HomeMy WebLinkAboutNC0000272_Analytical Fecal Coliform Date per Request_20180101 (23);Yl
NCDENR
North Carolina Department of Environment and Natrirai Resol-Irces
Division of Water Quality
Beverly Eaves Perdue Coleen H. Sullins
Governor Director
May 26, 2010
Mr. Dane Griswold, Plant Manager
Blue Ridge Paper Products
P.O. Box 4000
Canton, North Carolina 28716
Subject: NPDES Permit Issuance
Permit No. NCO000272
Blue Ridge Paper Products, Inc.
Haywood County
Dear Mr. Griswold:
Dee Freeman
Secretary
The Division of Water Quality is forwarding herewith the Final NPDES permit for Blue Ridge Paper Product's Canton
mill. This permit renewal is issued pursuant to the requirements of North Carolina General Statute 143-215.1 and the
Memorandum of Agreement between North Carolina and the U.S. Environmental Protection Agency dated October 15,
2007 (or as subsequently amended).
Public hearings were held in Tennessee and North Carolina seeking comments on the Draft permit and proposed removal
of the color variance. Subsequently, U.S. EPA submitted an objection letter (dated February 22, 2010) on the Draft permit,
and required several permit changes. This Final permit addresses public comments, the specific EPA objections, and
incorporates additional recommendations of the DWQ Hearing Officer. The specific changes that have been incorporated
into this Final permit are as follows:
Color Technolo. The starting annual average color limit has been changed to 38,020 lb/day based on EPA's use
of the 95% confidence limits. The final annual average color limit (after 4 years) has been changed to a range of
32,000-36,000 lb/day. A Color Reduction implementation plan will be required within one year of permit
issuance, and a reopener clause has been added that will allow the Division to include interim requirements and
dates for their achievement following review of the Implementation Plan. A Low Flow Contingency Plan for color
control shall be submitted within one year of permit issuance.
Color Variance. The consideration for color variance removal has been dropped from this permit renewal. The
facility will continue to operate under its current color variance, which will be subject to NC Environmental
Management Commission approval at a later date. Blue Ridge Paper may elect to conduct a color perception study
in the future to support removal of the color variance, and any such proposed study must be approved by the
Division of Water Quality.
CWA Section 316(a) Thermal Variance. The Balanced and Indigenous Population (BIP) study must conform with
EPA study guidelines, and is subject to EPA review. The monthly average delta temperature limit has been
changed to 8.5 degrees C based on EPA's use of a 95`" percentile, which can be modified in the future based on
1617 Mail Service Center. Raleigh, North Carolina 27699-1617
Location: 512 N. Salisbury St Ralegh, North Carolina 27604 One
Phone: 91M07-63001 FAX: 9IM07-64921 Customer Service: 1 -87 7.623-6748 NOrthCarolina
Internet: www.ncwaterquality.org Naturally Equal Opportunity i Affirmative Action Employer
Fest.tlts of the therntal modeling. Blue Rldgf, Pap-l- will con.ti_nue W ntonitorlraport daily maximum and mont1ily
average effluent temperatures,
Dioxin. A daily maximum dioxin effluent limit has been added, based on a 1.5 multiplier of the chronic limit.
Blue Ridge Paper will conduct three annual fish tissue monitoring events over the permit teen, Two events must
be fi-om Waterville Lake, while the third fish sampling may be from Waterville Lake or the mainstem Pigeon River
below the mill outfall.
Y Turbidi . Instream turbidity monitoring (upstream and downstream at Fiberville Bridge) will be required the first
year, at 2/Month monitoring frequency. A turbidity reopener clause has been added to the permit.
0 Hardness. Quarterly effluent hardness monitoring has been added to the permit.
la) AOX Limits. Though not required by EPA Effluent Guidelines, AOX production -based limits will be held at the
2001 permit levels, based on the facility's performance history.
The Division of Water Quality commends Blue Ridge Paper for the progress made to date in improving water quality in the
Pigeon River, including a 90% reduction in color since 1988 and successful fish reintroduction projects. The Division has
thoroughly considered the comments provided by Blue Ridge Paper, U.S.EPA, the State of Tennessee, local communities
and environmental interest groups to develop this Final permit, which requires additional color reductions.
If any parts, measurement.frequencies, or sampling requirements contained in this permit are unacceptable to you, you
have the right to an adjudicatory hearing upon written request within thirty (30) days following receipt of this letter. This
request must be in the form of a written petition, conforming to Chapter 150B of the North Carolina General Statutes, and
filed with the office of Administrative Hearings, 6714 Mail Service Center, Raleigh, North Carolina 27699-6714. Unless
such a demand is made, this permit shall be final and binding.
Please take notice that this permit is not transferable except after notice to the Division of Water Quality. The Division
may require modification or revocation and reissuance of the permit. This permit does not affect the legal requirements to
obtain other permits which may be required by the Division of Water Quality, the Division of Land Resources, the Coastal
Area Management Act, or any other federal or local governmental permit.
If you have any questions on this permit, please contact Tom Belnick at 919-807-6390.
Sincerely,
Jen. Sullinrj\_��
Hardcopy: Central Files, NPDES Files
Asheville Regional Office, SWPS
Email: US EPA, Region 4
Aquatic Toxicology Unit
Shannon Deaton, NC Wildlife Resources Commission
Paul Davis, TN Division of Water Pollution Control
David McKinney, TN Wildlife Resources Agency
Hope Taylor, Clean Water for NC
Hartwell Carson, French Broad Riverkeeper
Iliff McMahan, Mayor Cocke County, TN
1617 Mail Service Center, Raleigh, North Carolina 27699-1611
Location: 512 N. Salisbury St. Ralegh, North Carolina 27604 One
Phone: 919-807-63001 FAX: 919-807-64921 Customer Service: 1-877-623-6748 NorthCarolina
Internet www.ncwaterqualiV.org atura!!�
An Equal Opportunity 1 Affirmative Action Employer
Pf.rr,ait: Number. NC0000272
STATE OF NORTH C:AROLINA
DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES
DIVISION OF WATER QUALITY
Final PERMIT
TO DISCHARGE WASTEWATER UNDER THE
NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM
In compliance with the provision of North Carolina General Statute 143-215.1, other lawful standards and
regulations promulgated and adopted by the North Carolina Environmental Management Commission,
and the Federal Water Pollution Control Act, as amended,
Blue Ridge Paper Products Inc. dba Evergreen Packaging
is hereby authorized to discharge wastewater from a facility located at
Blue Ridge Paper Products Wastewater Treatment Plant
Off Highway 215
Canton
Haywood County
to receiving waters designated as the Pigeon River in the French Broad River Basin in accordance with
effluent limitations, monitoring requirements, and other conditions set forth in Parts I, H, III and IV
hereof.
This permit shall become effective July 1, 2010.
This permit and authorization to discharge shall expire at midnight on June 30, 2015.
Signed this day May 26, 2010. / ;
Coleen H. Sullins, Dirf'"' ctoi
Division of Water Qu lity
By Authority of the Environmental Management Commission
Peimi.t Number: NCO000272
SUPPLEMENTTO PERMIT COVER SHEET
Blue Ridge Paper Producis, Inc. dba Fvergreen Packaging
is hereby authorized to:
1. Continue operation of a 29.9 MGD wastewater treatment plant for the treatment of wastewater
associated with the Blue Ridge Paper Products Inc. pulp and paper mill, the Town of Canton's
chlorinated domestic wastewater and landfill leachate. The treatment system consists of the
following treatment units:
• Grit Chamber
• Bar Screen
• Lift Pumps
• Polymer addition
• pH control ( CO2 injection or H2SO4 backup)
• Three primary clarifiers
• Nutrient Feed
• Aeration basins
• Three secondary clarifiers
• Residual belt presses
• Effluent flow measurement
• Cascade post aeration with oxygen injection
• Instream oxygen injection facilities
The facility is located at the Blue Ridge Paper Products WWTP, off Highway 215, Canton,
Haywood County, and;
2. Discharge treated wastewater from said treatment works at the location specified on the attached
map through outfall 001 into the Pigeon River, which is classified C water, in the French Broad
River Basin.
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Latitude: 35*32'08" C (�V ! L ®� 7 "? Facility
t �t VV
Longitude: 82°50'42"
Quad# E7SE Location
Stream, Class:
Streass:C :Pigeon River glue Ridge Paper Products
Stream Class: C � p
Subbasin:40305 Carlton Mill +/\YI /� /o�� '
SCALE 1:24000
Permit Number: NC0000272
A. (I.) EFFLUENT LIMITATIONS ,AND MONITORING REQUIREMENTS
During the period beginning on the effective elate of the permit and lasting until expiration., the Permittee
is authorized to discharge treated industrial, municipal, stormwater and landfill wastewater through
outfall(s) 001. Such discharges sliall be limited and monitored by the Permittee as specified below:
Effluent Characteristics
Effluent Limits :
Monitoring Requirements
Mortfhly
Average
-Daily .
Maximum =
Measurement
FrequeMcj.
Sample Type
x ;Sample
Location1
Flow
29.9 MGD
Continuous
RecordingI
or E,
BOD, 5-day, 20°C
3205 lb/day
10897 lb/day
Daily
e
I, E,
Total Solids
12549 lb/day
49560 lb/day
Daily
Composite
1, E1
-Suspended
NH3-N
Daily
E,
AOX
1556.91b/day
2822.2lb/day
Weekly
Composite
E,
Color
52,000lb/day
105,250
lb/day
Daily
Composite
El
Dissolved Oxygen
Dail
Grab
Ej
Te -nature
Daily
Grab
El
pHo
Daily
Grab
El
Conductivity
Daily
Grab
Ei
Fecal Coliform
200/ 100 mL
400/ 100 mL
Weekly
Grab
E,
COD
Weekly
Composite
E,
Total Nitrogen
(NO,-N + NO3-N + TKN)
Monthly
Composite
E,
Total Phosphorus
Monthly
Composite
E,
Chronic ToxiCity7
QuarterlyComposite
E,
Trichlorophenof
30.6 lb/day
Quarterly
Composite
E,
Pentachloro henol
4.91b/day
Quarterly
Composite
El
Selenium
Annual
Composite
E,
2,3,7,8 Tetrachloro-dibenzo-
-dioxin
0.04 pg/L
0.06 pg/L
Annual
Composite
1, El
ConductivityloDaily
Grab
Pigeon River
Flow
Daily
Grab
Pigeon River
Fecal Coliformlo
Weekly
Grab
Pigeon River
Color
Variable
Grab
Pigeon River
Dissolved Ox en
Variable
Grab
Pigeon River
Temperature
Variable
Grab
Pigeon River
Zinc
Quarterly
Composite
Ei
Quarterl
Co ositeurbidity
[Hardness
2/Month
Grab
E,, Pigeon
River
Footnotes:
1. Sample Location: I- Influent, El — Effluent, Pigeon River - Instream sampling as specified in A. (5.) Instream
Monitoring Special Condition.
2. AOX monitoring shall be in accordance with the Sampling Plan for Cluster Rule Parameters (dated March 19,
2001) or subsequent modifications approved by the Division. AOX data shall be submitted on a quarterly basis
along with other Effluent Guideline chemical data; refer to A. (7.) Effluent Guideline Sampling Plan Special
Condition.
3. Annual average color limit is 38,020 lb/day, which will decrease to 32,000-36.000 lb/day no later than 4 years
after the permit effective date. See A. (8.) Color Analysis and Compliance Special Condition. All color limits
are measured as true color.
4. The daily average effluent dissolved oxygen concentration shall not be less than 6.0 mg/L. See A. (10.)
Dissolved Oxygen Special Condition.
5. The pennittee shall report daily and monthly average effluent temperature.
Perinit Number: NCO0002 72
6. The pH of the effluent shall not be less than 6.0 nor greater than 9.0 (on the standard units scale).
7. Chronic Toxicity (Ceriod4phnia) at 90% Effluent Concentration: March, June, September, December (see A.
(4.) Chronic Toxicity Permit Limit (Quarterly)).
8. Trichlorophenoi and Pentachlorophenol limits and monitoring are provisionally waived since the facility has
certified that chlorophenolic biocides are not used at this facility. If the facility changes operations to include
chlorophenolic biocide, the Permittee shall notified the Division prior to use and the limits and monitoring
requirements shall become immediately effective.
9. See A. (9.) Dioxin Monitoring Special Condition.
10. See A. (5.) Instream Monitoring Special Condition.
11. The monthly average instream temperature measured at a point 0.4 miles downstream of the discharge location
shall not exceed 32°C during the months of July, August, and September and shall not exceed 29 °C during the
months of October through June. The monthly average instream temperature measured at this location shall not
exceed the monthly average instream temperature of the upstream monitoring location by more than 8.5°C. This
value can be adjusted based on the results of thermal modeling [See Special Condition A.(12.) Temperature
Variance Review Special Condition].
12. Monitoring should be conducted in conjunction with Whole Effluent Toxicity Testing.
13. Monitoring should be conducted in conjunction with zinc monitoring.
14. Monitoring shall be conducted upstream of the discharge (mile marker 63.8) and at Fiberville Bridge for 1 year
(12 months). The monitoring shall not occur within 72 hours of a rain event. This permit may be reopened and
modified to include a turbidity jimit if a reasonable potential to exceed the State's numeric criterion is found to
exist.
There shall be no discharge of floating solids or visible foam in other than trace amounts.
See A. (6.) Best Management Practices (BMP) Special Condition.
See A. (11.) Town of Canton Inflow and Infiltration Special Condition.
Definitions:
MGD — Million gallons per day lb/day — Pounds per day
mL — Milliliter BOD — Biochemical Oxygen Demand
µg/L - Micrograms per liter AOX - Adsorbable Organic Halides
COD - Chemical oxygen demand pg/L - picograms per liter
Permit Nu nibe; : NCO000272
A. (2.) EFFLUENT LINII ATIONS AND NIGNITORING R.EQUIREIIIF:NTS
During the period beginning upon the effective elate of the permit and lasting until expiration, the
discharge of wastewater from the pine bleach plant to the wastewater treatment plant through
internal outfall(s) 002 (E2'), shall be limited and monitored by the Permittee as specified below and in A.
(7 1 Fffl„ -mt Oliideline Samnling Plan Special Condition:
Effluent Cl aracterishcs
{; ;
K g R> f
;.r
Limlts
Monitorinq:R J uit, ments
Monfhty
„� Daily ,
Measurement
;'Frequehcy...
Sample Types
59mpte
FIow7
Weekly
Calculated
E,
Chloroform
5.11b/day
8.61b/day
Quarterly
Grab
E2
2,3,7,8 Tetrachloro-dibenzo-
-dioxin TCDD)
< 10 pg/L
Annual
Composite
E,
2,3,7,8 Tetrachloro-dibenzo-
-furan TCDF)
31.9 pg/L
Annual
Composite
E2
Trichlorosyringol
< 2.5 µg/L'
Quarterly
Composite
EZ
3,4,5-Tricblorocatechol
< 5.0 µg/LS
Quarterly
Composite
E2
3,4,6-Trichlorocatechol
< 5.0 µg/L5
Quarterly
Composite
E2
3,4,5-Trichloroguaiacol
< 2.5 pg/L
Quarterly
Composite
E2
3,4,6-Trichloroguaiaeol
< 2.5 µg/L
Quarterly
Composite
E2
4,5,6-Trichloroguaiacol
< 2.5 µg/L
Quarterly
Composite
E2
2,4,5-Trichlorophenol
< 2.5 µg/L
Quarterly
Composite -
E2
2,4,6-Trichlorophenol
< 2.5 µg/L
Quarterly
Composite
E2
Tetrachlorocatechol
< 5.0 µg/L
Quarterly
Composite
E2
Tetrachloroguaiacoi
< 5.0 pg/L
Quarterly
Composite
E2
2,3,4,6-Tetrachiorophenol
< 2.5 µg/L
Quarterly
Composite
E2
Pentachlorophenol
< 5.0 µg/L
Quarterly
Composite
E2
Footnotes:
1. Sample Location: E2 — Effluent is composed of Bleach Plant Effluent -acid (acid sewer collected from tap
installed on filtrate pump from C102 bleaching stage D-100 and from tap installed on filtrate pump from C102
bleaching stage D-2) and Bleach Plant Effluent -alkaline (alkaline sewer collected from tap installed on filtrate
pump from alkaline extraction stage E j. See A. (7.) Effluent Guideline Sampling Plan Special Condition
2. Monitoring and flow calculations shall be in accordance with the "Sampling Plan for Cluster Rule Parameters"
(dated March 19, 2001) or subsequent modifications approved by the Division. Chemical results for Effluent
Guideline parameters as prepared by the pemuttee (Internal Outfall 002 parameters +internal Outfa11003
parameters + AOX from Outfall 001) shall be reported on a quarterly basis or more frequently; refer to A. (7.)
Effluent Guideline Sampling Plan Special Condition.
3. Sample Type: Calculated- calculate separate flows for alkaline and acid sewers by water balance or flow
meters, and report total bleach plant flow (acid + alkaline wastestreams) in DMRs. Grab- collect separate grab
samples every 4-hours for 24-hour period from both the acid and alkaline streams, which will then be
composited separately by the lab, and analyzed as separate 24-hr composite acid and alkaline samples.
Composite- collect separate grab samples every 4 hours for 24-hour period from both the acid and alkaline
streams, then prepare and analyze a single flo-,v-proportioned composite of the acid and alkaline wastestream.
I. For compliance purposes, the permittee must report the total chloroform mass loading based on addition of
separate acid and alkaline chloroform mass loadings.
5. Limits are based on Minimum Levels (ML) specified in 40 CFR 430.01.
Definitions:
lb/day — Pounds per day pg/L — Micrograms per liter
pg/L — Picograms per liter
Permit Nunnber: NC0000272
A. (3.) EFFLUENT LIMITATIONS AND MONITORING RFQIIIREMENTS
During the period beginning upon the effective date of the permit and Iasting until expiration, the
discharge of wastewater from the hardwood bleach plant to the wastewater treatment plant through
internal outfall(s) 003 (E31), shall be limited and monitored by the Permittee as specified below and in A.
(7.) Effluent Guideline Sampling Plan Special Condition:
Effluent. Cha- kig nstics`_
F _
Umlts
<. Monitorina Reaulremenis t ...
Monthly 4�
Average=
Daily
Maximum
Measurement
a} Frequency
Sample Type3 `
y
Sarrlple :x.
Location'
Flow-
Weekly
Calculated
E3
Chloroform
6.5lb/day
10.9lb/day
Quarterly
Grab
E3
2,3,7,8 Tetrachloro-dibenzo-
-dioxin (TCDD}
< 10 pg/L
Annual
Composite
E3
2,3,7,8 Tetrachloro-dibenzo-
-furan (TCDF)
31.9 pg/L
Annual
Composite
E3
Trichlorosyringol
< 2.5 µg/LS
Quarterly
Composite
E3
3,4,5-Trichlorocatechol
< 5.0 µg/L
Quarterly
Composite
E3
3,4,6-Trichlorocatechol
< 5.0 µgIV
Quarterly
Composite
E3
3,4,5-Trichloroguaiacol
< 2.5 µg/L
Quarterly
Composite
E3
3,4,6-Trichloroguaiacol
< 2.5 µg/L
Quarterly
Composite
E3
4,5,6-Trichloroguaiacol
< 2.5 µg/LS
Quarterly
Composite
E3
2,4,5-Trichlorophenol
< 2.5 µg/L
Quarterly
Composite
E3
2,4,6-Trichlorophenol
< 2.5 pg/L
Quarterly
Composite
E3
Tetrachlorocatechol
< 5.0 µg/I
Quarterly
Composite
E3
Tetrachloroguaiacol
< 5.0 µg/L5
Quarterly
Composite
E3
2,3,4,6-Tetrachlorophenol
< 2.5 µg/L
Quarterly
Composite
E3
Pentachlorophenol
< 5.0 µg/LS
Quarterly
Composite
E3
Footnotes:
1. Sample Location: E3 — Effluent is composed of Bleach Plant Effluent -acid (acid sewer collected from tap
installed on filtrate pump from C102 bleaching stage D-100) and Bleach Plant Effluent -alkaline (alkaline
sewer collected from tap installed on filtrate pump from alkaline extraction stage Eo). See A. (7.) Effluent
Guideline Sampling Plan Special Condition.
2. Monitoring and flow calculations shall be in accordance with the "Sampling Plan for Cluster Rule Parameters"
(dated March 19, 2001) or subsequent modifications approved by the Division. Chemical results for Effluent
Guideline parameters, as prepared by the permittee (Internal Outfall 002 parameters + internal Outfall 003
parameters + AOX from Outfall 001) shall be reported on a quarterly basis or more frequently; refer to A. (7.)
Effluent Guideline Sampling Plan Special Condition.
3. Sample Type: Calculated- calculate separate flows for alkaline and acid sewers by water balance or by flow
meter, and report total bleach plant flow (acid + alkaline wastestreams) in DMRs. Grab- collect separate grab
samples every 4-hours for 24-hour period from both the acid and alkaline streams, which will then be
composited separately by the lab, and analyzed as separate 24-hr composite acid and alkaline samples.
Composite- collect separate grab samples every 4 hours for 24-hour period from both the acid and alkaline
streams, then prepare and analyze a single flow -proportioned composite of the acid and alkaline wastestream.
4. For compliance purposes, the permittee must report the total chloroform mass loading based on addition of
separate acid and alkaline chloroform mass loadings.
5. Limits are based on Minimum Levels (ML) specified in 40 CFR 430.01.
Definitions:
lb/day — Pounds per day pg/L — Micrograms per liter
pg/L — Picograms per liter
Permit Number: NC00002 7 2
A. (4.) CHRONIC TOXICITY FERMI"f LuNm, (Q RTRLY)
The effluent discharge shall at no time exhibit observable inhibition of reproduction or significant mortality to
Ceriodaphnia duhia at an effluent concentration of 90%.
The permit holder shall perform at a minimum, . rq :artqUI , monitoring using test procedures outlined in the "North
Carolina Ceriodaphnia Chronic Effluent Bioassay Procedure," Revised February 1998, or subsequent versions or
"North Carolina Phase II Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent
versions. The tests will be performed during the months of March, June, September, December. Effluent sampling
for this testing shall be performed at the NPDES pemutted final effluent discharge below all treatment processes.
If the test procedure performed as the first test of any single quarter results in a failure or ChV below the permit
limit, then multiple -concentration testing shall be performed at a minimum, in each of the two following months as
described in "North Carolina Phase 1I Chronic Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or
subsequent versions.
The chronic value for multiple concentration tests will be determined using the geometric mean of the highest
concentration having no detectable impairment of reproduction or survival and the lowest concentration that does
have a detectable impairment of reproduction or survival. The definition of "detectable impairment," collection
methods, exposure regimes, and further statistical methods are specified in the "North Carolina Phase II Chronic
Whole Effluent Toxicity Test Procedure" (Revised -February 1998) or subsequent versions.
All toxicity testing results required as part of this permit condition will be entered on the Effluent Discharge
Monitoring Form (MR-1) for the months in which tests were performed, using the parameter code TGP313 for the
pass/fail results and THP313 for the Chronic Value. Additionally, DWQ Form AT-3 (original) is to be sent to the
following address:
Attention: North Carolina Division of Water Quality
Environmental Sciences Section
1621 Mail Service Center
Raleigh, North Carolina 27699-1621
Completed Aquatic Toxicity Test Forms shall be filed with the Environmental Sciences Branch no later than 30 days
after the end of the reporting period for which the report is made.
Test data shall be complete, accurate, include all supporting chemical/physical measurements and all
concentration/response data, and be certified by laboratory supervisor and ORC or approved designate signature.
Total residual chlorine of the effluent toxicity sample must be measured and reported if chlorine is employed for
disinfection of the waste stream.
Should there be no discharge of flow from the facility during a month in which toxicity monitoring is required, the
permittee will complete the information located at the top of the aquatic toxicity (AT) test form indicating the
facility name, permit number, pipe number, county, and the monthfyear of the report with the notation of "No Flow"
in the comment area of the form. The report shall be submitted to the Environmental Sciences Branch at the address
cited above. Should the permittee fail to monitor during a month in which toxicity monitoring is required,
monitoring will be required during the following month. Should any test data from this monitoring requirement or
tests performed by the North Carolina Division of Water Quality indicate potential impacts to the receiving stream,
this permit may be re -opened and modified to include alternate monitoring requirements or limits.
If the Permittee monitors any pollutant more frequently then required by this permit, the results of such monitoring
shall be included in the calculation & reporting of the data submitted on the DMR & all AT Forms submitted.
NOTE: Failure to achieve test conditions as specified in the cited document, such as minimum control organism
survival, minimum control organism reproduction, and appropriate environmental controls, shall constitute an
invalid test and will require immediate follow-up testing to be completed no later than the last day of the month
following the month of the initial monitoring.
Ferirtit. Number: NCO000272
A. (5e) INSTREANi MONITORING SPECIAL CONDITION
Stream
Mile
location Description
Parameter
Frequency
Designation
Marker
UP
63.8
Pigeon River upstream of the
Temperature
Daily
waste treatment plant outfall
B.O.
Daily
(prior to miring with the
Conductivity
Daily
discharge)
Color'
2/Week
Flow'
Daily
Fecal Coliform
Weekly
DN13
62.9
Pigeon River at Fiberville Bridge
Temperature
Daily
D.O.
Daily
Conductivity
Daily
Color'
2/Week
DN2
57.7
Pigeon River Above Clyde
Temperature
Daily
D.O.
Daily
DN3 3
55.5
Pigeon River Below Clyde
See Footnote 3
See Footnote 3
DN4
53.5
Pigeon River at NCSR 1625
See Footnote 3
See Footnote 3
DN5 42.6 Pigeon River at Hepco Temperature Weekly
D.O. Weekly
Color' Weekly
F1ow2 Daily
DN6 26.0 Pigeon River prior to mixing with Color' Weekly
Big Creek
BC — 26.0 Mouth of Big Creek prior to Color Weekly
mixing with the Pigeon River
DN7 24.7 Pigeon River at Browns Bridge Temperature Weekly
( NC/TN State Line) D.O. Weekly
Color' Weekly
All instream samples shall be grab samples.
Footnotes:
1. Color (See A. (8.) Color Analysis and Compliance Special Condition). All instream samples collected
shall be representative of the Pigeon River and Big Creek, respectively. Both true and apparent color
shall be monitored using the methods specified in A. (8.) Color Analysis and Compliance Special
Condition. Samples shall be collected at stations DN6, BC, and DN7 only when at least one generator
at Progress Energy is in operation and releasing water to the Pigeon River. Samples collected at DNI
shall be collected from the middle or midpoint of the transect of the Pigeon River.
2. Flow monitoring is necessary, as specified above for the True Color calculation.
3. Dissolved Oxygen. The average daily dissolved oxygen concentration measured at River Mile 62.9
(DN1), and 57.7 (DN2), shall not be less than 5.0 mg/L and the instantaneous minimum dissolved
oxygen concentration shall not be less than 4.0 mg/L (See A. (10.) Dissolved Oxygen Special
Condition). If the dissolved oxygen drops below 5.0 mg/L at station 57.7 then monitoring shall be
required at stations 55.5 (DN3) and 53.5 (DN4).
Permit Number: NCO000272
A. (6.) BEST MANAGFMENT PRACTICES (BNIP) SPECIAL, CONDITION
The permittee must implement the BMPs specified below. The primary BMP objective is to prevent
leaks and spills of spent pulping liquors, soap, and turpentine. A secondary objective is to contain,
collect, and recover at the immediate process area, or otherwise control, those leaks, spills, and intentional
diversions of spent pulping liquor, soap, and turpentine that do occur. BMPs must be developed
according to best engineering practices and must be implemented in a manner that takes .into account the
specific circumstances at the mill.
Section A BMP I plementation Requirements
1. The permittee must return spilled or diverted spent pulping liquors, soap, and turpentine to the
process to the maximum extent practicable as determined by the mill, recover such materials outside
the process, or discharge spilled or diverted material at a rate that does not disrupt the receiving
wastewater treatment system.
2. The permittee must maintain a program to identify and repair leaking equipment items. This program
must include: (i) Regular daily visual inspections of process area with equipment items in spent
pulping liquor, soap, and turpentine service; (ii) Immediate repair of leaking equipment items, when
possible. Leaking equipment items that cannot be repaired during normal operations must be
identified, temporary means for mitigating the leaks must be provided, and the leaking equipment
items repaired during the next maintenance outage; (iii) Identification of conditions under which
production will be curtailed or halted to repair leaking equipment items or to prevent pulping liquor,
soap, and turpentine leaks and spills; and (iv) A means for tracking repairs over time to identify those
equipment items where upgrade or replacement may be warranted based on frequency and severity of
leaks, spills, or failures.
3. The permittee must operate continuous, automatic monitoring systems that the mill determines are
necessary to detect and control leaks, spills, and intentional diversions of spent pulping liquor, soap,
and turpentine. These monitoring systems should be integrated with the mill process control system
and may include, e.g., high level monitors and alarms on storage tanks; process area conductivity (or
pff) monitors and alarms; and process area sewer, process wastewater, and wastewater treatment plant
conductivity (or pH) monitors and alarms.
4. The permittee must maintain a program of initial and refresher training of operators, maintenance
personnel, and other technical and supervisory personnel who have responsibility for operating,
maintaining, or supervising the operation and maintenance of equipment items in spent pulping
liquor, soap, and turpentine service. The refresher training must be conducted at least annually and
the training program must be documented.
5. The permittee must prepare a brief report that evaluates each spill of spent pulping liquor, soap, or
turpentine that is not contained at the immediate process area and any intentional diversion of spent
pulping liquor, soap, or turpentine that is not contained at the immediate process area. The report
must describe the equipment items involved, the circumstances leading to the incident, the
effectiveness of the corrective actions taken to contain and recover the spill or intentional diversion,
and plans to develop changes to equipment and operating and maintenance practices as necessary to
prevent recurrence. Discussion of the reports must be included as part of the annual refresher training.
6. The permittee must maintain a program to review any planned modifications to the pulping and
chemical recovery facilities and any construction activities in the pulping and chemical recovery areas
before these activities commence. The purpose of such review is to prevent leaks and spills of spent
pulping liquor, soap, and turpentine during the planned modifications, and to ensure that construction
and supervisory personnel are aware of possible liquor diversions and of the requirement to prevent
leaks and spills of spent pulping liquors, soap, and turpentine during construction.
7. The permittee must install and maintain secondary containment (i.e., containment constructed of
materials impervious to pulping liquors) for spent pulping liquor bulk storage tanks equivalent to the
volume of the largest tank plus sufficient freeboard for precipitation. An annual tank integrity testing
program, if coupled with other containment or diversion structures, may be substituted for secondary
containment for spent pulping liquor bulk storage tanks.
Permit I i mber: NC00001272
S. The permittee must install and maintain secondary containment for turpentine bulk storage tanks.
9. The permittee must install and maintain curbing, diking or other means of isolating soap and
turpentine processing and loading areas from the wastewater treatment facilities.
10. The permittee must conduct wastewater monitoring to detect leaks and spills, to track the
effectiveness of the BMPs, and to detect trends in spent pulping liquor losses. Such monitoring must
be performed in accordance with Section E.
Section B. BMP Plan Requirements
1. The permittee must maintain and implement a BMP Plan. The BMP Plan must be based on a detailed
engineering review as described in this section. The BMP Plan must specify the procedures and the
practices required for the mill to meet the requirements of Section A, the construction the mill
determines is necessary to meet those requirements including a schedule for such construction, and
the monitoring program (including the statistically derived action levels) that will be used to meet the
requirements of Section E. The BMP Plan also must specify the period of time that the mill
determines the action levels established under Section D may be exceeded without triggering the
responses specified in Section E.
2. The permittee must conduct a detailed engineering review of the pulping and chemical recovery
operations --including but not limited to process equipment, storage tanks, pipelines and pumping
systems, loading and unloading facilities, and other appurtenant pulping and chemical recovery
equipment items in spent pulping liquor, soap, and turpentine service --for the purpose of determining
the magnitude and routing of potential leaks, spills, and intentional diversions of spent pulping
liquors, soap, and turpentine during the following periods of operation: (i) Process start-ups and shut
downs; (ii) Maintenance; (iii) Production grade changes; (iv) Storm or other weather events; (v)
Power failures; and (vi) Normal operations.
3. As part of the engineering review, the permittee must determine whether existing spent pulping liquor
containment facilities are of adequate capacity for collection and storage of anticipated intentional
liquor diversions with sufficient contingency for collection and containment of spills. The engineering
review must also consider: (i) The need for continuous, automatic monitoring systems to detect and
control leaks and spills of spent pulping liquor, soap, and turpentine; (ii) The need for process
wastewater diversion facilities to protect end -of -pipe wastewater treatment facilities from adverse
effects of spills and diversions of spent pulping liquors, soap, and turpentine; (iii) The potential for
contamination of storm water from the immediate process areas; and (iv) The extent to which
segregation and/or collection and treatment of contaminated storm water from the immediate process
areas is appropriate.
4. The permittee must amend its BMP Plan whenever there is a change in mill design, construction,
operation, or maintenance that materially affects the potential for leaks or spills of spent pulping
liquor, turpentine, or soap from the immediate process areas.
5. The permittee must complete a review and evaluation of the BMP Plan five years after the first BMP
Plan is prepared and, except as provided in Section BA., once every five years thereafter. As a result
of this review and evaluation, the permittee must amend the BMP Plan within three months of the
review if the mill determines that any new or modified management practices and engineered controls
are necessary to reduce significantly the likelihood of spent pulping liquor, soap, and turpentine leaks,
spills, or intentional diversions from the immediate process areas, including a schedule for
implementation of such practices and controls.
6. The BMP Plan, and any amendments thereto, must be reviewed by the senior technical manager at the
mill and approved and signed by the mill manager. Any person signing the BMP Plan or its
amendments must certify to the Division under penalty of law that the BMP Plan (or its amendments)
has been prepared in accordance with good engineering practices and in accordance with this
regulation. The permittee is not required to obtain approval from the Division of the BMP Plan or any
amendments thereto.
Permit Number: NCO0002 2
Section C. BMP Recordkeepina Requirements
The permittee must maintain on its premises a complete copy of the current BMP Plan and the
records specified in Section C.2 and must make such BMP Plan and records available to the Division
for review upon request.
The permittee must maintain the following records for three _years from the date they are created: (i)
Records tracking the repairs performed in accordance with the repair program described in Section A;
(ii) Records of initial and refresher training conducted in accordance with Section A; (iii) Reports
prepared in accordance with Section A; and (iv) Records of monitoring required by Sections A and E.
Section D. Establishment of Wastewater Treatment System Influent Action Levels
1. The permittee must conduct a monitoring program per Section D.2, for the purpose of defining
wastewater treatment system influent characteristics (or action levels), described in Section D.3, that
will trigger requirements to initiate investigations on BMP effectiveness and to take corrective action.
2. The permittee must employ the following procedures in order to develop the action levels required by
Section D:
Monitoring parameters. The permittee must collect 24-hour composite samples and analyze the
samples for a measure of organic content (e.g., Chemical Oxygen Demand (COD) or Total
Organic Carbon (TOC)). Alternatively, the mill may use a measure related to spent pulping liquor
losses measured continuously and averaged over 24 hours (e.g., specific conductivity or color).
Monitoring locations. The permittee must conduct monitoring at the point influent enters the
wastewater treatment system. For the purposes of this requirement, the permittee may select
alternate monitoring point(s) in order to isolate possible sources of spent pulping liquor, soap, or
turpentine from other possible sources of organic wastewaters that are tributary to the wastewater
treatment facilities (e.g., bleach plants, paper machines and secondary fiber operations).
3. The permittee must maintain an influent action levels monitoring program using the procedures
specified in Section D and must maintain action levels based on the results of that program. A
wastewater treatment influent action level is a statistically determined pollutant loading determined
by a statistical analysis of six months of daily measurements. The action levels must consist of a
lower action level, which if exceeded will trigger the investigation requirements described in Section
E, and an upper action level, which if exceeded will trigger the corrective action requirements
described in Section E.
4. The permittee must complete a second six-month monitoring program using the procedures specified
in Section D and must establish revised action levels based on the results of that program. The initial
action levels shall remain in effect until replaced by revised action levels based on Section D5
requirements.
5. Action levels developed under this Section must be revised using six months of monitoring data after
any change in mill design, construction, operation, or maintenance that materially affects the potential
for leaks or spills of spent pulping liquor, soap, or turpentine from the immediate process areas.
Section E BMP Monitoring Corrective Action and Reporting Requirements
The permittee must conduct daily monitoring of the influent to the wastewater treatment system in
accordance with the procedures described in Section D for the purpose of detecting leaks and spills,
tracking the effectiveness of the BMPs, and detecting trends in spent pulping liquor losses.
Whenever monitoring results exceed the lower action level for the period of time specified in the
BMP Plan, the permittee must conduct an investigation to determine the cause of such exceedance.
Whenever monitoring results exceed the upper action level for the period of time specified in the
BMP Plan, the permittee must complete corrective action to bring the wastewater treatment system
influent mass loading below the lower action level as soon as practicable.
Permit Number: NCO000272
3. Although exceedances of the action levels will not constitute violations of an NPDES permit, failure
to take the actions required by Section E.2 as soon as practicable will be a permit violation.
4. The permittee must report to the Division the results of the daily monitoring conducted pursuant to
Section E.1. Such reports must include a summary of the monitoring results, the number and dates of
exceedances of the applicable action levels, and brief descriptions of any corrective actions taken to
respond to such exceedances. Submission of such reports shall be annually, by March 315C of the
following year.
Section F. BMP Definitions
1. Action Level: A daily pollutant loading that when exceeded triggers investigative or corrective action.
Mills determine action levels by a statistical analysis of six months of daily measurements collected at
the mill. For example, the lower action level may be the 75th percentile of the running seven -clay
averages (that value exceeded by 25 percent of the running seven-day averages) and the upper action
level may be the 90th percentile of the running seven-day averages (that value exceeded by 10
percent of the running seven-day averages).
2. Division: North Carolina DENR, Division of Water Quality, 1617 Mail Service Center, Raleigh,
North Carolina 27699-1617.
3. Equipment Items in Spent Pulping Liquor, Soap, and Turpentine Service: Any process vessel, storage
tank, pumping system, evaporator, heat exchanger, recovery furnace or boiler, pipeline, valve, fitting,
or other device that contains, processes, transports, or comes into contact with spent pulping liquor,
soap, or turpentine. Sometimes referred to as "equipment items."
4. Immediate Process Area: The location at the mill where pulping, screening, knotting, pulp washing,
pulping liquor concentration, pulping liquor processing, and chemical recovery facilities are located,
generally the battery limits of the aforementioned processes. "Immediate process area" includes spent
pulping liquor storage and spill control tanks located at the mill, whether or not they are located in the
immediate process area.
5. Intentional Diversion: The planned removal of spent pulping liquor, soap, or turpentine from
equipment items in spent pulping liquor, soap, or turpentine service by the mill for any purpose
including, but not limited to, maintenance, grade changes, or process shutdowns.
6. Mill: The owner or operator of a direct or indirect discharging pulp, paper, or paperboard
manufacturing facility subject to this section.
7. Senior Technical Manager: The person designated by the mill manager to review the BMP Plan. The
senior technical manager shall be the chief engineer at the mill, the manager of pulping and chemical
recovery operations, or other such responsible person designated by the mill manager who has
knowledge of and responsibility for pulping and chemical recovery operations.
8. Soap: The product of reaction between the alkali in kraft pulping liquor and fatty acid portions of the
wood, which precipitate out when water is evaporated from the spent pulping liquor.
9. Spent Pulping Liquor: For kraft and soda mills "spent pulping liquor" means black liquor that is used,
generated, stored, or processed at any point in the pulping and chemical recovery processes.
10. Turpentine: A mixture of terpenes, principally pinene, obtained by the steam distillation of pine gum
recovered from the condensation of digester relief gases from the cooking of softwoods by the kraft
pulping process. Sometimes referred to as sulfate turpentine.
Permit Number: NCO000272
A. (7.) EFFLUENT GUIDELINE SAMPLING PLAN SPECIAL CONDITION
The bleach plant effluent samples (Outfalls 002 and 003) shall be analyzed for 2,3,7,8-TCDD in
accordance with EPA Method 1613. A single sample, from each of the bleach plant effluents, may be
analyzed to determine compliance with the daily maximum effluent limitation.
The bleach plant effluent samples (Outfall 002 and 003) shall be analyzed for the 12 chlorinated phenolic
compounds in accordance with EPA Method 1653. A single sample, from each of the bleach plant
effluents, may be analyzed to determine compliance with the daily maximum effluent limitation. The
Minimum Levels for each of the 12 chlorinated compounds are the same as the Daily Maximum
concentrations listed on the effluent pages for the respective outfall(s).
The final wastewater treatment plant effluent sample (Outfall 001) shall be analyzed for AOX in
accordance with EPA Method 1650, or subsequent test methods approved by the Division.
The permittee may request future monitoring modifications to the Effluent Guideline requirements,
including 1) use of ECF certification in lieu of monitoring for chloroform in the bleach plant effluents
(Outfall(s) 002 and 003) 2) demonstrating compliance using samples collected less frequently than every
four hours; 3) using automated composite volatile samplers for chloroform sampling; and 4) using
automated composite samplers for chlorophenolic, 2,3,7,8 TCDD and 2,3,7,8 TCDF sampling. Such
future requests will be evaluated in accordance with 15A NCAC 2H.0114.
The flow calculations for internal Outfall(s) 002 and 003 shall not be subject to accuracy requirements
specified under Part H, Section D.3. This exclusion is similar to that provided for pump log flow
calculations.
Chemical data for Effluent Guideline parameters (Outfall(s) 002 and 003 parameters + AOX from Outfall
001) shall be submitted to the Division on a quarterly basis or more frequently (January- March, April -
June, July- September, October -December). Quarterly submissions shall be due 60 days following the
last day of each quarter (Due dates = May 31, August 31, November 30, and February 28). Chemical data
shall be submitted on Division -approved DMR forms, with a separate form provided for each month.
Permit Number: NC00002 72
A. (8.) REQUIREMENTS FOR 4,.'.OL,OE ANALYSIS AND COMPLIANCE SPECIAL CONDITION
The color reduction requirements contained in this special condition have been derived directly
from the mill's efforts to identify possible reduction measures and from the EPA Technology
Review Workgroup (TRW report dated February 25, 2008)
2. The average annual discharge of true color for each calendar year shall not exceed 38,020 pounds
per day. The monthly average effluent true color loading shall not exceed 52,000 pounds per day.
For the purpose of this permit only, "pounds of true color" is calculated by the following
equation:
Effluent Flow (MGD) x Effluent True Color Level (Platinum Cobalt Units) x 8.34.
All samples collected for color analysis and for use in the above calculation shall be measured
and reported using the procedure referenced in 39 FR 430.11 (b) (May 29, 1974) - true and
apparent color or as amended by the EPA.
4. Four years after the permit effective date, the average annual discharge of true color for each
calendar year shall not exceed 32,000-36,000 pounds per day
5. The permittee shall not increase the mill's pulp production capacity during the term of this permit,
unless the permittee can demonstrate that the increased production can be achieved while
reducing color loading. In addition, increasing the mill's pulp production capacity may require
permit revision in accordance with North Carolina's NPDES Permitting rules.
6. The NPDES Permit shall be subject to reopening in order to modify the color requirements based
upon the following:
• Any breakthrough in color removal technologies. Such breakthroughs shall be brought to
the NPDES Committee for consideration, by Blue Ridge Paper and the Division of Water
Quality, as soon as they are discovered.
• An acceptable statistical analysis of effluent color discharge data demonstrating
significantly better color removal performance than that currently prescribed in the
permit, except as noted herein.
• Successful application of end -of -pipe color reduction technology or in -mill color
minimization effort that results in significant and measurable reduced mass color
discharge.
The transfer of this NPDES permit will not proceed until any successor -in -interest to the current
permittee has agreed to accept the provisions of this permit.
The facility will provide annual progress reports to the Division on the color reduction efforts.
To minimize color discharges during periods of lowest river flow and higher recreational use in
the river, no major maintenance outages will be scheduled during the months of June, July and
August.
10. Based on the EPA TRW recommendations, the permittee shall evaluate the technologies
identified below and develop an implementation plan that would either utilize these technologies
Permit. Number: NC..O0002 i 2
when technically, operationally, or economically feasible, or identify other options that will result
in similar increments of color reduction. The TRW may review and comment on the justification
for any item among the following recommendations found by Blue Ridge Paper to be technically,
operationally, or economically infeasible:
A. The following suite of items will be implemented by the permittee, upon further expedited
evaluation if necessary to refine detailed design and operating parameters, during this permit
term:
e further improvements in leak and spill prevention and control (BMP's) covering all
process lines, including probable color -generating sources (e.g., sulfide containing)
among white and green liquors in the recovery cycle
o process optimization (enhanced extraction stages, reduced bleaching chemical use, etc.);
and
G addition of second stage oxygen delignification on the softwood/pine fiber line
The time necessary for Blue Ridge Paper to implement these items or alternatives in logical
sequence should realistically reflect the Mill's ability to design, fund, and install or implement
them at the earliest possible date. For example, an updated and detailed evaluation of the addition
of second stage oxygen delignification on the softwood fiber line should identify necessary
adjustments to upstream pulp digestion (e.g., kappa number targets), bleaching (e.g., bleaching
chemical usage rates, kappa factors) and downstream brightness/strength and other relevant
process control and product quality parameters, designing and costing, and refining color
reduction projections.
B. The following items will be evaluated and implemented as appropriate during this permit
term:
increasing filtrate recycle and use of the existing BFR process for the hardwood fiber line
reducing black liquor carryover by further evaluating in detail and adjusting operating
conditions in the direct contact evaporators (DCEs)
reducing impact of Chloride Removal Process (CRP) purge on treated effluent color by
gathering data sets over as long a period as possible, preferably at full scale, with and
without the CRP purge to better understand the impact on treatability of this source of
color. If it is determined that CRP color is found not to be removed in the treatment
system, further study should assess:
o securing whatever additional reductions are possible based on any
demonstrated technology that works and can be economically applied to this
waste stream, either within the mill and sewer system, or chlorine dioxide
pretreatment to reduce color in the CRP purge stream prior to introduction to
the treatment system
o avoiding release of the CRP purge during periods of low flow in the receiving
stream
better understanding and controlling, if possible, the physical and chemical mechanisms
underlying "sewer generated color". This will require a sustained effort going forward
beyond this permit term given that process changes and BMP improvements to be made
will more than likely further change the chemistry and mechanisms underlying "sewer
generated color".
improving color removal by the Mill's wastewater treatment plant via:
o better equalizing and further optimizing treatment by using polymers and other
chemicals to pretreat highly -colored segregated wastewaters including streams
that are diverted to the extra primary clarifier, or by other operational and/or
treatment means not yet identified
Permit Number: NCO0002 72
o investigating use of polymers or other chemicals upstream of the secondary
clarifiers, especially during periods of high influent color and/or low river flow
IL The facility shall submit the color reduction implementation plan within the first year of permit
issuance. The permit will be reopened and modified to include interim requirements and dates for
their achievement based on the submitted implementation plan.
12. The facility shall submit a low flow contingency plan for color control within the first year of
permit issuance.
A. (9.) DIOXIN MONITORING SPECIAL CONDITION
The permittee shall perform the analyses for dioxin and dibenzefuran as outlined below:
sama�in�Poiat,; >x
`�,�-Mona�ora�ags���
,
Influent to Wastewater
Annual
Composite
Treatment Plant'
Effluent'
Annual
Composite
Sludge
Annual
Composite
Landfill Leachate
Annual
Composite
Footnotes:
1. The samples shall be analyzed for 2,3,7,8-TCDD and 2,3,7,8 TCDF in accordance with EPA Method
1613. A single sample may be analyzed. Alternatively, the sample volumes may be collected to
enable the sample to be split (duplicate analysis). The Minimum Level in the effluent for 2,3,7,8-
TCDD and 2,3,7,8 TCDF by EPA Method 1613 is 10 pg/l.
2. The effluent samples shall be analyzed for the full range of dioxin and furan isomers as identified in
the list below and shall be in accordance with EPA Method 1613. A single sample may be analyzed.
Alternatively, the sample volumes may be collected to enable the sample to be split (duplicate
analysis). The minimum level using these methods for the purpose of compliance evaluation is
considered to be 10 picograms per liter
DIOXIN
DIBENZOFURAN
Isomer
Isomer
2,3,7,8
TCDD
2,3,7,8
TCDF
1,2,3,7,8
PeCDD
1,2,3,7,8
PeCDF
2,3,4,7,8
PeCDF
1,2,3,4,7,8
HxCDD
1,2,3,4,7,8
HxCDF
1;2,3,7,8,9
HxCDD
1,2,3,7,8,9
HxCDF
1,2,3,6,7,8
HxCDF
1,2,3,6,7,8
HxCDD
2,3,4,6,7,8
HxCDF
1,2,3,4,6,7,8
HpCDD
1,2,3,4,6,7,8
HpCDF
1,2,3,4,7,8,9 HpCDF
If dioxins or dibenzofurans are detected in the effluent above the minimum level, the permittee shall
initiate Quarterly monitoring of sludge, landfill leachate, and effluent.
Permit Number: NCO000272
Additional Requirements
Annual dioxin fish tissue analysis shall be performed during the 1$`, P, and 5`h calendar year of this
permit term in accordance with the Division of Water Quality approved monitoring plan. The monitoring
plan is an enforceable part of this permit. All dioxin data collected as part of this monitoring requirement
will be reported as required in the plan, no later than 180 days after sampling. The tissue monitoring will
be performed in Waterville Lake, although the facility may substitute one lake event with a sampling in
the Pigeon River below the outfall.
A. (10.) DISSOLVED OXYGEN SPECIAL CONDITION
The pernuttee shall maintain an average daily dissolved oxygen concentration of not less than 5.0 mg/L
with a minimum instantaneous value of not less than 4.0 mg/L at River Miles 62.9 (DN1) and 57.7
(DN2). The permittee shall operate oxygen injection facilities at the outfall structure, at 0.9 miles
downstream of the discharge, and at 2.1 miles downstream of the discharge, as necessary, to comply with
this requirement. These facilities shall be operated in a manner which will maintain the water quality
standard for dissolved oxygen in the Pigeon River downstream of the discharge. Blue Ridge Paper shall
report the date and duration of oxygen injection use as a supplement to the monthly Discharge Monitoring
Report (DMR) forms. If the dissolved oxygen drops below 5.0 mg/L at station DN2 then monitoring shall
be required at stations DN3 and DN4.
A. (11.) TOWN OF CANTON INFLOW AND INFILTRATION SPECIAL CONDITION
The permittee shall make continued efforts to promote reduction of inflow/infiltration to the Town of
Canton's wastewater collection system.
A. (12.) TEMPERATURE VARIANCE REVIEW SPECIAL CONDITION
Blue Ridge Paper shall complete an analysis of temperature, including thermal modeling and shall submit
a balanced and indigenous species study, no later than 180 days prior to the permit expiration date. As
part of this analysis, Blue Ridge Paper shall submit a complete temperature variance report documenting
the need for a continued temperature variance. The temperature delta of 8.5°C can be adjusted based on
the results of the BIP thermal modeling.
The study shall be performed in accordance with the Division of Water Quality approved plan. The
temperature analysis and the balanced and indigenous study plan shall conform to the specifications
outlined in 40 CFR 125 Subpart H and the EPA's Draft 316a Guidance Manual, dated 1977. The EPA
shall be provided an opportunity to review the plan prior to the commencement of the study.