lmajmms a6Jcn
-3A 3. ,l h _-- t8 - %iotallf Firs J 140'r `SJF-Rhonil ins 45,1753 pumps up to 1t'HP at 120 VAC and 1 HP at 230 VAC.or
SA .3 3n 5 1B Normally oI i4o'F sir-ro 6w 45iz22 control applications as tow as 120 VAC.100 niA.Model
t n A tdonnally Olin 14, , �n 10II(la 45J223
WET, �t#'WPS P ealeWa.NWIO*gte _ can be wired to work in either pump down(normally
120 Su knniBY 1)p I' i-n' 5ll'I:hon n s 5361(41 open)or pump up(normal) closed)applications(single
pev t3A 3 to 24' tstt t6 zlo 3b ryermallyCloned.. _ I P f y PP 9
item pole,double throw).Switch can be used in food grade
aeon ton TJor Ufa Wxh Brand No. and potable water applications
7, q.�i' i area. r . SJE-Rh ,I 45JI57 ..
RHe Aran ies Ta ref` T^ (Ni, 454756 Switch Accessories--No 45JZ57 can mountupto
�6Te m .14.:(in._ e. _ ,__ ,vrtN i t",ala 4111 45.15E 4 float cables No.45JZ5N seals oN cables coming into
e .D ._ BA. A Rhi,t i_ 45JI61 an enclosure.Nos 45JZ59 to 45JZ61 can mount a Goat
aTae lamp` litQa r e phomttos 45260
'Carr_Tq efamp 1_ll)' 'grA raga, ii/ra a •Ahoeibnio 45JZ59 cable to PVC pipe
1-800-GFAINGER(472-0643) WMRMY:Use only win nonflammable unu;ds compaunk with 2629
wrap,nnlwnen(matellals and In nbnitammabie/noneoplosrve almespfwles
1/1

SPEW) TRUE UNION 2000 STANDARD BALL VALVES
Features — PVC, CPVC
Economical, low profile quarter-turn shutoff valve is
excellent for general purpose and many O.E.M applica-
tions. PVC and CPVC valves are available in IPS sizes
1/2"through 4"with socket,regular thread,SR threaded
(Special Reinforced), flanged or spigot end connectors.
• Chemical & Corrosion Resistant PVC or CPVC
Construction
• Interchangeable with all True Union 2000 Valves,
Mates with Union 2000 Pipe Unions
• High Impact Polypropylene Handle
• Schedule 80 Full-Bore Design
• Strong, Buttress Thread Union Nuts
• Spears®Single 0-ring Safe-T-Shear®Stem Design
• Spears®Safe-T Blocked®Seal Carrier
Sample Engineering Specification • Replaceable PTFE/HDPE Floating Seat Design
All thermoplastic ball valves shall be True Union 2000 • EPDM or FKM 0-rings
Standard type manufactured to ASTM F 1970 and constructed • Sizes 1/2" 2" pressure rated to 235 psi @ 73°F
from PVC Type 1, ASTM D 1784 Cell Classification 12454
or CPVC Type IV. ASTM D 1784 Cell Classification 23447. • Sizes 2-1/2" - 4" and all flanged pressure rated to
All 0-rings shall be EPDM or FKM. All valves shall have 150 psi @ 73°F
Safe-T-Shear" stem with 0-ring stem seal. All handles shall • EPDM valves NSF®Certified for Potable Water use
be polypropylene. All union nuts shall have Buttress threads. • Suitable for Vacuum Service
All seal carriers shall be Safe-T-Blocked". All EPDM valves • Assembled with Silicone-Free, Water Soluble
shall be certified by NSF® International for use with potable Lubricants
water. All 1/2"-2"valves shall be pressure rated to 235 psi,all • Manufactured to ASTM F 1970
2-1/2" -4" and all flanged valves to 150 psi for water @ 73°F,
as manufactured by Spears" Manufacturing Company.
Quick-View Valve Selection Chart Optional Accessories*
Valve 0-ring PVC Part Numbers Pressure •Retro-Fit End Connector
Size Material Socket Threaded SR Threaded Flanged Spigot Rating Sets for Valve Replacement
1/2 EPDM 3629-005 included 3621-005SR 3623-005 3627-005 •Split-Nut Repair Kits for
FKM 3639-005 included 3631-005SR 3633-005 3637-005
EPDM 3629-007 included 3621-007SR 3623-007 3627-007 235 psi Union Nut Replacement
3/4 Non-Shock
FKM 3639-007 included 3631-007SR 3633-007 3637-007 Water •Supplemental End
1 EPDM 3629-010 included 3621-010SR 3623-010 3627-010 @ 73°F Connectors
FKM 3639-010 included 3631-010SR 3633-010 3637-010 •Round Safety Handles
1-1/4 EPDM 3629-012 included 3621-012SR 3623-012 3627-012 (Flanged
FKM 3639-012 included 3631-012SR 3633-012 3637-012 150 psi •Stem Extension Kits
1 112 EPDM 3629-015 included 3621-015SR 3623-015 3627-015 No h ock) •Square Operator Nuts
War
FKM 3639-015 included 3631-015SR 3633-015 3637-015
EPDM 3629-020 included 3621-020SR 3623-020 3627-020 73°F •Multi Mount Valve/
2 FKM 3639-020 included 3631-020SR 3633-020 3637-020 Actuation Mounting Kits
2-1/2 EPDM 3622-025 3621-025 3621-025SR 3623-025 3627-025 •Mini-Mount Actuation
FKM 3632-025 3631-025 3631-025SR 3633-025 3637-025 150 psi Mounting Kits
3 EPDM 3622-030 3621-030 3621-030SR 3623-030 3627-030 Non-Shock +See"BALL VALVE ACCESSORIES"
FKM 3632-030 3631-030 3631-030SR 3633-030 3637-030 Water section for details of individual products.
EPDM 3622-040 3621-040 3621-040SR 3623-040 3627-040 @ 73°F
4 FKM 3632-040 3631-040 3631-040SR 3633-040 3637-040
1:For CPVC valve,add the letter"C"to the part number(e.g.,3629-005C,3621-005CSR)
NOT FOR DISTRIBUTION OF COMPRESSED AIR OR GASES
22

TRUE UNION 2000 STANDARD BALL VALVES ) rnSPEAt
4 E
© 0 0 0 0 0 0 0
0 m Replacement Parts
litig No. Component Qty. Material
0 1 Seal Carrier 1 PVC/CPVC
49Fillt2 Body 1 PVC/CPVC
D `I 3 Carrier 0-ring 1 EPDM/FKM
4 Stem Bearing 1.2 1 PP
5 Stem 1 PVC/CPVC
1 ! F
6 Handle 1 PP
A 7 Stem 0-ring 1 EPDM/FKM
8 Ball 1 PVC/CPVC
9 10 Seat 2 PTFE/HDPE
Union Nut 2 PVC/CPVC
-. B ► 11 End Connector 0-ring 2 EPDM/FKM
12 End Connector 2 PVC/CPVC
C - 1:0-Ring up to 2"
2:PTFE Thrust Bearing:2-1/2",3"&4"
G
Dimensions, Weights, Operating Torque & Cv Values
Nominal B1 C Approx.Wt Oper,2 Cv Values3
Size A D E F G (Lbs•) Torque
Soc/Thd Spigot Socket Thread Spigot PVC CPVC(in.ibs•) SoclThd/Spig Flanged
1/2 1-7/8 2-7/16 2-7/8 4-3/16 3-13/16 4-5/8 1-5/8 2-1/2 3-1/2 2-31/32 .33 .35 12 29 18
3/4 2-1/4 2-3/4 3-1/4 4-3/4 4-1/4 5-1/4 2 3 3-7/8 3-5/16 .51 .54 20 63 39
1 2-1/2 2-7/8 3-1/2 5-1/8 4-11/16 5-3/4 2-5/16 3-7/16 4-1/4 3-5/8 .71 .75 25 120 73
1-1/4 3-1/16 3-1/4 3-13/16 5-3/4 5-3/16 6-5/16 2-13/16 3-9/16 4-5/8 3-31/32 1.12 1.17 35 243 151
1-1/2 3-1/2 3-1/2 4 6-1/4 5-7/16 6-3/4 3-1/16 3-7/8 5 4-3/8 1.47 1.53 45 357 223
2 4-1/4 4-3/4 5-13/16 7-3/4 6-3/4 8-1/4 3-3/4 5 6 5-1/4 2.62 2.75 94 599 395
2-1/2 6-3/16 7 7-13/16 10-1/2 8-1/2 11-3/8 5-7/8 7-5/8 7 6 7.42 7.70 120 856 579
3 6-3/16 7 7-13/16 10-11/16 9-3/4 11-9/16 5-7/8 7-5/8 7-1/2 6-13/16 7.46 7.81 120 1416 974
4 7-5/8 7-1/2 8-1/4 12-1/16 10-1/4 12-3/4 6-3/4 6-3/4 9-1/16 7-1/2 12.35 12.48 336 2865 1952
1:Valve Lay Length
2:Torque required at valve maximum internal pressure rating,5ft/sec.Flow velocity;due to adjustment differences during installation,actual valves may vary.
3:Gallons per minute at 1 psi pressure drop.Valves calculated from laying length,based on derivative of Hazen-Williams equation with surface roughness factor of C=150.
Temperature Pressure Rating
System Operating 100 110 120 130 140 150 160 170 180 190 200 210
Temperature°F(SC) (38) (43) (49) (54) (60) (66) (71) (77) (82) (88) (93) (99)
PVC 235 211 150 75 50 -0- -0- -0- -0- -0- -0- -0-
1/2"-2" (1.62) (1.45) (1.03) (.52) (.34) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-)
Valve 235 219 170 145 130 110 90 80 70 60 50 -0-
Pressure CPVC (1.62) (1.51) (1.17) (1.00) (.90) (.76) (.62) (.55) (.48) (.41) (.34) (-0-)
Rating
psi PVC 150 135 110 75 50 -0- -0- -0- -0- -0- -0- -0-
(MPa) 2-112°-4" (1.03) (.93) (.76) (.52) (.34) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-) (-0-)
CPVC 150 140 130 120 110 100 90 80 70 60 50 -0-
(1.03) (.97) (.90) (.83) (.76) (.70) (.62) (.55) (.48) (.41) (.34) (-0-)
NOT FOR DISTRIBUTION OF COMPRESSED AIR OR GASES
23

■SPt�INS Utility Swing Check Valves
PVC White
Std Mstr Disc
Size Socket Thread SR Threaded Pk Pk Code
1/2 S1520-05 51520-05F 51520-05FSR 35 0 026
\ -,� 15.85 15.85 18.49
'a S1520-07 51520-07F 51520-07FSR
3l4 16.36 16.36 20.12 35 0 026
S1520-10 51520-10F 51520-10FSR
1 17.04 17.04 22,28 20 0 026
11/4 S1520-12 S1520-12F S1520-12FSR 12 0 026
17.70 17.70 26.11
S1520-15 51520-15F 51520-15FSR
N 1-1/2 12 0 026
18.76 18.76 33.12
2 S1520-20 S1520-20F S1520-20FSR 15 0 026
„ : ,
29.12 29.12 44.70
S1520-25 S1520-25F 51520-25FSR
2-112 48.44 48.44 64.02 5 0 026
S1520-30 51520-30F S1520-30FSR
of
3 53.83 53.83 95.47 4 0 026
S1520-40 51520-40F S1520-40FSR
4 76.21 76.21 119.36 2 0 026
S1520-60 51520-60F 51520-60FSR
• Engineered for Maximum Flow,Quick Response& 6 160.13 160.13 211.21 1 0 026
Positive Shutoff 8 s1520-80 -_ -_ 1 0 026
297.47
• Excellent for Pool&Spa,OEM and General Purpose
Applications PVC Clear
• Compact,Space-Saving Design Std Mstr Disc
• PVC White or Clear Sealed Unit _ Size Socket Thread SR Threaded Pk Pk Code
• All Plastic Construction-No Metal Parts 1/2 S1520005 51520005F S1520C05FSR 35 0 026
• Angled Seat and Weighted Flapper for Low-Pressure Seal - 21.55 21.55 24.18
• High Grade EPDM Seat 3/4 S1520007 S1520007F S1520C07FSR 35 0 026
21.97 21.97 25.76
• Suitable for Horizontal or Vertical Up-flow Installations 51520C10 S1520C1OF S1520C1OFSR
• Socket,Threaded,or SR Threaded End Connections 1 22.39 22.39 27.64 20 0 026
1 1/4 51520C12 51520C12F S1520C12FSR 12 0 026
1 General Installation Information: Swing check valves are 23.51 23.51 31.89
1-1/2 51520C15 51520C15F 51520C15FSR 12 0 026
designed for horizontal installations,but may be installed in up flow 25.55 25.55 39.93
only vertical position. Check valves MUST be installed with the 2 S1520C20 51520C20F S1520C2OFSR 15 0 026
valves FLOW arrow pointing in the direction of the flow. Do not 36.78 36.78 s2.3s
install valve upside down. Flow velocityshould not exceed 5 s152oc25 sls2oc2sF S1520C25FSR
p 2-1/2 61.31 61.31 85.47 5 0 026
ft./sec.Minimum opening pressure less than 0.5 psi. 51520C30 51520C30F S1520C3OFSR
3 68.13 68.13 109.76 4 0 026
S1520C40 S1520040F S1520C4OFSR
Pressure Rating73°F 23°C Water 4 91.71 91.71 134.83 2 0 026
@ ( )� 51520060 S1520060F S1520C6OFSR
Full Flow(open) 150 psi 6 189.55 189.55 240.64 1 0 o2s
S1520080
Back Pressure(closed) 75 psi 8 316.63 1 0 026
Maximum Service Temperature
140°F(60°C)
Temperature/Pressure De-ratings Apply
NOT FOR USE WITH COMPRESSED AIR OR GAS
Page 1 Spears®Manufacturing Company
Progressive Products from Spears° Innovation and Technology

Utility Swing Check Valves SPEARS
Technical Information
1amilliCimi imi Nom ipmemmiNipmp
A Li•i in 4 cm um ow so -)0 in iiii D 11111111
III
i__ ""IC M=M 07116
I I III
B 8
C
FLOW
Dimensions
Dimension Reference(inches,±1116)
Nominal Size B
A Socket Threaded/SR Threaded C D
1/2 1-3/8 2-19/32 2-5/8 4-3/32 2-1/8
3/4 1-3/8 2-5/32 2-1/16 4-1/16 2-1/8
1 1-11/16 2-5/16 _ 2-15/16 4-9/16 2-5/8
1-1/4 2-1/16 2-15/16 3-5/8 5-1/2 3-3/8
1-1/2 2-7/16 3 3-11/16 5-5/8 3-3/8
2 3 3-5/8 4-3/8 6-3/8 4-1/4
2-1/2 3-9/16 4-3/8 _ 5-1/4 7-7/8 5-1/8
3 4-5/16 4-11/16 5-5/8 8-7/16 5-3/4
4 5-1/4 6 7-1/16 10-1/16 6-3/8
6 7-11/16 8-1/2 11-5/16 14-9/16 9-1/4
8 9-7/16 11-3/16 N/A 19-1/4 11-15/16
NOT FOR USE WITH COMPRESSED AIR OR GAS
Made in the U.S.A. Page 2
Progressive Products from Spears® Innovation and Technology

SULZER
Submersible mixers
type ABS XRW 210 and 300
y •
•
SULZER
' tytk
i
I
fff, 0 ® ,
f •
•
•
UIZER
rl

Main industries and applications
The submersible mixer type ABS XRW is a compact and versatile mixer with a wide range of applications,
including use in aggressive and abrasive liquids.
Its design makes it particularly suitable for mixing and stirring applications in sewage treatment plants and
industrial areas such as:
• Equalization of sewage
• Biological processes (aerobic, anoxic and anaerobic)
• Selector(contact zone)
Also applicable for homogenization of highly concentrated sludge and slurries such as:
• Primary, secondary and digested sludge in storage and buffer tanks
• Lime and mineral slurries
Hazardous locations: 0111
• Certification for ATEX(Ex II 2G Ex h db IIB T4 Gb), 0
FM and CSA available as an option
Water and General Pulp,paper
wastewater industry and board
Features and benefits
The following features and benefits apply to the 210 and 300 models of the submersible mixer
type ABS XRW, which are used for mixing at high speeds.
Energy-saving, Premium Efficiency 1E3 asynchronous motor
• Ensures the lowest possible energy consumption
• Keeps operating temperature low for longer product life
Large, long-lasting bearings
• Offer true reliability with a calculated lifetime of more than 100'000 operating hours
• Need no maintenance—lubricated for life
Pre-loaded upper bearing
• Prevents spinning through the design of the outer ring
• Eliminates backlash
• Ensures longer bearing life
Large rotor shaft
• Keeps shaft deflection to a minimum through heavy-duty construction
When you choose our
submersible mixer XRW, you
choose the market's best
ongoing energy performance.
You also get the best lifecycle
cost,from initial purchase to
ongoing operation.

Sealed connection chamber with quick-connection block
• Simplifies mixer maintenance
• Safeguards the motor to ensure high reliability
Triple seal system with dual oil chamber
• Improves motor protection
Enhanced mechanical seal protection system
• Keeps the mechanical seal clog-free
• Greatly extends the life of the seal
Hydraulic-optimized investment-cast propeller
• Ensures the highest possible mixing performance
• Reduces maintenance through self-cleaning
Abrasion-resistant, galvanically insulated mast bracket and suspension
• Reduces the risk of electrochemical corrosion
TCS (Thermo Control System)
• Provides a warning or switches off the motor automatically before the permissible temperature limit is
exceeded, whether due to high-temperature medium or another problem source
Q Premium Efficiency 1E3 motor
© Lower bearing
0 Upper bearing
Q Rotor shaft ,
Q Sealed connection chamber -
0 Dual oil chamber11111
,;
a..
Ar 0 © ;
0 0
olgt
y 0 Mechanical seal
0 Propeller
Q Mast bracket
© Suspension
0 TCS(Thermo Control System)

2 Technical data
The maximum noise level of the units of this series is 5 70 dB(A). In some types of installation it is possible that
the noise level of 70 dB(A)or the measured noise level will be exceeded.
Additional technical information is available in the XRW technical data sheets which can be downloaded from
www.sulzer.com > Products> Submersible Mixers.
2.1 Technical data XRW 210 and 300
m 1 a o
°� 3
i3 10 y T oa a in Co 3 E s
v
� O. O a a 'Uo = N 0- y N
o c = a) 1- 0 rn
o (n c
= 2 y c X N
0 m 3
cc o: a°
50 Hz [nun] [1/min] [kW] [kW] [A] [N] [kW] [kW] [kg]
2121 210 1424 PA 08/4 0.9 0.8 1.8 156 0.7 0.8 33
2131 210 1437 PA 15/4 1.8 1.5 3.7 207 1.0 1.2 41
2132 210 1437 PA 15/4 1.8 1.5 3.7 285 1.2 1.4 41
2133 210 1437 PA 15/4 1.8 1.5 3.7 304 1.5 1.7 41
2141 210 1424 PA 08/4 0.9 0.8 1.8 - - - 39
2151 210 1437 PA 15/4 1.8 1.5 3.7 - - - 47
2152 210 1437 PA 15/4 1.8 1.5 3.7 - - - 47
2153 210 1437 PA 15/4 1.8 1.5 3.7 - - - 47
3021 300 958 PA 15/6 1.8 1.5 3.5 289 0.9 1.1 62
3022 300 958 PA 15/6 1.8 1.5 3.5 350 1.2 1.4 62
3023 300 958 PA 15/6 1.8 1.5 3.5 409 1.3 1.6 62
3031 300 971 PA 29/6 3.5 2.9 7.3 456 1.6 2.1 82
3032 300 971 PA 29/6 3.5 2.9 7.3 564 2.2 2.6 82
3033 300 971 PA 29/6 3.5 2.9 7.3 695 2.7 3.2 82
3041 300 958 PA 15/6 1.8 1.5 3.5 - - - 73
3042 300 958 PA 15/6 1.8 1.5 3.5 - - - 73
3043 300 958 PA 15/6 1.8 1.5 3.5 - - - 73
3051 300 971 PA 29/6 3.5 2.9 7.3 - - - 93
3052 300 971 PA 29/6 3.5 2.9 7.3 - - - 93
3053 300 971 PA 29/6 3.5 2.9 7.3 - - - 93
60 Hz [mm] [1/min] (kW] [kW/hp] [A] [N] [kW/hp] [kW/hp] [kg/Ibs]
2121 210 1735 PA 18/4 2.1 1.8/2.4 3.5 255 1.1/1.5 1.3/1.6 41/90
2131 210 1735 PA 18/4 2.1 1.8/2.4 , 3.5 310 1.7/2.3 2.0/2.7 41/90
2141 210 1735 PA 18/4 2.1 1.8/2.4 3.5 - - - 47/102
1 2151 210 1735 PA 18/4 2.1 1.8/2.4 3.5 - - - 47/102
3021 300 1153 PA 18/6 2.2 1.8/2.4 3.4 484 1.7/2.3 2.1/2.8 62/131
3022 300 1169 PA 35/6 4.1 , 3.5/4.7 6.9 565 2.1/2.8 2.6/3.4 82/181
3023 300 1169 PA 35/6 4.1 3.5/4.7 6.9 660 2.3/3.1 2.8/3.8 82/181
3031 300 1169 PA 35/6 4.1 3.5/4.7 6.9 717 3.1/4.1 3.6/4.9 82/181
3041 300 1153 PA 18/6 2.2 1.8/2.4 3.4 - - - 73/162
3042 300 1169 PA 35/6 4.1 3.5/4.7 6.9 - - - 93/206
3043 300 1169 PA 35/6 4.1 3.5/4.7 6.9 - - - 93/206
3051 300 1169 PA 35/6 4.1 3.5/4.7 6.9 - - - 93/206
•50 Hz at 400 V;80 Hz at 480 V.
Starting:Direct On Line(D.O.L)
6

II
2.4 Dimensions (mm)
2.4.1 XRW 210
r 150 m
Ili
N �4
I ♦ § iii 1
0,4'.#4_ At
i 14•11:4::_i.s., El
m II
1u#'
Min.30' \ 0,..„,„
oa
,n PA 08/4,PA 08/4:438
A _ ,� PA T
PA 16/4:498 w Min.450 . a.
Vertical adjustment limits Wall mounted on adjustable bracket
Floor mounted on adjustable bracket Floor mounted on concrete base
4 I Fr
g 1 0
II g
S
im
II
)11im ,_ I ,
/ oily
NiitY
I at
135 .
013.5®\ _��.
!111
o
700
Figure 1:Dimensions XRW 210
9

15.0"
MAXAIR DIFFUSER (TYP)
21 .0" a illgto
BALLAST FRAME I
S.S. PIPE STRAP (TYP)
FEEDER AIRLINE TO
AIR LATERAL
hi 63.41 "
' • • • • • • • • • • • • 11 Co', A • • • • • • • • • 0 • • • •
jTIA
5.0"
NOTES:
1 . STAINLESS STEEL COMPONENTS (BY EDI) BALLAST FRAME
TO BE CAST IN CONCRETE.
2. BALLAST USES CONCRETE WITH A
DENSITY OF 145#/ CU.FT. MIN.
/ r \ (-ENG.BY. DWG.BY: ENVIRONMENTAL DYNAMICS INC.
MAXAIR DUPLEX DIFFUSER ASSEMBLY TEM 5601 PARIS ROAD
WITH PLASTIC BALLAST FORM REV DATE , COLUMBIA, MISSOURI 65202
TYPICAL INSTALLATION DETAIL B 10-3-08e PHONE:[phone]X:DATE: SCALE: DWG NO: FAX [phone]
5-11-94 N.T.S. / 5889 J WWW.WASTEWATER.COMJ

ESPECIFICACIONES F\/1 a x,A i r1M PVC
1 t1/41$6
DEL PRODUCTO
aeration(orlife Difusor de aurbuja gruesa
• Configuration simple o duplex.
II Duplex • Disenado para una alta capacidad de flujo de aire.
• Disponible en longitud de 610 mm (24 pulgadas).
,* -
• Diseno resistente a las obstrucciones con purga
-' • •• ' . • •• •: ' automatica.
• Perimetro completo de liberation de aire de 1220
mm (48 pulgadas).
• Hay unidades estandar en el inventario disponibles
para su envio inmediato.
• Unidades estandar con la parte inferior abierta y
Simplex con la parte inferior cerrada opcional disponibles.
• Construction de PVC u opcional de CPVC para
ofrecer la maxima resistencia quimica y termica.
• Descarga de aire de tres niveles para ofrecer una
operaciOn con un rango de flujo amplio.
• Completamente no metalico, resistente a la
- 14, corrosion.
SPECTRUM SADDLE MOUNT
LATERAL DE AIRE (EL MODELO PUEDE VARIAR)
•
ORIFICIO DE SALIDA DE AIRE(TYP)
CUNA d
MODELO CON PARTE INFERIOR MODELO CON DEFLECTOR
ABIERTA
SISTEMA METRIC() SISTEMA INGL S
Tipo de Flujo de aire Longitud Tamano del Flotabilidad Peso Tipo de Flujo de aire Longitud Tamano del Flotabilidad de Peso
difusor de diseno del difusor orlficio de operaci6n seco difusor de diseno del difusor Oriflcio operaciOn seco
m3ra/h mm m2 J kg kg scfm in ft2 I lb lb
Simplex 0-79 813 Disenado adec- 4.9 2.7 Simplex 0-50 32.0 Disenado adec- 11 6.0
uadamente para uadamente para
Duplex 0-158 1630 cada proyecto 7.7 5.0 Duplex 0-100 64.0 cada proyecto 17 11
Visite www.EnvironmentalDynamics.com o www.wastewater.com

Environmental Dynamics International
MaxAi r ` PVC : Difusor de burbuja gruesa
Procesos:
Aireacion biologica. +----
Procesos de lodos activados. --
Zanja de oxidation. - o.,72, '
Reactores disconttnuos secuenciales
... --
dAA (SBR, por sus siglas en ingles). '
..,,,,I biologicos de membrana
,i -' (MBR, por sus siglas en ingles). lik '",
Reactores biologicos de lecho movil _
17
(MBBR, por sus siglas en ingles).
DigestiOn/estabilizaciOn de lodo. — lit' ‘
," - 11116�r. Plantar paquete.
Aplicaciones: I I I ! I Industrias:
Aguas residuales municipales. �,I________( Alimentos y bebidas.
Aguas residuales industriales. ��" HoLacteos y queso.
Sistemas fijos a piso.
I I Pulpa y papel.
Sistemas removibles. 1 _ PetrOleo y gas.
Mezuado. Procesamiento animal.
Alta transferencia de oxigeno. Lixivados.
Perdida de carga baja. Energla y electricidad.
Farrnaceutica.
'( El exito de EDI se ha demostrado en
mas de 7,000 instalaciones realizadas
C en mas de 100 paises en todo el mun-
do, con lo que se ha brindado servicio
�� a mas de 400 millones de personas. ''
i Comuniquese con la oficina local 41%�' ^"` que se indica abajo para conocer los —f_
detalles de nuestros productos,
sistemas y procesos comprobados. .£ '*+*,
EDI Europa America del Norte:Of icinas centrales internacionales China
Diseno,fabrication y almacen Diseno,fabrication y almacen Oficina de diseno
Tel: [phone] Tel:[phone] Tel:[phone]
[e-mail] [e-mail] [e-mail]
Alemania Mexico Japan
Oficina de diseno Oficina de diseno Oficina de diseno
Tel: [phone] Tel: [phone] Tel: [phone]
[e-mail] [e-mail] [e-mail]
Francia Singapur(SEA) India
Oficina de diseno Diseno y almacen Oficina de diseno y fabrication
Tel: [phone] Tel: [phone] Tel: [phone]
[e-mail] [e-mail] [e-mail]
©Environmental Dynamics International,Inc.,todos los derechos reservados.
Debido a nuestra politica de desarrollo continuo de productos,Environmental Dynamics International,Inc.se reserva el derecho de modificar en una fecha posterior cualquier
especificacidn publicada sin previo aviso.
,," Visite www.EnvironmentalDynamics.com o www.wastewater.com

FLOATING PE AIR
LATERAL
MIMES.S. PIPE STRAP CONCRETE FILL
FLEXAIR MAGNUM U 1
TUBE (TYP) �` ROPE SNAP
_I IRMIMIIIIIMIEMI
P.P. RETRIEVAL ROPE FEEDER AIRLINE P.P. RETIEVAL ROPE
(TIED OFF AT DUAL LEG
ANCHOR ON DIFFUSER)
S.S. HOSE CLAMP ROPE SNAP DETAIL
,
,
PLASTIC BALLAST FORM
NOTES+
L STAINLESS STEEL COMPONENTS / l ENG.BY: DWG.BY:
(BY EDI) TO BE CAST IN CONCRETE. FLOATING MAGNUM DIFFUSER ASSEMBLY ENVIRONMENTAL DYNAMICS INC.
BLM TEM 5601 PARIS ROAD
FOR 88S-24,88S-16,88F/S-16,44S-24,44S-16 REv DATE - COLUMBIA, MISSOURI 65202
2. BALLAST USES CONCRETE WITH A TYPICAL INSTALLATION DETAIL F 10/30/13 I PHONE: [phone]
DENSITY OF 130#/cu,ft, i,\II: SCALE: DWG NO: FAX:[phone]
\ 1/16/2007 N.T.S. / 12234 WWW.WASTEWATER.COM�
3. TORQUE NUTS TO 20FT/LBS

6 e , ESPECIFICACIONES F e X A I r.1.�„ M c r1 um
DEL PRODUCTO Difusor con membrana flexible de burbuja fina
aeration for life
Ideal para actualizaciones de burbuja gruesa.
• Su geometria eficaz permite aplicaciones con una den-
sidad alta y cobertura del piso superior al 65 %.
• Diseno no flotante P ara reducir el es r't es en la conex-
ion de montaje.
000,....- ',-
* Membranas de calidad premium disponibles en EPDM,
i uretano y Matrix PIusTM para reducir Ia acumulacion
de residuos y requerir un mantenimiento minimo.
• Disponible en construction no metalica para ofrecer Ia
maxima resistencia quimica, termica y contra los rayos
411 Uv.
• Diseno con triple valvula de retention que reduce al
minimo el ingreso de liquidos y solidos en las tuberias.
Ideal para aplicaciones de encendido y apagado.
84P 42P
m__ I 1--0.5 m- I
.11111111111(0), 11 II
immommitraimmoimmil
iz
84P-4
h-- - -.4500nn
c
t
m
ui ` ` `�� �� "l _. Gam/4.'..000rls3G/f.///6//'n c../e10 l////. 1"/%/fl/''j'4 I't` 1
n
rr r�a r / r r ,� r-, c r � rfi ,,,A
SISTEMA. .,i //// vrir/!/�/AGO/6rar.:./r ///✓r/Gcid/r/,r//Ni�/h///%,roeii///w„rv,�rr(rr///ire/��/b/i,nu/ r//� /Nv�ii<�;-;; r //rn6n,,ii, //�/,,,N4„r,,.� v, „/e����//n60/� r<�,ri%/%///����//��/f'//��4y�,//� ����$,��✓�:;���i
SISTEMA METRICO 1� SISTEMA INGLES
Flujo de Longitud Peso rN Flujo de Longitud Peso
Modelo aire tipico total operational Peso seco - Modelo Peso seco
aire tipico total operational
m31,,/h mm kg kg scfm in lb lb
42P micropore 0-16 1390 2.6 3.2 'J42P micropore 0-10 54.8 5.8 7.1
42P Alta cap. 0-28 1390 2.6 3.2 42P Alta cap. 0-18 54.8 5.8 7.1
84P micropore 0-32 2400 2.9 5.2 4/84P micropore 0-20 94.3 6.3 11
84P Alta cap. 0-55 2400 2.9 5.2 84P Alta cap. 0-35 94.3 6.3 11
84P-4 micropore 0-64 4880 16.6 10.4 ! 84P-4 micropore 0.-40 192 36.7 23
��9
84P-4 Alta cap 0-110 4880 16.6 10.4 84P-4 Alta cap 0-70 192 36.7 23
0/N;o �/ � ;;;;,o /' r / �r r r mY- ,,,, / ",, Raw +n-
ppl!���� ,pp� �bo�
s, r/i,.,,��jYf/jf' /xm rr7ric/ �r.��f%rr�rr7ii�/� //6q'�� n��/,/Y/a,�'�rr�i�„HN���i/��i�r/7�i �/r%M/„� N � ti/hyr �' d ir r 1 b. ,',/r
* * Los valores indicados son para cada tubo,a menos que se especifique otra cosa.
* Se logra una optima eficiencia en la transferencia de oxigeno cuando se opera desde el medio hasta el extremo inferior del rango del flujo de aire.
* La presion aproximada de operation en el difusor en el rango medio es de 25.4 a 57.15 cm(10 a 22.5 pulgadas)de H2O(de 2.5 a 5.6 kPa).
* Operar la unidad en el extremo alto del rango provocara un desempeno menor y una presion operativa mayor.
* Use el valor maxima de flujo de aire para operaciones de corto plaza coma las cargas pica o el mantenimiento del sistema.
Visite www.EnvironmentalDynamics.com o www.wastewater.com

�
� E[lV'r[][]me[lfa| Dynamics |[lfe[[]af'o|]a|
^ nw
� � � � � U � �� � � ' ` �� ~ � ^�U �� � �� fU ��
� N �~ ���-� n � U �� U �� �� � � �~� � � k . L� � � ~~ ~^^� ^ �� ~. �^� ����
'
^ ' p,oce�a�
� �
xireadunh/ol6gica. m^
Pmcesuede !udosactivados
Zanja de ox/Uac'dn
Reactopesdiscontmuossecuencie|es
(SBR po/�us sig!asen ing|�� nr�
' �
Ren^oesbid0gicos6emembtana
<KxSK, poi sus sig(as en ingl�s" �-
` - Reac,oresbinl6gicnsde |echom0vil
WHIR, po, sus �ig}as en ing/�s)
�Nm '
_-` 0ges ,6�esmhi\��d�ode �dv� �-
Plpntaspaquete, `
Ap|icodones: |ndustrias:
Aguas us/duaies munio. A|imen*ay bebi6as.
Aguasesidua|esindurLna\* L6rteosyqueSu.
Sistemas Nos Piso. Pulpa y papei
Sistemas removib|es. Petr6|eu y gas.
Sistemasf|otanres. Pnocesanniento animal.
Mezuado, /~�� "�m Lixivados.
Alta tonsf*enda de oxkleno, , , ���}�-��- `�v«*»~�~� ' Energia y e|ectricidad.
P6rdida de carga baja. Farmac6utica.
`
'
86xitodeED|sehademosuradneo �
m�s de 7.000 inrtalarinnesre*Uzados
en m0s de 108pais*seomdoe| muo' �
do. con |onvese ha bnnd"do,en/icio �
am6sde400m8/ooe,depersnnas
�
cnmuniquee con bofic/nalocal wm—'
- qve se in dicuab�npa,aconocerlos L�~
detoUesdenuesumspmdoctns'
' siuemasy nmesnscompmbadca.
ED|Eumpa Arridirica del Norte:mmras centrales/nternacionales China
Dise0o'tabricadhnya|mac6n Diseho.fabrioadbnya|mac6n Ofidnadediseho
7e|: +44'1295'O1O58l 7e|:+l'573'474-945O le|: +8h'lO'5957'4336
ediEumpe@Envimnmenta|Dynamio.com ediNorthAmehca@Envimnmenta|Dynamks.com ediIhina@Envimnmenta|Dynamio.com
A|emania Wxiou ]apbn
Ofidnadediseft Ofidnadedisehn Ofidnadediseho
Tel: +49'(0)9O7392121Z Tp|: +l'877'334'247O 7e|: +Dl'3'5789'914O
ediGermany@Envimnmenta|Dynamics.com ediK4exico@Envimnmenta|Dynamicszom edi]apan@Envimnmenta|Dynamio.com
Handa 5ingapur<5EA> India
Ofidnadediseho Di»ehoya|mac6n Ofidnadedisehoyfabricadbn
Te|: +33'(0)-7O1'548'529 7e|: +65'0521-4S36 Tp|: +Ql'22'2422-4Z28
ediFrance@Envimnmenta|Dynamiomm K ediAaia@Envimnmenta|Dynamio.00m edi|ndia@Envimnmenta|Dynamio.com
m Environmental Dynamics International,m=.maos/muerochos renmoxm
Debido a nuestra polltica de desarrollo continuo de productos,Environmental Dynamics International,Inc.se resemao/aomchouemvmnca,pnvoa+ocha posterior mo/nu.e,
espouoouonnuuncaaa sin n,owoay.m.

Series 20SS Ball Valve SVF
Two-Piece Ball Valve,Full Port
Sizes 1/4" 3 " FLOW CONTROLS
The SVF Series 20SS full port ball valves are designed for general purpose performance in a
wide variety of utility applications. The 20SS is an economical, manually operated valve that
meets industry requirements for performance and dependability.
SERIES 20SS DESIGN FEATURES
%/Designed&built for economical
performance )c.'
✓Pressure rated for 1000 WOG
V Full Port flow path for maximum flow .:
✓316 Stainless Steel body,ball and stem
VThreaded End Connections
,/Vinyl grip handle
V Blowout proof stem adds safety&reliability
/Lockable in the"Open"or"Closed"position
✓Oval handles available-Sizes 1/4"to 2"
MATERIALS OF CONSTRUCTION
ITEM DESCRIPTION MATERIALS SPECIFICATIONS
i
316 Stainless Steel
1 Body
(ASTM A351-CF8M)
End 316 Stainless Steel O `4 _
2
Connector (ASTM A351-CF8M)
3 Ball 316 Stainless Steel
(ASTM A351-CF8M)
4 Stem 316 Stainless Steel
(ASTM A276-316) 0
5 Seat — ---- --------RTFE _--- O
I _
6 Body Seal RTFE O
7 Stem Seal RTFE
� I �
What do you need today?' I z y'tGcows
SVF Flow Controls•5595 Fresca Drive•La Palma,CA 90623•Tel:[phone]•[e-mail]
Specifications subject to change w/o notice.Al Data Sheets on our webstte supersede par publications•(SVF.205S.0720)

Series 20SS Ball Valve
1 ,
Two-Piece Ball Valve,Full Port SvF
Sizes 1/4" - 3 " FLOW CONTROLS
DIMENSIONS,WEIGHT,C V
A B D L Weight
Size Cv
-- 11
in. mm in. mm in. mm in. mm lbs 1 kg
1/4" 1.89 48 0.46 12 3.86 99 1.93 50 0.39 0.2 7
3/8" 1.89 48 0.49 13 3.86 99 1.93 50 0.39 0.2 8
1/2" 2.21 56 0.59 15 3.86 99 2.09 54 0.56 03 11
3/4" 2.56 65 0.79 20 4.73 121 2.48 63 0.87 0.4 21
1" 3.03 77 0.99 26 6.07 155 2.84 73 1.73 0.6 35
1-1/4" 3.55 90 1.26 33 6.07 155 3.05 ! 78 2.22 i 1.0 57
1-1/2" 3.86 98 1.50 39 7.25 185 I 3.62 92 2.99 1.44 80
r
2" 4.77 121 1.97 50 7.25 185 3.98 102 5.16 2.3 - 150
2-1/2" 5.71 145 2.56 66 9.65 246 5.08 130 10.19 4.6 265
3" 6.54 166 2.88 74 9.65 246 5.48 140 i 15.45 7.0 415
= J
20SS - PRESSURE/TEMPERATURE CHART
r D
(69) 1000
(55) 800
rcl
cn
(41) 600 ��
a I L
`1 )
N (28) 400 ----I -_
N
a (ta) 200 1
T- -
E
7
E - III - -)- - - ® --OB r
•x (7) 100
g
-40 0 50 100 200 300 400
(-40) (-18) (10) (38) (93) (150) (204)
A
Maximum Temperature Fahrenheit(Celsius)
J
Class 400
Note:Maximum pressure&temperature is limited to the seat material rating
20SS Series Part Numbers
Size Part# Size Part#
1/4" 20SSTH01 M 1 1/4" 20SSTHO6M11
3/8" 20SSTHO2M 1-1/2" 20SSTHO7M
1/2" 20SSTHO3M 2" 20SSTHO8M
3/4" 2OSSTHO4M 2-1/2" 20SSTHO9M
1" 20SSTHO5M 3" _ 20SSTH1OM --/
Note:Oval handle option available(PN:P2OLHOV13 sizes 1/4"to 1/2",PN:P2OLHOV4 size 3/4",PN:P2OLHOV56 sizes 1"to 1-1/4"and
PN:P2OLHOV78 sizes 1-1/2"to 2")
SVF Flow Controls•5595 Fresca Drive•La Palma,CA 90623•Tel:[phone]•[e-mail]
Specifications Subject to change w/o notice.AN Data Sheets on our wehsite Supersede prior publications.(SVF.20SS.0720)

CCENTechnologies
WavTex' by ENTEX Technologies Engineering
Clean Water
Solutions
Moving Flex Med: •.
. WavTex f" ,= r !�
• tea' "` . is a moving woven media system using �t.rr�",; t/*Or • „ir e ♦
'�'� " �4., ' Entex's patent pendingEnTextile" media ` ' ' ' - •., 0•
f. 1 .-4i .t� t�
lr• ' } ''• .• 7,° • in Integrated Fixed-film 1;..lm Activated Sludge i' ;.r�` `'.tt ..•n
lir
";; `•• ' *';. (IFAS)and Submerged Fixed-Film (SFF) rr"'.4' f. "'.;t+• •1 '•11
^� •, systems. ,,.�/' ,t1'."�.i� •' •.
ii,
its' . a.IndependentlymovingEnTextile media r.,t/' ''r ' ,' ,'�� '
40
�' sheets continually wave in the aeration 1. .1■it;.. .,..t. •''mot . ~4,/
r
basin in a random motion, ensuring
d *�.' ;'. excellent oxygen and substrate transfer. ,I !'! , , 4111- , , ,/
• • % ♦
• •1
% /AS - ,
77 WavTex is a cost-effective solution for WavTex means
its "` - existing activated sludge plants that Simplicity
. r need more advanced treatment. Because
WavTex equires no in
little or no additional tankage is required,
�. ,n.; . basin retention or
-'" +, ;'� WavTex is ideal for plants with limited
• drain screens and
. room for expansion.
can be used with
existing fine bubble
EnTextile Media It is also an excellent choice for space
diffuser grids for
EnTextile media provides an exceptionally efficient, high performance new plant maximum energy
designs.
high effective biological surface area, and efficiency and
minimum retrofit
the narrow thickness of the media provides
costs.
excellent transfer of waste and oxygen to
Entex Technologies Inc
the thin biological film,providing high rate 400 Silver Cedar Court
Suite 200
treatment. Chapel Hill,NC 27514
919.933.2770 phone
919.287.2258
entexinccom

WavTex by ENTEX Technologies, continued
WavTex Increase capaci ` • • High Performan •
means
WavTex moving flex media provides Developed based on over 20 years of
Versatility
extensive surface area for biomass experience using attached growth media
growth. The attached biomass popula- for wastewater treatment, EnTextile
Unlike traditional tion can more than double the effective media provides high biomass surface
moving media MLSS concentration. The vigorous area designed to maximize random
systems, WavTex motion of the EnTextile media in the turbulence and open pathways to create
moving flex media aeration basin provides a high shear optimum conditions for substrate and
can be used effectively on the surface of the EnTextile media, oxygen transfer while maintaining bio-
maintaining a thin biological film. The mass density control.
in both fine bubble
thin film provides for high rate biologi-
and coarse bubble cal kinetics.
Cost Effectiveness
systems, without
the need to remove , WavTex improves water treatment
Eliminates Screen •
existing efficient with little or no addition of aeration
fine bubble diffuser Never worry about plugging of retention basins or clarifiers. It's a significantly
screens. The WavTex system also allows less expensive way to upgrade activated
systems.
for a broader range of tank dimensions, sludge plants.
�•�f jr '`10e�40 � 't '0 :>' since the system eliminates the potential
.0 � •0.r 0.` 0• r, # for media "bunching"at the back end
' .k + '' 0•; ' f Advanced Systems.Proven Solutid'
I •,t�``�,� �•����.�'��,�+ of long basins. y
19r ' ENTEX engineers have been involved
.It+.-,l•..,�46 .�� .7.
+•f .}r�,�••y '`'� 'I' ' ' Nitrification&Denitrificatio` in hundreds of plant installations.
r t�•+,�;R'�i '"4, •• "At, 4Pa �:."4'r We'd like to be involved in yours.
,, '1..,•�....1.. ..� ... •. a--..,, .
.,.� 4.. .,}� , WavTex provides stable growth
-r, . ♦ * platforms for slow-growing nitrifiers.
.d,,�,*41,01,,,;iy.:7';'• " Nitrifying plants perform better;
07ur�� f m s ac .. h /' , f � i
,�::'�"hA1:�:� 'F"**:v1+�".:) non-nitrifying plants are able to
�, . �.,�.�af tr nitrify. Plants needing to convert
t e e
fj .1.4k,� �� ► , i to nitrification can do so at a far
+ ,j ' 'A. •6,.; �i.;�, lower cost than adding basins.
01 . 040d ' ENTIELIC
d 4 Technologies

. J T I e 1 e 47 . l 0 I ] T
Yygg NH ST
ZONE REV DEscRIPTION DATE DWN CNN
DISCHARGE 41.76 - A RELEASED PER ECN 1042672 4-8 NPT NPT ADDED HF406,IC4181 ADDED OTV AND
MODELS, O B2 ADDED SOHP MOTOR.
4.43 18.25 '1 DO B fA7�B3 AD E NOTE.IE6I B4ADDED 01I19N6 MWS RNS
CHECK VALVE DISCHARGE SILENCER jX 1.18 X.51 SLOT NOTE,ECN 104M23
.. 1.26 - j j
MOTOR ------ •.,Ina � \ -
- (50HP SHOWN) !1 5.151 _
i-
,...................(2!).._......)
t 25 50 -
g _III :�® •
• ,���
*1 e•8� RT T . 2 39 57 e , - -
29.43 � rri .
��,
Iiiiiiioii
0„. 5.510 �1�r1� i; -,� i " •70 - _ �i'
G - "
VIEW A-A � "s
•NE 1/2-14 NPT DRAIN USED
1-8.77-- FOR DF4506 AND DF4509
THIS LOCATION
e 36.23
NLET FILTER
DIFFERENTIAL PRESSURE INDICATOR
- • /INLET FILTER/SILENCER s +-
.11
OTOR JUNCTION BOX [Sp��
re' OTATION ARROW
•
BELT GUARD =
BLOWER
(HF408 SHOWN)
101
'�I •ILLEVEL /
-
. 1 _.„„s.,..,,,...
.....
w+ SIGHT GLASS 1 -
r._. •
•IL
47 50A _ �I SIGHTLEVEL
GLASS : :;;:;
11 ` 1` i �� •
IN �_•-- • •• -�I. i. � jPTmil 1l 1rA i06 F'� i9) o
ice- I
- �1.
e- g G- 11 • L4iik, 4, L._ ,
elm
E LLII��1t'
INV
AUTO BELT TENSIONER
MOUNTING ISOLATORS AL--- DISCHARGE DISCHARGE
PRESSURE GAUGE TEMPERATURE GAUGE
la
-- - - -- --_____tA ^.' "-""' :77 .�271±e,e..o�,.d�.. triZc "t "`
0110.4.0h0 AM III IMES
ITA
TOL ON DECIMALS Ft•*TO
THE MAXIMUM DIMENSION COULD BE 48.30 o w•' *.if .wrE�n ... ve OUTLINE-OW/PAC
IWO,w10+e 0E] o.nwwns i I"=""I-3008PB604 r
s
Ii 1

QuickPik
.
Sutorbilt Legend - 4LDSL
Dear
Sincerely.
Craig Bumess
Gardner Denver PHYSICAL
5491 Lucia Place weight 155 lbs. ,
Sarasota, FL 34238
Gear Diameter 1 4 in.
Center Distance
Product Information .
Connection Size 3U3d in
CORRECTED VALUES ORIGINAL UNITS ENGLISH UNITS . METRIC UNITS
Case Length 8 in.
Ambient Pressure I#696 PS A. 14.696 Psi, 1.013 bar a
Elevation 0 ALTI-FT 0 ALTI-FT 0 alt- 1 WRz 0.924 !
,.__ _r
1t2
Inlet Pressure 1 14 696 PSIG 0 PSIG 0 bar g C.Mentat1on , horizontal
Inlet Pressure Loss ; 0.3 PSIG 3 0.300 PSIG I 0 021 bar g PERFORMANCE
Inlet Temp 68 F f 68'F 20°C lvtaz Delta P 7 PSI
Inlet Flow 1 160 ICFM ' 160 ICFM 272 m'ln Max Temp 260°F
6 PSIG 6.000 PSIG 0.414 bar g
Discharge Pressure Y 3600
9 i May.Speed
Discharge Pressure Loss 0 2 PSIG 0 200 PSIG 0 014 bar g 1 RPM
rd—__F
Min Spccd 055 RPM
MEASURED VALUES ORIGINAL UNITS ENGLISH UNITS MI [RIC I.IN11 S .n
Speed 1433 RPM 133 RPM 1433 RPM Max Case Pressure 25 PSIG
�� Max Delta T 1 160'F
RPM Of Max 40 40 40 ,
, _,
Power 7.5 HP 7.5 HP 1 5 593 kW
Discharge Temp 1 172'F 172'F 78`C
Temp%of Max 66 66 66
{
Noise 79 dBa 79 d8a 79 dBa
Pressure%of Max 93 93 93
a.-.-- �._ 4... . _ _,.. ._�
Adiabatic Efficiency 52.46% 52 46% 52.46%
Created. 08-30-2022

QuickPik-
AMBIENT GAS PARAMETERS ENGLISH UNITS METRIC UNITS GAS MIX: VOL
Molecular Weight 28 867 Ibmilbmoi 23 367 kg/4mo! Ivo
R Value 53 522 ft.Ityfilbm_R 0.288 kJikg.1(
Density 0.075 1.200 Icgirn3
Performance Curves
Temperature Rise
DEFINED CONDITION S
104 F 15C1
RPM
oL
],.
Published Data
— Defined
Conditions
00C
Flow
DEFINED CONDMON 5
159 ICFM 60C
RPM
40.0
MEM
Published Data 20U
— Defined
Conditions
3 50'.:
Created 08-30-2022

QuickPik�
Performance Curves
Power
DEFINED CONDITIONS
7.5 HP
s
RPM
11111= 'o
S
aubnshed Data
Defined
Conditions
I00(i 150+
Torque
DEFINED CONDITIONS
27.5 ft-lb
:o
RPM
1433 1
Rubiished Data
— Defined
Conditions
�:iCir's 7 SDI
Created: 08-30-2022

'�■■���� SPECIFICATIONS
1111111111
DOCUMENT#W102
a xylem brand
YSI IQ SensorNet FDO®
Optical Dissolved Oxygen Sensor
The FDO is an optical, luminescent based DO sensor for the
IQ SensorNet system. During the biological nutrient removal
process at wastewater treatment plants, continuous and precise
measurement of dissolved oxygen concentration is of vital
importance for optimal performance and trouble-free operation.
Efficiency and energy demand is mainly determined by the
performance of the aeration control system. The FDO is a
reliable, proven, long-term solution for continuous DO data that
can help optimize your process and lower energy costs.
• Intelligent Sensor Cap
The sensor cap is individually factory calibrated. Calibration
data is stored on a chip that is embedded in the sensor cap.
No need to enter calibration coefficients. When a new cap is
Parameters: installed,the coefficients are recognized and sent directly to
Dissolved Oxygen(optical) the controller terminal eliminating the need to manually enter
Temperature
information.
• Equal Path Reference System
The optical measurement and reference paths are identically
designed. This allows for identical aging of the components
which enables accurate compensation and eliminates
.,111116 calibrations. That's correct,there is no calibration required.
• Green Light Technology
Softer, low-intensity excitation light increases the lifetime of the
The FDO's lower cap. This translates into a two year warranty on the standard
energy green light
excitation technology cap.
extends the sensor
cap lifetime.
Or
Learn More:
Scan with a smart4
• y
+ g phone or tablet,
I to see the FDO
f + , «�
0 f angled sensor tip
❑� '+'x
- . allow bubbles to
pass by.

IQ SensorNet FDO Optical Dissolved Oxygen General Specifications
Sensor Cap Replacement Yes;the cap,can be replaced.Automatic recognition by the sensor of the cap including the factory calibration.
Calibration Capability Yes;not required,factory calibrated
Interferences None
Minimum Flow Rate None;no flow requirement
Response Time at 25°C 700 IQ and 70010 SW•T90=<150 seconds;T95=<200 seconds
701 IQ and 701 IQ SW-T90=<80 seconds
Signal Output Digital
Lightning Protection Yes
Power Consumption 0.7 watts
Maximum Pressure 10 bars(145 psi);with sensor connection cable
Electrical Connections 2-wire shield cable with quick sensor connection
Conformance/Certifications EN 61326,Class B,FCC Class A;Intended for indispensable operation,CE,cETlus
Temperature Conditions Operating Temperature: 23to122°F(-5to50°C)
Storage Temperature: -13 to 122°F(-25 to 50°C)
Sensor Material: Housing-VA steel 1.4571;Sensor Cap and Locking Cap-POM(Poiyoxmethyiene),PVS,silicone,PMMA
Rating: IP-68;waterproof
Dimensions: 4001 x 40 D mm(15.75 Ix 1.57 Din)
(length x diameter) 400Lx59.5Dmm(15.75Lx2.34Din)Salt Water version
Weight: 900 g(1.98 I bs)
1,500 g(3.31 Ibs)Salt Water version
Warranty: 2 years
IQ SensorNet FDO Optical Dissolved Oxygen Technical Specifications
Dissolved Oxygen Range
Concentration 0 to 20,00 mgiL
Saturation 0 to 200.0%
Dissolved Oxygen Resolution
Concentration 0.01 mg?L
Saturation 0.1%
Temperature
Measurement 23 to 140°F(-5 to 60°C)
Compensation 32 to 140°F(0 to 60"C)
IQ Se nsorNet FDO Ordering Information (order 2020 XTterminal.modules,cables,sensors separately)
FDO 70010(#201 650Y) Optical DO sensor for monitoring and control;includes 1 factory calibrated sensor cap.
FDO 700 IQ SW(#201 652Y) Salt Water Design Optical DO sensor for monitoring and control;includes 1 factory calibrated sensor cap.
FDO 701 10(#201 660Y) Optical DO sensor for monitoring and control;faster response time;includes 1 fast response factory calibrated cap.
FDO 701 IQ SW(#201 653Y) Salt Water Design Optical DO sensor for monitoring and control;faster response time;includes 1 fast response factory calibrated cap.
SC-FDO 700(#201 654Y) Replacement;universal factory calibrated sensor cap for FDO 700 IQ and FDO 700 IQ SW
SC-FDO 701(#201 655Y) Replacement;fast response factory calibrated sensor cap for FDO 701 IQ and FDO 701 IQ SW
YSI
1 72 5 Brannum Lane,Yellow Springs,OH 45387
Tel[phone].897.4151 (US)
[e-mail] •�������
YSl.com MEMEMENI
\'SE and FDO are registered trademarks.
Specifications are subject to change. Please visit YS1.com to verify at specs.
Pi 's:
9 a xylem brand
g arin!adintheUS:� �.. �i+2?Jay,20�2

■i•■umiu SPECIFICATIONS
iiir,Iiii
j j ; ail
DOCUMENT#W118-02
YSI
YSI Digital SensoLyt`' pH/ORP Sensor for the IQ Sensor-
a xylem brand Net System
The SensoLyt® is a rugged, online probe for measuring pH and
ORP concentrations using a combination electrode for the most
accurate wastewater process monitoring.
The SensoLyt'® probe is used within the IQ SensorNet system
and can therefore be networked with other probes and param-
eters for a complete process monitoring and control system. It
't can measure and display pH or ORP.A built-in pre-amplifier and
temperature sensor with SensCheck function helps to monitor the
sensor.
The SensoLyt® is the ideal probe for quantitative measurement
of pH/ ORP in a wastewater treatment plant.Various SensoLyt®
electrodes(SEA/DWA/ECA/PtA) meet the needs of different ap-
plications.
Parameters: • SensCheck function monitors sensors
pH
ORP • Electrodes are protected
• Electrodes can be removed and calibrated in the lab or in
the field
• Provides pre-amplification of the electrode signal
• Digital sensor stores calibration value
• Automatic temperature compensation
• Electrodes can easily be replaced without tools
• 2-year warranty on the probe, 6 months on electrodes
The SensoLyt®sensor provides
continuous data to help with
operational improvement
decisions.

Sensolyt® 700 IQ Technical Specifications
Electrode Type Measuring Range Accuracy Application
ECA 2to 12 pH units +1-0.2 pH standard wastewater
SEA 2 to 12 pH units +!-0.2 pH seawater
SEA-HP 4 to 12 pH units +1-0.2 pH seawater!high pressure
DWA 0 to 14 pH units +!-0.2 pH drinking water
PtA +1-2000 mV +J-20mV
Temperature Integrated NTC-5 to 60°C(23 to 140°F) +1-0.5'K
Operating&Compensation Range Temperature 0 to 60°C(32 to 140°F)
Warranty 2 years on probe,6 months on electrode
Dimensions 508 Lx 40 D mm(20 Lx 1.57 Din);SW design:515 l x 59.5 D mm(20.78 Lx 2.34 Din)
Certifications CE,cETlus
Protection Class Sensor with SACIQ cable connected:IP68
Operating Conditions Overpressure/Temperature
ECA 6 bar(87 psi)!68°F(20°C);1 bar(14.5 psi)!140°F(60°C)
SEA 10 bar(145 psi)/68°F(20°C);1 bar(14.5 psi)!140°F(60°C)
SEA-HP 10 bar(145 psi)!140°F(60°C)
DWA 6 bar(87 psi)/68°F(20°C);1 bar(14.5 psi)/140°F(60°C)
PtA 10 bar(145 psi)!68°F(20°C);1 bar(14.5 psi)!140°F(60°C)
Lightning/Voltage Protection Yes
Electrical Power Consumption:0.2 W,Two wire shielded IQ cable provides power and communication
Materials Housing:V4A Stainless Steel 1.4571(SW version POM(Polyoxmethylene)),protection cap PVC;sensor holder
POM(for electrode material see product manual)
SensoLye® Plus 700 IQ Sensor Ordering Information
Name Item if Description
Sensolyt 700 IQ 109 170Y Robust digital pH/ORP probe for combination electrodes,Sensolyt 5 SEA,SEA-HP,DWA,ECA,PtA.Order pH or ORP electrodes
and SACIQ cable separately
Sensolyt 700 IQ SW 109 171Y Robust digital pH/ORP probe with amplifier for use in salt water applications.Order pH or ORP electrodes separately
SensoLyt SEA 109 115Y pH electrode ideal for highly polluted wastewater,emulsions and suspensions,media containing sulfides and proteins for use
with the IQ SensorNet system
Sensolyt SEA-HP 109 118Y pH electrode ideal for high pressure and temperature conditions for use with the IQ SensorNet system
Sensolyt DWA 109 119Y pH electrode with built in reference,Sensolyt 70010,ideal for drinking water or iow conductivity applications
Sensolyt ECA 109 117Y pH electrode ideal for general wastewater applications
Sensolyt PtA 109 125Y ORP electrode ideal for municipal and industrial wastewater,emulsions and suspensions,media containing sulfides and proteins
SACI0-1.5 480 040Y Sensor cable for all 10 SensorNet sensors,IP-68 waterproof connection;cable length 4.9 ft(1.5 m)
SACIQ-7.0 480 042Y Sensor cable for all 10 SensorNet sensors,IP-68 waterproof connection;cable length 23 ft(7 m)
SACIQ-15.0 480 044Y Sensor cable for all 10 SensorNet sensors,IP-68 waterproof connection;cable length 49 ft(15 m)
SACIO-SO 480 041VY Sensor cable for all IQ SensorNet sensors,IP-68 waterproof connection;cable length special order up to 330 ft(100 m)
SACIO-20.0 SW 480 045Y Sensor cable for all IQ SensorNet sensors,IP-68 waterproof connection;cable length 65 ft(20 m)with screwable SACIQ-Plug
SACIQ-25.0 SW 480 066Y Sensor cable for all IQ SensorNet sensors,IP-68 waterproof connection;cable length 82 ft(25 m)with screwable SACIQ-Plug
SACI0-50.0 SW 480 060Y Sensor cable for all IQ SensorNet sensors,IP-68 waterproof connection;cable length 162 ft(50 in)with screwable SACIQ-Plug
SACI0-75.0 SW 480 067Y Sensor cable for all IQ SensorNet sensors,IP-68 waterproof connection;cable length 243 ft(75 m)with screwable SACIQ-Plug
SACI0-100.0 SW 480 062Y Sensor cable for all IQ SensorNet sensors,IP-68 waterproof connection;cable length 330 ft(100 m)with screwable SACIQ-Plug
SACIQ-SO SW 480 064VY Sensor cable for all IQ SensorNet sensors,1P-68 waterproof connection;cable length special order up to 330 ft(100 m)with screw-
able SACIQ-Plug
SACIO-Plug 480 065Y Screwable plug for all SACIQ sensor cables for IQ sensors
Visit YSl.comllQ for additional information on the entire IQ SensorNet system
YSI
1725 Brannum Lane,Yellow Springs,OH 45387
Tel[phone].897.4151 (US) ■1111■■Ci111111
[e-mail] mom
YSI.com @YSlinc facebook.com/myYSl MI
;ii
YSI and SensoLyt are registered trademarks. Y S '
Specifications are subject to change. Please visit YSI.corn to verify all specs.
02015 YSI,a xylem brand
I Printed in the USA.W118-02 August,2015 ® I.:'fry a xylem brand

L AIII AAA NiffilfmarmIllailliffirlie
. ,,,,,,,,„...m." II1LWI rccMc/rlt
tw
The Pulsatron Series A Plus offers manual function controls over Operating Benefits
stroke length and stroke rate as standard with the option to select
P g
9 p
external pace for automatic control. • Reliable metering performance.
• Rated"hot"for continuous duty.
Ten distinct models are available, having pressure capabilities to • High viscosity capability.
250 PSIG(17 BAR)@ 12 GPD(1.9 Iph),and flow capacities to 58
GPD(9.1 Iph)@ 100 PSIG(7.0 BAR),with a standard turndown • Leak-free, sealless, liquid end.
ratio of 100:1,and optional ratio of 2000:1. Metering performance is
reproducible to within±3%of maximum capacity.
Features
• Manual Control by on-line adjustable stroke rate and stroke
length. rl
• Highly Reliable timing circuit.
• Circuit Protection against voltage and current upsets.
• Solenoid Protection by thermal overload with auto-reset.
• Water Resistant,for outdoor and indoor applications.
• Internally Dampened To Reduce Noise.
• Guided Ball Check Valve Systems,to reduce back flow and ''_'
enhance outstanding priming characteristics.
• Few Moving Parts and Wall Mountable.
• Safe&Easy Priming with durable leak-free bleed valve ca
1111
assembly(standard). ;*,. - -•
• Optional Control: External pace with auto/manual selection. -'•
e
Controls +:
m Manual Stroke Rate -
Y
fill.:. TO •
Manual Stroke Length ,
•
•
e foe.d External Pacing—Optional `
P
M•
r
re M External Stop- Optional
.. External Pace With Stop- Aftermarket
Optional (125 SPM only) • KOPkits • Tanks
• Gauges • Pre-Engineered Systems
Control Options • Dampeners • Process Controllers
Standard • Pressure Relief Valves (MicroVision)
Feature Configuration Optional Configuration'
External Pacing - Auto/Manual Selection 2
External Stop - Auto/Manual Selection' ash • 41.11110 101°amp
External Pace wl Stop
(125 SPM only) Auto I Manual Selection 2 •��� • •— • •• « -
Manual Stroke Rate 10:1 Ratio �200:1 Rathifig/ '
Manual Stroke Length 10:1 Ratio 10:1 Ratio i �
Total Turndown Ratio 100:1 Ratio 2000:1 Ratio "-. _ ' --
Note 1:0n S2,S3&S4 sizes only. 41. CO \ .
Note 2:Not available on 2000:1 turndown pumps. . -110
Tended and Certified by WQA
against NSF/ANSI 61&372.
E
4• R t )41 ) PULSAfroT `' Series A Plus
" ` Pumps Electronic Metering Pumps
Winona,pawners.

rr rii i k i p Series A Plus
Specifications and Model Selection
MODEL LBC2 LB02 LBC3 LB03 LB04 LB64 LBC4 LBS2 LBS3 LBS4
Capacity GPH 0.25 0.25 0.42 0.50 1.00 1.25 2.00 0.50 1.38 2.42
nominal GPD 6 6 10 12 24 30 48 12 33 58
(max.) LPH 0.9 0.9 1.6 1.9 3.8 4.7 7.6 1.9 5.2 9.14
GFPP,PVDF,316SS
or PVC(W code)
Pressure' w/TFE Seals) PSIG 250(17) 150(10) 250(17) 150(10) 100(7) 100(7) 50(3.3) 250(17) 150(10) 100(7)
(max.) PVC(V code)Vibn or (Bar)
CSPE Seas/Degas
Liquid End 150(10) 150(10)
Connections: Tubing 1/4"D X 3/8'0D 3/8•D X 1/2'0D 1/4"ID X 3/8"OD
Piping 1/4'FNPT
Strokes/Minute SPM 125 I 250
Note 3:Pumps with rated pressure above 160 PSI will be de•rated to 160 PSI Max.when sslecting certain valve options,ass Price took for de
Engineering Data Engineering Data
Pump Head Materials Available: GFPPL Reproducibility: +/-3%at maximum capacity
PVC Viscosity Max CPS: 1000 CPS
PVDF Stroke Frequency Max SPM: 125/250 by Model
316 SS Stroke Frequency Turn-Down Ratio: 10:1/200:1 by Model
Diaphragm: PTFE-faced CSPE-backed Stroke Length Turn-Down Ratio: 10:1
Check Valves Materials Available: Power Input: 115 VAC/50-60 HZ/1 ph
Seats/O-Rings: PTFE 230 VAC/50-60 HZ/1 ph
CSPE Average Current Draw:
Viton @ 115 VAC;Amps: 0.6 Amps
Balls: Ceramic @ 230 VAC; Amps: 0.3 Amps
PTFE Peak Input Power: 130 Watts
316 SS Average Input Power @ Max SPM: 50 Watts
Alloy C Approvals: Conforms to ANSI/NSF STD.50
Fittings Materials Available: GFPPL ,
PVC
PVDF Custom Engineered Designs -
Bleed Valve: Same as fitting and check valve Pre-Engineered Systems
selected,except 316SS
Injection Valve&Foot Valve Assy: Same as fitting and check valve Pre-Engineered Systems
selected ems ® HIM Pulsafeeder's Pre-Engineered Systems are
Tubing: Clear PVC designed to provide complete chemical feed
solutions for all electronic metering
ite PEImportant:Material Code-GFPPL=GIassNflled Polypropylene, 0f 0 ii - applications.From stand alone simplex pH
control applications to full-featured,redundant
PVC=Polyvinyl Chloride,PE=Polyethylene,PVDF=Polyvinylidene
Fluoride,CSPE=Generic formulation of Hypalon,a registered trademark sodium hypochlorite disinfection metering,
of E.I.DuPont Company.Viton is a registered trademark of E.I.DuPont {/ these rugged fabricated assemblies offer turn-
Company.PVC wetted end recommended for sodium hypochlorite.
' ._ key simplicity and industrial-grade durability.
i The UV-stabilized,high-grade HDPE frame
offers maximum chemical compatibility and
structural rigidity.Each system is factory
Dimensions assembled and hydrostatically tested prior to
shipment.
Sariss A PLUS Dimensions(Inches) -
i Shipping ."-,=, E •.
Model No. A B C D E Weight BLEED VALVE Di, ,.
IIU a i!IL
LB02/S2 5.0 9.6 9.5 6.5 8.2 10 .T.
LBC2 5.0 9.9 9.5 6.5 8.5 10 'I' k."
LBC3 50 9.9 9.5 6.5 8.5 10LB03/S3 5.0 9.9 9.5 6.5 8.5 10 FD E :•4
LB04/S4 5.0 9.9 9.5 6.5 8.5 10 I 4111 r/ Itip \'
L964 5.0 9.9 9.5 6.5 8.5 10 i_ 1 II/ iini `
LBC4 5.0 9.9 9.5 6.5 8.5 10 -
NOTE Inches X 2.54=cm C - F"-A_-1
www.puisatron.com
Via amiss w w rrrwrw•
IMVLwTN/'CCi/Cli ❑a -�.CI27101 Airport Road -}: N: EMP025 E20
Punta Gorda, FL 33982 0 TSo•�
Phone: [phone] '
Fax: [phone] An ISO 9001 Certified Company

GALENE
AMF FILTERS
AMF filters are suitable for the widest range of applications and particularly effective for
removal of organic and/or inorganic suspended solids from water down to 5 micron and below.
The Deep Bed, multimedia filters are suited for many applications as re-use applications, water
pre-treatment applications for reverse osmosis and de-ionization systems, granular activated
carbon, production of drinking water, Iron & Manganese removal from surface, ground or well
water, waste water tertiary treatment, swimming pools filtration, cooling water side stream
recycling etc.
AMF filters use a unique design of a double chamber, divided by a welded
reinforced steel plate. The upper chamber contains the media;the lower chamber is empty and collects
the filtered water.The plate is covered by"mushroom"type diffusers which are PP, slotted conical
units. They disperse the water uniformly, using the whole media volume effectively, avoiding the
occurrence of channeling or caking when operated correctly.
The backwash process is designed to clean the filter media.The flow direction is reversed and
the flow rate is increased,thus causing a turbulent expansion of the multimedia as a fluidized bed.The
backwash process flushes out the entrapped debris effectively.After the backwash is completed,there
is a direct wash and then the filter resumes its normal filtering mode as clean as a new filter. Air scour
option is available if required.
Galene Water Treatment
516 NE 190th Street, Miami, Florida, 33179, USA
[phone]
www.Galenewt.com

GALENE
Normal working conditions are obtained when head loss is less than 0.3 bar(5 psi)at a
clean filter. If head loss exceeds 0.3 bar(5 psi) -filter is either partially clogged or operating under an
excessive flow rate.
The filter back flushing process starts automatically,according to one of the following criteria;
Differential pressure between the inlet and outlet of the filters,a preset time interval elapses,or
manually activation.
Below, a general schematic presenting the filter in operation and back-flushing mode.As can be
seen,there a uniform distribution created by the even dispersment of the nozzles on the lower
dispersing plate. In the back-flushing mode, it creates an even lift up of the media, reducing the
entrapment of particles.
FILTERING PROCESS BACKFLUSHING PROCESS
4 4
Filtering
1 f��1► /.lr f ���.` Media
Nik
111111111 ttttt .tt .tt ._,
/tr„
�t Filtering Elements
?0,7 . ' T1Z11' 170? e `,t (Nozzle)
l . 7" 4 4 3
r,f i�'Y. i j•'r t �ts7 t .rY i�rt 2t ] S 1 (� r 41
Lower Dispersing Plate
f 4
Galene Water Treatment
516 NE 190th Street, Miami, Florida,33179,USA
[phone]
www.Galenewt.com

GALENE
Material of Construction:
All filters installed in the filtration systems are manufactured from robust carbon steel ASTM-
A570-GR36. They ensure long lasting system operating life.
Protective Coating:
The coating process provides GALENE products with maximum anti-corrosion protection.
For filters up to 60" (included)the coating process is performed in seven stages, as follows:
1st stage: Automated shot blast cleaning of products to a level of SA 2.5 as per
international standard ISO 8501.
2nd stage: Phosphatization.
3rd stage: Rinsing.
4th stage: Sealing.
5th stage: Drying.
6th stage: Electrostatic polyester/epoxy spraying.
7th stage: Oven curing.
This process creates a perfectly coated product with a protective layer of 100 micron.
For filters 72" & bigger,the coating process includes two stages,as follows:
Stage 1: Automated shot-blast cleaning to a level of SA 2 %2 as per ISO 8501.
Stage 2: Internal coating of 2-3 layers with epoxy paint.
This lining process creates a perfectly coated product with a protective layer of 150-200 micron.
Galene Water Treatment
516 NE 190th Street, Miami, Florida, 33179, USA
[phone]
www.Galenewt.com

Clack Filter-Ag Plus° is a clinoptilolite natural media with a large
surface area and microporous structure, which can be used as a highly
efficient filter media for the reduction of suspended matter.
Fi• r-A Plus®1
t�
1
ADVANTAGES Clack Filter-Ag Plus is a unique natural Filter-Ag Plus prevents a rapid buildup of
ore called clinoptilolite that has many head loss and blinding problems that are
• Deep bed filtration results in superior outstanding advantages over common associated with typical sand filters.The
water quality and reduces the load granular filter sands and multimedia used longer filter run times reduce backwash
on downstream equipment. for suspended solids reduction.Viewed frequency,which provides conservation of
• High sediment removal capacity under an electron scanning microscope, water.This ideal combination of particle
results in longer filter runs,with the granules reveal an angular shape, shape,texture and porosity make it a good
a substantial savings in backwash rough surface and microporous void choice where quality water filtration and
water and time out of service. spaces as small as 3 microns.This creates water conservation are important.
• High service flow rates result in a surface area over 100 times greater than Substantial savings can be realized
lower equipment costs and a savings silica sand.The angularity of the granules when designing a system using Clack
in space. and the tapered internal pore spaces allow Filter-Ag Plus. Its low pressure drop, high
• Reduced shipping cost due to lighter for reduction of dirt, silt and organic matter service flow rates and high bed loadings
weight/cu.ft. suspended in water by bridging, straining combined with lower backwash frequency
• Replacement of multimedia with and adhesion.The rough surface and allow economy in equipment downsizing
Filter-Ag Plus in existing installations internal porosity provide a high surface and reduced pumping requirements.
may increase filter capacity. area for efficient reduction of suspended Its low density also saves on handling
• Filter-Ag Plus is an all-natural, matter. Utilizing deep bed filtration can expense and shipping costs.
environmentally safe product. typically reduce suspended solids down to Clack Filter-Ag Plus can be applied to
the 5 micron or less range. Filter-Ag Plus' systems designed for either pressure or
PHYSICAL PROPERTIES structure typically creates less pressure gravity flow. Because of its unique physical
• Color: Light tan to near white loss through the filter and allows deeper characteristics, Filter-Ag Plus can be used
• Dry Bulk Density:50 lbs/cu.ft sediment penetration into the bed for to replace multimedia(graded density)
higher sediment loading and longer filter filter designs.
• Specific Gravity:2.2 g/cc runs.The deep bed filtration capacity of
• Mesh Size: 14x30
• Effective Size:0.55mm
• Uniformity Coefficient: 1.8
• Hardness:4-5(Mohs Scale)
CONDITIONS FOR OPERATION
•Water pH:Wide range
• Max.Water Temp.: 140°F/60°C
• Bed Depth:24-36 inches
.
.,.
• Freeboard:50%of bed depth
• Backwash Flow Rate: 15-20 gpm/
sq.ft.
• Backwash Bed Expansion:30-40%
of bed depth .
• Service Flow Rate: 12-20 gpm/sq.ft. * ��� '
• Local conditions may require lower
flow rates
•A gravel support bed is required
•Allow bed to saturate before initial ..
backwash : , _ `
# ma ,

Service Flow Pressure Drop Backwash Bed Expansion
1.0 _... so°ro
0.9
m• 0.8 :::
„Am
1 032 11:
o
zz,
O▪ 0.6 -alp. G� -- bp 16G1
E 0.5 4 2 w n 30% ��\ lti�°G
FAI
a g0.3 � 20°� -Wv00.
�• 0.2 I A
-0m 10°k
a
0.1 INI---
0.0 0%
0 5 10 15 20 25 0 5 10 15 20 25
Flow Rate Flow Rate
(Gallons per Minute/Square Foot of Bed Area) (Gallons per Minute/Square Foot of Bed Area)
0
Certified to NSF/ANSI Standard 61
ORDER INFORMATION
Part No. Description Cu. Ft./Bag Wt./Cu. Ft.* Bags/Pallet Weight/Pallet Pallet Dimensions
A8023 Filter-Ag Plus® 1 50 lbs. 40 2050 lbs. 40"x 48"x 44"
*Weight per cubic foot is approximate.
The information and recommendations in this publication are based on data we believe to be reliable.They are offered in good faith,but do not imply
any warranty or performance guarantee,as conditions and methods of use of our products are beyond our control.As such,Clack makes no express
or implied warranties of any kind with respect to this product, including but not limited to any implied warranty of merchantability or fitness for a
particular purpose.We recommend that the user determine whether the products and the information given are appropriate,and the suitability and
performance of our products are appropriate,by testing with its own equipment.Specifications are subject to change without notice.
The information and recommendations given in this publication should not be understood as recommending the use of our products in violation of any
patent or as a license to use any patents of the Clack Corporation.
The filter medias listed in this brochure do not remove or kill bacteria.Do not use with water that is microbiologically unsafe or of unknown quality
without adequate disinfection before or after the system.
Clack will not be liable under any circumstance for consequential or incidental damages, including but not limited to,lost profits resulting from the use
of our products.
CALIFORNIA PROPOSITION 65 WARNING:This product contains crystalline silica which is known to the State of California to cause cancer and other
substances which are known to the State of California to cause cancer,birth defects and reproductive harm.
CICoCV ClackCorporation
'� 4462 DURAFORM LANE•WINDSOR,WISCONSIN 53598-9716 USA
www.clackcorp.com PHONE[phone] FAX[phone] SALES/CUSTOMER SERVICE FAX[phone] Form No.2718.9/3/2008