WQ0005763_Application_20100715 (2)

McGifl
A S S O C I A T E S
July 15, 2010
Mr. Jon Risgaard
North Carolina Department of Environment
And Natural Resources
Division of Water Quality
2728 Capital Boulevard
Raleigh, North Carolina 27604
Dear Mr. Risgaard:
r"ECEw ®
i' JG 13 2610
Asheville regional Office
Re: Distribution of Residual Solids
Tuckaseigee Water and Sewer Authority
Wastewater Treatment Plant No. 1
Jackson County, North Carolina
On behalf of the Tuckaseigee Water and Sewer Authority (TWSA), please find attached
application for major modification to the Distribution of Residual Solids Permit No.
WQ005763. TWSA is expanding WWTP No. 1 from 1.5 mgd to 3.5 mgd and will utilize a
sludge dryer to produce a. ' Class A residual. Application package includes "Distribution of
Residuals Solids Application"; "Residuals Source Certification Attachment(RSCA) for WWTP
No. 1 and RSCA for Whittier, application fee, three (3) sets of detailed plans and
specifications, Engineering Calculations, and Residuals .Management Plan. Note that the
Whittier Facility has not produced any residuals to date and sampling data in RSCA is from
WWTP No. 1. An Authorization to Construct has been previously issued by Construction,
Grants and Loans for the proposed project. Information required by Item 5 in the application is
included in the Residuals Management Plan.
If you have any questions or need additional information please don't hesitate to give
me a call at 828-252-0575 or email at davidh e,mcgillengineers.com. Thank you for your
assistance.
Sincerely,
McGILL ASSOCIATES, P.A.
DAVID L. HONEYCUTT, PE
Project Engineer
Enclosures
cc: Joe Cline, Tuckaseigee Water and Sewer Authority RECEIVED / DENR / DWQ
Harry Buckner, PE, McGill Associates, P.A. Aquifer Protection Section
P:\2005\05734\Letters\jrI3julyIO.doc JUL 19 2010
E n g i n e e r i n g 0 P l a n n i n g F i n a n c e
McGill Associates, P.A. • P.O. Box 2259, Asheville, NC 28802 • 55 Broad Street, Asheville, NC 28801
828-252-0575 • Fox.828-252-2518

AQUIFER PROTECTION SECTION
APPLICATION REVIEW REQUEST FORM
Date:
To: ® Landon Davidson, ARO-APS ❑ David May, WaRO-APS
❑ Art Barnhardt, FRO-APS ❑ Charlie Stehman, WiRO-APS
❑ Andrew Pitner, MRO-APS ❑ Sherri Knight, WSRO-APS
❑ Jay Zimmerman, RRO-APS
From: Alice M. Wessner ®LAU
E-Mail: [e-mail]
Telephone: [phone]
A. Permit Number: WQ005763
C. Facility/Operation:
❑ Proposed ® Existing
D. Application:
MG 13 2610
Asheville Regional Office
Fax:[phone] Aquifer Protection
B. Owner: Tuckaseigee WASA
❑ Facility ❑ Operation
I. Permit Type: ❑ Animal ❑ Surface Irrigation ❑ Reclaimed ❑ H-R Infiltration
❑ Recycle ❑ I/E Lagoon ❑ GW Remediation (ND)
❑ UIC - (5A7) open loop geothermal ❑ Single Family Residence
® Residuals
2. Project Type: ❑ New ® Major Mod. ❑ Minor Mod. ❑ Renewal ❑ Renewal w/ Mod.
E. Comments/Other Information: ❑ I would like to accompany you on a site visit.
Attached, you will find all information submitted in support of the above -referenced application for your
review, comment, and/or action. Within 30 calendar days, please take the following actions:
® Return a Completed APSARR Form.
❑ BIMS indicates monitoring wells locations are not complete. Please update monitoring well
locations not currently in BIMS.
® BIMS indicates ongoing ❑ NDMR ❑NDAR ❑ GW monitoring violations. Please investigate
reoccurring compliance issues and summarize results in staff report. NOV for Monitoring
❑ Attach Well Construction Data Sheet.
❑ Process Attachment B for Certification by the Land Application Unit (LAU).
❑ Issue an Attachment B Certification from the RO.*
*coordinating site visits and reviews, as well as additional information requests with other RO-APS
representatives in order to prepare a complete Attachment B for certification. Refer to the RPP SOP for
additional detail.
Please indicate the name and date assigned in the spaces below, make a copy of this sheet, and return it to
the appropriate Central Office -Aquifer Protection Section contact person listed above.
RO-APS Reviewer: --,7, C '-) -'_� Date:
FORM: APSARR 03/10 Page 1 of 1

Price, Bev
From:
Wessner, Alice
Sent:
Friday, October 08, 2010 11:31 AM
To:
Price, Bev
Subject:
FW: Tuckaseigee-Whittier RSCA
Attachments:
Whittier RSCA.pdf
For your records.
Alice M. Wessner
Environmental Engineer
Land Application Unit
Aquifer Protection Section
Division of Water Quality
1636 Mail Service Center
Raleigh, NC 27699-1636
919-715-5208
919-715-0588 (fax)
http://h2o.enr.state.nc.us/aps/lau.htm
From: David Honeycutt[mailto:[e-mail]]
Sent: Friday, October 08, 2010 8:10 AM
To: Wessner, Alice
Subject: Tuckaseigee-Whittier RSCA
Alice,
Please find attached RSCA for Whittier. Per our discussion as they have not hauled any solids from the Whittier facility
(at the time of application) there is no sample data available for solids produced at that facility. It is a 100% domestic
facility and sample data in the RSCA is for the Tuckaseigee Water and Sewer Authority Plant No. 1 which is expected to
be similar. Please let me know if you are missing any other supporting documentation listed on the last page of this PDF.
Thanks for your assistance on this permit modification. Please don't hesitate to give me a call or email if you have any
questions. Thanks,
David L. Honeycutt, PE
Project Engineer
McGill Associates, P.A.
Phone [phone]
Fax [phone]

State of North Carolina
Department of Environment and Natural Resources
Division of Water Quality RECEIVED / DENR /D WQ
DISTRIBUTION OE RESIDUAL SOLIDS Protection Section
JUL(FORM: DRS 070807) 19 2010
The Division of Water Quality will not accept this application unless all the instructions are followed. Plans and
specifications must be prepared in accordance with 15A NCAC 2T .1100, and good engineering practices.
Failure to submit all required items will lead to additional processing and review time.
For more information, visit our web site at: http://h2o.e ar.state.n.c.iis/laufinain.html
A. Application Form (All Application Packages):
✓ Submit one original and two copies of the completed application package. Any changes made to this form will result in the
application being returned. The Division of Water Quality will only accept application packages that have been fully
completed and all applicable items are addressed.
✓ The project name should be consistent on the plans, specifications, etc.
✓ The signing official must meet the criteria stipulated in 15A NCAC 2T .0106(b). An alternate person may be designated as
the signing official, provided that a delegation letter from a person who meets the referenced criteria is submitted. The
delegation letter does not have to be resubmitted if the signing official has not changed since the last permitting action
associated with this residuals land application program.
✓ If this project involves a modification of an existing permit, submit one copy of the existing permit.
✓ Please submit this application form at least 180 days prior to the expiration date on the existing permit, or 90 days prior to
operation of proposed facility(ies) for application packages involving new or changes to treatment and storage units.
B. Application Fee (New and Major Modification Application Packages):
✓ For new permits submit a check in the amount of $1,310 if over or equal 3,000 dry tons per year are generated for disposal or
$810 if less 3,000 dry tons per year are generated for disposal, made payable to: North Carolina Department of Environment
and Natural Resources (NCDENR). Major modification fee are $395 and $245, respectively.
C. Cover Letter (All Application Packages):
✓ Submit a cover letter, which lists all item and attachments included in the application package as well as a brief project
description.
✓ If necessary for clarity, include attachments to the application form. Such attachments will be considered part of the
application package and should be numbered to correspond to the section to which they refer.
D. Retailed Plans and Specifications (Application Packages Involving New or Changes to Treatment and Storage Units):
✓ Submit three sets of detailed plans and specifications signed, sealed, and dated by a NC Professional Engineer per 15A
NCAC 2T .1104(a). Specifications for standard equipment may only be omitted for municipalities with approved standard
specifications, but use of the standard specifications must be noted on each sheet of the plans.
✓ Plans must include the following minimum items: a general location map, a topographic map, plan and profile view of the
residuals treatment and storage units as well as the proximity of the residuals treatment and storage units to other utilities and
natural features within 500 feet of all treatment and storage facilities, and detail drawings of all items pertinent to the
residuals treatment and storage units. Depict minimum separations required in 15A NCAC 2T .1108 (a) on the plans.
✓ Specifications must include, at a minimum, the following for all items pertinent to residuals treatment and storage units:
description of materials to be used, methods of construction, quality of construction testing procedures to ensure the integrity
of the final product in accordance with 15A NCAC 2T .1104(a)(2)(B), including leakage and pressure testing as appropriate.
Plans and specifications must not be labeled with preliminary phrases (e.g., FOR REVIEW ONLY, NOT FOR
CONSTRUCTION, etc.) that indicate that they are anything other than final plans and specifications. However, the plans
and specifications may be labeled with the phrase: FINAL DESIGN — NOT RELEASED FOR CONSTRUCTION.
E. Engineering Calculations (Application Packages Involving New or Changes to Treatment and Storage Units):
✓ Submit three copies of all design calculations signed, sealed, and dated by a NC Professional Engineer per 15A NCAC 2T
.1104(a).
***INSTRUCTIONS CONTINUE ON NEXT PAGE (, r V E D
FORM: DRS 070807 Page 1 of 6 A,'��a 1� 24�tachinenU Order 1
.Anhovill' Regional Office

r
F. Environmental Assessments (Maybe Required— See 15A NCAC 1C .0300):
✓ Submit one copy of the Findings of No Significant Impact (FONSI) or Environmental Impact Statement (EIS). Also, include
information on any mitigating factor(s) from the Environmental Assessment (EA) that impact the construction of the
residuals treatment and storage facilities. An EA may also be required for private systems if any public funds and/or lands
are used for the construction of the subject facilities.
G. Residuals Source Information (All Application Packages):
✓ Attach FORM: RSCA (Residuals Source Certification Attachment) and all associated documentation.
✓ FORM: RSCA can be downloaded at http://h2o.enr.state.nc.us/lau/gl2lications.litml
2610
Asheville Regional Office
--A-g�aifer Protection
FORM: DRS 070807 Page 2 of 6
Attachment Order 1

State of North Carolina
Department of Environment and Natural Resources
Division of Water Quality
DISTRIBUTION OF RESIDUAL SOLIDS
(FORM: DRS 070807)
(THIS FORMMAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL)
Application Number: (to-b"o»apteted-by L)-W-
I. OWNERSHIP INFORMATION: RECEIVED
1. Specify whether the process facility is owned by: `A.Ijb Zb ot�
❑ County; ❑ Federal; N Municipal; ❑ State; ❑ Non -Government. g Asheville Regional Office
I /= ouifer Protection
2. Owner's name (please specify the name of the municipality, corporation, individual, etc.):
TUCKASEIGEE WATER AND SEWER AUTHORITY
Mailing address: 1246 West Main Street
City: Sylva State: North Carolina Zip: 28779
Physical address: 1246 West Main Street
City: Sylva State: North Carolina Zip: 28779
Telephone number: ( 828 ) 586-5189 Facsimile number: ( )
E-mail address: [e-mail]
3. Signing official's name and title: (See Instruction A)
Robert J. Cline. Executive Director
Mailing address: 1246 West Main Street
City: Sylva State: North Carolina Zip: 28779
Physical address: Same as above
City:
State:
Telephone number: ( 828 ) 586-5189 Facsimile number: (
E-mail address: [e-mail]
H. PERMIT INFORMATION:
Zip:
1. Application is for: ❑ new; ® modified; ❑ renewed permit (check all that apply).
2. Fee Submitted: $ 245 (See Instruction P)
3. If this application is being submitted to renew or modify an existing permit, provide the following:
Permit number: WQ0005763 (please attach a copy of the existing permit).
Most recent issuance date: August 26, 2005 , and the expiration date: July 31, 2010
RECEIVED IDENRIDWQ
Aquifer Protection Section
FORM: jDRS 070807 Page 3 of 6 JUL 19 2010 Attachment Order 1

M. FACILITY INFORMATION:
1. Name of facility where residuals are processed:
TWSA WWTP Plant No. 1
Physical address: 1871 North River Road
City: Sylva State: North Carolina Zip: 28779
Telephone number: ( 828 ) 586-9318 Facsimile number: (
County where facility is located: Jackson County
Latitude: 350 21' 02" Longitude: 830 14' 15" of residual process facility.
2. Facility contact (person familiar with residuals preparation):
Stan Bryson
Mailing address: 1246 West Main Street
City: Sylva State: North Carolina Zip: 28779
Physical address: 1871 North River Road
City: Sylva State: North Carolina Zip: 28779
Telephone number: ( 828 ) 586-9318 Facsimile number: ( )
E-mail address:
3. Program contact person and/or consulting firm who prepared application (If different from the above):
Harry B. Buckner P E McGill Associates P.A.
Mailing address: Post Office Box 2259
City: Asheville State: North Carolina Zip: 28802
Physical address: 55 Broad Street
City: Asheville State: North Carolina Zip: 28801
Telephone number: ( 828 ) 252-0575 Facsimile number: ( 828 ) 252-2518
E-mail address: hbbuckner(@mc ig llenaineers com
4. Is the residual process facility also the generator? ® Yes; ❑ No
5. If the residual process facility is not the same as the generator, please specify delivery frequency and quantity of residual to
be processed: n/a
6. Length of residuals storage at facility: 30 (liquid) days (the Division requires a
are separate from treatment system, i.e. not in clarifiers, aeration basins, etc.).
IV. RESIDUALS QUALITY INFORMATION:
1. Specify if residuals are regulated under (check one): ® 40 CFR Part 503 or
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AaLlifer Protect_ iOn
FORM: DRS 070807
Page 4 of 6
Attachment Order 1

up
2. Specify how these residuals will be distributed:
❑ sold or given away in bags or other containers; ® lawn (bulk); ® home garden (bulk);
❑ other;
3. Complete the following if residuals are to be mixed with other materials:
Type of Materials I Amounts to be added
per 1.0 dry ton of residuals (dry ton)
4. Approximate amounts of the final product to be distributed 659 dry tons per year.
5. Provide a description of the onsite storage management plan for the treated residuals (including estimated average and
maximum storage times prior to distribution): Solids from the diver will be discharged to an 86 cubic foot storage
hopper. Solids from the storage hopper will be conveyed by a blower system to a 94 cubic yard storage silo. Dried sludge
will be conveyed from the storage silo to the end -users The storage silo will provide 35.2 days of storage at the permitted
design flow for the facility. The anticipated average storage time is 14 days.
ADDITIONAL REQUIRED INFORMATION:
1. Provide a narrative explaining the following:
a. How will the materials be handled and transported from where the residuals were produced to where it will be
treated?
b. How will the residuals be processed/treated (attach process flow diagram).
c. How will leachate collection be handled?
d. Where will the residuals be stored until processed?
e. How will the final product be distributed (packaging)?
2. Attach a marketability statement detailing destinations and approximate amounts of the final product to be distributed.
3. Provide either a label that shall be affixed to the bagged processed residual or an information sheet that shall be provided
to the person who receives the processed residual. The label or information sheet shall contain, at a minimum, the
following information:
a. The name and address of the person who prepared the residual that is sold or given away in a bag or other container
for application to the land.
b. A statement that application of the residual to the land is prohibited except in accordance with the instructions on the
label or information sheet.
c. A statement that the residuals shall not be applied to any site that is flooded, frozen or snow-covered.
d. A statement that adequate procedures shall be provided to prevent surface runoff from carrying any disposed or stored
residuals into any surface waters.
e. Information on all applicable setbacks in accordance with 15A NCAC 02T .1108(b).
f. A statement that the residuals shall be applied at agronomic rates and recommended rates for intended uses.
dA°JG 1 ^ 2G I0
FORM: DRS 070807 Page 5 of 6 P Asheville regional Off&ttacl" ent Order 1
Atmil`or Protection

Professional Engineer's Certification: (Application Packages Involving New or Changes to Treatment and Storage Units)
I, Harry B. Buckner, P.E. , attest that this application for Tuckaseigee Water and Sewer Authority
Wastewater Treatment Plant No. 1
has been reviewed by me and is accurate and complete to the best of my knowledge. I further attest that to the best of my knowledge
the proposed design has been prepared in accordance with the applicable regulations. Although certain portions of this submittal
package may have been developed by other professionals, inclusion of these materials under my signature and seal signifies that I
have reviewed this material and have judged it to be consistent with the proposed design.
North Carolina Professional Engineer's Seal, Signature, and Date:
,`�� till !0
•• �s
• v
'L
0
a
g SEAL • 0
22541 a
a
Applicants Certification: ordReaaittd
The applicant or any affiliate has not been convicted of an environmental crime, has not abandoned a wastewater facility without
proper closure, does not have an outstanding civil penalty where all appeals have been exhausted or abandoned, are compliant with
any active compliance schedule, and do not have any overdue annual fees under Rule 2T .0105.
® Yes ❑ No, Explain;
I, Robert J. Cline , attest that this application for Tuckaseigee Water and Sewer Authority
has been reviewed by me and is accurate and complete to the best of my knowledge. I understand that if all required parts of this
application are not completed and that if all required supporting information and attachments are not included, this application
package will be returned "e as incpnplete.
Signature
Date ?r � r /d
THE COMPLETED APPLICATION PACKAGE,
INCLUDING ALL SUPPORTING INFORMATION AND MATERIALS,
SHOULD BE SENT TO THE FOLLOWING ADDRESS:
NORTH CAROLINA DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES
DIVISION OF WATER QUALITY
AQUIFER PROTECTION SECTION
LAND APPLICATION UNIT
By U.S. Postal Service:
1636 MAIL SERVICE CENTER
RALEIGH, NORTH CAROLINA 27699-1636
By Courier/Special Delivery:
2728 CAPITAL BOULEVARD
RALEIGH, NORTH CAROLINA 27604
TELEPHONE NUMBER: [phone]
FORM: DRS 070807 Page 6 of 6 Attachment Order 1

State of North Carolina
Department of Environment and Natural Resources
Division of Water. Quality
RESIDUALS SOURCE CERTIFICATION ATTACHMENT
(FORM: RSCA 070807)
(THIS FORMMAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL)
The Division of Water Quality (Division) will not accept this attachment unless all the instructions are
followed, Failure to submit all required items will lead to additional processing and review time.
For more information, visit our web site at: h1tp•//It2o erv:state.itc.irsllatilntaln.htnil
.INSTRUCTIONS TO THE APPLICANT: _
A. Attachment Form:
✓ Do not submit this attachment form for review without a corresponding residuals program application
form (FORM: NDRLAP, FORM: DRS, or FORM: SDRS).
✓ Any changes to this attachment form will result hi the application package being returned.
✓ For new residuals programs or renewe residuals programs, submit a separate attaclunent form for each
residuals source -generating facility to be certified for this residuals program.
✓ For modified residuals programs in which any modification to the certified residuals -source generating
facilities is proposed, submit a separate attachment form for oil those residuals source -generating facilities
that are affected by the proposed modification.
✓ The attachment should be organized prior to submission in the following order (i.e., by facility):
♦ Attachment Order 2: Residuals;Source Certification Attachment (FORM: RSCA).
➢ Attachment Order 2-a: Vicinity map.
➢ Attachment Order 2-b: Process flow diagram and/or narrative.
➢ Attachment Order 2-c: Quantitative justification for residuals production rate.
➢ Attachment Order 2-d: Sampling plan.
➢ Attaclunent Order 2-e: Laboratory analytical reports'and operational data.'
B. Residuals. Source -Generating Facility hiformatlon:
✓ Attach a vicinity map that shows the location of the facility and meets all of the criteria in time latest version of
the document entitled "Guidance for the Preparation of Vicinity/Buffer Maps for North Carolina Residuals
Permitting Programs." . -
✓ Attach a detailed narrative and/or process flow diagram that describes how the residuals are to be generated,
treated, processed, and stored at the facility.
✓ Attach a quantitative justification for the value provided in Item I. 8. Ensure that the amount of residuals
listed is the maximum amount expected to be generated by the facility for the life of time permit. In addition,
ensure that this amount is equivalent to that which is actually to be land applied, distributed, and/or disposed,
including any chemicals, amendments, or other additives that are added to the residuals during processing.
C. Residuals Quality Information: . • . . • . • • 1.
✓ Attach a detailed sampling plan for the residuals source -generating facility. Ensure that the plan identifies
sampling points, sampling. frequency, sample type, as,well as-the•Division-certified laboratory to be used. In
addition, ensure that the plan details how the facility. and/or the residuals are monitored for any applicable
pathogen reduction and vector attraction reduction requirements. Note that all sampling and monitoring must
be completed on the residuals as they are to be land applied, distributed, and/or disposed.
✓ Attach reports for all laboratory analyses used to complete this attachment form. Attach documentation that
time facility complies and/or the residuals comply with any applicable pathogen reduction and vector
attraction reduction requirements.
✓ Item II. 3. does not have to be completed for facilities that are less than 0.5 MGD in design flow that treat
I 00°/anon-inunicipali• domestic wastewater. only.
FORM: RSCA 070807 Page 1 of 8 Attachment Order 2

State of North Carolina
Department of Environment and Natural Resources
Division of Water Quality
RESIDUALS SOURCE CERTIFICATION ATTACHMENT
(FORM: RSCA 070807)
(THIS FORMMAYBE PHOTOCOPIED FOR USE ASAN ORIGINAL)
Applicant's name: Tuckaseigee Water and Server Authority
Check all that apply: ❑ NEW RESIDUALS PROGRAM ❑ RENEWED RESIDUALS PROGRAM
® INCREASE ❑ DECREASE the maximum permitted annual dry tonnage for this residuals source -
generating facility certified for this residuals program.
Current: 250 Dry Tons/yr. and proposed: 659 Dry Tons/yr.
® ADD ❑ DELETE this residuals source -generating facility to/from those certified for this
residuals program.
I.
❑ OTHER Explain:
RESIDUALS SOURCE -GENERATING FACILITY INFORMATION (See Instruction B.):
1. Name of facility: TWSA Whittier Sanitary District W WTP
2. Facility permit holder: Tuckaseiaee Water and Sewer Authority
Facility permit holder is (check one): ❑ federal, ❑ state, ® local government, or ❑ private.
Facility permit number: NPDES No. NCO087602
Facility permit issued by (check one): ® Div. of Water Quality, ❑ Div. of Environmental Health, or
❑ other (explain: )•
3. if the facility permit is not issued by the Div. of Water Quality, complete the following:
a. Facility contact person and title:
Facility complete mailing address:
City: State: Zip:
Telephone number: ( ) Facsimile number: ( }
E-nail address:
b. Facility complete location address:
City: State: Zip:
Latitude: and longitude:
4. County where facility is located: Jackson County
5. Purpose of the facility (check one):
® treatment of municipal wastewater, ❑ treatment of 100% domestic wastewater,
❑ treatment of potable water, ❑ treatment of 100% industrial wastewater,
❑ treatment of industrial wastewater mixed with domestic wastewater, or
(approximate percentages: % industrial and % domestic)
❑ other (explain:
FORM: RSCA 070807 Page 2 of 8 Attachment Order 2

6. Does the facility have an approved pretreatment program: ❑ yes ® no
7. Facility.permitted/dQsign flow: 0.1 MGD and facility average daily flow: <0.005 MGD.
B. Average amount of residuals being generated at this facility �_ dry tons per year.
9. Specify the following regarding- lreatnieut and storage,volumes available at the facility:
Type and volume of residuals treatment:. See Page 3 of the attached Residuals Management Plan.
Type and volume of residuals storage (i.e,, outside of residuals treatment units): Dried Solids will be
stored in a 94 CY storage silo which providesa roxim el 36.1 days of storage at the permitted design
flow for the facility.
II. REsIDUALs QUALITY INTORMATION (See Instruction C.):
1. Specify if residuals are regulated under (check one): ® 40 CFR Part 503 or ❑ 40 CFR Part 257.
2. Specify if residuals are intended for (check one):
® Land Application/Distribution (Class A or Equivalent).
Complete all items EXCEPT Items II.4b., 7b., and 7c.
❑ Land Application (Class B or Equivalent).
Complete all items EXCEPT items II.4b., 7a., and 7c.
❑ Surface Disposal.
Complete all items EXCEPT Items H. 4a., 5., 7a., 7b., and 8.
FORM: RSCA 070807 Page 3 of 8 Attachment Order 2

3. Hazardous Waste Determination: Complete the following to demonstrate that the residuals are non-
hazardous under RCRA:
a. Are the residuals are listed in 40 CFR §261.31-§261.33: ❑ yes ® no.
If yes, list the number(s):
b. Specify whether or not the residuals exhibit any of the characteristics defined by 40 CFR §261.21-
§261.24: ❑ yes ® no. Fill in the following tables with the results of the latest toxicity
characteristic leaching procedure (TCLP) analysis as well as those for corrosivity, ignitability, and
reactivity: laboratory: Pace Analytical, Asheville and date of analysis: 8/25/2009 (3/11/lQ)
Passed corrosivity test: ® yes ❑ no. pH: 11.16 (lime stab) 6.54 dewatered s.u. (2 < pH < 12.5).
Passed ignitability test: ® yes ❑ no. Flashpoint: >140 °F (> 140°F).
Passed reactivity test: Z. yes ❑ no. HCN: ND mg/kg (<250) & HzS: ND mg/kg (<500).
TCLP Parameter
Limit
OWL)
Result
NgQ
TCLP Parameter
Limit
NA)
Result
(i)tg/L)
Arsenic '
5.0
ND
Hexachlorobenzene
0.13
ND
Barium
100.0
0.039
Hexacliloro-1,3-Butadiene
0.5
ND
Benzene
0.5
ND
Hexachloroethane
3.0
ND
Cadmium
I.0
ND
Lead
5.0
ND
Carbon Tetrachloride
0.5
ND
Lindane
0.4
ND
Chlordane
0.03
ND
Mercury
0.2
ND
Chlorobenzene
100.0
ND
Methoxychlor
10.0
ND
Chlorofonn
6.0
ND
Methyl Ethyl Ketone
200.0
0,319
Chromium
5.0
ND
Nitrobenzene
2.0
ND
m-Cresol
200.0
Pentachlorophenol
100.0
ND
o-Cresol
200.0
ND
Pyridine
5.0
ND
p-Cresol
200.0
Selenium
1.0
ND
Cresol
200.0
0.218
Silver
5.0
ND
2,4-D
10.0
ND
Tetrachloroethylene
0.7
ND
1,4-Dichlorobenzene
7.5
ND
Toxaphene
0.5
ND
1,2-Dicltloroetliane
0.5
ND
Trichloroethylene
0.5
ND
1,1-Dichloroethylene
0.7
ND
2,4,5-Trick loropliettol
400.0
ND
2,4-Dinitrotoluene
0.13
ND
2,4,6-Trichlorophenol
2.0
ND
Endrin
0.02
ND
2,4,5-TP (Silvex)
1.0
ND
Heptachlor and its Hydroxide
0.008
ND
Vinyl Chloride
0.2
ND
FORM: RSCA 070807 Page 4 of 8 Attachment Order 2

4. Metals Determination:. Complete one of the following tables (i.e., as applicable) to demonstrate that the
residuals do not violate the ceiling concentrations for metals regulated under 15A NCAC 02T .1105.
a. For Class A or Class B: Fill in the following table with the results of the latest analyses (i.e., on a dry
weight basis) for the following metal parameters:
Laboratory: Pace Analytical Asheville/Huntersville, NC and date of analysis: 8/24/2009
Parameter
Ceiling
Concentration
'Limits
"(ClnssA &ClassB
(nrg1kg)
Monthly Average
Concentration Limits
(For Class A Only)
(rng/kg) :.
Result
Ongft)
Arsenic
75
41
6.6
Cadmium
85
39
0.6.
Copper
4,300
1,500
104
Lead
840
300
6.0
Mercury
57
17
0.50
Molybdenum
75
n/a
1.0
Nickel
420
420
4.6
Selenium
100
100
5.8
Zinc
7,500,
2,800
324
b. For Stu;%Cce Disposal: Fill in the following table with the results of the latest analyses (i.e., on a dry
weight basis) for the.following metal parameters:
Laboratory: and date of analysis:
Closest Distance
to. Property Lines
(neters)
Arsenic
(tng/k)
Chromium
(ing/kg)
Nickel
(rng/kg)
> 0 but < 25
30
200
210
? 25 but < 50
.. ' , 34
220
240
> 50 but < 75
39
260
270
>_ 75 but < 100
46
300
320
>_ 100 but < 125
53
360
390
> 125 but < 150
62
450
420
>_ 150
73
600
420
FORM: RSCA 070807 Page 5 of 8 Attachment Order 2

5. Nutrient/1llicronutrient Determination: Complete the following:
a. Total solids: 57.2 %.
b. Fill hi the following table with the results of the latest analyses (i.e., on a dry weight basis) for the
following nutrient and micronutrient parameters: Iaboratory: Pace Analvtical Asheville/Huntersville,
NC and date of analysis: „ 8/24/2009 ,
Parameter
Result
(niglkg, dq height)
Aluminum
9,460
Ammonia -Nitrogen
286
Calcium
331,000
Magnesium • ,
;.'-2,920.•... .
Nitrate -Nitrite Nitrogen
ND
pH (Standard Unit)
12.4
Phosphorus
155
Potassium
3,690 -
Sodium
ND
Total Kjeldalil Nitrogen
11,900 ..;
c. Using the results listed in Item II.Sb, above, calculate the sodium adsorption ration (SAR): 0 .
d. Specify the mineralization rate to be used in calculating the plant available nitrogen (PAN) of the
residuals: 30 %. This rate is a ® default value or ❑ actually established.
If the residuals are not generated from the treatment of municipal or domestic wastewater, explain or
provide technical justification as to why the selected default value is appropriate to be applied to these
residuals:
Calculate the PAN for the residuals (i.e., on a dry weight basis) and list the results in the following table:
Application Method
First Year
Five -Year
PAN
Maximum Adjusted
PAN
0119/W
(mgft)
Surface
3,630
5,625
Injection/Incorporation
3,770
5,765
c. Are the residuals a registered fertilizer with the NC Department of Agriculture and Consumer Services:
❑ yes ® no. If yes, provide date of registration approval:
the current registration number:
and the fertilizer equivalent: %, %, and %.
FORM: RSCA 070807 Page 6 of 8 Attachment Order 2

6. Other Pollutants Determination: Specify whether or not.there are any other pollutants of concern in the
residuals and list the results of the latest analyses: No other pollutants of concern.
7. Pathogen Reduction Determination: Specify which alternative(s) will be used to meet the pathogen
reduction requirements:
a. For C1assA orEquivalent:
® A fecal coliforn density that is demonstrated to be less than 1,000 MPN per gram of total dry solids.
OR
❑ A salmonella sp. density.that is demonstration to be less than 3 MPN per 4 grains of total dry solids.
AND one of the following (except for residuals regulated under 40 CFR Part 257 that are to be distributed):
❑ Alternative 1 [40 CFR §503.32 (a)(3)] - Time/Temperature Compliance.
❑ Alternative 2 [40 CFR §503.32 (a)(4)] - Alkaline Treatment.
❑ Alternative 3 [40 CFR §503.32 (a)(5)] - Prior Testing for Enteric Virus/Viable Hehninth Ova,
❑ Alternative 4 [40 CFR §503.32 (a)(6)] - No Prior Testing for Enteric Virus/Viable Helmuith Ova.
® Alternative 5 [40 CFR §503.32 (a)(7)] - Process to Further Reduce Pathogens (PFRP).
Specify one: ❑ composting, ® heat drying, . ❑ .heat treatment, ❑ pasteurization,
❑ thernnophilic aerobic digestion, ❑ beta ray irradiation, or ❑ gamma ray irradiation.
❑ Alternative 6 [40 CFR §503.32 (a)(8)] - PFRP-Equivalent Process.
Explain:
b. For Class B or Equivalent:
❑ Alternative 1 [40 CFR §503.32 (b)(2)] - Fecal Colifor . Density Demonstration.
❑ Alternative 2 [40 CFR §503.32 (b)(3)] - Process to Significantly Reduce Pathogens (PFRP).
Specify one: ❑ aerobic digestion, ' ❑ air drying, "❑ anaerobic digestion,
❑ 'composting, or ❑ lime stabilization.
❑ Alternative 3 [40 CFR §503.32 (b)(4)] - PSRP-Equivalent Process.
Explain:
❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution.
c. For Surface Dis osal:
❑ Alternative for Surface Disposal Units Only [40 CFR §503.33 (b)(11)] - Soil/OtherMaterial Cover.
❑ Select One of the Class'A'oir Equivalent Pathogeii Reduction Alternatives in Item E. 7a, above.
❑ Select One of the Class B or Equivalent Pathogen Reduction Alternatives in Item Il. 7b. above.
❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution.
FORM RSCA 070807 ' :�'' Page 7 of 8 Attachment Order 2

8. Vector Attraction Reduction Determination: Specify ,which alterhative(s).will be used to meet the vector
attraction reduction requirements:
❑ Alternative 1 [40 CFR §503.33 (b)(1)] - 38% Volatile Solids Reduction (Aerobic/Anaerobic Digestion).
❑ Alternative 2 140 CFR §503.33 (b)(2)] - 40-Day Bench Scale Test (Anaerobic Digestion).
❑ Alternative 3 [40 CFR §503.33 (b)(3)] - 30-Day Bench Scale Test (Aerobic Digestion).
❑ Alternative 4 [40 CFR §503.33 (b)(4)] - Specific Oxygen Uptake Rate Test (Aerobic Digestion).
❑ Alternative 5 [40 CFR §503.33 (b)(5)] -14-Day Aerobic Processes.
❑ Alternative 6 [40 CFR §503.33 (b)(6)] - Alkaline Stabilization.. i.
❑ Alternative 7 [40 CFR §503.33 (b)(7)] - Drying of Stabilized Residuals.
® Alternative 8 [40 CFR §503.33 (b)(8)] - Drying of Unstabilized Residuals.
❑ Alternative 9 [40 CFR §503.33 (b)(9)] - Injection.
❑ Alternative 10 [40 CFR §503.33 (b)(10)] - Incorporation.
❑ Alternative for Surface Disposal Units Only [40 CFR §503.33 (b)(I1)] - Soil/Other Material Cover.
❑ Alternatives for Animal Processing Residuals Only: ,
Specify one: ❑ injection, ❑ incorporation, or ❑lime addition to raise pH to 10.
❑ Not Applicable - Non -Biological Residuals with NO Domestic Wastewater Contribution.
FORM: RSCA 070807 Page 8 of 8 Attachment Order 2

Whittier Sanitary District WWTP
Residuals -Source Certification Attachment..Order 2:,
Attachment Order.2 a. Viclr ity, Map..See Whittier_. plan sheet C3 ..
Attachment Order 2-b: Process Flow Narrative. See Residuals Management Plan
Page 3.
Attachment Order 2-c :Quantitative Justification for residuals production rate.
See Design Calculations Page 1.
Attachment Order 2-d:+Sampling Plan: Attached
Attachment Order 2-inIaboratory Analytical "reports and Operational Data:
Attached.

State of North Carolina
Department of Environment and Natural Resourees
Division of Water Quality
RESIDUALS SOURCE CERTIFICATION ATTACHMENT
(FORM: RSCA 070807)
(THIS FORM MAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL)
The Division of Water Quality (Division) will not accept this attachment unless all the instructions are
followed. Failure to submit all required items will lead to additional processing and review time.
For snore info nation, visit our web site at: http://h2o.e7ir.state.nc.usllauhnain.htrnl
INSTRUCTIONS TO THE APPLICANT:
A. Attachment Form:
✓ Do not submit this attachment form for review without a corresponding residuals program application
form (FORM: NDRLAP, FORM: DRS, or FORM: SDRS).
✓ Any changes to this attachment form will result in the application package being returned.
✓ For new residuals programs or renewed residuals programs, submit a separate attachment form for each
residuals source -generating facility to be certified for this residuals program.
✓ For modified residuals programs in which any modification to the certified residuals -source generating
facilities is proposed, submit a separate attachment form for o& those residuals source -generating facilities
that are affected by the proposed modification.
✓ The attachment should be organized prior to submission in the following order (i.e., by facility):
♦ Attachment Order 2: Residuals Source Certification Attachment (FORM: RSCA).
➢ Attachment Order 2-a: Vicinity map.
➢ Attachment Order 2-b: Process flow diagram and/or narrative.
➢ Attachment Order 2-c: Quantitative justification for residuals production rate.
➢ Attachment Order 2-d: Sampling plan.
➢ Attachment Order 2-e: Laboratory analytical reports and operational data.
B. Residuals Source -Generating Facility Information:
✓ Attach a vicinity map that shows the location of the facility and meets all of the criteria in the latest version of
the document entitled "Guidance for the Preparation of Vicinity/Buffer Maps for North Carolina Residuals
Permitting Programs."
✓ Attach a detailed narrative and/or process flow diagram that describes how the residuals are to be generated,
treated, processed, and stored at the facility.
✓ Attach a quantitative justification for the value provided in Item I. 8. Ensure that the amount of residuals
listed is the maximum amount expected to be generated by the facility for the life of the permit. In addition,
ensure that this amount is equivalent to that which is actually to be land applied, distributed, and/or disposed,
including any chemicals, amendments, or other additives that are added to the residuals during processing.
C. Residuals Quality Information:
✓ Attach a detailed sampling plan for the residuals source -generating facility. Ensure that the plan identifies
sampling points, sampling frequency, sample type, as well as the Division -certified laboratory to be used. In
addition, ensure that the plan details how the facility and/or the residuals are monitored for any applicable
pathogen reduction and vector attraction reduction requirements. Note that all sampling and monitoring must
be completed on the residuals as they are to be land applied, distributed, and/or disposed.
✓ Attach reports for all laboratory analyses used to complete this attachment form. Attach documentation that
the facility complies and/or the residuals comply with any applicable pathogen reduction and vector
attraction reduction requirements.
✓ Item II. 3. does not have to be completed for facilities that are less than 0.5 MGD in design flow that treat
100% non -municipal, domestic wastewater only.
RECEIVED / DENR / DWQ
Aquifer Protection Section
FORM: RSCA 070807 Page 1 of 8 JUL 19 2010 Attachment Order 2

State of North Carolina
Department of Environment and Natural Resources
Division of Water Quality
RESIDUALS SOURCE CERTIFICATION ATTACHMENT
(FORM: RSCA 070807)
(THIS FORM MAYBE PHOTOCOPIED FOR USE AS AN ORIGINAL)
Applicant's name: Tuckaseigee Water and Sewer Authority
Check all that apply: ❑ NEW RESIDUALS PROGRAM ❑ RENEWED RESIDUALS PROGRAM
® INCREASE ❑ DECREASE the maximum permitted annual dry tonnage for this residuals source -
generating facility certified for this residuals program.
Current: 250 Dry Tons/yr. and proposed: 659 Dry Tons/yr.
ADD ❑ DELETE this residuals source -generating facility to/from those certified for this
residuals program.
❑ OTHER Explain:
I. RESIDUALS SOURCE -GENERATING FACILITY INFORMATION (See Instruction B):
1. Name of facility: TWSA Wastewater Treatment Plant No. 1
2. Facility permit holder: Tuckaseigee Water and Sewer Authority
Facility permit holder is (check one): ❑ federal, ❑ state, E local government, or ❑ private.
Facility permit number: NPDES No. NCO039578
Facility permit issued by (check one): ® Div. of Water Quality, ❑ Div. of Environmental Health, or
❑ other (explain:
3. If the facility permit is not issued by the Div. of Water Quality, complete the following:
a. Facility contact person and title:
Facility complete mailing address:
City:
Telephone number: ( )
E-mail address:
b. Facility complete location address: _
City:
Latitude:
4. County where facility is located: Jackson County
State:
Zip:
Facsimile number: ( )
State:
and longitude:
Zip:
5. Purpose of the facility (check one):
® treatment of municipal wastewater, ❑ treatment of 100% domestic wastewater,
❑ treatment of potable water, ❑ treatment of 100% industrial wastewater,
❑ treatment of industrial wastewater mixed with domestic wastewater, or
(approximate percentages: % industrial and % domestic)
❑ other (explain:
FORM: RSCA 070807 Page 2 of 8 Attachment Order 2

6. Does the facility have an approved pretreatment program: ❑ yes ® no
7. Facility permitted/design flow: _3.5 MGD and facility average daily flow: _0_9 MGD.
8. Average amount of residuals being generated at this facility _158.77 dry tons per year.
9. Specify the following regarding treatment and storage volumes available at the facility:
Type and volume of residuals treatment: See Page 3 of the attached Residuals Management Plan.
Type and volume of residuals storage (i.e., outside of residuals treatment units): Dried Solids will be
stored in a 94 CY storage silo which provides approximately 36 1 days of storage at the permitted design
flow for the facility.
H. RESIDUALS QUALITY INFORMMATION (See Instruction C.):
1. Specify if residuals are regulated under (check one): ® 40 CFR Part 503 or ❑ 40 CFR Part 257.
2. Specify if residuals are intended for (check one):
® Land Application/Distribution (Class A or Equivalent).
Complete all items EXCEPT Items II.4b., 7b., and 7c.
❑ Land Application (Class B or Equivalent).
Complete all items EXCEPT Items II. 4b., 7a., and 7c.
❑ Surface Disposal.
Complete all items EXCEPT Items II. 4a., 5., 7a., 7b., and 8.
***FORM: RSCA CONTINUES ON NEXT PAGE***
FORM: RSCA 070807 Page 3 of 8 Attachment Order 2

3. Hazardous Waste Determination: Complete the following to demonstrate that the residuals are non-
hazardous under RCRA:
a. Are the residuals are listed in 40 CFR §261.31-§261.33: ❑ yes ® no.
If yes, list the number(s):
b. Specify whether or not the residuals exhibit any of the characteristics defined by 40 CFR §261.21-
§261.24: ❑ yes ® no. Fill in the following tables with the results of the latest toxicity
characteristic leaching procedure (TCLP) analysis as well as those for corrosivity, ignitability, and
reactivity: laboratory: Pace Analytical, Asheville and date of analysis: 8/25/2009 (3/11/10)
Passed corrosivity test: ® yes ❑ no. pH: 11 16 (line stab) 6.54 dewatered s.u. (2 < pH < 12.5).
Passed ignitability test: ® yes ❑ no. Flashpoint: _>140_ OF (> 1400F).
Passed reactivity test: ® yes ❑ no. HCN: ND_ mg/kg (<250) & HzS: ND_ mg/kg (<500).
TCLP Parameter
LimitTRes/ul)t
(mg/L)MgL
TCLP Parameter
Limit
(nig/L)
Result
(nzg/L)
Arsenic
5.0
ND
Hexachlorobenzene
0.13
ND
Barium
100.0
0.039
Hexachloro-1,3-Butadiene
0.5
ND
Benzene
0.5
ND
Hexachloroethane
3.0
ND
Cadmium
1.0
ND
Lead
5.0
ND
Carbon Tetrachloride
0.5
ND
Lindane
0.4
ND
Chlordane
0.03
ND
Mercury
0.2
ND
Chlorobenzene
100.0
ND
Methoxychlor
10.0
ND
Chloroform
6.0
ND
Methyl Ethyl Ketone
200.0
0.319
Chromium
5.0
ND
Nitrobenzene
2.0
ND
m-Cresol
200.0
Pentachlorophenol
100.0
ND
o-Cresol
200.0
ND
Pyridine
5.0
ND
p-Cresol
200.0
Selenium
1.0
ND
Cresol
200.0
0.218
Silver
5.0
ND
2,4-D
10.0
ND
Tetrachloroethylene
0.7
ND
1,4-Dichlorobenzene
7.5
ND
Toxaphene
0.5
ND
1,2-Dichloroethane
0.5
ND
Trichloroethylene
0.5
ND
1, 1 -Dichloroethylene
0.7
ND
2,4,5-Trichlorophenol
400.0
ND
2,4-Dinitrotoluene
0.13
ND
2,4,6-Trichlorophenol
2.0
ND
Endrin
0.02
ND
2,4,5-TP (Silvex)
1.0
ND
Heptachlor and its Hydroxide
0.008
ND
Vin�Chlo�ride
0.2
ND
FORM: RSCA 070807 Page 4 of 8 Attachment Order 2

4. Metals Determination: Complete one of the following tables (i.e., as applicable) to demonstrate that the
residuals do not violate the ceiling concentrations for metals regulated under 15A NCAC 02T .1105.
a. For Class A or Class B: Fill in the following table with the results of the latest analyses (i.e., on a dry
weight basis) for the following metal parameters:
Laboratory: Pace Analytical Asheville/Huntersville. NC and date of analysis: _8/24/2009
Parameter
Ceiling
Concentration
Limits
(ClassA & ClassB)
(mg/kg)
Monthly Average
Concentration Limits
(For Class A Only)
(mg/kg)
Result
(nig/kg)
Arsenic
75
41
6.6
Cadmium
85
39
0.6.
Copper
4,300
1,500
104
Lead
840
300
6.0
Mercury
57
17
0.50
Molybdenum
75
n/a
1.0
Nickel
420
420
4.6
Selenium
100
100
5.8
Zinc
7,500
2,800
324
b. For Surface Disposal: Fill in the following table with the results of the latest analyses (i.e., on a dry
weight basis) for the following metal parameters:
Laboratory: N/A and date of analysis:
Closest Distance
to Property Lines
(meters)
Arsenic
Onglkg)
Chromium
(mg/Icg)
Nickel
(nig/kg)
> 0 but < 25
30
200
210
> 25 but < 50
34
220
240
> 50 but < 75
39
260
270
> 75 but < 100
46
300
320
> 100 but < 125
53
360
390
> 125 but < 150
62
450
420
> 150
73
600
420
FORM: RSCA 070807 Page 5 of 8 Attachment Order 2

5. Nutrient/Micronutrient Determination: Complete the following:
a. Total solids: 57.2 %.
b. Fill in the following table with the results of the latest analyses (i.e., on a dry weight basis) for the
following nutrient and micronutrient parameters: laboratory: Pace Analytical Asheville/Huntersville.
NC and date of analysis: 8/24/2009
Parameter
Result
(mg/kg, dry weight)
Aluminum
9,460
Ammonia -Nitrogen
286
Calcium
331,000
Magnesium
2,920
Nitrate -Nitrite Nitrogen
ND
pH (Standard Unit)
12.4
Phosphorus
155
Potassium
3,690
Sodium
ND
Total Kjeldahl Nitrogen
11,900
c. Using the results listed in Item II. 5b. above, calculate the sodium adsorption ration (SAR): _0_ .
d. Specify the mineralization rate to be used in calculating the plant available nitrogen (PAN) of the
residuals: 30 %. This rate is a JZJ default value or L_J actually establisnecl.
If the residuals are not generated from the treatment of municipal or domestic wastewater, explain or
provide technical justification as to why the selected default value is appropriate to be applied to these
residuals:
Calculate the PAN for the residuals (i.e., on a dry weight basis) and list the results in the following table:
Application Method
First Year
Five -Year
PAN
Maximum Adjusted
PAN
(ing/kg)
(mg/kg)
Surface
3,630
5,625
Injection/Incorporation
3,770
5,765
e. Are the residuals a registered fertilizer with the NC Department of Agriculture and Consumer Services:
❑ yes ® no. If yes, provide date of registration approval:
the current registration number:
and the fertilizer equivalent: %, %, and %.
FORM: RSCA 070807 Page 6 of 8 Attachment Order 2

6. Other Pollutants Determination: Specify whether or not there are any other pollutants of concern in the
residuals and list the results of the latest analyses: No other pollutants of concern.
7. Pathogen Reduction Determination: Specify which alternative(s) will be used to meet the pathogen
reduction requirements:
a. For Class A or Equivalent:
® A fecal coliform density that is demonstrated to be less than 1,000 MPN per gram of total dry solids.
OR
❑ A salmonella sp. density that is demonstration to be less than 3 MPN per 4 grams of total dry solids.
AND one of the following (except for residuals regulated under 40 CFR Part 257 that are to be distributed):
❑ Alternative 1 [40 CFR §503.32 (a)(3)] - Time/Temperature Compliance.
❑ Alternative 2 [40 CFR §503.32 (a)(4)] - Alkaline Treatment.
❑ Alternative 3 [40 CFR §503.32 (a)(5)] - Prior Testing for Enteric Virus/Viable Helminth Ova.
❑ Alternative 4 [40 CFR §503.32 (a)(6)] - No Prior Testing for Enteric VirasNiable Helminth Ova.
® Alternative 5 [40 CFR §503.32 (a)(7)] - Process to Further Reduce Pathogens (PFRP).
Specify one: ❑ composting, ® heat drying, ❑ heat treatment, ❑ pasteurization,
❑ thermophilic aerobic digestion, ❑ beta ray irradiation, or ❑ gamma ray irradiation.
❑ Alternative 6 [40 CFR §503.32 (a)(8)] - PFRP-Equivalent Process.
Explain:
b. For Class B or Equivalent:
❑ Alternative 1 [40 CFR §503.32 (b)(2)] - Fecal Coliform Density Demonstration.
❑ Alternative 2 [40 CFR §503.32 (b)(3)] - Process to Significantly Reduce Pathogens (PFRP).
Specify one: ❑ aerobic digestion, ❑ air drying, ❑ anaerobic digestion,
❑ composting, or ❑ lime stabilization.
❑ Alternative 3 [40 CFR §503.32 (b)(4)] - PSRP-Equivalent Process.
Explain:
❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution.
c. For Surface Disposal:
❑ Alternative for Surface Disposal Units Only [40 CFR §503.33 (b)(11)] - Soil/Other Material Cover.
❑ Select One of the Class A or Equivalent Pathogen Reduction Alternatives in Item II. 7a. above.
❑ Select One of the Class B or Equivalent Pathogen Reduction Alternatives in Item II. 7b. above.
❑ Not Applicable - Regulated under 40 CFR Part 257 with NO Domestic Wastewater Contribution.
FORM: RSCA 070807 Page 7 of 8 Attachment Order 2

8. Vector Attraction Reduction Determination: Specify which alternative(s) will be used to meet the vector
attraction reduction requirements:
❑ Alternative 1 [40 CFR §503.33 (b)(1)] - 38% Volatile Solids Reduction (Aerobic/Anaerobic Digestion).
❑ Alternative 2 [40 CFR §503.33 (b)(2)] - 40-Day Bench Scale Test (Anaerobic Digestion).
❑ Alternative 3 [40 CFR §503.33 (b)(3)] - 30-Day Bench Scale Test (Aerobic Digestion).
❑ Alternative 4 [40 CFR §503.33 (b)(4)] - Specific Oxygen Uptake Rate Test (Aerobic Digestion).
❑ Alternative 5 [40 CFR §503.33 (b)(5)] - 14-Day Aerobic Processes.
❑ Alternative 6 [40 CFR §503.33 (b)(6)] - Alkaline Stabilization.
❑ Alternative 7 [40 CFR §503.33 (b)(7)] - Drying of Stabilized Residuals.
® Alternative 8 [40 CFR §503.33 (b)(8)] - Drying of Unstabilized Residuals.
❑ Alternative 9 [40 CFR §503.33 (b)(9)] - Injection.
❑ Alternative 10 [40 CFR §503.33 (b)(10)] - Incorporation.
❑ Altemative for Surface Disposal Units Only [40 CFR §503.33 (b)(11)] - Soil/Other Material Cover.
❑ Alternatives for Animal Processing Residuals Only:
Specify one: ❑ injection, ❑ incorporation, or ❑ lime addition to raise pH to 10.
❑ Not Applicable - Non -Biological Residuals with NO Domestic Wastewater Contribution.
FORM: RSCA 070807 Page 8 of 8 Attachment Order 2

TWSA Plant No. 1
Residuals Source Certification Attachment Order 2:
Attachment Order 2-a: Vicinity Map. See plan sheet C3
Attachment Order 2-b: Process Flow Narrative. See Residuals Management Plan
Page 3.
Attachment Order 2-c: Quantitative Justification for residuals production rate.
See Design Calculations Page 1.
Attachment Order 2-d: Sampling Plan: Attached
Attachment Order 2-e: Laboratory Analytical reports and Operational Data:
Attached.

Tuckaseigee Water and Sewer Authority
Residuals Distribution Permit- Sampling Plan
Residuals will be sampled after the dryer process has completed at the pneumatic
conveyor or storage silo.
Toxicity Characteristics Leaching Procedure Analysis shall be performed annually.
For Product distribution up to 319 Dry. Tons per year residuals will be tested once per
year for aluminum, magnesium, phosphorus, ammonia -Nitrogen, Mercury, Potassium,
Arsenic, Molybdenum, Selenium, Cadmium, Nickel, Sodium, Calcium, Nitrate -Nitrate
Nitrogen, Total Kjeldahl Nitrogen, Copper, pH, Total Solids, Lead, Plant Available
Nitrogen and Zinc.
For product distribution from 319 dry tons per year to 659 dry tons the above shall be
sampled quarterly.
Pathogen Reduction shall be verified by Total Solids > 90% dry solids or maintenance
of 158 degrees F for at least 30 minutes.
Vector Attraction shall be verified by total solids > 90% dry solids.
All samples will be completed by Tuckaseigee Water and Sewer Authority Certification
No. 160 or Pace Analytical Services Inc. - Asheville Certification No. 40

DESIGN CALCULATIONS
WASTEWATER TREATMENT PLANT NO. 1 IMPROVEMENTS
SLUDGE MANAGEMENT
TUCKASEIGEE WATER AND SEWER AUTHORITY
JACKSON COUNTY, NORTH CAROLINA
PREPARED BY: DAVID L. HONEYCUTT, P.E.
REVIEWED BY: HARRY B. BUCKNER, P.E.
McGfll
A S S O C I A T E S
Engineering • Planning • Finance
Post Office Box 2259
Asheville, North Carolina 28802
JULY 2010
05734
i SEAL
2254;
`fAEetetet►d`�` -7 ,01 ,1oI a

TABLE OF CONTENTS
I. SLUDGE HOLDING.....................................................................................1
II. SLUDGE HANDLING SYSTEM FEED PUMP .......................................... 4
III. SOLIDS HANDLING FACILITY................................................................. 5
IV. PLANT AVAILABLE NITROGEN.............................................................. 7

i
Io SLUDGE HOLDING
Determine sludge wasting rate
Q = V/ SRT (Ref. Wastewater Engineering, Metcalf and Eddy 4t' edition, pg 693)
V = 2,235,000 gal. Per WWTP No. 1 Design Calculations
SRT =13.1 days Per WWTP No. 1 Design Calculations
Q = 2,235,000 gal. / 13.1 days=170,611 GPD at 4,500 mg/l
Lbs solids wasted = 0.170611 mgd * 4,500 mg/l * 8.34 = 6403 lbs/day
Assuming 75% volatile solids and 75% reduction of volatile solids digestion
Solids to disposal = 6403 — 6403*0.75 *0.75 = 2801 lbs/day
2801 lbs/day at 3.5 mgd = 0.80 lbs/day
Based on historic data the plant has produced 0.95 lbs/1000 gallons.
In addition the plant receives solids from the Cashiers WWTP with a permitted flow of 0.2 mgd
and the Whittier WWTP with a permitted flow of 0.1 ingd.
At 0.95 lbs/1000 gallons *3.8 ingd = 3,610 lbs/day
3,610 * 365 days/year = 659 dry tons per year
Size Sludge Holding for sludge production at Plant No. 1.
At 0.95 lbs/1000 gallons *3.5 mgd = 3,325 lbs/day
30 days of solids storage required per 15A NCAC 02H.
Assume 2 %. solids concentration (ref. Metcalf and Eddy, Wastewater Engineering 3rd Edition, pg
774)
3,325 lbs solids / day * 1/ (62.4 lbs / cubic foot water * 1.015 (SG of 2% sludge) x 0.02 (solids
content) = 2,625 cubic feet per day=19,634 GPD
19,634 GPD * 30 days = 589,025 gal sludge produced in 30 days
Existing Sludge Holding tank basin is 50' - 6" 0 x 19' W.L.
Volume = 50.52 * pi/4 * 19' * 7.48 gallons/CF = 284,660 gallons
Page 1

Existing Flow Equalization Basin is 53' - 4" x 20'-6" W.L.
Volume = 53.332 * pi/4*20.5*7.48 gallons/CF = 342,522 gallons
Total Sludge Storage Volume = 627,182 gallons
Greater than 589,025 gal therefore, 30 days storage requirement met.
Proposed Sludge Holding Tank Air Requirements
Calculate the air required for mixing and to prevent anaerobic conditions in the proposed sludge
holding tank.
Per Metcalf and Eddy Wastewater En ineering 3'd edition, pg 837 air requirements for sludge
holding is 20-40 SCFM per 1000 CF of sludge holding volume. Therefore use 30 SCFM per 1000
CF.
Air required for Proposed Sludge Holding Tank (existing Flow Equalization):
342,522 gallons / 7.48 gallons/CF *30 SCFM/1000 CF =1374 CFM, Use 1375 CFM
Determine discharge pressure required.
Discharge pressure = head of water above diffusers + piping friction head + silencer/filter
losses + diffuser headloss
Water above diffusers = 20.5 ft
Silencer/Filter Head = 2.25 ft
Diffuser Headloss = 1 ft
Air header is a total of 100' long. Per Duct Resistance Chart 0.35" of headloss per 100 ft for
1375 SCFM in 12" piping.
Air header friction loss = 0.35 in (0.03 ft)
Discharge Pressure = 20.5' + 2.25' + 0.25' + 0.03' = 23.03' (9.97 psi)
Specify duplex blowers, each 1375 SCFM cr 10.5 psi
Use 24" coarse bubble diffusers loaded at 16 SCFM each requires 86 diffusers.
Air required for Existing Sludge Holding Tank
284,660 gallons / 7.48 gallons/CF *30 SCFM/1000 CF=1141.7 CFM, Use 1145 CFM
Determine discharge pressure required.
Discharge pressure = head of water above diffusers + piping friction head + silencer/filter
losses + diffuser headloss
Page 2

Water above diffusers = 19.5 ft
Silencer/Filter Head = 2.25 ft
Diffuser Headloss =1 ft
Air header is a total of 100' long. Per Duct Resistance Chart 0.2" of headloss per 100 ft for
1145 SCFM in 12" piping.
Air header friction loss = 0.2 in (0.016 ft)
Discharge Pressure =19.5' + 2.25' + 0.25' + 0.016' = 22.02' (9.53 psi)
Specify duplex blowers, each 1145 SCFM tt 10 psi
Use 24" coarse bubble diffusers loaded at 16 SCFM each requires 72 diffusers.
Both basins are existing structures and therefore buoyancy calculations are not necessary.
Page 3

U. SLUDGE HANDLING SYSTEM FEED PUMP
Size progressive cavity pump to feed belt press at 50-100 gpm.
High Point at ceiling in sludge handling facility = 2061.6
Assume pumping from bottom EL. of Proposed Sludge Holding Tank = 2000.0
Static Head = 2061.6-2000.0 = 61.6'
The friction loss in the 4-inch force main can be represented as:
Head iri,.tion = 10.57 Q1.85 L
C1.85 D4.87
For L in feet, Q in GPM, and D in inches
For 100 GPM,
Head f;,,t,on = 10.57 * 1001.85 550
1201.85 44.87
Head fii�tton = 4.85 ft
Total Dynamic Head = 61.6 + 4.85 = 66.5'
Size pump for 100 gpm at 67' TDH.
Page 4

III. S®LIDS HANDLING FACILITY
Belt Press
Belt press is proposed to be relocated from existing solids handling process
Existing Press has a 1 meter effective width.
Verify capacity is adequate for 3.5 mgd design flow with flow from Cashiers and
Whittier. Note that sludge from TWSA Plant No. 2 is also hauled to this facility. The
3.5 mgd design flow for Plant No. 1 includes all flow from Plant No. 2 to be pumped to
Plant No. 1 in the future.
Per sludge calculations 3,610 dry lbs/day of sludge at 26/o solids will be produced.
Belt Press Hydraulic capacity is 60-70 gpm assume 65 gpm.
65 gpm *8.34 lbs/gallon * 0.02 lbs solids*60 min/hr = 650.5 lbs/hr
3610 lbs/day/ 6501bs/hr = 5.55 hrs/day
To press only 5 days a week would require the press to run 7.77 hrs/day. Therefore Belt
Filter Press capacity is adequate at the design flow.
Solids Dryer
Proposed utilize indirectly heated dryer to produce Class A biosolids.
Estimate volume from belt press for dewatered sludge at 16% solids.
Assume a density of dewatered sludge of 62.4 lbs/CF * 1.07 = 67 lbs/CF
(1.07 is Specific gravity per Metcalf and Eddy)
65 gpm * 0,02% solids * 8.34 lbs/gallon * 60 min. = 650.5 lbs dry solids/hr
650.5 lbs dry solids/hr/0.16 = 4,065.75 lbs wet 16 % solids/hr
Water weight = 4065.75-650.5=3,415.25 lbs water/hr
Volume = 4,065.75/67 lbs/CF = 60.68 CF/hr
Proposed storage hopper between belt press and solids dryer is 50 CY
50 CY / (60.68 CF/27) = 22.25 hrs belt press run time to fill hopper.
Page 5

Dryer Capacity is 9.5 CY per batch
EPA 40 CFR 503 regulations require pathogen reduction and vector attraction reduction
for class A biosolids.
1. Pathogen Reduction
176° F and 90% solids
Or 158°F for 30 minutes (Pasteurization)
Proposed dryer will produce of 90% solids and provide over 158° F for greater than
30 minutes.
2. Vector Attraction Reduction
Dry un-stabilized solids to 90% solids.
Determine therms natural gas required for drying.
Calculate per wet ton at 16% solids
20001bs * 0.16% = 3201bs dry solids/wet ton
320 lbs dry solids at 90% solids = 365 lbs (451bs water remaining)
2000 lbs wet sludge — 365 lbs =1644 lbs water evaporated per wet ton.
16441bs water evaporated/wet ton * 1600 BTUs/lb = 2,630,400 btu/wet ton
2,630,400 btu/wet ton / 1,000,000 btu/ MCF Natural Gas = 2.63 MCF/wet ton
Natural Gas required at design flow
3610 dry lbs/day / 0.16 = 22,562.5 wet lbs/day =11.28 wet tons/day
11.28 wet tons/day * 2.63 MCF/wet ton = 29.67 MCF/day at 3.8 imgd
Check Proposed Silo Storage Volume
Silo Inside Diameter =12 ft noire.
Silo Height = 21 ft
Silo Cone Height = 3.5 ft
Silo Cone Lower Inside Diameter = 4 ft
Volume Silo = pi/4* 12 f 2 (21 ft) = 2,375 CF
Volume Silo Cone = pi/4 (1/2(12+4))2(3.25) = 163 CF
Total Volume Silo = 25538 CF
Unit Weight Sludge = 40 to 50 lb/CF use 50 lb/CF
Total Dry Sludge Capacity = 2,538 CF * 50 lb/CF = 63.45 tons
63.45 tons/ 3610 lbs/day = 35.2 days storage at Design Flow.
Page 6

IV. PLANT AVAILABLE NITROGEN
Determine PAN for TWSA Biosolids (first year and 5-year max.)
First Year PAN = AN(Kvol) + NN + ONo(Ko)
Ref. EPA Design Manual 625/R-95/001 September 1995 pg 77.
Assume no denitrification losses
AN = Aininonia-nitrogen (lb/ton) = 286 mg/kg(sainple data)*0.002 lb/ton / mg/kg = 0.5721b/ton
NN = Nitrate -nitrogen (lb/ton) = 0 mg/kg * 0.002 lb/ton / mg/kg = 0 lb/ton
ONo = Organic Nitrogen during year of application (lb/ton) = TKN — AN — NN = 11,900-286-0=
11,614 mg/kg * 0.002 lb/ton / mg/kg = 23.23 lb/ton
Ko = mineralization rate of ON during year of application rate = 0.30 per Table 7-7 EPA Design
Manual 625/K-95/001 September 1995
Kv01 = Volatilization losses of AN Typically 0.5 for surface application per Table 7-8 EPA
Design Manual 625/R-95/001 September 1995
Kv01= Volatilization losses of AN Typically 1.0 for incorporation per Table 7-8 EPA Design
Manual 625/R-95/001 September 1995
Surface First Year PAN = 0.572 * 0.5 + 0 + 23.23 * 0.30 = 7.26 lb/ton
7.26 lb/ton / 0.0021bs/ton / mg/kg = 3630 mg/kg
Incorporated First Year PAN = 0.572 * 1 + 0 + 23.23 * 0.30 = 7.54 lb/ton
7.54 lb/ton / 0.0021bs/ton / mg/kg = 3770 mg/kg
Determine 5 year max PAN
5 year max. PAN = First Year PAN + PAN fiom previous applications
Per Table 7-7 EPA Design Manual 625/R-95/001 September 1995 the following mineralization
rates will be used
Years After Application
Kmin for Aerobically Digested Sludge
1-2
0.15
2-3
0.08
3-4
0.04
5 Year Max. PAN = First Year PAN + ON12 (0.15) + ON23(0.08) + ON34(0.04)
Page 7

5 Year Max. PAN= Year 1 PAN + Year 2 PAN + Year 3 PAN + Year 4 PAN
Year 1 Pan = 7.26 lb/ton
Year 2 PAN = [(23.23-Year 1 PAN)*0.15) = 2.40 lb/ton
Year 3 PAN = [23.23-Year 1 PAN — Year 2 PAN] *(0.08) =1.09 lb/ton
Year 4 PAN = [23.23 — Year 1 PAN — Year 2 PAN — Year 3 PAN] * (0.04)=0.50 lb/ton
5 Year Max. PAN=11.251b/ton
11.25 lb/ton / 0.002 lbs/ton / mg/kg = 5625 mg/kg
Page 8

TUCKASEIGEE WATER AND SEWER
AUTHORITY
RESIDUALS MANAGEMENT PLAN
FEBRUARY 2009

The Tuckaseigee Water and Sewer Authority is proposing to construct facilities for heat drying of
municipal wastewater sludge from their wastewater treatment plant. The EPA 503 regulations
allow for pathogen reduction by subjecting the material to high temperatures for a certain length of
time. After the liquid sludge is dewatered to approximately 16% solids by a belt filter press, the
dewatered sludge will be conveyed to a gas -fired dryer for final heat and drying treatment. One of
the following two (2) methods of compliance with EPA regulations for pathogen reduction will be
performed to achieve a Class A biosolids product.
PATHOGEN REDUCTION METHODS
1. Heat Drying
The dewatered sludge will be dried by indirect contact with hot gases to reduce the moisture
content to 10% or lower (i.e., at least 90% dry solids). The temperature of the sludge will
be raised to at least 80 degrees C (176 degrees F) during this process.
2. Pasteurization
The temperature of the dewatered sludge in the dryer will be maintained at 70 degrees C
(158 degrees F) or higher for at least thirty minutes to achieve pasteurization of pathogens.
EPA regulations also stipulate that vector attraction reduction methods be utilized to achieve a
Class A biosolids. The vector attraction reduction requirements will be met by one of the following
two methods.
VECTOR ATTRACTION REDUCTION METHODS
1. Thermal drying of unstabilized biosolids to at least 90% dry solids.
Page 1

2. Thermal drying of stabilized biosolids to at least 75% dry solids.
After the heat drying process is completed, the final Class A biosolids product will be conveyed to
either a truck or silo storage. The product will be sold or given away to local farmers, nurserymen
and landowners for use as a soil amendment.
Page 2

B. BIOSOLIDS PROCESSING FACILITIE
Waste activated sludge will be pumped at 400 gpm from the sequencing batch reactor basins to one
of two (2) aerated sludge holding tanks. The total sludge holding tank volume is 627,182 gallons
which provides 30 days storage at the design flow at 2% solids. The thickened sludge will then be
pumped at 50-100 gpm to a belt filter press to be dewatered to approximately 16% dry solids. Per
design calculations the belt press will be required to run an average of 5.3 hrs per day at 65 gpm
feed rate at the plant design flow of 3.5 mgd. Dewatered sludge from the belt filter press will be
discharged to a 50 cubic yard storage hopper. The dewatered sludge will be conveyed from the
storage hopper to a gas -fired dryer for final heat and drying treatment. The dryer has a capacity of
9.5 cubic yards per load and therefore the storage hopper can store up to 5 loads. The dryer will
utilize either liquid petroleum or natural gas to heat oil, and will heat and dry the sludge by through
indirect contact. Sludge will be dried to 90% solids and then conveyed to an 86 cubic foot storage
hopper. A blower system will be used to blow the dried sludge from the storage hopper through a 4
inch ductile iron pipe to the sludge storage silo. The sludge storage silo provides 94 cubic yards of
storage capacity or 36.1 days at design flow. The dried sludge will be distributed from the silo to
the final users. It is expected that the final product will be distributed in bulk.
Page 3

C.
Heat dried biosolids from the Tuckaseigee Water and Sewer Authority Solids Handling Facility
will be attractive to several markets including fanning businesses and the private sector.
It is anticipated that both commercial and private fanners, landscape professionals, golf courses and
private landowners in Jackson County will be interested in obtaining the Class A biosolids material
for utilization as a soil amendment.
Page 4

Page 5

USE OF HEAT DRYED WASTEWATER DI®SOLIDS
AS A S®II, AMENDMENT
A Guide for the Consumer
Heat Dryed Biosolids
Tuckaseigee Water and Sewer Authority
Jackson County, North Carolina
For fiwther technical guidance contact your
County Agricultural Extension Service Agent.
The Tuckaseigee Water and Sewer Authority may be contacted at the address below:
Tuckaseigee Water and Sewer Authority
1246 West Main Street
Sylva, North Carolina 28779
Page 6

THE HEAT DRYING PROCESS
The EPA 503 regulations allow for pathogen reduction by subjecting the material to high
temperatures for a certain length of time. After the liquid sludge is dewatered to approximately
16% solids by a belt filter press, the dewatered sludge will be conveyed to a gas -fired dryer for final
heat and drying treatment. One of the following two (2) methods of compliance with EPA
regulations for pathogen reduction will be performed to achieve a Class A biosolids product.
PATHOGEN REDUCTION METHODS
1. Heat Dryin
The dewatered sludge will be dried by indirect contact with hot gases to reduce the moisture
content to 10% or lower (i.e., at least 90% dry solids). The temperature of the sludge will
be raised to at least 80 degrees C (176 degrees F) during this process.
2. Pasteurization
The temperature of the dewatered sludge in the dryer will be maintained at 70 degrees C
(158 degrees F) or higher for at least thirty minutes to achieve pasteurization of pathogens.
EPA regulations also stipulate that vector attraction reduction methods be utilized to achieve a
Class A biosolids. The vector attraction reduction requirements will be met by one of the following
two methods.
VECTOR ATTRACTION REDUCTION METHODS
1. Thermal drying of unstabilized biosolids to at least 90% dry solids.
2. Thermal drying of stabilized biosolids to at least 75% dry solids.
After the heat drying process is completed, the final Class A biosolids product will be conveyed to
either a truck or a covered storage area. The product will be sold or given away to local farmers,
nurserymen and landowners for use as a soil amendment.
Page 7

The heat drying method of producing biosolids is approved by the EPA as an effective method of
sludge stabilization and pathogen reduction and results in an environmentally safe product with
multiple beneficial uses.
GENERAL, USES, PROPERTIES, AND PRECAUTIONS
Heat dryed biosolids can be utilized advantageously by the local, large scale fanner as a soil
amendment or to supplement fill material. It can also be used by individuals wishing to enhance
their lawns and gardens or any other area that may need a soil amendment. Heat dryed biosolids
should improve the physical properties of soil in the following ways:
• hnproved Permeability - Helps snake clay or other heavy soils more friable
and loose, reducing compaction.
Improved aeration - Looser soil encourages root growth.
• Supplement other fill material
Heat dryed wastewater biosolids are a product of municipal sewage. Heat dryed biosolids should
be free of dangerous pathogens and toxic substances, but it should be treated with respect. Contact
with children and pets should be minimized and direct ingestion of heat dryed biosolids should be
avoided. Also as a precaution, prolonged contact with the heat dryed biosolids should be avoided.
Heat dryed biosolids should not be applied to any site that is flooded, frozen or snow covered and
adequate procedures shall be provided to prevent surface runoff from carrying any disposed or
stored residuals into any surface waters. Residuals also cannot be placed any closer than ten (10)
feet from any public or private water supply source (including wells) and any stream, lake, river, or
natural drainage way.
Application of these residuals is prohibited except as in accordance with the instructions on this
information sheet.
Page 8

January 26, 2010
DENR/DWQ/Water Quality Section
Non -Discharge Compliance Unit
1617 Mail Service Center
Raleigh NC 27699-1617
Attn: Non -Discharge Compliance Unit,
Enclosed is the Annual Residuals Report for the Tuckaseigee Water and Sewer Lime
Stabilization facility (permit 4WQ0005763) for the period of January 1, 2009 - December
31, 2009.
Should you have any questions or if I can provide you any additional information, please
don't hesitate to contact me.
Sincerely,
Stan Bryson
Wastewater Plant Operations Superintendent
Tuckaseigee Water & Sewer Authority
Enc.

TABLE OF CONTENTS
(1) REPORTING REQUIREMENTS/PERTINENT INFORMATION
(2) CERTIFICATION
(a) 2009 distribution and marketing summary
PartA & B
(b) Annual Residuals Sampling Summary Form
(c) 2009 Residuals Analysis. Lab Sheets
(d) TCLP analysis
(e) Annual Pathogen and Vector Attraction Reduction Forms
(fl Pathogen & Vector Attraction Reduction Lab Sheets/Records
(g) 2009 sludge production data

ANNUAL SEWAGE SLUDGE REPORT
OF
�l 'I'iTCKASEIGEE WATER AND SEWER
AUTHORITY
PLANT # fl-NPHiES # NC0039578
(WQ0005763)
for the period of
1 00)
January 1, 2009-December 31, 2009
as required by
40 CFR, PART 503
STANDARDS FOR THE USE OR
DISPOSAL OF SEWAGE SLUDGE

a
L
L
1
1 1 . )1 1l'►MKy
Facilities responsible for reporting annually are described in the regulations as:
1. Publicly Owned Treatment Works (POTW) with an average design
influent flow rate equal to or greater than 1.0 MGD.
2. POTW's serving a population of 10,000 or more.
3. Class I (facilities with an approved pretreatment program) sludge
management facilities
The Tuckaseigee Water and Sewer Authority Wastewater Treatment Plant is a 1.5 MGD
design facility. The facility also treats the sludge from two additional plants owned by the
authority.
Pertinent information includes:
facility name: Tuckaseigee Water & Sewer Authority Plant # 1
NPDES # NC0039578
correspondence address: 1246 West Main St
Sylva NC 28779
physical address: 1871 North River Rd
Sylva NC 28779
facility operator: Stan Bryson
Wastewater Plant Operations Superintendent
ph. 828-586-9318
e-mail: [e-mail]

I - -
CERTIFICATION REQUIREMENTS
PART I - POLLUTANT CONCENTRATIONS
Ceiling
Concentrations
mg/kg
Parameter
Sample.
Analysis
value
Maximum
Permitted
value
Arsenic
6.7
75
Cadmium
0.42
85
Chromium,
8.8
300
Copper
86
4,300
Lead
5.0
840
Mercury
0.313
57
Molybdenum
0.5
75
Nickel
2.6
420
Selenium
6.2
100
Zinc
268
7,500
PART II - PATHOGEN REDUCTION (40 CFR 503.32)
X Class A - Class B
PART III - VECTOR ATTRACTION (40 CFR 503.33)
option Option 2 Option 3
Option 5 X Option 6 Option 7
Option 4
Option 8

-CERTIFICATION
" I certify under penalty of law, that the Class A pathogen requirements in 40 CFR, Part
503. 32 have been met and the vector attraction reduction requirement in 40 CFR, Part
_
[50133(b)(6}] has been met. I am aware that there are significant penalties for false
certification including fine and imprisonment."
i
Signeo this 5th day of . _ February, 2009
Stan Bryson, Wastewater Superintendent..
Nil

t
Appendix (a)
2009
a .
Distribution and
Marketing
Summary
(Part A)

MM
'%
ANNUAL DISTRIBUTION AND .MARI STING/ SURFAd DISPOSAL CERTIFICATION AND SUMMARY;FORM
PERMIT #: L!0_ DD T_rl(a 3 FACILITY NAME:
PHONE: gam_ eJ g& _ ?.318 COUNTY: ��c�C�i o F-1 . OPERATOR:
FACILITY TYPE lease check one): e
❑ Surface Disposal`(coniplete;Part A- (Source(s) and •"Resi ual In" Volume only) and Part C)
II Distribution and Marketing (complete Parts A, B, and C)
Was the facility in operation during the past calendar. year?.. No.If No skip parts A, B, C and certify form below
Part A*;,
Part B*:
Sources(s) (include NPDES # if .:Volume (dry, tons)
Month Amendment/
applicable). Residual In `Product Out : Name(s)..
Bulking Agent
unary —
bruarp
irch
IV
t
October
November
December
Totals:
olume (dry tons)I - Intended use(s)
nuuuflg 4geni s) useo:
* If more space than given is required, please -atta& additional infoniiatioi sheet s
() Check box if additional sheets) are. attached
Part C:
Facility was compliant during calendar, year. a 661. with* 41f-con,
dit ons .of the ermif includin but npt limited to items 1-3-below) issued by the
P•.. (
Division:of'Water Quality.. .3 Yes 0 No- If No, please provide_ a. written. descri description'. .the facility
p y ty.vvas not compliant.
1. All monitoring was done in accordance with the pci7nit and reported:for the year as required and tliree:(3) copies of certified laboratory results are attached.
2. All operation and maintenance requirements were compiled with or, in'the case of a deviation, prior authorization was received from the Division of Water
Quality.
.3. No contravention of Ground Water Quality Standards occurred at a monitoring. well,
"I certify, under penalty of law; that the above information'is' to the best of.iny knowledge and -belief, true, accurate and complete. I am aware
tha ere are si nificant penalties for submitting. false information, including the possibility of fines and imprisonment for knowing violations."
Signature of Permitt a Date Signature of Preparer**-. Dater
'(if different:from P.ermittee).**Preparer is defined in 40 .QFRPart.503.9(r)
. i - �.„.::` .• In;=A1D GnDKA MhfiQMEZ 14 4 /nnnr_

Part A
Residual Sources and Volume
Sludge
A
Volume
Sludge Volume
SludgeClass
Volume
Month Source
Produced
(dry tons
Dewatered
Residual Volume
Treated Lime Added Produced
July TWSA
(dry tons)
(dry tons) (dry tons) (dry tons)
Plant # 1 (NC0039578)
19.11
TWSA Plant # 2 (NC0020214)
2.73
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
2.85
Monthly Totall
24.69
13.72
0
0.00
August TWSA Plant # 1 (NC0039578)
23.51
TWSA Plant # 2 (NC0020214)
1.13
®
TWSA Plant -# 3. (NC0063321)
0.00
Septage Received
2.69
otal
27.33
15.95
0
® 0
II
September TWSA Plant # 1 (NC0039578)
22.84
TWSA Plant # 2 (NC0020214)
3.00
TWSA Plant # 3 (NC0063321)
2.11
Septage Received
1.80
Month!y Total
29.75
15.21
0
0 0
�(-
October TWSA Plant # 1 (NC0039578)
25.27
1
TWSA Plant # 2 (NC0020214)
0.00
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
2.89
IxIIrM!y Total
28.16
18.03
p
0 0
November TWSA Plant # 1 (NC0039578) 22.28
TWSA Plant # 2 (NC0020214) 1.49
TWSA Plant # 3 (NC0063321) 0.00
Septage Received 1.62
Month Total 25.39 20.63
' December TWSA Plant # 1 (NC0039578) 17.12
TWSA Plant # 2 (NC0020214) 0.00
TWSA Plant # 3 (NC0063321) 0.00
Septage Received 2.87
- Month) Total 19.99 11.83
T ��
Total Sludge produced by all sources for 2009= 305.36 dry tons
Total "sludge" dewatered by belt press in 2009= 203.96 dry tons
Total "sludge" treated in pastuerization process in 2009= 45.90 dry tons
Total lime added in pastuerization process in 2009= 112.87 dry tons
�Total "residual" produced for distribution in 2009=158.77 DRY TONS
I
0

Appendix A
TWSA PLANT
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2009
Part A
Residual Sources and Volume
Sludge Volume Sludge Volume Sludge Volume
Class A
Month Source
Produced Dewatered Treated Lime Added
(d tons)
Residual Volume
Produced
January TWSA Plant * I (NC003957
(dry tons) d Ions) (dry tons)
13.47
(d tons
TWSA Pla4f2 (NC0020214)
0.00
TWSA Plant * 3 (NC0063321)
0.00
Septage Received
1.29
Monthly Total
14.78 13.14 0.00 0.00
0.00
February, TWSA Plant# I (NC0039578)
18.91
TWSA Plant # 2 (NC0020214)
2.74
TWSA Plant # 3 (NC0063321)
0.00
Septage Received
3.14
Month) Total
24.79 20.78 0.00 0.00
March TWSA Plant * 1 (NC0039578)
20.51
0.00
TWSA Plant # 2 (NC0020214)
2.27
TWSA Plant # 3 (NC0063321)
0
Septage Received
1.53
Month) Total
24.31 14.80 0.00 0.00
0.00
April TWSA Plant# 1 (NC00P9578)
23.34
TWSA Plant # 2 (NC0020214)
5.20
TWSA Plant # 3 (NC0063321)
0
Septage Received
2.29
13.9 1 27
IR

N
Appendix (a)
2009
Distribution and
Marketing,
Summary
(Part B)
1. i

q TWSA PLANT # 1
ANNUAL DISTRIBUTION AND MARKETING SUMMARY
2009
A
I
Part B
Recipient Information
Est. Volume
Month Name Address wet tons Intended Use
_ Janyary.
_ _ _.
Monthly Total
0
7uary
Month IV Total
0
March
Chester Sorrells
274 Davis Cove Rd.
26
Commercial Hauler
Waynesville NC 28786
Jim Rhineheart
PO Box 303
182
Pasture/Hayfields
Webster NC 28788
ph: 828-399-1878
Phil Woody
376 Mack -town Gap Rd.
0.5
Garden
Sylva NC 28779
ph: 828-631-4607
Harold Cole
128 Holstein Drive
20
Hayfield
Sylva. NC 28779
ph: 828-586-6770
Lloyd Green
60 Zion Hill Church Rd.
1
Pasture
Sylva NC 28779
ph: 828-586-6383
Monthly Total
229.5
April
Lloyd Green
60 Zion Hill Church Rd.
Sylva NC 28779
4
Pasture
h: 828-586-6383
Monthly Total
4
May
Chester Sorrells
274 Davis Cove Rd.
26
Commercial Hauler
Waynesville NC 28786
Monthiv Total
26
June
Monthly Total
0

4
I -
Jul
Arnold Frady
270 Christmas Tree Lane
2
Pasture/Hayfields
Sylva NC 28779
h: 828-631-3858
Monthly Total
2
August
Tony Collins
40
Pasture/Hayfields
Franklin NC
828-421-0140
Monthly Total
40
September
Chester Sorrells
274 Davis Cove Rd.
36
Waynesville NC 28786
Tony Collins
20
Franklin NC
828-421-0140
Monthly Totall
56
October
Chester Sorrells
274 Davis Cove Rd.
Waynesville NC 28786
14
Pasture/Hayfields
Monthly Total
14
November
Monthly Total0
December
Monthl Total
Annual Total 371.5 wet tons (est.)
Annual vet tons x 55.4 (avg % solids) = 205.8 dry tons distributes!.
h

Appendix (b)
2009,
Annual Residual Sampling
Summary Form

f . 2009
Annual Residampling Summary Form
Attach this form to the corresponding Annual Report
Please note that your permit may contain additional parameters to be analyzed than those required to be summarized on this form.
Permit Number:WQ 0005763
Facility Name: Tuckasei9ee Water and Sewer Auth.
NPDES # NC 0039578
WQ # : WQ 0005763
WWTP Name: TWSA Plant # 1
='lai E
Sample
Date
2/17
5/5
7/14
8/11
8/18
8/24
Avg.
i ` li..
Percent Solids
54.3
49.6 .
55.5
58.3
57.2
57.4
55.4
Aluminum
8,720
7,910
8,590
9,460
8,670
P
Arsenic
7.7 1
6.7
5.7
6.6
6.68
A
Cadmium
0.36
0.44
0.25
0.63
0.42
R
Calcium
295,000
319,000.
339 000
331,000
321,000
A
Chromium
7.6
7.0
8.6
11.9
8.8
M
Copper
84.2
62.6
93.1
104
86
E
Lead
4.6
3.5
5.9
6.0
5.0
T
Magnesium*
2,850
2,570
2,820
2,920
2,790
E
Mercury
0.053
0.41
0.29
0.5
0.313
R
Molybdenum
< 0.62
< 0.55
1 1.1
1.0
0.5
S
Nickel
1.3
1.3
3.3
4.6
2.6
h
12.3
12.0
11.9
12.4
Potassium
2,960
3,730
3,320
3,690
3,425
Selenium
7.8
6.6
4.5
5.8
6.2
Sodium
647
555
< 795
< 870
301
Zinc
256
208
284
324
268
TKN
1,520
15,500
11,700
11,900
10,155
mg/
Ammonia -Nitrogen
241
134
208
286
217
kg
Nitrate -Nitrite
< 16.7
< 18.1
< 14.3
< 18.1
0.0
Plant Available N
504
4,680
2,070
3,630
2,721
Total Phosphorous
235
3640
206
155
1,059
Fecal Coliform
< 200
< 4
< 4 .
< 20
< 20
<. 3
I certify, under penalty of law, that this document was prepared under my direction or supervision in accordance with a system
designed to assure that qualified personnel properly gathered and evaluated the information submitted. I am aware that there are
significanWenalties for submitting false information, including the possibility of fines and imprisonment for knowing violations."
Of
��Tl Date

Appendix (c)
Residual Analysis

Pace Analytical Services, Inc.
2225 Riverside Dr.
` r SIC Asheville, NC 28804
[phone]
_ March 03, 2009
Pace Analytical Services, Inc.
9800•KinceyAve. Suite100
Huntersville, NC 28078
[phone]
Mr. Stan Bryson
Tuckaseigee. Water & Sewer Co.
1246 West Main Street
Sylvia, NC 28779
RE: Project: Lime Residual '2/17/09
Pace Project No.: 9238154 r
rY
Dear Mr. Bryson:
Enclosed are the analytical results for sample(s) receivetl- by the laboratory on February 17, 2009.
The -results relate only to the samples included in this report. Results reported herein conform to the
most current NELAC standards, where applicable, unless otherwise narrated in the -body of the..
report:
Inorganic Wet Chemistry and Metals analyses were performed at our Pace Asheville laboratory and
Organic testing.was performed at,our Pace Huntersville laboratory unless otherwise footnoted. All
Microbiological analyses were performed at the laboratory where the samples were received.
If you: have any questions concerning this report, please feel free to contact.me.
erely,
m Williams
'[e-mail] '"���`''�:`
_ Project Manager -
.Enclosures
4 REPORT'OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
-without the written consent of Pace Analytical Services, Inc..
Page 1 of 14

4~ ,,,,II
S` R PrI�II6IlG�CI!
a{' Pace Analytical Services, Inc.
Pace Analytical Se ' "
Yt rvices, Inc.
d ," '`" wwwp"'acetabs c°rrr
2225 Riverside Dr.
Asheville, NC 28804
9800 Kince Ave
y. Suite 100
HuntersyiIle,
NC 28078
(828)2547176
(704)875_9092
ANALYTICAL -RESULTS
_P_[oject; Lime. -Residual, 2/17/09
'Pace Project No.: 9238154 .
:.-.Sampler TWSA Lime Residual Lab ID: 9238154001 Collected: 02/17.109 10:00 Received: 02/17/09 12:16
_ Results -reported on. a `dry-weight".basis
MatriSolid
x:
- Parameters
Results Units Report Limit DF
Prepared Analyzed
CAS No.
6010 MET ICP
Analytical Method: EPA 6010 Preparation Method: EPA 3050
Qual'
Aluminum
Arsenia -
8720 mg/kg 12.4 1
7.7 m /k -'
g g
02/1.8109 15:30 02/20/09 13:01
7429-90-5
0. 1
__.._.._ _07.7 m /k 9
02/18/ob 15:30 02/20/09 13:01
7440-38-2
Calcium
-2
12 1
g
295000 mg/kg 1240. 100
02118/0915:30 02/20/09 13:01
7440-43-9
C- .pper m
7.6 mg/kg
02/18/09 15:30 02/20/09 15:51
7440-70-2
Copper
; tE 6� 1
84.2 mg/kg C : s �' :
02/18/09 15:30 02/20/09 13:01
7440-47-3
:. Leadz.3
1
4.6 m /k
g g
02/18/09 15:30 02/20/09 13:01
1
7440-50-8
4 Magnesium.
2850 mg/kg `
02/18/09 15:30 02/20/09 13:01
7439-92-1
Molybdenum
, 72 4 1
ND mg/kg
02/1810915:30 02/20/09 13:01
7439-95 4
Nicker
0.62 1
1.3 mg/kg
g g
02/18/09 15:30 02/20/09 13.01
7439=98-7 : P8
Potassium
0.62 1
2960 mg/kg
02/18/0915:30 02/20/0913:01.
7440=02-0
Selenium
622 1
7 8'mg/kg
02/18/09 16.30.. 02/20/09 13:01
'7440-09-7
'Sodium
1.2 1
647 mg/kg
02/18/09 15:30 02120/0913:01
•
7782-49-2
Zinc
622 1
256 mg/kg
02/18/09 15:30 02120/0913:01
7440-23-5
7471 Mercury
1.2 1
02/18/09 15:30 02/20/09 13:01
7440-66-6
Analytical Method: EPA 7471 Preparation Method: EPA 7471
erctry
scent Moisture
0.053 m /k
g g 0.0067' 1
02/1910916:20 02/20/0911:11
7439-97-6
r
Analytical Method: ASTM D2974-87
Percent Moisture :.
' . 42.6 % '
9045 pH Soil
0.10 1
03/03/09 13:39
.;
Analytical Method: EPA 9045
pH at25.Degrees G
12.3 Std. Units 0.10 1
Plant Available Nitrogen
Analytical Method: 40CFR PART 503
02/19/09-18:45
.
Plant Available Nitrogen
504 mg/kg.
Total. Nitrogen Calculation
01GQ 1
Analytical. Method: 40CFR PART 503 UM12r 7.
03/03/09 14.08
�. ,Nitrogen
i2�
350.1 Ammonia
1520 mg/kg ,
A.T._ 1
03/0310914:09 7727-37-9
Analytical Method: EPA:350.1
Nitrogen Ammonia
'
351.2 Total Kjeldahl Nitrogen
241 mg/kg -1b':1 1
02/24/09 10:04 776441
-7
Analytical Method: EPA 351.2 -
Nitrogen, Kjeldahl, Total
1520 mg/kg
353.2 Nitrogen NO2IN0 3 .
87.1 1
Analytical Method: EPA 353.2
03/021091.4:35 7727-37-9 Mo
'
Nitrogen, NO2 plus NO3
ND mg/kg
365.1 Phosphorus, Total
16.7 1
Analytical Method: EPA 365.1
02/23/09 15:30
- Phosphorus
235 mg/kg 17.4 5
02/19/0917:37 7723-14-0 R1
Ai
Vie: 03/03/2009 04:26 PM
REPORT OF LABORATORY AN S
Page 4 of 14
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..

A Analytical Results
®�=any .
IL-- -
Pacii�E1a"Wical Mhe.-V@0'e For: 9238154
2225 Riverside Drive
Asheville PVC 28804
Entered 2/18/2009
Reported:_:._-.2/19/2009 _..::'.. .
Sample Remark **RAN OUT OF HOLD per clients request...

Pace Analytical Services, Inc. Pace Analytical Services, Inc.
2225 Riverside Dr. 9800 Kincey Ave. Suite 100
Asheville, NC 28804 Huntersville; NC 28078
[phone] [phone]
ANALYTICAL RESULTS
sdival 5/5/09
race rro)ect No.: 9243444,
1 ... . vv.jn 1-111je 1Ce51Qual
Lab lu: 9243444001 Collected:
05/05/09 10:15 Received: 05/05/09 14:00 Matrix Solid.
Results reported on a "dry -weight" basis
Parameters
Results Units Report Limit
DF
Prepared Analyzed
CAS No.
Qua[ .
6010 MET ICP
Analytical Method: EPA 6010 Preparation Method: EPA 3050
Aluminum :
7916 mg/kg
10.9
1
05/11/09 16:19 05/14/09 00:28
7429-90-5
MO
Arsenic
--Cadmium
6.7 mg/kg
0.55
1
05/11/09 16:1.9 05/14/09 00:28
7440-38-2
___._ __ _ _
0'.44 n g/kg
0.11
1
05/11/09 16:19 05/14/09 00:28
7440-43-9
Calcium
319000 mg/kg
1090
100
05/1170916:19 05/14/09 10:31
7440-70-2
MO
Chromium
7.0 mg/kg
0.55
1
05/11/09 16:19 05/14/09 00:28
7440-47-3
Copper
Lead
62.6 mg/kg
0.55
1
05/11/09 16:19 05/14/09 00,28
7440-50-8
Magnesium
3.5 mg/kg
0.55
1
05/11/09 16:19 05/14/09 00:28
7439-92-1
Molybdenum
2570 mg/kg
10.9
1
05/11/09 1.6:19 05/14/09 00:28
7439-95-4
ND mg/kg
0.55
1
05/11/b9 16:19 05/14/09 00:28
7439-98-7
Nickel
1.3 mg/kg
0.55
1
05/11/09 16:19 05/14/09 00:28
7440-02-0
Potassium
3730. mg/kg
546
1
05/11/09 16:19 05/14/09 00:28
7440-094
MO
Selenium .
6.6 mg/kg
1.1
1
05/11/0916:19 05/14/09 00:28
7782-49-2
Sodium
555 mg/kg
546
1
05/11/09 16:19 05/14/69 00:28
7440-23-5
MO
Zinc
208 mg/kg
1.1
1
05/11/09 16:19 05/14/09 00:28
7440-66-6
.7471 Mercury
Analytical Method: EPA 7471 Pre aration Method: EPA
p . 7471
Mercury
0.41 mg/kg
0.041
5
05/15/0911:30 05117/0913:36
7439-97-6
entWisture
Analytical Method: ASTM D2974-87
Percent Moisture
46.8 %
0.10
1
05/07/0913:40
9045 pH Soil
Analytical. Method: EPA 9045
.- pHat25D egrees C .
.12.0 Std. Units
0.10
1
05/12/0911:25
H1
Plant Available Nitrogen
Analytical Method: 40CFR PART 503
Plant Available Nitrogen
4680 mg/kg
1.0
1
06/05/09 09:20
..
-Total Nitrogen Calculation.
Analytical* Method: 40CFR PART 503
Nitrogen
15500 mg/kg
40.0
1
06/0410910:39
7727-37-9
350.1 Ammonia
Analytical Method: EPA 350.1
Nitrogen, Ammonia
134 mg/kg
16.8
1
05/12/09 11:05
7764-41-7
353.2 Nitrogen; NO2/NO3
Analytical Method: EPA 353.2
Nitrogen, Nitrate
Nitrogen, Nitrite
ND mg/kg
ND mg/kg
18.1-
18.1
1
1
05/15/09 09:08.
Nitrogen, NO2 plus NO3
ND mg/kg
18.1
1
05/15/09 09:08
05/15/09 09:08
365.1 Phosphorus, Total
Analytical Method: EPA 365.1
phosphorus
3640 mg/kg
9.0
1
05/14/09 21:07 7723-14-0
oi'�.
6/05/2009 09:20 AM
REPORT OF LABORATORY ANALYSIS
Page 4 of 13
This report shall not b d
e repro ueed, except in full,
without the written consent of Pace Analytical Services, Inc..

Analytical Results
Pace Analytical Asheville For: 9243444
2225 Riverside Drive
Asheville. NC 28804
Entered 5/6/2009
P.O. Box 228 • -Statesville, North Carolina 28687. 704/872/4697

Analytical X I-sults
Pace Analy-tical Ashevilie For: 9248499
2225 Riverside Drive
Asheville NC 28804
Entered 7/16/2009
Repgited: 7/20/2009
P.O. Box 228 • Statesville, North Carolina 28687 ,, 704/872/4697

c Pace Analytical Services, Inc.
® 2225 Riverside Dr.
" n�irtJcaf.
wwwpacelabs_com; Asheville, NC 28804
}. [phone]
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
ANALYTICAL
RESULTS
Project: Lime Residual 8/11/0*9
Pace Project No.: 9250568=
Sample:. TWSA Lime Residual.
Lab ID: 9250568001 Collected: 08/10/09 00:00 Received: 08/1110915:52 Matrix: Solid
Results reported on a "dry -weight' basis
Parameters
Results Units Report Limit DF
Prepared Analyzed CAS No
�6010 MET ICP
Analytical Method: EPA 6010 Preparation
Method: EPA 3050
. Aluminum.
Arsenic
8590 mg/kg
15.9 1
08/14/00 08:25 08/14/09 19:22 7429-90-5
Cadmium - -
5.7 mg/kg
- _.. - .
- -.
0.79 1
08/14/09 08:25 08/14/09 19:22 7440-38-2.
- ---- -
Calcium
0.25 mg/kg
0.16 1
08/14/09 08:25 08/14/09 19:22 7440 43-9
Chromium
339000 mg/kg
795 50 _
08/14/09 08:25 08/17/09 14:10 7440-70-2
Copper
8.6 mg/kg
93.1 mg/kg
0.79 1
08/14/09 08:25 08/14/09 19:22 7440-47-3
Lead
0.79 1
08/14/09 08:25 08/14/09 19:22 7440-50-8
Magnesium
5.9 mg/kg
0.79 1
08/14/09 08:25 08/14/09 19:22 7439-92-1
Molybdenum
2820 mg/kg
15.9 1
08/14/09 08:25. 08/14/09 19:22 7439-95-4
Nickel
1.1 mg/kg
0.79 1
08/14/09 08:25 08/14/09 19:22 7439-98-7
Potassium
ISelenium
3.3 mg/kg
0.79 1
08/14/09 08:25 08/14/09 19:22 7440-02-0
3320 mg/kg
795 1
08/14/09 08:25 08/14/09 19:22 7440-09-7
Sodium
4.5 mg/kg
1.6 1
08/14/09 08:25 08/14/09 19:22 7782-49-2
Zinc
ND mg/kg
795 1
.08/14/09 08:25 08/14/09 19:22 7440-23-5
17471
284 mg/kg
1.6 1
08/14/09 08:25 08/14/09 19:22 7440-66-6
Mercury
Analytical Method:
Yt EPA 7471 Preparation Method: EPA 7471
Mercury .
0.29 mg/kg
0.042 5
08/13/09 11:41 08/1410911:47 7439-97-6
1 nt Moisture
Analytical Method: ASTM D2974-87
Percent Moisture
41.7 %
0.10 1
08/12/09 00:00
t045 pH Soil
Analytical Method: EPA 9045
H at 25 Degrees C
11.9 Sid. Units
0.10 1
08/14/09 18:45
lant Available Nitrogen
Analytical Method: 40CFR PART 503
(ant Available Nitrogen `
2070 mg/kg
1.0 1
08/25/09 15:53
Total Nitrogen Calculation
Analytical Method: 40CFR PART 503
itrogen
6830 mg/kg
40.0 1
08/25/09 15:53 7727-37-9
350.1. Ammonia
Analytical Method: EPA 350.1 ..
itrogen, Ammonia
208 mg/kg
19.1 1
08/13/09 15:41 7764-41-7
1.. 2 Total Kjeldahl Nitrogen
,
Analytical Method: EPA 351.2
itrogen, Kjeldahl, Total
11700 mg/kg ..
1450 50
08/16/09 11:18 7727-37-9
3.2 Nitrogen, NO2/NO3
Analytical Method: EPA 353.2
Nitrogen, Nitrate
ND. mg/kg
14.3 1
trogen; Nitrite
ND mg/kg
14.3 1
08/18/09 18:01
trogen, NO2 plus NO3
--
ND mg/kg
14.3
08/18/09 18:01
1
08/18/09 18:01
365:1 Phosphorus, Total
Analytical Method: EPA 365.1
osphorus
206 mg/kg
16.3 2
08/1810913:22 7723-14-0
e ovzoos 12:14 PM
REPORT OF I ABORATO
W
H1
Qua[
RY ANALYSIS Page 4 of 13
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..

Analytical Results
i�-
Pace Analytical -Asheville For: 9250568 � T
2225 Riverside Drive.
Asheville NG 28804
Entered 8/12/2009
�-Reported: 8/17/2009
Sample Remark__._
liample ID Parameter CCust I.D Result Units Method Date Analyzes! Analyst
090812-2 %.Solids 9250568001 58.3 % SM2540B , 8/12/09 MD
,090812-2. Fecal Colifoim MTF 9250568001 <20 MPN/g SM92210E 8/12/09 MD
Respectfully submitted,
C ena .Myers
NG Cert #440,.
f NCDW Cert #37755,
P.O. Box 228 o Statesville, North Carolina 28687. 704/872/4697

Analytical Results
Pace Analytical -Asheville For: 9251122
-12225 Riverside Drive
-Ashevillum NC 28804
Entered 8/19/2009
Reported: '8i26/2009
Sample Remark
Osample ID Parameter Cutt I*D Result Units -Metho'd
Date Analyzed Analyst
09081.9-2 % Solids Linie Residual 57.2. SM2540B- 8/19/09
MD
090.819-2 Fecal Colif6rm MTF Lime Residual <20 MPN/g SM9221 CE 8/19/09
MD
Respecffullysubmifted,
fv�
-A
L
NC Cert #440;
NCDW C'ert#'37'7*
EPA. NCO0909
P.O. Box 228 9 Statesville, North Oarolina, 28687 a 704/872/4697

Pace Analyticat Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
ANALYTICAL RESULTS
ct: Lime Residual OS/24
-ae.Proiect No:: 9251576. "
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28018
[phone]
ample: TWSA LIME RESIDUE .-
Lab ID: 9251576001 Collected:
08/24/0911:00
Received: uaizaaua -1z:09 iwauix Qunu
esults reported on'a "dry -weight" basis
Parameters
Results Units Report Limit
DF
Prepared Analyzed
CAS No. Qual
�i010 MET ICP -
Analytical Method: EPA 6010 Preparation Method: EPA 3050
Aluminum
9460 mg/kg
17.4
1
08/25/0913:37 08/27/09 06:10
7429-90-5
:.
0.87
1
08/25/0913:37 08/27/09 06:10
7440-38-2
Igrsenic - ...
admium
0.63 mg/kg
0.17
1
08/25/0913:37 08/27/09 08:10
.7440-43-9
331000 mg/kg
1740
100
08/25/0913:37 08/28/0912:54
7440-70-2
calcium
Chromium
11.9 mg/kg
1.9
0.87
1
08125/0913:37 08/27/09 06:10
7440-47-3
tipper
04 mg/kg
0.87
1
08/25/09 13:37 08/27/09 06:10
7440-50-8
R-op
mg/kg
0.87
1
08/25/0913:37 08/27/09 06:10
7439-92-1
29.0 mg/kg
20
17.4
1
.08/25/0913:37 08/27/09 06:10
7439-95-4
Magnesium
Molybdenum
mg/kg
0.87
1
08125/0913:37 08/27/09 06:10
7439-98-7
_Molybdenum
i
4.6 mg/kg
0.87
1
08/25/0913:37 08/27/09 06:10
7440-02-0
otassium
3690 mg/kg
870
1.
08/25/0913:37' 08/27/09 06:10
7440-09-7
Selenium
5.8 mg/kg.,
1.7
10
08/25/0913:37 08/27/09 06:10
7782-49-2
ND mg/kg
870
1
08/25/0913`:37 ' 08/27/09 06:10
7440-23-5
Sodium
324 mg/kg
1.7
1
08/2510913:37 08/27/09 06:10
7440-66-6
inc :
Analytical Method: EPA 7471 Preparation Method: EPA 7471
7471 Mercury
- '
0.50 mg/kg
0.038
5
09/01/09 08:02 09/01/09 13:48
7439-97-6
eerrcury
t Moisture
Analytical Method: ASTM D2974-87
Percent Moisture
44.7 %
0.10
1.
08/31/0914:11
045.pH Soil
Analytical Method: EPA 9045
pH at 25 Degrees C
12.4 Std. Units
0.10
1
09/04/0916:00
H1
lant Available Nitrogen..
Analytical Method: 40CFR PART 503
R-lant Available Nitrogen
3630 mg/kg.
1.0
1
08/31/0916:09
otal Nitrogen Calculation
Analytical Method: 40CFR PART 503
itro en
g
11900 mg/kg
40.0
1
08/31/09 16:06
, 7727-37-9
:�.-.-350.1 Ammonia
Analytical Method: EPA 360.1
itrogen, Ammonia
286 mg/kg
15.1
1
08/27/09 17:01
7764-41-7
.
351.2 Total Kjeldahl Nitrogen
Analytical Method: EPA 351.2
Kjeldahl, Total _
11900 mg/kg
862
10
08/30/09 12:02 7727-37-9
.1 Wit.rogen,
i,,53.2- Nitrogen, NO2IN03
Analytical Method: EPA 353:2
Nitrogen, Nitrate
ND mg/kg
18.1
1
08/28/09 09:00
itrogen, Nitrite
ND mg/kg4
18.1
1
08/28109 09:00
itrogen, NO2 plus NO3
ND mg/kg
18.1
1
08/28/09 09:00
i.1 Phosphorus, Total . Analytical Method: EPA 365.1
�sphorus 155.mg/kg 15.1 1 09107/0914:00 7723-140
it 09/11/2009 04:37 PM. REPORT OF LABORATORY ANALYSIS.
This report shall not be reproduced, except in full,
without the written consent of Pace. Analytical Services, Inc..
- ,N ♦CCpR�'
1 n
Page 4 of 14

F -
'y
Analytical Results
!ace Analytica-A.4hevAlle For: 9251576
2225 Riverside Drive
Asheville NC 28804
Entered 8/25/2009
Reported:, 9/2/2009
-Sample Remarks '
Sample OD Parameter. Cust.113 Result Unit Method Date Ana�yaed Analyst
090825-13 % Solids 9251576001 57.4 % SM2540B 8/25/09 CL
090825-13 Fecal Col'iform IVITF 9251576001 <3 MPN/g SM92210E 8/25109 CL
Respectfully submitted,
Dena Myers J
=: NCDW Cert. #37755
EPA NC00909
P.O. Box 228 • Statesville, North Carolina 28687 0 704/872/4697

A.,
Appendix (d)
zoo9
TCLP Analysis

ace -Mali cal
f
www.pacebbs co.:
Pace Analytical Services, Inc.
2225 Riverside Dr.
Asheville, NC 28804
[phone]
ANALYTICAL RESULTS
Pace Analytical Services, Inc.
9800 Kincey Ave. Suite 100
Huntersville, NC 28078
[phone]
Project: TWSA #1 Sludge 8/18/09
Pace Project No.: 9251120
Sample: Sludge Lab ID: 9251120001 Collected: 08/18/0910:30 Received: 08/18/09 13:00 Matrix: Water
Parameters, Results Units Report Limit DF Prepared Analyzed CAS No. Qual
8081 GCS Pesticides, TCLP SPE
Analytical Method: EPA 8081 Preparation Method: EPA 3535
Leachate Method/Date: EPA 1311; 08/25/09 14:42
gamma-BHC (Lindane)
ND ug/L
0.50 1
08/28/09 14:00 09/02/09 11:36
(Technical)
ND. ug/L
3.0 1
.58-89-9
08/28/09 14:00 09/02/09 11:36 57-74-9
UChlordane.
; Hepta
Heptachlor epoxide.
ND ug/L
0.50 1
08/28/09 14:00 09/02/09 11:36 72-20-8
Methoxychlor
ND ug/L
0.50 1
08/28/09 14:00
09/02/09 11:36 1024-57-3
Toxaphene
ND ug/L
ND ug/L
1000 1
08/28/09 14:00
09/02/09 11:36 72-43-5
Decachlorobiphenyl (S)
11 %
3.0 1
08/28/09 14:00
09/02/09 11:36 8001-35-2
Tetrachloro-m-xylene (S)
19 %
10-138 1
08/28/09 14:00
09/02/09 11:36 2051-24-3
10-110 1
08/28/09 14:00
09/02/09 11:36 877-09-8
6010 MET ICP, TCLP
Analytical Method: EPA 6010 Preparation Method: EPA 3010
Leachate
Method/Date: EPA 1311; 08/24/09 15:13
Arsenic
Barium
ND mg/L
0.025 1
08/25/09 09:25
08/27/69 03:37 7440-38-2
.
Cadmium
0.039 mg/L
ND mg/L
0.025 1
0.0050 1
08/25/09 09:25
08/25/09 09:25
08/27/09 03:37 7440-39-3
i Chromium
08/27/09 03:37 7440-43-9
Lead
ND mg/L
0.025 1
08/25/09 09:25
08/27/09 03:37 7440-47-3
ND mg/L
0.025 1
08/25/09 09:25
08/27/09 03:37 7439-92-1
,'. rnium
ND mg/L.
0.050 1
08/25/09 09:25
08/27/09.03:37 7782-49-2
(44f
ND mg/L
0.025 1
08/25/09 09:25
08/27/09 03:37 7440-22-4
7470 Mercury, TCLP
Analytical Method: EPA 7470 Preparation Method: EPA 7470
Leachate Method/Date: EPA 1311; 08/24/09 15:13
Mercury
ND ug/L
0.20 1
08/25/09 09:16
08/25/09 12:37 7439-97-6
8270 MSSV TCLP Sep Funnel
Analytical Method: EPA 8270 Preparation Method: EPA
3510
Leachate Method/Date: EPA 1311; b8/25/09 14:42
1,4-Dichlorobenzene
ND ug/L
25.0 1
08/31/09 10:00
09/03/0914:58 106-46-7
_-:- 2,4-Dinitrotoluene
Hex6chloro-1,3-butadiene
ND ug/L
25.0 1
08/31/09 10:00
09/03/09 14:58 121-14-2
` Hexachloeobenzene
ND ug/L
25.0 1
08/3110910:00
09/03/09 14:58 87-68-3
.
Hexachloroethane
ND ug/L
25.0 1
08/31/09 10:00
09/03/09 14:58 118-74-1
2-Methylphenol(o-Cresol)
ND ug/L
ND ug/L
25.0 1
08/3110910:00
09/03/09 14:58 67-72-1
3&4-Methylphenol(m&p Cresol)
218 ug/L
25.0 1
08/31/09 10:00
09/03/09 14:58 95-48-7
Nitrobenzene
25.0 1
08/31/09 10:00
09/03/09 14:58
Pentachlorophenol
ND ug/L
25.0 1
08/31/09 10:00.
09/03/0914:53 98-95-3
Pyridine
ND ug/L
25.0 1
08/31/09 10:00
09/03/09 14:58 87-86-5
2,4,5-Trichlorophenol
ND ug/L
ND
25.0 1
08/31/09 10:00
09/03/09 14:58 110-86-1
-52-
4,6lrichlorophenol.
ug/L
ND ug/L
25.0 1
08/31/09 10:00
09/03/09 14:58 95-95-4
; "Nitrobenzene d5 (S)
49 %
25:0 1
08/31/09 10:00
09/03/09 14:58 88-06-2
k.
=rpheFluorobiphenyl (S)
56 %
30-150 1
08/31/09 10:00
09/03/09 14:58 4165-60-0
nyl d14 S)
U-Te
55 %
30-150 1
08/31/09 10:00
09/03/09 14:58 321-60-8
i--
;` Phenol-d6 (S)
30-150 1
08/31/09 10:00
09/03/09 14:58 1718-51-0
-...
=-2=Fluorophenol (S)
25 %
34 %
25-150• 1
08/31/09 10:00
09/03/09 14:58 13127-88-3
.--.24,6-Tnbromophenol(S)
49 %.
25-150 1
08/31/09 10:00
09/03/09 14:58 367-12-4
,Jas
25-150 1
08/31/09 10:00
09103/0914:58 118-79-6
09/04/2009 02:43 PM REPORT OF LABORATORY ANALYSIS
This report shall not be reproduced, except in full,
without the written consent of Pace Analytical Services, Inc..
`K\ 4
Page 5 of 15

Pace Analytical Services, Inc. Pace Analytical Services, Inc.
aceMal rtcal
2225 Riverside Dr. 9800 Kincey Ave. Suite 100
/r
nnvwpeceia6s°com: Asheville, NC 28804 Huntersville, NC 28078
t [phone] [phone]
ANALYTICAL RESULTS
Project: TWSA #1 Sludge 8/18109
Pace -Project No.: 9251120
Sample: Sludge Lab ID: 9251120001 Collected: 08/18/09 10:30 Received: 08/1.8/0913:00 Matrix Water
Parameters Results Units - Report Limit DF Prepared Analyzed CAS No. Qual
8260 MSV TCLP Analytical Method: EPA 8260
Benzene ND ug/L 125 25 08/24/09 15:20 71-43-2
2-Butanone (MEK) 319 ug/L 250 25 - 08/24/09 15:20 78-93-3
Carbon tetrachloride ND ug/L 125 25 08/24/09 15:20 5
Chloroform
Chiorobenzene —_ --_— -- - " ND ug/L 125 25 08/24/09 15:20 56-23-56-23--7
ND ug/L 125 25 08/24/09 15:20 67-66-3
1,4-Dichlorobenzene ND ug/L 125 25 08/24/09 15:20 106-46-7
®1,2-Dichloroeth:ug/L 125 25 08/24/09 15:20 107-06-2
1,1-Dichloroethene ne ND ND ug/L 125 25 08124/0915:20 75-35-4
Tetrachloroethene ND ug/L 125 25 08/24/09 15:20 127-18 4
Trichloroethene ND ug/L 125 25 08/24/0915:20 79-01-6
Vinyl chloride ND u /L 08/24/09 15:20 75-01-4
bl*uei *e-d8 S) ' d4 (S) 94 % 79-120 25 08/24/09 15:20 17060-07-0
Toluene-d8 (S) 101 % 70-120 25
4Bromofluorobenzene (S) 96 % 08/24/09 15:20 2037-26-5
87-109 25 08/24/09 15:20 460-00-4
Dibromofluoiomethane (S) 94 % 85-115 25 08/24/09 15:20 1868-53-7
9095 Paint Filter Liquid Test' Analytical Method: EPA 9095
Free Liquids 0 mL/5min 1.0 1 08/28/0919:45
i l
09/04/2009 02:43 PM REPORT. OF LABORATORY ANALYSIS Page 6 of 15
This report shall not be reproduced, except in full,
r without the written consent of Pace Analytical Services, Inc..

R"
Analytical Environmental Services, Inc Date: 26-Aug-09
Client: Pace Analytical Services, Inc.
Client. Sample ID: SLUDGE -
Project: 9251120 Collection Date: 8/18/2009 10:30:00 AM
Lab ID: 090809-001 Matrix: Aqueous,
Analyses
Result
Reporting Qual
Units BatchED
Dilution
Date Analyzed Analyst
Limit
Factor
HERBICIDES, TCLP SW1311/8151A
(SW3510B)
2,4,5-TP (Silvex)
BRL
0.20
mg/L. 117392
1
08/2412009 21:38 AK
2,4-D
BRL
0.20
mgIL 117392
1
08/24/2009 21:38 AK
S.: DCAA
94.9
36.6-149
%REC .117392
1
08/24/2009 21:38 AY,
w
Qualifiers:
Value exceeds maximum contaminant livtil
E Estimated (value above quantitation range)
BRL Belowrepqrting limit
S Spike Recovery outside limits due to matrix
H Holding times forprdparation oranalysis exceeded a
Nan' See case narrative
N Analyte not NELAC certified
NC Not confirmed
B Analyte detected in the associated method blafik�
< Less than Result vain
> Greater than Result value
Page 3 of 5

j
A
Appendix (e)
v
Pathogen and.'
Vector Attraction
Reduction Form

7
ANNUAL PATHOGEN AND VECTOR ATTRACTION REDUCTION FORM
Facility Name: p P-e- Permit Number: (Arc) 0006 9/93
i... Ak
VNffPNanie: NPDES. Number: AE
Monitoring Period: From Th To
Pathogen Redix6tion. (40 CFR 503.32) - Please indicate level achieved and alternative performed:
Class A:
Alternative 1 D
Alternative 2 ❑
Alternative 3 ❑
.... .. . ....
........ . .
Alterndtive.4
Alternative 5
Al
Alternative
ive' 6 0
.......
If applicable to alternativeperformed (Class A only) indicate "Process to Further Reduce Pathogens":
Compost E3
Heat Drying �Ej
Heat Treatment ❑
Thermophilic ❑
Beta Ray
'a Ray [I
Pasteurization
_77 Alternative2 [3
--C-4ass-B.—I���—Alte-mative--IEI:& - . . Alternative 3 El
if.applicable to alternative performed (Class B only) indicate "Process to- Significantly Reduce Pathogens": —
Lime Stabilization ❑
Air Drying El Composting. El '
jAerobic Digestion 0
Anaerobic Digestion[]
...........
................ ........................................
X ...................
................. .. ........ : ....... 1.1.!.-.1...-....1.*.1.*:1 .................................
....... ........ .......
If -applicable to alternative performed (Class A or. Class B) complete the following monitoring data:
iAllo . wdble-Ltiel
Pathogen Density
Number of
Excee-
Frequency
'Sample
Analytical
Paradneter,
in Sludge
Minimum
Geo. Mean
MaximuTr
Uni S
dences
(if Amalygis
Type
Tech -pique
2 x .10 to..the 6th.
power 1M.PN per
gram of total
.
solids or2x 10to
'Fecal'Co"lifdrm
tho 6t4: power
..gj=
CFU'1j 'um of
i000 rapfiper
of total.solid
,rA P P11r
M.
(dry weight)'
'[
Salmonella badtPria.
3 NTN per 4.
jffi.lieu.of fecal.
granis total solid.
(di* Weight).
Vector Attraction Reductio*11:.(4.0'CFR 503.33) Please indicate .option performed:
............
Op
tion 'El] - Option 3 -0" JOption El' Option 5 [1
...........
Option 0joption-7. 111Option 8. .0. option 9 ❑ 1.Option 10
. ................
.................. e1.'.'.'.*.1 ................
................ ....................
.... ............
.................................
................
No: vector attraction reduction options were performed 0 .............. I ... X.7 ...................
.. ..........................................
CERTIFICATION STATEMENT (please check the appropriate -statement)
"I certify,. nn . der penalty of law, that the: . pathogen. requirements in 40 CFR 503.32 and the vector
,
-attraction -t e-duction- requirement -in 40 CFR 503.33 have been met."
El ."I- certify, under penalty of law,, that the.pathogeii requirements in 40 CFR 503.32 and the vector
attraction reduction requirein e*n*t in 40 CFR 503.33 have not been biet." (Please note if you check
this. statement attach an explanation why you have not met one or both of the requirements.)
"This determination has been made under my direction and supervision in accordance with the
system designedlo. ensure that qualifie.d.pers6nnel properly gather and evaluate. the information
'used to determine that the pathogen athogen and vector attraction reduction requirements -have been met. I
,,*g'axn aware that there are significant penalties for false certification including fine and imprisonment."
Sb r ,4;5W _W w
P-repar r Nameand Title .(type or print) Land Applier Name and Title (if applicable)(type'or print)
'*

Appendix (g)
2009 SLUDGE DATA
TWSA PLANT # 1 (1.5 mgd)
NPDES # NC0039578
SLUDGE TO DIGESTOR............................................................... 11,467,000 gallons
total lbs....................................................................497,315 lbs
total tons.............................................................. .248.7 tons
-- -- - -- - total metric tons........................................................225.5 metric tons
TWSA PLANT # 2 (.5 mgd)
NPDES # NCO020214
SLUDGE HAULED TO PLANT # 1................................................ 322,746 gallons
total tons...................................................................24.86 tons
total metric tons........................................................22.55 metric tons
TWSA PLANT # 3 (.1 mgd)
NPDES # NCO063321
SLUDGE HAULED TO PLANT # 1.................................................... 47,006 gallons
total tons............................:........................................ 4.36 tons
total metric tons...........................................................3.95 metric tons
Septage Receiving Station................................................347209 gallons
total tons................................................................20.25 tons
total metric tons......................................................18 37 metHe tons
A portion of the sludge that was generated at the Tuckaseigee Water and Sewer Authority
during 2009 was hauled by a private contractor to a designated landfill.
Landfill: R&BLandfill
610 Frank Bennett Road
Homer GA 30080
A total of 93a 2 wit tons were hauled to the landfill during 2009.
Copies of haul tickets can be provided if needed.

PROCESS SUMMARY SHEET
PLANT NAME TWSA #1
. ANNUAL (2009)
)R THE PERIOD OF
1/1/2009 THROUGH
12/31/2009
ANT FLOW, mgd
0.887
daily avg
FLUENT BOD, mg/I
180.8
daily avg
'FLUENT SS, mg/I
27.2
daily avg
LSS, mg/l
2636
daily avg
3SS, mg/I
5254
daily avg
AS RATE, mgd
0.03142
daily avg
_R. BASIN VOL., mg
0.468
.ARIFIER VOL, mg
0.1508
M RATIO
LB APPLIED/LB UNDER AERATION
CRT
i It , ;1 DAYS
_._..- -- - -._ ._ _ ---.-----AC-T-IVAT-ED SLUDGE DATA
30 MIN
SETT.
SLUDGE
485
MLSS
m /I
3044
MLVSS
m /I
2462
EFF
FLOW
MGD
0.979
RSSS
m /I
6679
ZSV
ftthr
4.6
SVI
159
MCRT
da s
13
SLUDGE WASTING
allons Ibs
522,000 26,939
704
2932
2494
0.889
5358
3.2
E34
794,500
37,830
;10
510
2332
1975
0.857
5375
6.3
210
1,033,500
41,016
653
2765
2262
0.901
- 5823
4.8
231
8
954,000
46,677
528
2670
2133
0.914
5423
5.1
194
10.
828,000
37,905
542
2590
2060
0.706
4666
4.3
205
8
1,134,000
46,690
530
2351
1884
0.665
4271
4.7
219
9
1,035,000
38,218
562
2468
2048
0.719
4305
5.2
223
8
1260,000
47,013
591
2560
2033
0.995
4818
3.4
230
8
1,161,000
45,672
587
2852
2270
0.949
6020
4.2
203
8
974,250
50,550
401
2642
2169
1.015
5298
5.7
148
8
999,000
44,566
403
2429
1955
1.049
5007
5.8
160
9
771,750
34,239
541 2636 2145 0.887 5254 4.8 201 9
704 3044 2494 1.049 6679 6.3 234 13
401 2332 1884 0.665 4271 3.2 148 8
Total Gallonsil1,467,000
Daily Averag
Te%+mi +nnc X 9n7 metric
955,583
1,260,000
522,000
1363
50550
`26939
497,315
31 416
248.7
ton/English
ton=
225.5 My Metric Ton
�datly;;
dotal lbs.
Total tons

2009
TWSA #2 SLUDGE PRODUCTION
MONTH
DATE
Gals Hauled To
TWSA # 1
% SOLIDS
TOTAL
DRY TON
Hauler
JanuarV
0
0.00
.,IT,... ta'l
Februa
2116
24,729
2.66
2.74
Plank
1
1! 41
March
3/26
19,132
2.08
1.66
Cooper
3/27,
6,936
2.11
0.61.
Cooper
1 If I H 11
i I I I I iM,
April
4/14
4.,494
1.87
0.35
Plank
4/15
16,738
1.79
1.25
Cooper
4/16,
4,843
1.72
0.35
Cooper
4/21
13,671
1.81
1.03
Plank
4/29
25,303
2.11
2.22
Plank
May
5/22
23,478
1.97
1.93
Cooper
a
4n 7
in it
June
6/3
22,891
2.14
2.04
Plank
6/23
26,629
2.10
2.33
Cooper
M,
July
7/27
19,077
1.23
0.98
Cooper
7/28
7269
1.17
0.35
Cooper
7/30
23342
1.44
1.40
Plank
t
.14
August
8/27
11,649
1.79
0.,87
TWSA
8/28
4,795
1.33
0.27
TV1JSA
n ffill T:,
A
1 '3
September
913
21,584
1.33
1.20
TWSA
914
16904
1.35
0.95
TWSA
9/10
7210
1.46
0.44
TWSA
9/17,
7200
0.41
TWSA
jw
it it
ij:. if 1 R!
October
0.00
TWSA
Manthl
0ti
5i
il Pildbo
November
11/18
7,082
1.44
0.42
TWSA
11/19
14,330
1.78
1.06
TWSA
M
- -
1� ----T..-b
-1-111.112*
-11A
Tl
Decemberl
-fl W-9.
TOTAL 3227461
TOTAL 24.86 X.907 metric ton/English Ton
22.55 = Dry Metric Tons

.2009
TWSA #3
Sludge Production
MONTH
Date
Gals Hauled To
TWSA # I
AVG
% SOLIDS
TOTAL
DRY TON
Hauler
JanuarV
Feb.
0
H. ......
R nth ;,TotalMarch
HLA lit"
'060*0
HNM-;Iji'
Nil
----------
A. 40011Y.-Twi
April
7777777
11 t
hthh-.IT
NOW
May
5/15
6,194
2.82
0.75
Coopers
5116
4,039
0.39
Coo ers
5/18
4,682
1.52
0.30
Coopers
5/19
7,016
1.63
0.48
Coo ers
5/20.
2,342.
3.39.
0.33
Coopers
N�'.
t*tbI.vhiITb
June
M hthk:Tote
Julyl
vil-r-jr-l-Ill-il"'
Auaust
Mill
n t h 1, T-f - I
11/9
4,581
2.54
Hit M.0
0.48
Coopers
Sep.
11110
4602
2.54
0A9
Coo ers
11/11
2202
2.57
0.24
Coopers
11112
2340
2.59
0.25
Coopers
11116
4413
1.76
0.32
Coopers
11/17
4405
. . P, 1 " I i -.
0.32
Coopers
IN.p[liq -.M
-
h, 1 IT
H 22 fiQ
Oct
Mon.
Tote t
IiIN N
Nov.
,
Toll[; i7l'ifl-11 00
Dec.
11, Mfg
47.006
1
4.36
TOTAL 1
TOTAL 4.36 X .907 metric ton/English Ton
3.95 = Dry Metric Tons

2009
Septage Receiving Station
MONTH
Beginning
Reading
Ending
Reading
Gals Received @
TWSA # 1
- Gals of Sludge from
TWSA # 2 & 3
= total gallons
se to a received
January
11882,660
1904,881 881
22,171
0
22,171
February
1,904,831
1,983,471
78,640
24,729
53 911
March
1,983,471
2,035,792
52,321
26,068
26,253
_Aril
_ _ 2,035,792,
2,140 043
104,251
65 049
39 202
Ma
2 140 043
2 237 394
97 351
47 941
49 410
June
2,237,394
2,314 773
77,379
49,520
27,859
July,2,314,773
2 406 789
92,016
43,148,
48,868
August
2,406,789
2,469,350
62,561
16,444,
46,117
September
2,469 350
2,553,049
83,699
52,898
30,801.
October
2,553,049
2,602,583
49,534
0
49534
November
2,602,583
2,651,765
49,182
21,412
27770
December
2,651,765
2,700,047
49.182
0
49 182
TOTAL
818,287
347 209
471 778 .
TOTAL _347.209 gallons x 1 4% (1994 long term monitoring)
24000
= 20.25 tons x .907metric tons/English ton
=18.37 dry metric tons

SECTION 11244 POLYMER FEED SYSTEM
PART 1: GENERAL
1.01 SCOPE OF WORK
A. The polymer feed system shall include all components necessary for the
mixing, storage and metering of emulsion polymer, the metering of the
water supply, and all necessary starters, and control panels. The system
shall be furnished complete with all components described herein to
ensure uniformity of appearance of the installation and eliminate divided
responsibility for parts, service, and operation. The equipment furnished
shall be installed at the location indicated on the plans.
B. Unless otherwise noted, all materials and equipment supplied under this
Section shall be new, of good quality, and in good condition.
1.02 SYSTEM DESCRIPTION
A. General: The polymer feed system shall automatically meter, dilute, activate
and feed emulsion polymer and water. The system shall be a self contained
unit supplied on a skid with connections for power, water supply, emulsion
polymer, and mixed polymer discharge.
1.03 QUALITY ASSURANCE
A. The polymer feed system shall be the product of a company which has
manufactured chemical feeders of comparable type and capacity for at
least five years.
1.04 SUBMITTALS
A. Shop Drawings: The Contractor shall submit at least six (6) copies of
complete shop drawings to the Engineer for approval.
B. Operation and Maintenance Manuals: The Contractor shall submit at least
three (3) sets of operation and maintenance manuals to the Engineer.
1.05 DELIVERY, STORAGE AND HANDLING
A. All materials and equipment shall be delivered, stored and handled in
strict accordance with the manufacturer's recommendations.
Rev. 6123/09 PROJECT # 05734 11244 - Page 1

1.06 WARRANTY
A. The manufacturer shall warrant the equipment to be free from defects in
material and workmanship for a period of one (1) year after being placed
into operation.
1.07 MANUFACTURER AND SUPPLIER INFORMATION
A. Manufacturer Nameplate:A manufacturer's nameplate shall be securely
and permanently mounted to each individual piece of equipment furnished
under this Section. The nameplate shall be constructed of a durable, non-
corrosive material. Critical information shall be clearly engraved or
otherwise permanently stamped on the nameplate, and shall be fully
legible. The information contained on the manufacturer nameplate shall
include at least the following:
1. Manufacturer's Serial Number
2. Name, address and telephone number of equipment manufacturer
3. Model and/or Part Number, including pump impeller sizes, when
applicable
4. Performance Criteria (i.e., capacity, design point, etc.)
5. Motor size, speed and voltage
6. Enclosure Type or Rating
7. Any other pertinent information
Note: All equipment shall include a nameplate with a manufacturer serial
number validating the equipment as new. Failure to meet these
requirements will be cause for rejection of the equipment.
B. Supplier and Service Information: A durable nameplate, stamp or sticker
shall be adhered to each individual piece of equipment containing the
name, address, and telephone number of the local business that supplied
the equipment, and the name, address and telephone number of the local
business that can provide service and replacement parts for the
equipment. A 24-hour emergency service telephone number should also
be included.
Rev. 6/23/09 PROJECT # 05734 11244 - Page 2

PART 2: PRODUCTS
2.01 EQUIPMENT
A. GENERAL REQUIREMENTS
The polymer feed system shall automatically meter, dilute, activate and
feed emulsion polymer and water. Concentrated polymer and water shall
be blended in a completely mixed environment that shall meet polymer
supplier's recommendations at maximum throughput. The equipment
furnished shall be installed at the location indicated on the plans.
B. POLYMER SYSTEM
The system shall include a progressive cavity type polymer metering
pump capable of pumping emulsion type polymer at an output range
suitable for a 1.0 meter belt filter press. The system shall include a
metering pump calibration assembly with isolation valves. The system
shall have a solenoid valve for on -off control of dilution water supply and a
flow indicator equipped with an integral rate adjusting valve. The water
flow rate shall be adjustable in a flow range suitable for a 1.0 meter belt
filter press. Solids concentration of the sludge as fed to the belt filter press
shall be 1.0 to 4.0 percent oven dried solids (ODS).
C. Drum Mixer
The manufacturer shall provide (1) mechanical mixer sized to completely
mix the contents of a 55 gallon drum.
D. CONTROLS
An independent polymer system control panel shall be provided for the
operation of the system. The complete system shall be UL listed and
labeled as a system. Provision shall be made for both manual and
automatic control with individual stop and start pushbuttons for all
motor -driven components and actuation of the water supply. The controls
shall be arranged such that in the event of water supply failure it shall shut
down automatically. Upon restoration of the water supply, or of power
after power failure, the system must be restarted in automatic mode.
Timing controls shall be provided for adjustment of polymer mixing cycle.
The control panel shall obtain a 4-20ma control signal from the Belt Filter
Press Control Panel to set the polymer flow rate. The control panel shall
provide an output signal to the Belt Filter Press Control panel in the event
of polymer system failure. Control panel shall be designed to accept
120/208 V, 1 phase, 3 wire power supply.
Rev. 6123109 PROJECT # 05734 11244 - Page 3

PART 3: EXECUTION
3.01 INSTALLATION
A. All equipment shall be installed as shown on the drawings, and in strict
accordance with the manufacturer's recommendations.
3.02 QUALITY CONTROL AND FIELD TESTING
A. Quality Control: The polymer system manufacturer shall provide a trained
service engineer for initial start-up, calibration and adjustment of
equipment and instruction of plant personnel for one (1) eight hour day.
The manufacturer shall, during the warranty period of one year, furnish all
service necessary to repair defective equipment or work, and no charge
will be made for any service due to these reasons. A complete written
report shall be furnished to the Owner and' -Engineer after each service
visit giving the reason for failure and recommendations to prevent
recurrence.
B. Field Testing: The Contractor shall demonstrate to the Owner and the
Engineer that all equipment is operating as designed and specified.
3.03 SPARE PARTS
A. The Contractor shall furnish one (1) complete set of manufacturer
recommended spare parts and convey the spare parts to the Owner.
END OF SECTION
Rev. 6/23109 PROJECT # 05734 11244 - Page 4

SECTION 11315 PROGRESSIVE CAVITY SLUDGE PUMPS
PART 1: GENERAL
1.01 SCOPE OF WORK
A. This section shall include the furnishing and installing of electrically
operated progressive cavity sludge pump with all accessories and
appurtenances as specified herein and shown on the plans. All electrical
appurtenances shall be furnished and installed in accordance with the
Electrical Section of these specifications.
B. Unless otherwise noted, all materials and equipment supplied under this
Section shall be new, of good quality, and in good condition.
1.02 QUALITY ASSURANCE
A. All equipment shall be supplied by reputable manufacturers with at least
five (5) years of experience in the manufacture of progressive cavity
sludge pumps. The manufacturer shall have at least five (5) successful
installations of similar design, and shall submit evidence of experience if
requested by the Engineer.
1.03 SUBMITTALS
A. Shop Drawings: The Contractor shall submit six (6) sets of complete shop
drawings, including performance curves, dimensions, catalogue cut
sheets and materials of construction.
B. Operation and Maintenance Manuals: The Contractor shall submit three
(3) copies of operation and maintenance manuals to the Engineer.
1.04 DELIVERY STORAGE AND HANDLING
A. All materials and equipment shall be delivered, stored and handled in
strict accordance with the. manufacturer's recommendations.
1.05 WARRANTY
A. All complete pumping units, including electric motors, auxiliary units, and
mounts shall be warranted by the Contractor against all defects in
materials and workmanship for a period of one (1) year from the date of
final acceptance. The Contractor shall be obligated within one year at no
cost to the Owner.
Rev. 6123/09 PROJECT # 05734 11315 - Page 1

C. The performance of all pumps, motors and auxiliary units shall be
guaranteed at the specified pumping conditions.
1.06 MANUFACTURER AND SUPPLIER INFORMATION
A. Equipment shall be as manufactured by Monoflow Inc., Moyno Inc.,
Seepex Inc., or Tarby. Manufacturers are listed only to denote the quality
standard of product desired, general style, type, character and do not
restrict bidders to a specific manufacturer. Substitution of equipment of
equivalent or equal design shall be submitted to the Engineer for approval
or disapproval in accordance with Article 11 of the Instructions to Bidders.
B. Manufacturer Nameplate: A manufacturer's nameplate shall be securely
and permanently mounted to each individual piece of equipment furnished
under this Section. The nameplate shall be constructed of a durable, non-
corrosive material. Critical information shall be clearly engraved or
otherwise permanently stamped on the nameplate, and shall be fully
legible. The information contained on the manufacturer nameplate shall
include at least the following:
1. Manufacturer's Serial Number
2. Name, address and telephone number of equipment manufacturer
3. Model and/or Part Number, including pump impeller sizes, when
applicable
4. Performance Criteria (i.e., capacity, design point,, etc.)
5. Motor size, speed and voltage
6. Enclosure Type or Rating
7. Any other pertinent information
Note: All equipment shall include a nameplate with a manufacturer serial
number validating the equipment as new. Failure to meet these
requirements will be cause for rejection of the equipment.
B. Supplier and Service Information: A durable nameplate, stamp or sticker
shall be adhered to each individual piece of equipment containing the
name, address, and telephone number of the local business that supplied
the equipment, and the name, address and telephone number of the local
business that can provide service and replacement parts for the
equipment. A 24-hour emergency service telephone number should also
be included.
Rev. 6/23/09 PROJECT # 05734 11315 - Page 2

PART 2: PRODUCTS
2.01 EQUIPMENT
A. Pump Design and Construction:
1. The pump shall be capable of handling sludge generated from
water and wastewater treatment plants, and sized to pump 25 - 100
gpm over a 50 PSI range at a maximum speed of 175 RPM.
Maximum total dynamic head at the higher operating condition is
67 feet.
2. The pump shall be cradle mounted with the suction port capable of
being rotated through a full 3600. The pump unit shall be provided
with anti -rotation devices to prevent reverse rotation of the pump
when stopped. The drive unit shall be standard integral electric
motor direct connected into the pump unit. The complete pump
and motor unit shall be steel base mounted with anchor bolts
provided.
3. The pump shall be driven by a direct -connected variable speed 7.5
HP drive or gear reducer. Pump motor shall be TEFC inverter duty
rated design for 480 volt service. A heat sensor thermostat shall be
imbedded in top of winding and be connected in series with the
motor starter coil in control box to stop motor if temperature rises in
excess of the manufacturers recommendation for any reason.
4. The pump casing shall be of cast iron with all exposed nuts and
bolts to be stainless steel. The pump shall be constructed such
that a single helix rotor revolves eccentrically within a double helix
stator of twice the pitch length so that the formed cavities progress
toward the discharge end of the pump. The suction and discharge
connections shall be standard flanged. The stator shall be
compounded elastomers and the rotor chromium plated steel. The
pump drive shaft shall be a machined steel, chromium -plated
hollow shaft with a gear -type universal joint. The packing and
stuffing box shall contain a packing gland and lantern ring with
fittings for grease lubrication.
5. Progressive Cavity Sludge Pump shall be controlled by the Sludge
Processing Area Control Panel (SPACP-550) via the Sludge Feed
Control Panel (SFCP-550) over the fiber optic network. Refer to
Division 13 and the system architecture plan for the composition of
this system.
Rev. 6/23/09 PROJECT # 05734 11315 - Page 3

PART 3: EXECUTION
3.01 INSTALLATION
A. All equipment shall be installed as shown on the drawings and in strict
accordance with the manufacturer's recommendations.
3.02 QUALITY CONTROL AND FIELD TESTING
A. Quality Control: The manufacturer shall provide the services of a qualified
field representative for one (1) 8-hour day to inspect the installation and
provide start-up, field testing and operator training services.
B. Field Testing: The pump(s) shall be field tested after proper installation.
The field running tests shall be conducted by the Contractor and
witnessed by the Engineer and shall demonstrate the following under all
conditions of operation, insofar as the available flow will permit; that the
unit has been properly installed and has no mechanical defects, that the
unit is in proper alignment and has: been properly connected, that the unit
is free from undue vibration over the full range of operating conditions,
that the unit is free from overloading or overheating of any parts; that the
unit is performing in accordance with the specifications. All power
equipment, supplies, materials, labor, and instruments required for the
field running tests shall be furnished by the Contractor.
3.03 SPARE PARTS
01
The Contractor shall furnish to the Owner one (1) complete set of
manufacturer's recommended spare parts.
The Contractor shall be responsible for furnishing any special tools and
lubrication devices required to perform maintenance
power unit. Three (3) copies of printed instructions
other preventive maintenance operations shall be
Engineer with the shop drawings.
END OF SECTION
or any pumping or
for lubrication and
furnished to the
Rev. 6123/09 PROJECT # 05734 11315 - Page 4

SECTION 11365
PART 1: GENERAL
1.01 DESCRIPTION OF WORK
SLUDGE DRYER SYSTEM
A. Scope: The work to be performed under this item consists of furnishing and
delivering one (1) complete sludge drying and conveying system as shown on
the drawings and specified herein. All equipment shall be furnished by a
single supplier. The system shall include all equipment and appurtenances
required to produce a Class A material as defined by 40 CFR Part 503.
B. Type: The sludge dryer system shall be a prefabricated unit consisting of
a skid mounted dewatered sludge hopper, sludge dehydration chamber, hot
oil heat exchanger fired by either liquid petroleum (LP) or natural gas, control
panel, scrubber/condenser and required integral and external conveying
devices. This dryer shall be an automated batch, indirect heated, sludge
dehydration system. All equipment shall be mounted on skids for installation
by the Contractor.
C. Design Data: The indirect heated sludge dryer system shall be designed to
operate in an automated batch process. The system shall have a design
capacity to process 9.5 cubic yards of, wet sludge per batch, and 3,500
pounds per hour wet weight of municipal sludge that has been dewatered to
16% dry solids.
1.02 QUALITY ASSURANCE
A. Standardization: All parts of the equipment shall be the product of one
manufacturer experienced in the design and fabrication of automated batch
biosolids dehydration systems. The manufacturer shall have constructed at
least two (2) units of similar design.
B. Coordination: The contract documents provide details of a complete
equipment installation for the purpose specified. It shall be the responsibility
of the Contractor to coordinate all the details required for a complete
operating system, such as protective coatings, piping, pumps and wiring. The
Contractor shall provide for all work required to properly install, adjust and
place into operation a complete working system.
C. Manufacturer's Quality Control: The manufacturer shall be responsible to
assure compliance with all material and fabrication requirements of these
specifications.
Rev. 6123109 PROJECT # 05734 11365 - Page 1

1.03
0
1.04
SUBMITTALS
The Supplier shall submit eight (8) copies of the following shop drawings to
the Engineer for approval.
1. Complete outline dimension drawings, including front view, side view,
arrangement, and interface points for piping, foundation, electrical and
controls.
2. Complete electrical wiring and instrumentation diagrams and control
panel layouts showing dimensions and power requirements at each
and every connection.
3. The 'motor HP, RPM, WR2 value, motor dimensions, and any
special/pertinent motor information.
4. Mounting details and foundation loads.
5. Complete diagrams of the variable speed drive(s), (if required).
6. Location, size and type of all bolts and welds, (if required).
7. Edge preparation of joints to be welded shall be detailed with shop and
field welds distinguished, (if required).
8. Calculations and details for hold down lugs including foundation loads
and anchor bolt uplift (if required).
9. Speed reducer information and ratings, (if required).
10. Any other auxiliary equipment information as well as performance
information.
11. Weights of equipment.
12. Complete bill of materials (catalog number and rating of all devices).
13. Spare parts furnished by Manufacturer with equipment.
14. Spare parts recommended to be purchased by Owner for stock.
15. Source and current prices of replacement parts and supplies.
16. Original Manufacturer's part or model number of identification number.
17. Special storage or handling requirements.
18. Copies of operation and maintenance manuals for all equipment
provided.
19. Calculations for determination of conveyor speeds.
20. Any other information required to obtain approval of the items included.
21. Copy of Process Guarantee and Performance Bond.
PROCESS GUARANTEE
The supplier of the sludge dryer equipment shall guarantee the performance of
the equipment shall be such that a Class A biosolid is consistently produced that
meets the regulatory definition of 40CFR 503 for a Class A product. The supplier
shall furnish a performance guarantee secured by a Performance Bond issued by
the supplier. The face value of the performance bond shall be equal to the cost
of the equipment, including installation. The Bond shall remain in effect until
completion of successful demonstration of the equipment.
Rev. 6123/09 PROJECT # 05734 11365 - Page 2

1.05 FUNCTIONAL REQUIREMENTS
A single supplier shall furnish the complete sludge dryer system and be
responsible for its proper design and subsequent operation. The supplier shall
be responsible for coordination with other portions of the project including
structural, electrical and instrumentation, be the prime supplier of materials and
equipment in the system, and provide all of the manufacturer's service as
required for a complete and operable system.
The Contractor shall perform all electrical work necessary to provide a complete
and operable system based on the approved shop drawings and the Contract
Drawings and Specifications. Contractor shall coordinate with the equipment
manufacturer prior to bidding and during construction to determine scope of
supply and installation requirements.
The system shall be designed and furnished in accordance with all applicable
codes and regulations.
The sludge dryer equipment shall produce Class A sludge in accordance with
40CFR 503. Specifically, Class A pathogen reduction shall be met by reducing
the moisture content of the sludge to 10% or lower. Additionally, either the
temperature of the sludge particles shall exceed 80 degrees C (176 deg F), or
the wet bulk temperature of the gas in contact with the sludge as the sludge
leaves the dryer shall exceed 80 degrees C (176 deg F). Vector attraction
reduction in accordance with 40CFR 503 shall also be accomplished by
increasing the solids content of the sludge to 90% or greater. Compliance with
40CFR 503 Class A shall be verified at start-up.
1.06 PATENTS LICENSES AND ROYALTIES
A. Patents: The supplier shall guarantee the Owner that all equipment offered
under these specifications or that any process resulting from the use of such
equipment in the manner stated, is not the subject of patent litigation, and that
he is not knowingly offering equipment, the installation or use of which is likely
to result in a. patent controversy, in which the Owner as user is likely to be
made the defendant.
B. Licenses and Royalties: Where patent infringements are likely to occur, the
supplier shall submit with the prequalification submittal the license agreement
between himself, or the manufacturer of the equipment, and the patent owner
or the controller of the patent, which will permit the use in the specified
manner of the equipment. In the event that the supplier is the controller or
owner of the patent, the supplier shall submit, with the prequalification
submittal, a license agreement to be executed by the supplier and the Owner.
Any and all fees to be paid by the .Owner shall be clearly specified in the
license agreement.
Rev. 6/23/09 PROJECT # 05734 11365 - Page 3

C. Liability: The supplier shall submit a hold harmless agreement in which the
supplier agrees to hold and save the Owner or its officers, agents, servants
and employees harmless for liability of any nature or kind, including cost and
expenses, for, or on account of, any patented or unpatented invention,
process, article or appliance manufactured or used in the performance of the
work under this contract, including the use of same by the Owner.
1.07 SHOP DRAWINGS
The Contractor shall submit to the Engineer at eight (8) copies of shop drawings
of all items listed in paragraph 1.03. Each submittal shall be clearly marked with
the project name, dated and accompanied by a letter of transmittal listing all
items included in the submittal and referencing the project specification page and
article numbers applicable to each item.
The equipment supplier has tested its system and has designed the equipment
and selected the components; therefore, approval of shop drawings by the
Engineer will be general only, and such approval will not relieve the supplier of
responsibility for accuracy of such shop drawings, proper fitting, coordination,
construction of work and furnishing materials and work required by the Contract,
but not indicated on shop drawings. Approval of shop drawings shall not be
construed as approving departures from any Contract requirements particularly
the requirement for production of Class A product pursuant to 40CFR Part 503.
1.08 OPERATIONS AND MAINTENANCE MANUALS
The equipment supplier shall furnish three (3) sets of O&M manuals for all the
equipment provided.
All equipment shall be warranted by the equipment supplier to be free from all
defects in workmanship and material for a period of one year after the date of
final acceptance. All defects that are detected during the, one-year warranty
period shall be repaired by the equipment supplier at no cost to the Owner.
PART 2: PRODUCTS
2.01 MANUFACTURING CODES AND SPECIFICATIONS
A. Codes: The system shall comply with all applicable codes, including, but not
limited to:
• National Electrical Code (NEC)
Rev. 6/23/09 PROJECT # 05734 11365 - Page 4

Plastic Piping Handbook
AGE and IRI Gas System Specifications and Standards
OSHA
ASME
B. Electrical
1. Control enclosure: Stainless steel, NEMA 4X, with UL stamp.
2. Machine wiring: Wired to National Electrical Codes.
C. Gas Burner
1. Arranged and piped to Industrial Risk Insurer requirements.
D. Steel Fabrications
1. All welds will be minimum 3/16 fillets.
2. All welds related to the inner heater coil and a minimum of 10% of the
welds related to the outer heater coil shall be subjected to an x-ray
inspection at the manufacturing facility.
3. The system will designed and manufactured for galvanizing and bolt up
assembly under ASTM A143, A384 and A385.
4. The thermal oil system will be designed and "U" stamped according to the
specifications of the ASME Sectioin VIII-Pressure Vessel Code for 750
degrees. F at 250 psig. The coils will be hydrotested per ASME. The
expansion tank will be ASME Section VIII Code Stamped.
E. Galvanizing
1. Steel fabrications specified to be galvanized will be hot dipped galvanized
in accordance with ASTM A123-97.
2. Any defects or damage caused in manufacturing will be thoroughly
cleaned, wire brushed, wiped clean with a suitable solvent and dried. The
prepared area will be coated with a zinc rich compound specifically
formulated for touch up of galvanizing. The zinc rich coating will be a
minimum of 3.4 mills thick and will be in accordance with SSPC standards.
F. Seals
1. The thermal fluid pump shall be manufactured by a major manufacturer of
pumping equipment for heat transfer fluids. Seal specifications are:
a. Stationary member- Silicon Carbide.
b. Rotary member- Carbon.
c. O-ring- Viton.
d. Spring- CrNi steel.
Rev. 6/23/09 PROJECT # 05734 11365 - Page 5

2. Thermal Fluid rotary seals:
a. Seals are of stuffing box design; using carbon impregnated braided
Teflon packing.
3. Dehydration Chamber end seals
a. One (1) reinforced silicon gasket
b. Multiple rings of carbon impregnated braided Teflon packing.
G. Bearings
1. Bearings will be oil or grease lubricated, with lubrication points piped to a
central lubrication block for accessibility.
2. Bearings shall be a minimum of L-10 rated life of 50,000 hours.
H. Balance
1. Drive motors shall be manufactured by a major supplier of Premium
Efficiency electric drive motors. Balancing specifications are to ISO
1940/73
Condenser Blower
1. The condenser blower shall be manufactured by a major manufacturer of
blower units. Balancing specifications are to AMA 204, section 6, quality
grade G2.5 standards.
J. Thermal Fluid Heater Gas Burner
1. The oil heater gas burner shall be manufactured by a major manufacturer
of industrial burner systems. Blower balancing specifications are to ISO
1940-73'.
K. Equipment Guards
1. Equipment guards are designed for OSHA regulations and are 14 gauge
hot rolled steel with expanded metal insert, where applicable, to allow
visual inspection. All guards are designed for easy removal.
2. Guards shall be sand blasted to near white and painted with safety
orange.
3. Chemical and fade resistant decals shall be affixed to the equipment
where equipment may start automatically, have rotating parts or heat
zones. Decals will be displayed in areas that are visually obvious. Decals
are to be black print with yellow background.
L. Hardware
1. Bolts shall be ASTM Class 449, Type 5 or greater.
Rev. 6123/09 PROJECT # 05734 11365 - Page 6

2. Flanges, other than structural connections, shall be ANSI B16, class 150
type raised face, slip on weld.
3. Pipe threads shall be ANSI 11.5 V or 8V, depending on size.
M. Couplings
1. Where couplings are used where the drive is greater then 1/2 hp, and
where angular misalignment, parallel misalignment, end float and cushion
shock or vibration dampening may need to be addressed, a flexible
member with synthetic tension member bonded in rubber shall be
provided. The flexible member shall be attached to the flanges by meads
of clamps, rings and caps screws. The flanges shall be attached to the
shaft by key seat and setscrews.
N. Electrical
1. Contactors shall be Square D, Telemecanique, and Thermal Magnetic.
Rated for 30 million operations.
2. Contactors shall be UL, ASE, and CSA approved.
3. Switches shall be 22 mm.
4. 9300 Rades Ethernet Modem
5. Allen Bradley Panel View Plus 1000
O. Gauges
1. Manufacturer to supply a water flow switch, natural gas test plugs, one
magnehelic airflow gauge and one thermal fluid pressure switch.
2.02 EQUIPMENT
A. Materials of Construction: (Note: All painted surfaces to be sand blasted to
near white metal prior to painting)
ITEM
Structural Steel Main Skid
MATERIALS
10" x 22# beam
FINISH
Galvanized
Main Skid Floor
1/8 "floor plate
Galvanized
Hopper walls & ends
3/8" hot rolled steel
Galvanized
Hopper structural support steel
4" x 9.5 # beam
Galvanized
Hopper chain guard housing
12-ga hot rolled steel
Orange paint
Motor bases
Dehydrator frame
1" plate
6" x 15# beams
Galvanized
Galvanized
Dehydration chamber end
plates
Y2" plate
Blasted & hi temp black
paint
Dehydration chamber
3/8" rolled steel
Insulated and wrapped
18ga 304 S.S.
Electro polish to #3 finish
D- chamber crown and lid
10 ga 304 S.S.
Hand polish
Rev. 6/23109 PROJECT # 05734 11365 - Page 7

Steam exhaust duct
14 ga 304 S.S.
Hi temp black paint
Condenser
10 ga hot rolled steel
Galvanized
Hot oil combustion tank
Base
18 ga 304 S.S.
3" x 4.1# channel
N/A
Galvanized
Cover
10 ga hot rolled steel
Black paint
Combustion exhaust stack
14 ga 304 S.S.
Black paint
Hot oil expansion tank
3/16" thick hot rolled steel
Black paint
Support legs
Product discharge head box
4" x %" angle
1/" hot rolled steel
Galvanized
Black paint
Discharge screw conveyor
body & cover
10 ga hot rolled steel
Galvanized
Condenser fan piping
6" dia. - .187" wall pipe
Galvanized
Hot oil piping
Sch 40 - SA1O6B
seamless pipe
Insulated except valves
and overflow/piping
Chain hopper
#140 roller chain w/ cotter
ins
N/A
Dehydrator rotor
#180 roller chain w/ cotter
pins
N/A/
Gear hopper
Forged steel to meet
ANSI Type II
N/A
Dehydration rotor
Forged steel to meet
ANSI Type II
N/A
Dehydrator
1/" S.S. tubing
N/A
Hopper
1/" S.S. tubing
N/A
Control Panel
40" w x 18" d x 84" h —
NEMA 12 polished 304
S.S.
N/A
Electrical conduit
Steel properly sized
Galvanized
J-Boxes
Steel properly sized
Galvanized
Condenser water piping
Drain pipe
Gas piping
Steel pipe/Buns-N hose
& S.S. noz.
6" dia. x .187" wall pipe
2" dia. Sch. 40 black pipe
Galvanized steel
Galvanized
I N/A
B. Wet Sludge Conveying Equipment: Product conveying equipment shall be
supplied by the sludge dryer equipment supplier in the general arrangement
shown on the plans. The sludge dryer supplier shall provide the feed product
screw conveyor to transport the feed stock to the dryer and to the outside of
the building. The screw conveyors shall be shipped loose to be installed by
the Contractor. The conveyor shall be suitable for transporting wet sludge at
14 to 18 percent dry solids. All materials of construction shall be suitable for
contact with dewatered municipal sludge. The equipment supplier shall be
responsible for determining conveyor speeds and shall submit calculations to
document the determination.
Rev. 6/23/09 PROJECT # 05734 11365 a Page 8

Cable operated OSHA safety stop switches shall be provided on both sides of
each conveyor with pull cord along both sides of the full length. Each shall
have a SPDT contact rated 5 amperes at 120 volts.
A zero speed switch shall be provided on each conveyor, which will trip off the
conveyor in a "jamming" condition. Each switch shall have a SPDT contact
rated 5 amperes at 120 volts.
Power supply to equipment will be 480 volts, 3 phase, 60 Hertz.
All conveyor frames and supports will be constructed of ASTM-A-36 structural
members with spreaders sized as required to limit deflection to 1/400 at
longest support span. All necessary supports shall be provided by the
Equipment Manufacturer. The top of the channel frame will be covered with a
fiberglass reinforced plastic or aluminum return cover to prevent product
spillage onto return run of belt. The entire frame assembly is to be hot dip
galvanized after fabrication.
Additional supports as required shall be designed and furnished by the
conveyor manufacturer.
All conveyors are to be provided with OSHA style guards at all "nip points"
and motor driven rotating components, specifically including motor drive and
tail pulley guards. The drive guard is to be constructed of FRP or aluminum.
The conveyor manufacturer shall design and furnish all chutes between screw
conveyors. Materials of construction for all chutes shall be minimum 3/16-
inch 304 stainless steel, with external reinforcement as required.
The equipment supplier shall provide all necessary equipment and
appurtenances for a complete and operable system.
All screw conveyors shall be constructed of carbon steel. Flights shall be full
pitch and shall be minimum 3/16" thick, and shall be designed and sized by
the manufacturer to for the specified carrying capacities. Troughs shall be
"U" type, minimum 1/4 inch thick. Trough covers shall be 12 gauge minimum.
The center pipe of the screw shall be sized so that intermediate hanger
bearings are not required and deflection is 1 /4 inch or less. Tail bearings
shall be grease lubricated flanged ball bearing. A plated type seal shall
prevent sludge from passing the seal. Transfer chutes shall be flange
connected to the screw conveyor and shall be minimum 12 gauge carbon
steel.
The screw conveyors shall be belt driven by a motor and speed reducer.
Motors shall be sized by the equipment supplier. Each speed reducer shall
have a service factor of 1.4 based on the calculated developed horsepower.
Rev. 6/23/09 PROJECT # 05734 11365 - Page 9

The motor shall be connected to the speed reducer through a belt drive which
is suitably covered with a 14 gauge OSHA approved guard.
Motor starters and controls for the alkaline screw conveyors shall be provided
as part of the biosolids processor main disconnect panel.
C. Wet Sludge Feed Hopper: A. One (1), custom sludge feed hopper, fabricated
from 3/8"thick mild steel with fifty (50) cubic yard holding capacity. Internals
include two (2) mild steel rotary wiper mechanisms and two (2) 11" diameter
mild steel augers. Externals include a chain and sprocket system to turn the
rotary wiper and auger. Sprockets will be industrial quality to accept heavy-
duty roller chains. Two (2) mild steel motor shelves will be properly designed
and mounted to the hopper to support the drive motors and gearbox
assembly. Chain guards are provided to comply with OSHA regulations. The
hopper interior and exterior will be hot dip galvanized. One (1) custom 11" dia.
Auger system installed between the feed hopper discharge and the
dehydrator wet feed inlet complete with properly sized motor and gearbox.
One (1) linear screw operated door installed in the feed port to act as an
airlock. One (1) 9" dia. auger coupled to a Y2" hp drive is mounted on the
hopper rim for automatic sludge leveling.
D. Dehydration Unit: Each unit is designed, fabricated and supplied as follows:
1. One (1) structural steel frame designed and fabricated to support the
dehydration chamber and motor drive package. All external steel surfaces
will be finished per the Construction Materials and Finishes section. The
cylindrical dehydration chamber is insulated with 2" high -density ceramic
insulation and wrapped with an aluminum skin to prevent external heat
loss. The inspection cover is left uninsulated. Dehydrator wet sludge feed
port is equipped with an electrically operated shut off gate. Dehydrator top
is furnished with two (2) 304 stainless steel inspection covers. Dehydrator
crowned top is furnished with one (1) stainless steel exhaust duct, which is
connected to the provided condenser system.
2. One dehydrator end is furnished with a linear screw actuated discharge
gate. One (1) 3/8" steel dehydration chamber measuring approximately
72" dia. .x 144" long. The chamber has a smooth inner surface. One (1)
thermal fluid external jacket integrally welded to the dehydration chamber
for heat transfer to the dehydration chamber wall. One (1) 72" dia. thermal
fluid type hollow disk / blender fabricated from 5/16" steel, complete with
wall wipers. Two (2), rotary joints to provide thermal fluid inlet and outlet to
the rotating disks. Two (2) '/z" thick steel plate ends enclose the
dehydration chamber.
3. One (1) heavy-duty structural steel support base to support the dehydrator
drive package. One (1) engineered dehydrator rotary disk drive package
complete with reversible motor, gearbox, chain and bearings to drive the
disks. One (1) dried sludge discharge system consisting of a linear screw
Rev. 6123/09 PROJECT # 05734 11365 - Page 10

operated door and an enclosed auger drive package to convey the dried
sludge to a discharge point on one side of the dehydration chamber.
Multiple thermocouple probes for temperature readings and control
including thermal fluid, exhaust, dehydration vapor, thermal fluid
expansion tank and thermal fluid return from shell and rotor disks.
E. Thermal Fluid System: One (1) custom natural gas fired thermal fluid heater
fabricated from stainless steel and A36 steel, with a maximum rating of 8.25
Mbtus per hour. Internals of the air to thermal fluid heat exchanger are steel
and designed for industrial use. The outer shell of the thermal fluid heater is
10-gauge stainless steel, with a chamber top constructed with A36 steel. The
top section is painted with high temperature paint. The outer shell is insulated
with 2" of high -density ceramic insulation. An industrial natural gas system will
be supplied consisting of natural gas burners, control valves, temperature
controls and piping. The natural gas system will conform to ASME CSD 1.The
entire unit will be fabricated, assembled and tested before shipment. A
thermal fluid expansion tank complete with a relief port is mounted in an
elevated position. A special thermal fluid pump, filter, and valves will be
furnished to circulate the thermal fluid through the dehydrator system. The
combustion gasses will be collected in a 22" dia. duct, which will terminate
above the unit.
F. Natural Gas Burner: One (1) industrial natural gas system consisting of one
(1) natural gas burner with modulating controls configured to meet ASME
CSD 1. The system will be pre -piped and pre -mounted. The programmable
controller will run various time / temperature recipes for total control of the
dehydration process. Times and temperature regimes will be established
during machine start-up and entered into the programmable controller. All
necessary thermocouples and instrumentation are furnished in this proposal.
The flue gasses are collected in a 22 dia. duct and terminated above the
machine. Thermal fluid heater has an 8.25 Mbtus maximum firing rate. Actual
natural gas usage will vary depending on the amount of actual water being
evaporated however; since we must elevate the total load (solids and water)
to 2120 F, the solids differential between applications does not significantly
change the estimated cost of dehydration.
G. Condenser/Scrubber: One (1) condenser/scrubber unit will be provided with
the dehydration unit. The unit shall be connected to the plant re -use water
system with a minimum of 140 gpm at 40 psi (not to exceed 45 psi). Pressure
reducing valves and flow meters shall be supplied and installed by the
General Contractor. Reuse water supplied to the Condenser/Scrubber will be
filtered through 300-micron Y-Strainer (provided and installed by the
Contractor) prior to connection to the Condenser/Scrubber system. The
scrubber will be a high efficiency enclosed Venturi type to remove air borne
particulate, and will be piped to the supplied Biofilter and carbon pack. The
Rev. 6/23/09 PROJECT # 05734 11365 - Page 11

blow -down water will be piped to a drain where it will return to the head of the
plant.
H. Bio-Filter with Carbon Pack: One (1) 8'D x 9'8"H @ 500 CFM bio-filter
package mounted on a 8' x 12' galvanized steel skid will be provided. The
basic concept of biofiltration is to have odorous airflow through a media that
supports biological active organisms. Organisms specific for the degradation
of the specific odorous compounds accumulate on the media and multiply.
Temperature, humidity, pH and nutrients are controlled to optimize the
multiplication and effectiveness of these organisms.
The warm 90 - 100 deg. F moist air is pulled through the scrubber/condenser
system and piped to the bio-filter through 8" dia. CPVC pipe. The correct
moisture level is maintained through the manual adjustment of a valve and
tubing arrangement from the condenser water system. The heat is controlled
by manually adjusting the water flow through the scrubber system. Once field
set upon startup these adjustments are infrequently reset if conditions
change.
The bio-filters configuration of media trays are easily removed for media
replacement or maintenance. Air flows into the bottom of the vessel and
passes through the series of media and exits out the top.
The bio-filter canister shall be manufactured of high quality, fiberglass. The
segregated internal trays are made of fiberglass reinforced plastic grating,
polypropylene media retention screen and tray supports. There will be a total
of 300 cubic feet of organic, natural, fully biodegradable, non -synthetic
composition. Malodorous compounds will be removed in the organic bio-filter
media. The media will consist of three components, shredded wood (65%),
nugget bark (25%), and compost (10%). The mixture shall have a pH
between 6 and 8, an air -filled pore space of 25%-55% and moisture content
of 40%.
A carbon pack is added after the bio-filter. The carbon pack will filter foul air
as it flows into the bottom of the linear PE canister. The foul air moves up
through the inlet plenum, which diffuses the air and then up through the high
capacity coconut shell carbon and potassium impregnated media bed where
odorous compounds are removed by the active sties on the media.
Dried Product Surge Bin: One (1) dried product surge bin shall be provided
with the sludge dryer system, fabricated from 3/16" steel plate with a
galvanized finish.
1. Capacity 86 cu. ft.
2. Cover with 2" FPT vent fitting. (Piped to dryer water-cooled
condenser).
Rev. 6/23109 PROJECT # 05734 11365 - Page 12

K.
L
3. Discharge flanged outlet.
4. Two (2) Y2" FPT fittings for addition of spray nozzles.
5. One (1) 12" dia. access cover.
6. One (1) 10 hp motor drive package with gearbox.
7. One(1) dried biosolids eductor, for feeding dried biosolids to the
storage silo.
8. Two (2) positive displacement blowers sized as necessary to move the
dried biosolids from the dried product storage bin through the eductor
to the storage silo.
Control Panel: One (1) master control panel shall be provided to conform to
National Electrical Code, specifications. The cabinet will be a NEMA 4X,
stainless steel enclosure. An Allen Bradley SLC 5/05 programmable
controller shall be provided, complete with internal timers to control the
time/temperature regimes and all machine functions. Necessary 1/0 devices
shall be furnished to operate the equipment safely and efficiently and to
monitor and certify that the dried sludge meets the requirements for Class A
sludge classification.
One (1) main disconnect shall be provided in the enclosed cabinet. The panel
shall be equipped with an Allen Bradley 9300 RADES Ethernet modem for
connection to a designated phone line. Manufacturer will also supply ladder
logic diagrams and initial cycle programming for one (1) time temperature
dehydration cycle. All hard wiring schematics are furnished.
Control Voltage: One 3 KVA step down transformer (120V/1 ph/60HZ) is
furnished in the control panel
General Operation PLC Controlled Automated Batch
The master control panel shall be designed to accommodate the following
general operation, or other operation as determined by the Sludge Dryer
Manufacturer:
i. The Sludge Dryer, under PLC control, is started to heat the thermal
fluid to a system operating temperature.
ii. The infeed hopper receives waste material from the belt filter press,
with a storage capacity as specified previously.
iii. The process temperature is raised to an optimum operating
temperature as determined and specified by the sludge dryer
manufacturer.
iv. The PLC calls for dewatered biosolids to be fed to the drier
chamber.
2. lnfeed airlock door opens.
3. lnfeed auger feeds biosolids to the drier chamber per level control.
Rev. 6/23109 PROJECT # 05734 11365 - Page 13

4. The internal, oil heated, rotor moves and breaks up the biosolids to create
maximum exposure to the heated surface of the rotor and the oil heated
drier chamber.
5. The PLC senses the satisfaction of the time/temperature requirement of
the dehydration process.
6. The discharge door opens, integral discharge and final product conveyors
are activated, the rotor is changed to a one direction rotation to move the
dried material to discharge.
7. When the discharge time is satisfied the discharge door is closed and the
PLC resets to automatically infeed a new batch and start the process over.
8. This automatic batch process continues to cycle until the operator stops
the sequence and sets the system to cool down cycle.
M. Dried Solids Storage Silo: The Sludge Dryer System manufacturer shall
provide a new dried solids storage silo with a minimum working capacity of 94
CY. Silo structure shall be designed for installation at the location shown on
the plans and in accordance with all local codes and regulations. Silo shall
consist of a welded carbon steel tank, 60 degree hopper with 12" diameter
flanged outlet, with support and truck drive through 14' width and 13' vertical
clearance. Tank shall include name plate, level indicator, thermocouple, 20"
square flush mount tophat manway in hopper, 24" roof combination manway
pressure relief valve, aluminum deck perimeter handrail, outside ladder with
safety cage. and lockable hoop, full area working platform at 14' above grade,
stairtower from grade to 14' above grade per drawings. System shall also
include a separate baghouse sized for the proposed application.
2.03 MODULARIZATION
A. All equipment in this proposal will be factory mounted on five (5) heavy-duty
structural steel bases.
1. The main skid will include the dehydration chamber, the
condenser/scrubber (including ductwork), and the electrical control panel
with all motors and sensors wired to the panel. The ductwork with
precooling and duct cleaning spray and the precooling manifold will be
piped for one point connection.
2. The second skid includes the thermal fluid heat exchanger, the gas burner
and gas valve train.
3. The third skid includes the wet sludge hopper and the wet sludge feed
conveyor.
4. The fourth skid includes the biofilter, carbon pack, and the condenser
blower.
Rev. 6/23109 PROJECT # 05734 11365 - Page 14

PART 3 EXECUTION
3.01 INSTALLATION AND STARTUP SERVICES
A. During installation and before the equipment is placed in operation, the
equipment supplier shall inspect and certify that the unit and accessories
have been properly installed and adjusted, all by a qualified properly trained
representative at no additional cost to the Owner. Inspection shall consist of
a minimum of three trips with 8 hours on site for each trip.
B. The equipment supplier shall start up all equipment, supervise the initial
operation thereof, and be responsible for the satisfactory operation of all
equipment furnished under this Contract. The supplier shall allow a minimum
of five days (40 hours) on site by the qualified properly trained representative
for installation and start up.
3.02 TRAINING SERVICES
A. The Supplier shall provide the services of a qualified properly trained
representative to instruct the Owner's WWTP operators. The instructions
shall include hands on operations of the proposed equipment and the
furnishing of any and all technical guides that are required. At least twenty
four (24) hours of instruction during two (2) trips shall be provided and shall
be coordinated with the start-up of the other sludge processing equipment.
B. Furnish for the Engineer's approval six (6) sets of instructions for the job
which shall fully instruct the employees of the Owner in correct practice and
method of operations and maintenance of equipment furnished.
3.03 TESTING
A. Acceptance Test: After all equipment has been placed in service, a
performance test will be conducted over a two day period. The Equipment
Supplier shall furnish all instruments, meters, gauges, recorders and any
other devices necessary to verify that the equipment meets the performance
specifications. In the event the equipment fails to meet the performance
requirements described in these Specifications, the equipment supplier will
have 30 days to modify said equipment and complete additional tests to
demonstrate the ability of the equipment to meet these Specifications. After
said modifications have been made, a second performance test will be
conducted over a two day period.
The performance test run shall be for a period of two (2) eight hour working
days with data from the final day of testing used to determine compliance.
Delays due to inclement weather or auxiliary equipment malfunction shall be
Rev. 6/23/09 PROJECT # 05734 11365 - Page 15

excluded as determined by the Engineer. All sampling and sample testing
during the one day certification run shall be performed at the expense of the
supplier by an independent laboratory approved by the Owner. Samples shall
be taken before and after each batch, for a minimum of two batches. Each
sample shall be analyzed as required by 40CFR 503 for the pathogen
reduction and the vector attraction reduction method used. In addition,
sampling to determine the throughput in pounds of sludge per hour shall be
conducted. Each sample shall meet the requirements of 40CFR 503 for a
Class A product.
B. Failure of Equipment to Meet Performance Requirements: If the equipment
supplier is unable to meet the performance requirements within 60 days of
start up of the equipment, the equipment supplier shall, at no cost to the
Owner, remove all equipment from the job site and refund to the Owner the
full amount paid. The manufacturer shall also refund the installation cost for
their equipment including all labor, and materials that are not utilized by
subsequent equipment installed by the Owner
3.04 SPARE AND REPLACEMENT PARTS
A. Replacement Parts: The equipment supplier shall furnish all replacement
parts for a period of one (1) calendar year after the end of the one year
warranty period. These parts shall include defective parts, parts that fail due
to normal wear including consumable parts, and parts that render the
machines ineffective due to wear. These will be installed by the Owner at no
cost to the supplier.
B. Spare Parts to be Furnished: The equipment supplier shall furnish one set of
recommended spare parts. At a minimum, the spare parts to be provided
shall consist of the following:
1 — Proximity Switch
1 — Rotary Union Packing Gland
1 — Chamber Packing Gland
1 — Solenoid Valve
1 — Dual Lead Thermocouple
1 — Single Lead Thermocouple
1 — Input / Output Card for the PLC Controller.
END OF SECTION
Rev. 6/23109 PROJECT # 05734 11365 - Page 16

SECTION 11376 POSITIVE DISPLACEMENT BLOWER
PART 1: GENERAL
1.01 SCOPE OF WORK
A. Furnish all labor, equipment, materials and incidentals required to
completely install and place into operation three (3) prefabricated positive
displacement blower packages at the locations shown on the drawings.
B. Unless otherwise noted, all materials and equipment supplied under this
Section shall be new, of good quality, and in good condition.
1.02 SYSTEM DESCRIPTION
A. Blowers:
1. Post Aeration Basin: Three blowers, 154 SCFM @ 4 PSI, 5HP max
2. Existing Sludge Holding Basin: Two blowers, 1145 SCFM @ 10
PSI, 100 HP max
3. Proposed Sludge Holding Basin: Two blowers, 1375 SCFM @ 10.5
PSI, 100 HP max
B. Each system shall be furnished and installed with all necessary accessory
equipment and appurtenances, whether specifically mentioned in these
specifications or not. Each unit shall be prefabricated and shall include
the positive displacement blower, drive system, drive motor, inlet filters,
inlet silencers, combination base/discharge silencer/relief valve, and
expansion joint.
C. Existing Sludge Holding Basin and Proposed Sludge Holding Basin
blowers shall be identical models with the exception of the blower speed.
1.03 QUALITY ASSURANCE
A. General:
All blowers shall be given the following factory tests:
1. Standard factory slip test:
Standard factory slip RPM test at one (1) psig pressure. This slip
RPM (uncorrected) must meet the maximum 1 psig factory slip
Rev. 6/23/09 PROJECT # 05734 11376 - Page 1

RPM specified for the frame blower tested. The test consists of
blocking off the discharge and measuring the speed of the blower
to maintain discharge pressure of 1 psig.
2. Certified Performance Test:
For all blowers of 30 hp and larger, a performance test in
accordance with ASME PTC-9 (latest revision) shall be conducted
on each blower to be supplied. A test report confirming capacity
and power will be furnished to the Engineer.
1.04 SUBMITTALS
A. Shop Drawings: Shop Drawings for the equipment to be furnished under
this specification shall include at least the following:
1. Descriptive literature, bulletins, catalog cuts and drawings for the
equipment and accessories.
2. Complete bill of materials.
3. Performance curves for each type of blower.
4. Certified performance curves for each blower prior to shipment of
the blowers.
5. List of spare parts.
6. Warranty.
B. Operation and Maintenance Manuals: The Manufacturer shall furnish at
least three (3) copies of operation and maintenance manuals for all
equipment supplied.
1.05 DELIVERY, STORAGE AND HANDLING
A. No shipment shall be made until the equipment and the certified
performance curves have been approved by the Engineer.
B. All equipment shall be properly protected so that no damage or
deterioration will occur during shipment or storage.
C. All equipment and ports shall be properly protected from damage and
deterioration during storage at the site.
1.06 WARRANTY
A. All equipment shall be warranted to be free from defects in workmanship,
design and materials for a period of one (1) year under normal use,
Rev. 6123/09 PROJECT # 05734 11376 - Page 2

operation and service. Should any part of the equipment fail during the
one (1) year warranty period, it shall be replaced and the unit restored to
service at no expense to the Owner.
1.07. MANUFACTURER AND SUPPLIER INFORMATION
A. Equipment shall be as manufactured by Dresser Roots, Inc., Gardner
Denver Sutorbuilt, Hibon Inc., Kaeser Compressors, Inc. Tuthill Vacuum
and Blower Systems, United Blower Inc. Manufacturers are listed only to
denote the quality standard of product desired, general style, type,
character and do not restrict bidders to a specific manufacturer.
Substitution of equipment of equivalent or equal design shall be submitted
to the Engineer for approval or disapproval in accordance with Article 11
of the Instructions to Bidders.
B. Manufacturer Nameplate: A manufacturer's nameplate shall be securely
and permanently mounted to each individual piece of equipment furnished
under this Section. The nameplate shall be constructed of a durable, non-
corrosive material. Critical information shall be clearly engraved or
otherwise permanently stamped on the nameplate, and shall be fully
legible. The information contained on the manufacturer nameplate shall
include at least the following:
1. Manufacturer's Serial Number
2. Name, address and telephone number of equipment manufacturer
3. Model and/or Part Number, including impeller sizes, when
applicable
4. Performance Criteria (i.e., capacity, design point, etc.)
5. Motor size, speed and voltage
6. Enclosure Type or Rating
7. Any other pertinent information
Note: All equipment shall include a nameplate with a manufacturer serial
number validating the equipment as new. Failure to meet these
requirements will be cause for rejection of the equipment.
B. Supplier and Service Information: A durable nameplate, stamp or sticker
shall be adhered to each individual piece of equipment containing the
name, address, and telephone number of the local business that supplied
the equipment, and the name, address and telephone number of the local
business that can provide service and replacement parts for the
equipment. A 24-hour emergency service telephone number should also
be included.
Rev. 6/23/09 PROJECT # 05734 11376 - Page 3

PART 2: PRODUCTS
2.01 EQUIPMENT
A. Blowers:
General: The air blowers shall be of the rotary positive
displacement type, and shall be constructed with inlet and
discharge connections oriented as shown on the contract drawings.
Each blower shall be equipped with steel mounting feet. Maximum
blower speed shall be 3,000 rpm.
2. Casing: One-piece close -grained cast iron.
3. Impellers: High -strength cast iron, straight, tri-lobe involute type.
The impellers shall operate without rubbing or liquid seals or
lubrication. The impellers shall be dynamically balanced and
center -timed to permit rotation in either direction.
4. Shafts: Alloy steel, pressed into the impeller body and pinned.
5. Impeller/Shaft Assemblies: Each impeller and shaft assembly shall
be supported by oversized anti -friction bearings engineered for
long service life and fixed to control the axial location of the
impeller/shaft unit. A cylindrical roller bearing shall be provided at
the drive shaft designed to handle the stresses of V-belt drive,
while single -row ball bearings shall be used at all other locations.
6. Timinq Gears: The impellers shall be timed by a pair of carbolized
and ground steel spur gears, mounted on the shafts with a tapered
fit, and secured by a locknut.
7. Lubrication: Each bearing shall be provided with a positive lip -type
oil seal designed to prevent lubricants from entering the air stream.
Further provisions shall be made to vent the impeller side of the oil
seal to atmosphere to eliminate any possible carry-over of lubricant
into the air stream. The drive end bearings shall be grease
lubricated, and shall be provided with grease fittings. The timing
gears and the gear and bearings shall be lubricated by splash from
the gears dipping into the oil.
B. Drive System: V-belt drive with weatherproof guard meeting all applicable
Federal, State and Local health and safety requirements.
C. Drive Motor: Motors shall be 480 V, 60 Hz, 3 phase, totally enclosed fan
cooled (TEFC) with a 1.15 service factors, and shall be non -overloading at
Rev. 6123109 PROJECT # 05734 11376 - Page 4

the design conditions specified. A heat sensor thermostat shall be
imbedded in top of winding and be connected in series with the motor
starter coil in control box to stop motor if temperature rises 'in excess of
the manufacturers recommendation for any reason.
Pressure Switches shall be provided on the discharge of each blower.
Refer to Specification Section 13420 for information regarding this device.
D. Inlet Filter: The inlet filter shall have a weatherhood mounted upright for
maximum watershed with capacity equal to or greater than design
conditions, and shall include air filter restriction gauge to measure
pressure drop across the filter element. Inlet filter shall be as
manufactured by Universal Silencers, Division of Nelson Industries, Inc.,
or equal.
E. Inlet Silencers: Horizontal arrangement, carbon steel plate, rigidly
connected to the blower suction, multi -chamber design with internal tubing
and porting. Silencers shall be a standard grade silencer as
manufactured by Universal Silencer or equal.
F. Combination Base/Discharge Silencer/Relief Valve: The discharge
silencer shall be of horizontal arrangement connected to the blower
discharge by a reinforced silicone rubber flexible connector to isolate the
blower from thermal related stresses. The silencer shall be of carbon
steel plate with two (2) shell layers, multi -chamber design with internal
tubing and porting. The silencer shall be welded to a heavy steel
machinery base with anti -vibration welded reinforcements. The silencer
shall be Model RD as manufactured by Universal Silencer or equal.
Bolted construction is not acceptable. Fork lift access shall be provided
and identified by prominent markers. The relief valves shall be mounted
on the exit chamber of the silencer, and shall be as manufactured by
Roots, or equal.
G. Noise Enclosure: An 80 dBA or less free field guaranteed noise
enclosure should be provided for each blower system. The enclosure
outer material must be zinc coated steel with a surface preparation and
paint as follows: Powder coat with texture finish 40-100 microns (65
microns average) powder coat process to be proven to- pass 500 hour salt
spray test satisfactory with no rust evidence. The enclosure must be
suitable for outdoor installation, 20 lb per square foot snow load and 90
MPH wind speed. The enclosure shall include a vent system with cooling
fan and (3) removable panels for easy access and maintenance. The
noise enclosure shall be provided with min. 1" foam and the foam shall
comply with UL94-HF 1 for flammability. The noise enclosure shall provide
up to 22-dba attenuation, free field.
Rev. 6/23/09 PROJECT # 05734 11376 - Page 5

PANT 3: EXECUTION
3.01 INSTALLATION
A. Installation of the equipment shall be in strict accordance with the
manufacturer's instructions and recommendations.
3.02 QUALITY CONTROL AND FIELD TESTING
A. Quality Control: The equipment manufacturer shall provide the services of
a qualified service engineer for one (1) day to inspect the installation of
the equipment and provide operation and maintenance training.
B. Field Testing: The equipment manufacturer representative will also verify
the performance of the blowers during the inspection, including air flow
and pressure, and shall demonstrate to the Owner and the Engineer that
the equipment is operating as specified.
END OF SECTION
Rev. 6/23109 PROJECT # 05734 11376 - Page 6