NC0036668_Staff Report_19940103

NPDES DOCUMENT SCANNING; COVER SHEET
NC0036668
Kenansville WWTP
NPDES Permit:
Document Type:
Permit Issuance
Wasteload Allocation
Authorization to Construct (AtC)
Permit Modification
Complete File - Historical
Engineering Alternatives (EAA)
Correspondence
Owner Name Change
/ 5Y-er /repd"
Instream Assessment (67b)
Speculative Limits
Environmental Assessment (EA)
Document Date:
January 3, 1994
This document is printed on reuse paper - ;Ignore any
content on the rererse side

SOC Priority Project: Ye`
If Yes, SOC No.
To: Permits and Engineering Unit
Water Quality Section
Attention: Susan Wilson
Date: January 3, 1994
No X •--
:
•
VAN 4 1994
'�i�l��i�l'�rI'l6. �t • •� r .t � teM CN
NPDES STAFF REPORT AND RECOMMENDATION
County: Duplin
Permit No. NC0036668
PART 1 - GENERAL INFORMATION
1. Facility and Address:
Town of Kenansville
Post Office Box 420
Kenansville, NC 28349
2. Date of Investigation: December 7, 1993
3. Report Prepared by: Pat C. Durrett
4. Persons Contacted and Telephone Number:
Richard Brown, Operator in Responsible Charge
[phone]
5. Directions to Site: Travel north in Kenansville on SR1301. After
crossing Grove Creek, travel 0.4 mile to entrance road to WWTP on right.
6. Discharge Point:
Latitude: 33 ° 58'07" Longitude: 77 ° 57' 57"
Attach a USGS map extract and indicate treatment facility site and discharge point on
map.
U.S.G.S. Quad No. H 27 NW U.S.G.S. Quad Name Kenansville

7. Site size and expansion area consistent with application?
X Yes No If No, explain:
8. Topography: Elevation is approximately 25 feet MSL
9. Location of nearest dwelling: No dwellings within 1000 yards.
10. Receiving stream or affected surface waters: Grove Creek
a. Classification: Class "C-Sw"
b. River Basin and Subbasin No.: Cape Fear 03-06-22
c. Describe receiving stream features and pertinent
downstream uses: Rural Stream and Swamp
PART II - DESCRIPTION OF DISCHARGE AND TREATMENT WORKS
1. a. Volume of Wastewater to be permitted: 0.170 MGD
b. What is the current permitted capacity of the Waste Water Treatment
facility? 0.170 MGD
c. Actual treatment capacity of the current facility? 0.170 MGD
d. Date and construction activities allowed by previous Authorizations to
Construct issued in the previous two years: None
e. Please provide a description of existing or substantially constructed
wastewater treatment facilities:
The facility consists of the following units: Influent pumps, grit chamber,
bar screen, single rotor oxidation ditch, secondary clarifier, chlorine
contact chamber, post aeration, continuous flow recording, aerated sludge
holding tank, and sludge drying beds.

f. Please provide a description of proposed wastewater treatment facilities:
g. Possible toxic impacts to surface waters: Possibly chlorine
h. Pretreatment Program (POTWs only): Not required
2. Residuals handling and utilization/disposal scheme:
a. If residuals are being land applied, please specify DEM permit No.
W00006816
Residuals Contractor McGill Environmental Systems, Composting
Telephone Number 1-800-728-4130
b. Residuals stabilization: PSRP X PFRP Other
c. Landfill:
d. Other disposal/utilization scheme: Permittee also is on Russell Lewis's
Land Application Permit, No. WQ0000455.
3. Treatment plant classification: Class II Facility
4. SIC Code: 4952
Wastewater Code of actual wastewater:
Primary 01 Secondary
Main Treatment Unit Code: 10005
PART III - OTHER PERTINENT INFORMATION
1. Is this facility being constructed with Construction Grant Funds or are any
public monies involved? No
2. Special monitoring or limitations (including toxicity) requests: None

3. Important SOC, JOC, or Compliance Schedule dates: (Please indicate)
Date
Submission of Plans and Specifications
Begin Construction
Complete Construction
4. Alternative Analysis Evaluation: Has the facility evaluated all of the
non -discharge options available. Please provide regional perspective for each
option evaluated.
Spray Irrigation: Unknown
Connection to Regional Sewer System: None
Subsurface: Unknown
PART IV - EVALUATION AND RECOMMENDATIONS
The facility must demonstrate compliance with Rule 15A NCAC 2H .0223,
"Demonstration of Future Wastewater Capacities". Plans should indicate treatment
to meet more stringent stream limits. The facility is operating at approximately 99%
of their design capacity at present and are still able to meet limits. Problems with
ammonia removal could occur with the high flows during the winter months.
It is recommended that a permit be drafted and placed at public notice
containing the effluent limits prepared by the Technical Support Branch. If no
significant adverse public comment is received, it is recommended that NPDES Permit
No. NC0036668 be reissued in accordance with the basinwide permitting strategy.
Signature of report preparer
//3/9' 5Z"
Date
i/0
ater Quality Regional Supervisor Date
PD:NC36668.SR
cc: Wilmington Regional Files
Technical Support Branch
Central Files

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RATING SCALE FOR CLASSIFICATION OF WATER POLLUTION CONTROL SYSTEMS
Name of Facility: 1 O (A) OP 0N/9NS
Owner or Contact Person: krctiAg.Ib $20,4)^! -Df,evcrae oC Pa bf/a,Q/<,S
Mailing Address: Po ' aDc 44070 1ENANs c 4/
County: Ilvfz./A/ Telephone: qi 9 796. 0361
Present Classification: 2 New Facility Existing Facility
NPDES Per. No. NC00 3444 8 Nondisc. Per. No.WQ omc &114 Health Dept.Per No._
Telephone: 39 5 - 3 Soo Date: /Z/7/53
Reviewed by:
Rated by: fci.
ORC: giC ked ,f3/orv,J
Check Classification(s): Subsurface
Wastewater Classification: (Circle One)
Health Dept.
Regional Office
Central Office
Grade: 7t
Spray Irrigation
III IV
Telephone:
Telephone:
Telephone:
Telephone: Z 9 3 - 0 367
.__ Land Application
Total Points: 4/5
jN-PLANT PROCESSES AND RELA.TEp CONTROL EQUIPMENT WHICH ARE AN INTEGRAL PART OF INDUSTRIAL PRODUCTION SHALL NOT BE
CONSIDERED WASTE TREATMENT FOR THE PURPOSE OFCLASSIFICATION. ALSO SEPTIC TANK SYSTEMS CONSISTING ONLY OF SEPTIg TAN(
AND GRAVITY NITRIFICATION LINES ARE EXEMPT FROM CLASSIFICATION,
SUBSURFACE CLASSIFICATION
(check all units that apply)
1septic tanks
2. pump tanks
3siphon or pump -dosing systems
4, sand filters
5. grease trap/interceptor
6 oil/water separators
7, gravity subsurface treatment and disposal:
8. pressure subsurface treatment and disposal:
SPRAY IRRIGATION CLASSIFICATION
(check all units that apply)
1 preliminary treatment (definition no. 32 )
2. lagoons
3septic tanks
4. pump tanks
5. -- pumps
6.sand filters
7- grease trapinterceptor
8. oil/water separators
9disinfection
10. chemical addition for nutrient/algae control
11. spray irrigation of wastewater
In addition to the above classifications, pretreatment of wastewater in excess of these components shall
be rated using the point rating system and will require an operator with an appropriate dual certification.
LAND APPLICATION/RESIDUALS CLASSIFICATION (Applies only to permit holder)
1. Land application of biosolids, residuals or contaminated soils on a designated site.
WASTEWATER TREATMENT FACILITY CLASSIFICATION
The following systems shall be assigned a Class 1 classification, Lnless the flow is of a significant quantity or the technology is unusually
complex, to require consideration by the Commission on a case -by -case basis: (Check €f Appropriate)
1Oil/water Separator Systems consisting only of physical separation, pumps and disposal;
2, Septic TanWSand Filter Systems consisting only of septic tanks, dosing apparatus, pumps.sand filters, disinfection
and direct discharge;
3. Lagoon Systems consisting only of preliminary treatment, lagoons, pumps, disinfection, necessary chemical treatment for
algae or nutrient control, and direct discharge;
4, Closed -loop Recycle Systems;
5Groundwater Remediation Systems consisting only of olYwater separators, pumps, air -stripping, carbon adsorption, disinfection
and disposal;
6:Aquaculture operations with discharge to surface waters;
7 Water Plant sludge handling and back -wash water treatment;
8. Seafood processing consisting of screening and disposal.
9. Single-family discharging systems, with the exception of Aerobic Treatment Units, will be classified €f permitted after July 1.
1993 or if upon inspection by the Division, it Is found that the system is not being adequately operated or maintained. Such
systems will be notified of the classification or reclassification by the Commission, in writing.

The following scale is used for rating wastewater treatment facilities: (circle appropriate points)
ITEM POINTS
(1) Industrial Pretreatment Units or industrial Pretreatment Program (see definition No. 33) 4
(2) DESIGN FLOW OF PLANT IN gpd [not applicable to non -contaminated cooing waters, sludge handing facilities for
water purification plants, totally closed cycle systems(see definition No. 11), and facittties consisting only of Item
(4)(d) or Items (4)(d) and (11)(d)) .
0 - 20.000 1
20,001 • 50,000 2
50.001 - 100,000
100.001 - 250.000 4
250.001 - 500.000 5
500.001 - 1,000.000 ,6
1.000.001 - 2,000.000 10
2.000.001 (and up) rate 1 point additional for each 200,003 gpd capacity up to a maximum of 3 0
Design Flow (gpd)
(3) PRELIMINARY UNITS/PROCESSES (see definition No.32)
(a) Bar Screens
or
(b) Mechanical Screens. Static Screens or Comminuting Devices...................».»....».»....».......»....».»....»..........6
(c) Grit Removal
or
(d) Mechanical or Aerated Grt Removal 2
(e) Fbw Measuring Device 1
or
(I) Instrumented Flow Measurement 2
(g) Preaeration 2
(h) Influent Flow Equalization 2
(I) Grease or Oil Separators - Gravity.-............—.—....................--- ......... .....-----.........-----...... 2
Mechanical .... ,3
Dissolved Air Flotation ,6
()) Prechtortnatlon 5
(4) PRIMARY TREATMENT UNITS/PROCESSES
(a) Septic Tank (see definition No. 43) 2
(b) Imhoff Tank. .5
(c) Primary Clarifiers .5
(d) Settling Ponds or Settling Tanks for Inorganic Non•toxlc Materials (sludge handling facilities for water
purification plants. sand. gravel. stone, and other mining operations except recreational activities such as gem
or gold mining) ... 2
(5) SECONDARY TREATMENT UNITS/PROCESSES
(a) Carbonaceous Stage
(I) Aeration -High Purity Oxygen System 20
Diffused Air System ..,
10
Mechanical Air System (fixed. floating or rotor)....................»...»...»....,.............»..........t
Separate Sludge Reaeratlon
(1I) Trickling Filter
HighRate»...•........».»».».»»..............».....»...».»...»..».».... »....»...».7
Standard Rate ....... ....».......................... »..»».»..».5
Packed Tower .5
(III) Biological Aerated Fitter qr Aerated Biological Filter..M.»»»...w.»»».»»».»».....»»».N...»N.10
(iv) Aerated Lagoons 10
(v) Rotating Biological Contactors 10
(vi) Sand Filters -intermittent biological 2
Recirculating biological...... .......................»....»»....». ........ »............ 3
(vfI) Stabilization Lagoons .........».........».»....»...».......».»..........»....»......»...,�
(vm) Clarifier f�}
(ix) Single stage system for combined carbonaceous removal of BOO and nitrogenous removal by
nitrification (see definition No. 12)(Points for this Item have to be in addition to Items
(5)(a)(1) through (5)(a)(v111).
utilizing the extended aeration process (see definition No.3a)
utilizing other than the extended aeration process. ..... ........ ..... -..... »....»..... ....... ......».-.t
(x) Nutrient additions to enhance BOO removal ..... »...».»............ »..»....»»............ ».......... »8
(xi) Biological Culture ('Super Bugs')addition..........»........ ...»....... ........ »....»......».».»5
(b) Nitrogenous Stage
(I) Aeration - High Purity Oxygen System.....»..».»..»...».......»................»..........»....»........20
Diffused Air System 10
Mechanical Air System (fixed. floating or rotor)-..—..—...—,.---...- ........ .........------.8
Separate Sludge Reaeratlon ....»» »....»» 3
(Ii) Trickling Fllter-High Rate..».......»......». .» 7
Standard Rate ..».....».......».»......»..»»....»....... .»..»..».»...»............ ».....5
Packed Tower 000000000000000 000004 ....»............... .... ...»»...... »..5
(6)
o
(!ii) Biological Aerated Fitter or Aerated Biological Fitter.»»...»...»».»»......»........»»...».»...»».».10
(Iv) Rotating Biological Contactors »....»...».». 10
(v) Sand Filter - Intermittent biological .........».».».» ................. 2
Recirculating biological..»..» ..... »...............f ... 3
(v1) Clarifier -..»..»........».......»...».»...»....»....».»......».».....».».».»......»...5
TERTIARY OR ADVANCED TREATMINT LMRS/PROCESSES
(a) Activated Carbon Beds -
wi'thout carbon regeneratlon.....»».....................».....»»».....»»»....».......».......».....».........».»5
whh carbon regeneration.»......... » » ».»......-...»......»»15
(b) Powdered or Granular Activated Carbon Feed -
without carbon regeneratlon.»».»....»....»».....»......».........».......»...»-.....»»».».......»..»......5
/�
with carbon regeneration...»..............N»»».».......»»..».».»».»»........NM..NN»...».....».».»....1 5
(c) Alr stripping ....»....».»»..........».».»...»»»M..» ...»..»....... »...... »».». 5
(d) Denhrificatlon Process».»....».»....».»...»..........»».....».».».»....»»».....».»....».MM.w...».».N..»»..»...»»..»»10
(e) Electrodialysls.».........»........».........».»...»......»»....»...»».».»-».....»»»».»».»»............»»....».....»..»».»....5
(f) Foam Separatlon.»..»M»».»».»..»....».»»..N»..»...».».».»....».»»..»...».»N».»»..NN»w..»N.»..N».»......»»»».5
(g) ton Exchange....»....».»...». ...... »..»..»»»...»»»»...»«..».....»......»».»»....»..»..».»N»..».»».».»»..»»».»......5
(h) Land Application of Treated Effiuert (see definition No. 22b) (not applicable for sand. gravel. stone
and other similar mining operations) by high rate lnfiitratlon.»»...»..........»...»».»».»»»....»»....»...»...»».»....4
(I) Microscreens......»...................... ..........1......... »........ 04..... »...............»....».»..»»........»....»».......5
()) Phosphorous Removal by Blological Processes (See detlnttlon No. 26)....»»....»...»...... .............. ........ ».20
(k) Polishing Ponds - without aeratlon...................»»»»»».......»........»....»».».»».»_».....»»...»»..»».»».»..2
with aentiion....»».»..»»..».».........»».»».....»...........».»...».»».......»....»»....»...»»........5

(I) Post Aeration - cascade 0
diffused or mechanical
(m) Reverse Osmosis 5
(n) Sand or Mixed -Media Fitters - low rate 2
high rate 5
(o) Treatment processes for removal of metal or cyanide 15
(p) treatment processes for removal of toxic materials other than metal or cyanide.....- ............. .. ...... —........-1 5
(7) SWDGETREATMENT •
(a) Sludge Digestion Tank - Heated (anaerobic) 10
Aerobic 5
Unheated (anaerobic) 3
(b) Sludge Stabilization (chemical or thermal) 5
(c) Sludge Drying Beds - Gravity
Vacuum Assisted .9
(d) Sludge Elutriation
5
(e) Sludge Conditioner (chemical or thermal) .5
(1) Sludge Thickener (gravity) .. 5
(g) Dissotved Air Flotation Unit (not applicable to a unit rated as (3)(i)) 8
(h) Sludge Gas Utilization (including gas storage)
(I) Sludge Holding Tank - Aerated 41)
Non -aerated 2
(J) Sludge incinerator (not including activated carbon regeneration) 10
(k) - Vacuum Fitter, Centrifuge. or Fitter Press or other similar dewatering devices----....--- ....... ---- ........... -1 0
(8) RESIDUALS UTiLiZATIONVDISPOSAL (Including incinerated ash)
(a) Lagoons 2
(b) Land Application (surface and subsurface) (see definition 22a)
by contracting to a land application operator or landfill operator who holds the land application permit
or landfill permit 2
( ) (c)45
dicated Landfill(burial) by the permlttee of the wastewater treatment facility
9
(a) Chlorination (b) Dechlorination 5 .5
(c) Ozone 5
5 •
(d) Radiation 5
(10) CHEMICAL ADDITION SYSTEM(S) ( see definition No. 9) [not applicable to chemical additions rated as item (3)0).
(5)(a)(x1). (6)(a), (6)(b), (7)(b). (7)(e). (9a). (9)(b) or (9)(c) 5 points each:
List
(11) MISCELLANEOUS UNTTSlPROCFSgFR
(a) Holding Ponds, Holding Tanks or Settling Ponds for Organic or Toxic Materials including wastes from mining
operations containing nitrogen or phosphorus compounds to amounts significantly greater than is common
for domestic wastewater A
(b) Effluent Flow Equalization (not applicable to storage basins which are Inherent in !and application systems)--2
cd; SStageDischarge (not applicable to storage basins inherent In land application systems)............»........»......_
Ps
(e) Stand -By Power Supply
(f) Thermal Pollution Control Device
TOTAL POINTS
CLASSIFICATION
Class! 5-25 Points
Class 11 26-50 Points
Class 51-65 Points
Class IV 66-Up Points
5
5
5
5
5
Facilities having a rating of one through four points. inclusive. do not require a codified operator.
Facilities having an activated sludge process will be assigned a minimum classification of Class II.
Facilities having treatment processes for the removal of metal or cyanide will be assigned a minimum classification of Class It.
Facilities having treatment processes for the biological removal of phosphorus will be assigned a minimum classification of Class III.
(�
.0004 DEFINITIONS
The following defintttons shall apply throughout this Subchapter.
(1) Activated Carbon Beds. A physical/chemical method for reducing sotubte organic material from wastewater effluent; The column -type beds used in this
method will have a flow rate varying from two to eight gallons per minute per square foot and may be either upflow or downtlow carbon beds. Carbon may or
may not be regenerated on the wastewater treatment plant she;
(2) Aerated Lagoons. A basin in which all solids are maintained in suspension and by which biological oxidation or organic matter is reduced through artificially
accelerated transfer of oxygen on a flow -through basis;
(3) Aeration. A process of bringing about Intimate contact between air or high purify oxygen In a liquid by spraying. agitation or diffusion,(3a) Extended
Aeration. An activated sludge process utilizing a minimum hydraulic detention time of 18 hours.
(4) Agriculturally managed site. Any site on which a crop Is produced. managed. and harvested (Crop Includes grasses. grains. trees, etc.);
(5) Air Stripping. A process by which the ammonium ion is first converted to dissolved ammonia (pH adjustment) with the ammonia then released to the
atmosphere by physical means; or other similar processes which remove petroleum products such as benzene. toluene. and xylene;
(6) Carbon Regeneration. The regeneration of exhausted carbon by the use of a furnace to provide extremely high temperatures which volatilize and oxidize the
absorbed impurities;
(7) Carbonaceous Stage. A stage of wastewater treatment designed to achieve 'secondary' effluent limits;
(8) Centrifuge. A mechanical device in which centrifugal force is used to separate solids from Liquids or to separate liquids of different densities;
(9) Chemical Addition Systems- The addition of chemical(s) to wastewater at an application point for purposes of Improving solids removal. pH adjustment.
alkalinity control. etc.; the capability to experiment with different chemicals and different application points to achieve a specific result will be considered one
system; the capability to add chemical(s) to dual units will be rated as one system; capability to add a chemical at a different application points for different
purposes will result in the systems being rated as separate systems;
(10) Chemical Sludge Conditiordng. The addition of a chemical compound such as lime, ferric chloride, or a polymer to wet sludge to coalesce the mass prior to
Us application to a dewatering device;
(11) Closed Cycle Systems. Use of holding ponds or holding tanks for oontatnment of wastewater containing Inorganic, non -toxic materials from sand. gravel.
crushed stone or other similar operations. Such systems shall carry a maximum of two points regardless of pumping facilities or any other appurtenances;
(12) Combined Removal of Carbonaceous BOD and Nitrogenous Removal by Nttrification- A single stage system required to achieve permit effluent limits on BOD
and ammonia nitrogen within the same biological reactor.
(13) Dechlortnatlon. The partial or complete reduction of residual chlorine in a liquid by any chemical or physical process;
(14) Denitrtficatlon Process. The conversion of nitrate -nitrogen to nitrogen gas;

State of North Carolina
Health and Natural Resources '
Department of Environment,
Division of Environmental Management
`5.
James B. Hunt, Jr., Governor Jonathan B. Howes, Secretary p E H N F{
A. Preston Howard, Jr., P.E., Director
limmnirmt•
hi DEC U 8 1993 �J
November 30, 1993
MAYOR CONRAD H. JENKINS
TOWN OF KENANSVILLE
P. O. BOX 420
KENANSVILLE, NORTH CAROLINA 28349
Subject: Application No. NC0036668
KENANSVILLE WWTP
Duplin County
Dear MAYOR JENKINS:
The Division's Permits and Engineering Unit acknowledges receipt of your permit application and
supporting materials received on November 30, 1993. This application has been assigned the number
shown above. Please refer to this number when making inquiries on this project.
Your project has been assigned to Susan Wilson for a detailed engineering review. A technical
acknowledgement will be forthcoming. If this acknowledgement is not received within thirty (30)
days, please contact the engineer listed above.
Be aware that the Division's regional office, copied below, must provide recommendations from the
Regional Supervisor for this project prior to final action by the Division.
I am, by copy of this letter, requesting that our Regional Office Supervisor prepare a staff report and
recommentations regarding this discharge. If you have any questions regarding this application,
please contact the review person listed above.
Sincerely,
r / Coleen H. Sullins, P.E.
�'' Supervisor, Permits and Engineering Unit
cc: Wilmington Regional Office
Pollution Prevention Pays
P.O. Box 29535, Raleigh, North Carolina 27626-0535 Telephone [phone]
An Equal Opportunity Affirmative Action Employer

N. C. DEPARBEIT OF NATURAL RESOURCES & COMMUNITY DEVELOPMENT
ENVI Rti 'ENTAL MANAGES TT COMMISSION
NATIONAL POLLUTANT DISCHARGE ELIt1INATION SYSTQI
APPLICATION FOR PERMIT TO DISCHARGE - SHORT FORMA
To be filed only by municipal wastewater dischargers
1 t
FOR
AGENCY
USE t-:
Do not attempt to complete this form before reading the accompanying instructions
Please print or type
1. Name of organization responsible for facility
APPLICATION -NUMBER
Ado IcI3k4.l(kOle
n r RTICIPTWD
_ ...:..... ii0 . ..,.DAY .
1 M giao:r.- .4
Town of Kenansville
2. Address, location, and telephone number of facility producing discharge:
A. Name Kenansville Municipal Wastewater Treatment Facility
B. Mailing address:
1. Street address P. O. Box 420
2. city Kenansville , 3: county Duplin
4. State NC 5. ZIP ' 28349
C. Location:
1. Street Routledge Road
2. City Kenansville 3. County. Duplin
4. State
NC
D. Telephone No. _ 296-0369
Area
Code
If all your waste is discharged into a publiclyowned waste treatment facility and
to the best of your. knowledge you are not required to obtain a discharge permit,
proceed to item 3. Otherwise proceed directly to item 4.
3. If you meet the condition stated above, check here L/ and supply the information
asked for below. After completing these items, please complete the date, title, and
signature blocks below and return this form to the proper reviewing office without
completing the remainder of the form.
A. Name of organization responsible for receiving waste
•
•
rN
• • ,.., ••-:. :;;
•
.Ls
:. ,��►+o: i, 'q,a) • C Z
B. Facility receiving waste;
1. Name
2. Street address
3. City 4. County
5. State 6. ZIP.
4. Type of treatment: - ---
_ .os'o:+2.: 1 '.
• A. / /None B. L/Primary C. L/Intermediate D. LLSecondary E. L /Advanced
5. Design floe (average daily) of facility •]:70112gd.
6. Percent B0D removal (actual): •
A. L/0-29.9 B. L/30-64.9 C. / /65-84.9 D. 12785-94.9 E. L /95 or more
7. Population served: •
A. / /1-199 B. L/200-499 C. L/500-999 D. / 1,000-4,999 E. ./5,000-9,999 P. Eh0,000 or more
8. Number of separate discharge points:
A /W1 8. //2 C. / /3 D. L/4 E. L/5 P. L/6 or more

9. Description of waste water discharged to surface eaters only (check as applicable).
Discharge per
operating day
00010.
Flow, MGD (million gallons per operating day)
Volume treated before
discharging (percent)
o-
0.0099
(1) ,
0:01 0.05- 10.1-
0.049 1 0.099 0.49
(2) (3) (4)
0.5- 1.0-
0.99 4.9
(5) (6)
5 or
more
(7)
None
(8)
0.1-
34.9
(9)
35-
64.9
(10)
A. Average
X
i
65- 95-
94.9 100
(11) (12)
X
B. Maximum
X
10. If any waste water, treated or untreated, is discharged to places other than
Surface waters, cnecn vcivw sa art, • .
"^
Waste eater is
discharged to
Flow, MGD (million gallons per operating days
0-0.0099
(1)
0.01-0.049
(2)
0.05-0.099
(3)
0.1-0.49
(4)
0.5-0.99
(5)
1.0-4.9•
(6) •
5 or more
(7)
A. Deep well
_
lagoon
B. Evaporation
system•
C. Subsurface percolation
D. Other, specify: Grove Creak
. X
-11. as.any-sludge ultimately returned to a waterway?
A•- Yes .. B. LVNo
12. a. Do you receive industrial waste?
-•-- 1:-L%Yes .....- 2. AC/No • .
b:-If yen --enter approximate number of industrial dischargers into system
13. Type of collection sewer system:
• A.•Separate sanitary
B. 1/Combined sanitary and storm - ._
. C. £TBoth separate and combined sewer systems.
'14. Name of receiving water or waters Grove Creek
15. Does your discharge contain or is it possible for your discharge to contain .
one or more of the following substances: ammonia,
cyanide, aluminum,
pheberyllium,
cadmium, chromium, copper, lead, mercury,.
0
A.. L?Yea B. J 'No
I certify that I am familiar with the information contained in the application and that
to -the best of my knowledge and belief such information is true, complete, and accurate.
• Conrad If. Jenkins
Printed Name of Person Signing
Novciaze±29, 1993 .
Date Application Signed .
• S gnature of A
c
North Carolina General Statute 143-215.6(b)(2) provides that: Any person who knowingly makes any
false statement representation,'or certification in any application, record, report. plan, or •"
other document files or required to be maintained under Article 21 or regulations of the Environmental
Management Commission implementing that Article, or who falsifies, tampers with, or knowly renders
inaccurate any recording or monitoring device or metiod required to be operated or maintained under
Article 21 or regulations of the Environmental Management Commission implementing that Article, shall
be guilty of a misdemeanor punishable by a fine not to exceed S10,000, or by imprisonment not to
exceed six months, or by both. (18 U.S.C. Section 1001 provides a punishment by a fine of not more
than $10,000 or imprisonment not more than 5 years, or both, for a similar offense.)