HomeMy WebLinkAboutNC0038377_Final Permit_20071214i>IVAT�C�
Michael F. Easley, Governor
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State of North Carolina
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William G Ross, Jr., Secretary
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Department of Environment and Natural Resources
Coleen H Sullins, Director
Division of Water Quality
December 14, 2007
Mr Larry E. Hatcher, Plant Manager
Progress Energy Carolinas, Inc.
Mayo Electric Generating Plant
10660 Boston Road
Roxboro, NC 27574
Subject. Issuance of NPDES Permit NCO038377
Mayo Steam Plant
Person County
Dear Mr. Hatcher.
Division personnel have reviewed and approved your application for modification of the subject
permit Accordingly, we are forwarding the attached NPDES discharge permit This permit is issued pursuant
to the requirements of North Carolina General Statute 143-2151 and the Memorandum of Agreement between
North Carolina and the U S Environmental Protection Agency dated October 15, 2007 (or as subsequently
amended)
This final permit contains the following significant changes from the draft you were sent on June 6, 2007:
➢ Limits and monitoring requirements for antimony, boron, cobalt, and molybdenum have been added
based on the unforeseeable potential these parameters may have to cause an exceedance of water
quality criteria
➢ The minimum flow limit has been removed based on your company's decision to accept additional
metals monitoring.
➢ The beryllium limit has been updated to reflect the current aquatic life standard of 6.5 jig/ L.
If any parts, measurement frequencies or sampling requirements contained in this permit modification
are unacceptable to you, you have the right to an adjudicatory hearing upon written request within thirty (30)
days following receipt of this Ietter 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 demand is made, this decision shall be
final and binding
Please note that this permit is not transferable except after notice to the Division. 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 or permits
required by the Division of Land Resources, the Coastal Area Management Act or any other Federal or Local
governmental permit that may be required. If you have any questions concerning this permit, please contact
Toya Fields at telephone number (919) 733-5083, extension 551
Sincerely,
S7-
�en HSullins
cc Central Files
Raleigh Regional Office/Surface Water Protection
NPDES Unit �
Aquatic Toxicology Unit
Marshall Hyatt / EPA
1617 Mad Service Center, Raleigh, North Carolina 27699-1617 Telephone (919) 733-7015 FAX (919) 733-0719 OnrthCarolina
512 N Salisbury Street, Raleigh, North Carolina 27604 On the Internet at http Hh2o enr state nc us/ Naturally Equal Opportunity/Affirmative Action Employer
It
Permit NCO038377
STATE OF NORTH CAROLINA
DEPARTMENT OF ENVIRONMENT AND NATURAL RESOURCES
DIVISION OF WATER QUALITY
PFRMTT
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,
Carolina Power and Light d/b/a/ Progress Energy Carolinas, Inc.
is hereby authorized to discharge wastewater from a facility located at the
Mayo Steam Electric Generating Plant
off of US Highway 501
northeast of Roxboro
Person County
to receiving waters designated as the Mayo Reservoir in the Roanoke River Basin in
accordance with effluent limitations, monitoring requirements, and other conditions set forth
in Parts I, II, III, and IV hereof.
The permit shall become effective January 1, 2008.
This permit and the authorization to discharge shall expire at midnight on March 31, 2012.
Signed this day December 14, 2007.
.een H. Sullins, Director
,ision of Water Quality
Authority of the Environmental Management Commission
Permit NC00383177
SUPPLEMENT TO PERMIT COVER SHEET
All previous NPDES Permits issued to this facility, whether for operation or discharge are hereby
revoked. As of this permit issuance, any previously issued permit bearing this number is no longer
effective. Therefore, the exclusive authonty to operate and discharge from this facility arises under the
permit conditions, requirements, terms, and provisions included herein.
Carolina Power and Light d/b/a/ Progress Energy Carolinas, Inc.
is hereby authorized to:
1. Continue to operate the following systems located at Mayo Steam Electric Generating
Plant, off of US Highway 501, northeast of Roxboro, Person County:
• Cooling Tower System (Outfall 001). Less than once per year the cooling towers
and circulating water system are drained by gravity and discharged directly to
Mayo Reservoir.
Ash Pond Treatment System (Outfall 002). Outfall 002 discharges directly to
Mayo Reservoir. The ash pond receives ash transport water, coal pile runoff,
stormwater runoff, cooling tower blowdown, and various low volume wastes such
as boiler blowdown, oily waste treatment, wastes/backwash from the water
treatment processes, plant area wash down water, equipment heat exchanger
water, and treated domestic wastewater.
• Internal Outfall 008. Cooling tower blowdown is directly discharged to the ash
pond. Cooling tower blowdown is usually mixed with ash sluice water prior to
discharge to the ash pond. Cooling tower blowdown is indirectly discharged to
Mayo Reservoir via the ash pond treatment system (Outfall 002).
• Internal Outfall 009. Discharge from the FGD blowdown treatment system.
• Stormwater Discharge System The facility is permitted to discharge stormwater
to Mayo Reservoir through the following outfalls:
• Outfall 004 - Drainage from the outside storage area.
• Outfall 005 - Drainage from the industrial area and the oil/bottled
gas storage area.
• Outfalls 006a, 006b, 006c, 006d, 006e - Drainage from the cooling
tower(s) chemical feed building structure and the cooling tower area.
2. Discharge from said treatment works and/or outfalls at the locations specked on the
attached maps into Mayo Reservoir, which is classified as WS -V waters in the Roanoke
River Basin.
Permit NCO038377
A. (1) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS [001]
During the period beginning on the effective date of the permit and lasting until expiration, the
Permittee is authorized to discharge from Outfall 001 (Cooling Tower System) Monitoring is
required only during discharge events to the Mayo reservoir Such discharges shall be limited and
monitored by the Permittee as specified below
PARAMETER
LIMITS
MONITORING REQUIREMENTS
Monthly Daily
Average Maximum
Measurement Sample Type Sample
Frequency Locationl
Flow
Daily
Pump Logs or similar
readings
Effluent
Free Available Chlorine2
200 lig/L 500 Ng/L
Weekly
Grab
Effluent
Time of Chlorine Addition2
2 hours
Weekly
Logs
Total Chromium3
0 2 mg/L 0 2 mg/L
2 / Month
Grab
Effluent
Total Zinc3
10 mg/L 10 mg/L
2 / Month
Grab
Effluent
Priority Pollutants 3
No Detectable Amount
Annual
Grab
Effluent
pH
> 6 0 and < 9 0 standard units
Weekly
Grab
Effluent
Notes:
1 Samples taken in compliance with the monitoring requirements listed above shall consist of cooling
tower effluent prior to its discharge to Mayo Reservoir
2. Monitoring is required only if chlorine -based compounds is added to the system Neither free
available chlorine nor total residual chlorine may be discharged from any single generating unit for
more than two hours per day, unless the Permittee demonstrates to the Division of Water Quality
that discharge for more than two hours is required for macroinvertebrate control The 500 µg/l
limitation is an instantaneous maximum and is to be measured during the chlorine release period
The 200 µg/l limitation is an average during the chlorine release period Simultaneous multi -unit
chlorination is permitted
3 Limitations and monitoring requirements for the 126 Priority Pollutants (per 40 CFR Part 423,
Appendix A, exclusive of zinc and chromium) apply only if these substances are added by the
permittee for cooling tower maintenance Compliance with the limitations for the 126 priority
pollutants in 40 CFR 423 13 (d) (1) may be determined by engineering calculations which
demonstrate that the regulated pollutants are not detectable in the final discharge by the analytical
methods in 40 CFR Part 136 All primary industries are required to submit a, priority pollutant
analysis in accordance with 40 CFR Part 122 with their application for permit renewal.
The above listed effluent limitations shall be sampled prior to draining the cooling tower(s), at a
location prior to discharge to Mayo Reservoir
There shall be no discharge of polychlorinated biphenyl compounds such as those commonly used for
transformer fluid
Permit NCO0383 77
A. (2) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS [008]
During the period beginning on the effective date of the permit and lasting until expiration, the
Permittee is authorized to discharge from Outfall 008 (internal outfall, Cooling Tower System)
Such discharges shall be limited and monitored by the Permittee as specified below:
PARAMETER
LIMITS
MONITORING REQUIREMENTS
Monthly Daily
Average Maximum
Measurement Sample Sample
Frequency Type Locationl
Flow
Daily
Pump Logs or
similar readings
Effluent
Free Available Chlorine2
200 lug/L 500 ug/L
Weekly
Grab
Effluent
Time of Chlorine Addition2
2 hours
Weekly
Logs
Total Chromium3
0 2 mg/L 0 2 mg/L
2 / Month
Grab
Effluent
Total Zinc3
10 mg/L 10 mg/L
2 / Month
Grab
Effluent
Priority Pollutants 3
No Detectable Amount
Annual
Grab
Effluent
pH
> 6 0 and < 9 0 standard units
Weekly
Grab
Effluent
Notes:
1 Samples taken in compliance with the monitoring requirements listed above shall consist of
cooling tower blowdown after mixing with the fly and bottom ash, but prior to discharging into
the ash pond
2 Monitoring is required only if chlcrine-based compound is added to the system Neither free
available chlorine nor total residual chlorine may be discharged from any single generating unit
for more than two hours per day, unless the Permittee demonstrates to the Division of Water
Quality that discharge for more than two hours is required for macroinvertebrate control The
500 pg/l limitation is an instantaneous maximum and is to be measured during the chlorine
release period The 200 µg/l limitation is an average during the chlorine release period
Simultaneous multi -unit chlorination is permitted
3 Limitations and monitoring requirements for the 126 Priority Pollutants (per 40 CFR Part 423,
Appendix A, exclusive of zinc and chromium) apply only if these substances are added by the
permittee for cooling tower maintenance Compliance with the limitations for the 126 priority
pollutants in 40 CFR 423 13 (d) (1) may be determined by engineering calculations which
demonstrate that the regulated F-ollutants are not detectable in the final discharge by the
analytical methods in 40 CFR Part 136 All primary industries are required to submit a priority
pollutant analysis in accordance with 40 CFR Part 122 with their application for permit
renewal.
This outfall is not authorized to discharge directly to the Mayo Reservoir
Permit NCO038377
A. (3) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS
[002 without FGD wastewater]
During the period beginning on the effective date of the permit and lasting until expiration, the
Permittee is authorized to discharge from Outfall 002 (Ash Pond Treatment System). Such
discharges shall be limited and monitored by the Permittee as specified below.
PARAMETER
LIMITS
MONITORING REQUIREMENTS
Monthly Daily
Average Maximum
Measurement Sample Sample
Frequency Type Locationl
Flow
Weekly
Pump Logs or
similar readings
Effluent
Oil and Grease
15 0 m /L 20 0 m /L
Monthly
Grab
Effluent
Total Suspended Solids
30 0 m /L 100 0 m /L
Monthly
Grab
Effluent
Total Selenium2
3 8 lbs/day
2 / Month
Grab
Effluent
Acute Toxicit 3
Quarterly
Grab
Effluent
Total Arsenic4
Quarterly
Grab
Effluent
'Total Copper
Quarterly
Grab
Effluent
Total Iron
Quarterly
Grab
Effluent
pH
> 6 0 and < 9 0 standard units
2 / Month
Grab
Effluent
Notes:
1. Samples taken in compliance with the monitoring requirements listed above shall be taken prior to
mincing with other waste streams.
2. See A. (8).
3. Acute Toxicity (Fathead Minnow 24hr) No significant mortality at 90%, February, May, August, and
November, See A. (7).
4. See A. (13).
After the FGD treatment system is used to treat FGD wastewater, the effluent limits in Conditions A
(4) and A (5) apply
There shall be no discharge of floating solids or visible foam in other than trace amounts outside an
area five(5) meters from the discharge pipe No chemical metal cleaning waste may be discharged to
the ash pond There shall be no discharge of polychlorinated biphenyl compounds such as those
commonly used for transformer fluid
Permit NCO038377
A. (4) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS
[002 with FGD wastewater]
During the period beginning upon commencement of the FGD treatment system to treat FGD
wastewater and lasting until expiration, the Permittee is authorized to discharge from Outfall 002
(Ash Pond Treatment System) Such discharges shall be limited and monitored by the Permittee as
specified below
PARAMETER
LIMITS
MONITORING REQUIREMENTS
Monthly
Average I
weekly
Average
Daily
Maximum
Measurement
Frequency
Sample Type ,
r
, Sample
Location'
Flow
Weekly
Pump Logs
or similar readings
Effluent
Oil and Grease
15 0 m /L
20 0 m /L
Monthly
Grab
Effluent
Total Suspended Solids
30 0 m /L
100 0 m /L
Monthly
Grab
Effluent
Total Selenium
3 8 lbs/day
Weekly
Grab
Effluent
Acute Toxicit 3
Quarterly
Grab
Effluent
Total Mercury2,4
0 012 /L
Weekly
Grab
Effluent
Total Arsenics
Weekly
Grab
Effluent
Total Ber Ilium2
6 5 /L
Weekly
Grab
Effluent
Total Cadmium2
2 0 /L
Weekly
Grab
Effluent
Total Chlondes2
672 0 m iL
860 0 m /L
Weekly
Grab
Effluent, MZ6
Total Chromium2
50 0 /L
Weekly
Grab
Effluent
Total Copper
Weekly
Grab
Effluent
Total Fluoride2
18 m /L
Weekly
Grab
Effluent
Total Lead2
25 0 p lL
33 8 /L
Weekly
Grab
Effluent
Total Man anese2
200 0 H /L
Weekly
Grab
Effluent
Total Nickel
Weekly
Grab
Effluent
Total Silver
Weekly
Grab
Effluent
Total Zinc
Weekly
Grab
Effluent
Total Banum2
10 mg/L
Weekly
Grab
Effluent
Total Thallium2
0 35 pg/L
Weekly
Grab
Effluent
Total Vanadium2
24 0 H /L
Weekly
Grab
Effluent
Total Antimon 2
5 6 p9iL
Weekly
Grab
Effluent
Total Boron2
750 0 /L
Weekly
Grab
Effluent
Total Cobalt'
65 0 c/L
Weekly
Grab
Effluent
Total Mol bdenum2
170 N L
Weekly
Grab
Effluent
'Total Iron
Quarterly
Grab
Effluent
H
> 6 0 and < 9 0 standard units
2 / Month
Grab
Effluent
Notes:
1 Samples taken in compliance with the monitoring requirements listed above shall be taken prior to
mixing with other waste streams
2 The limit and monitoring frequency becomes applicable 24 months after the commencement of the
FGD system Twice monthly monitoring is required upon initial commencement of the FGD
system
3. Acute Toxicity (Fathead Minnow 24 -hr) No significant -mortality at 90%; February, May, August,
and November [see A. (7)]
4 The mercury limit will take effect one year after commencement of the FGD system to treat FGD
wastewater
5 See A. (13).
6 Instream sampling for chlorides is required at the edge of the mixing zone, 200 meters linear
distance from the discharge point Monitoring shall begin upon commencement of the FGD system
and shall last for 5 years
After the FGD treatment system is used to treat FGD wastewater, the effluent limits in Conditions A
(4) and A (5) apply
Progress Energy shall inform this office as well as the Raleigh Regional Office, via phone call and via
letter, as to when the FGD treatment system will be used to treat FGD wastewater.
Permit NCO038377
A. (4) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS
[002 with FGD wastewater] Continued
There shall be no discharge of floating solids or visible foam in other than trace amounts outside an
area five (5) meters from the discharge pipe No chemical metal cleaning waste may be discharged to
the ash pond There shall be no discharge of polychlorinated biphenyl compounds such as those
commonly used for transformer fluid
A. (5) EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS [009]
During the period beginning upon commencement of the FGD treatment system to treat FGD wastewater
and lasting until expiration, the Permittee is authorized to discharge from Internal Outfall 009
(treated FGD wet scrubber wastewater) Such discharges shall be limited and monitored by the
Permittee as specified below
PARAMETER
LIMITS
Monthly Daily
Average Maximum
MONITORING REQUIREMENTS
Measurement Sample Sample
Frequency Type Locationl
Flow
Monthly
Instantaneous
E
Total Suspended Solids
Weekly
Grab
E
Total Mercury
Weekly
Grab
E
Total Selenium
Weekly
Grab
E
Total Arsenic
Weekly
Grab
E
Total Beryllium
Weekly
Grab
E
Total Cadmium
Weekly
Grab
E
Total Chlorides
Weekly
Grab
E
Total Chromium
Weekly
Grab
E
Total Copper
Weekly
Grab
E
Total Fluoride
Weekly
Grab
E
Total Lead
Weekly
Grab
E
Total Manganese
Weekly
Grab
E
Total Nickel
Weekly
Grab
E
Total Silver
Weekly
Grab
E
Total Barium
Weekly
Grab
E
Total Thallium
Weekly
Grab
E
Total Vanadium
Weekly
Grab
E
Total Antimony
Weekly
Grab
E
Total Boron
Weekly
Grab
E
Total Cobalt
Weekly
Grab
E
Total Molybdenum
Weekly
Grab
E
Total Zinc
Weekly
Grab
E
Notes:
1 E — Effluent from the FGD treatment system prior to discharge to the Ash Pond
Permit NC0038377
A. (6) STORMWATER MONITORING REQUIREMENTS/ Qualitative Monitoring
Qualitative monitoring requires a qualitative inspection of each stormwater outfall, regardless of
representative outfall status, for the purpose of evaluating the effectiveness of the Stormwater
Pollution Prevention Plan and assessing new sources of stormwater pollution. No analytical tests are
required. Qualitative monitoring of stormwater outfalls does not need to be performed during a
representative storm event
Stormwater Discharge Characteristics
Measurement
Frequencyi
SampleLocation
U f
Color
Semi -Annual
Stormwater Discharge Outfall
Odor
Semi -Annual
Stormwater Discharge Outfall
Clarity
Semi -Annual
Stormwater Discharge Outfall
Floating Solids
Semi -Annual
Stormwater Discharge Outfall
Suspended Solids
Semi -Annual
Stormwater Discharge Outfall
Foam
Semi -Annual
Stormwater Discharge Outfall
Oil Sheen
Semi -Annual
Stormwater Discharge Outfall
Other obvious indicators of stormwater pollution
Semi -Annual
Stormwater Dischar a Outfall
Notes:
1. Measurement Frequency Qualitative monitoring will be performed twice per year, once in the
spring (April - June) and once in the fall (September - November)
A. (7) ACUTE TOXICITY PASS/FAIL PERMIT LIMIT (Quarterly)
Outfall 002 (Ash Pond)
The permittee shall conduct acute toxicity tests on a quarterlu basis using protocols defined in the
North Carolina Procedure Document entitled "Pass/Fail Methodology For Determining Acute Toxicity
In A Single Effluent Concentration" (Revised -July, 1992 or subsequent versions). The monitoring shall
be performed as a Fathead Minnow (Prmephales promelas) 24 hour static test The effluent
concentration at which there may be at no time significant acute mortality is 90% (defined as
treatment two in the procedure document) Effluent samples for self-monitoring purposes must be
obtained during representative effluent discharge below all waste treatment The tests will be
performed during the months of February, May, August and November
All toxicity testing results required as part of this permit condition will be entered on the Effluent
Discharge Monitoring Form (MR -1) for t_ie month in which it was performed, using the parameter code
TGE6C Additionally, DWQ Form AT -2 (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 and accurate and include all supporting chemical/ physical measurements
performed in association with the toxicity tests, as well as all dose/response data. 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 month/year 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
Permit NCO038377
Should any single quarterly monitoring indicate a failure to meet specified limits, then monthly
monitoring will begin immediately until such time that a single test is passed. Upon passing, this
monthly test requirement will revert to quarterly in the months specified above.
Should the permittee fail to monitor during a month in which toxicity monitoring is required, then
monthly monitoring will begin immediately until such time that a single test is passed. Upon passing,
this monthly test requirement will revert to quarterly in the months specified above.
Should any test data from either these monitoring requirements 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
NOTE: Failure to achieve test conditions as specified in the cited document, such as minimum control
organism survival 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.
A. (8) SELENIUM STUDY
The Permittee shall conduct biological and physical/ chemical studies on selenium and its effect in the
reservoir. The results shall be submitted each year by May 1 for the prior calendar year. The plan of
study shall be submitted to the Director of the Division of Water Quality for approval.
A. (9) CRUTCHFIELD BRANCH
There shall be no direct discharge of wastewater from the ash pond to Crutchfield Branch. There shall
be no violation of water quality standards in Crutchfield Branch due to any indirect discharge from the
ash pond. The Permittee shall monitor the waters of Crutchfield Branch, 100 yards downstream of the
dike, once per year by grab sample for the following- arsenic, copper, and selenium.
A. (10) DOMESTIC WASTEWATER TREATMENT PLANT
The domestic wastewater treatment plant shall be properly operated and maintained to ensure
treatment of domestic wastewater to secondary levels.
A. (11) STORMWATER POLLUTION PREVENTION PLAN
The permittee shall develop a Stormwater Pollution Prevention Plan, herein after referred to as the
Plan. The Plan shall be considered public information in accordance with Part II, Section E. 10. of this
permit. The Plan shall include, at a minimum, the following items:
a. Site Plan: The site plan shall provide a description of the physical facility and the potential
pollutant sources which may be expected to contribute to contamination of regulated
stormwater discharges. The site plan shall contain the following:
(1) A general location map (USGS quadrangle map, or appropriately drafted equivalent
map), showing the facility's location in relation to transportation routes and surface
waters, and the name of the receiving water(s) to which the stormwater outfall(s)
discharges. If the discharge is to a municipal separate storm sewer system, the name of
the municipality and the ultimate receiving waters, and accurate latitude and longitude
of the point(s) of discharge must be shown.
Permit NCO038377
(2) A narrative description of storage practices, loading and unloading activities, outdoor
process areas, dust or particulate generating or control processes, and waste disposal
practices
(3) A site map (or series of maps) drawn to scale with the distance legend indicating
location of industrial activities (including storage of materials, disposal areas, process
areas, and loading and unloading areas), drainage structures, drainage areas for each
outfall and activities occurring in the drainage area, building locations and impervious
surfaces, the percentage of each drainage area that is impervious. For each outfall, a
narrative description of the potential pollutants which could be expected to be present
in the regulated stormwater discharge.
(4) A list of significant spills or leaks of pollutants that have occurred at the facility during
the 3 previous years and any corrective actions taken to mitigate spill impacts.
(5) Certification that the stormwater outfalls have been evaluated for the presence of non-
stormwater discharges. The certification statement will be signed in accordance with
the requirements found in Part II, Section B 11.
b. Stormwater Management Plan- The stormwater management plan shall contain a narrative
description of the materials management practices employed which control or minimize the
exposure of significant materials to stormwater, including structural and non-structural
measures. The stormwater management plan, at a minimum, shall incorporate the following:
(1) A study addressing the technical and economic feasibility of changing the methods of
operations and/or storage practices to eliminate or reduce exposure of materials and
processes to stormwater. Wherever practicable the permittee should consider covering
storage areas, material handling operations, manufacturing or fueling operations to
prevent materials exposure to stormwater. In areas where elimination of exposure is
not practicable, the stormwater management plan shall document the feasibility of
diverting the stormwater runoff away from areas of potential contamination.
(2) A schedule to provide secondary containment for bulk storage of liquid materials,
storage of Section 313 of Title III of the Superfund Amendments and Reauthorization
Act (SARA) water priority chemicals, or storage of hazardous materials to prevent leaks
and spills from contaminating stormwater runoff. If the secondary containment devices
are connected directly to stormwater conveyance systems, the connection shall be
controlled by manually activated valves or other similar devices [which shall be secured
with a locking mechanism] and any stormwater that accumulates in the containment
area shall be at a minimum visually observed prior to release of the accumulated
stormwater. Accumulated stormwater shall be released if found to be uncontaminated.
Records documenting the individual making the observation, the description of the
accumulated stormwater and the date and time of the release shall be kept for a period
of five years.
(3) A narrative description of Best Management Practices (BMPs) to be considered such as,
but not limited to, oil and grease separation, debris control, vegetative filter strips,
infiltration and stormwater detention or retention, where necessary. The need for
structural BMPs shall be based on the assessment of potential of sources contributing
significant quantities of pollutants to stormwater discharges and data collected through
monitoring of stormwater discharges.
(4) Inspection schedules of stormwater conveyances and controls and measures to be taken
to limit or prevent erosion associated with the stormwater systems.
C. Spill Prevention and Response Plan: The Spill Prevention and Response Plan shall incorporate
a risk assessment of potential pollutant sources based on a materials inventory of the facility.
Facility personnel (or team) responsible for implementing the plan shall be identified in the
plan A responsible person shall be on-site at all times during facility operations that have the
Permit NC0038377
potential to contaminate stormwater runoff through spills or exposure of materials associated,
with the facility operations.
d. Preventative Maintenance and Good Housekeeping Program- A preventative maintenance
program shall be developed. The program shall document schedules of inspections and
maintenance activities of stormwater control systems, plant equipment and systems.
Inspection of material handling areas and regular cleaning schedules of these areas shall be
incorporated into the program.
e. Training schedules shall be developed and training provided at a minimum on an annual basis
on proper spill response and cleanup procedures and preventative maintenance activities for all
personnel involved in any of the facility's operations that have the potential to contaminate
stormwater runoff. Facility personnel (or team) responsible for implementing the training shall
be identified in the plan.
L The Stormwater Pollution Prevention Plan shall identify a specific position(s) responsible for the
overall coordination, development, implementation, and revision to the Plan. Responsibilities
for all components of the Plan shall be documented and position(s) assignments provided.
g. Plan Amendment: The permittee shall amend the Plan whenever there is a change in design,
construction, operation, or maintenance which has a significant effect on the potential for the
discharge of pollutants via a point source to surface waters. The Stormwater Pollution
Prevention Plan shall be reviewed and updated on an annual basis.
The director may notify the permittee when the Plan does not meet one or more of the
minimum requirements of the permit. Within 30 days of such notice, the permittee shall
submit a time schedule to the Director for modifying the Plan to meet minimum requirements.
The permittee shall provide certification in writing (in accordance with Part III, Standard
Conditions, Section B.11.) to the Director that the changes have been made.
h. Facility Inspections: Inspections of the facility and all stormwater systems shall occur at a
minimum on a semiannual schedule, once in the fall (September - November) and once during
the spring (April - June). The inspection and any subsequent maintenance activities performed
shall be documented, recording date and time of inspection, individual(s) making the inspection
and a narrative description of the facility's stormwater control systems, plant equipment and
systems. Records of these inspections shall be incorporated into the Stormwater Pollution
Prevention Plan.
Visual monitoring as required in A(4) Stormwater Monitoring Requirements/ Qualitative
Monitoring shall be performed in addition to facility inspections.
L Implementation: Implementation of the Plan shall include documentation of all monitoring,
measurements, inspections, maintenance activities and training provided to employees,
including the log of the sampling data. Activities taken to implement BMPs associated with the
industrial activities, including vehicle maintenance activities, must also be recorded. All
required documentation shall be kept on-site for a period of five years and made available to
the Director or his authorized representative immediately upon request.
A. (12) STORMWATER MINIMUM MONITORING AND REPORTING REQUIREMENTS
Minimum monitoring and reporting requirements are as follows unless otherwise approved in writing
by the Director of the Division of Water Quality:
- a. If a facility has multiple discharge locations with substantially identical stormwater discharges
that are required to be sampled, the permittee may petition the Director for representative
outfall status. If it is established that the stormwater discharges are substantially identical
and the permittee is granted representative outfall status, then sampling requirements may be
performed at a reduced number of outfalls.
Permit NCO038377
b. Visual monitoring for color, odor, solids, foam, outfall staining, visible sheens and dry weather
flow shall be performed at all stormwater discharge outfall locations. All visual monitoring
shall be documented and records maintained with the Stormwater Pollution Prevention Plan.
The initial visual monitoring event shall be performed during the Spring of 2006.
C. For purposes of the stormwater sampling required in this permit, all samples shall be collected
from a discharge resulting from a representative storm event (See definitions in Part II, Section
A). Failure to monitor storm events in accordance with the specified frequency shall constitute
a violation of this permit. If the stormwater runoff is controlled by a detention pond, the
following sampling requirements shall apply:
(1) If the detention pond detains the runoff generated by one inch of rainfall for 24 hours,
visual observations for color, foam, outfall staining, visible sheens and dry weather flow
are required, but analytical sampling shall not be required
(2) If the detention pond discharges only in response to a storm event exceeding a 25 -year,
24-hour storm, the pond shall be considered a non -discharging stormwater control
system and not subject to NPDES requirements, unless the discharge causes a violation
of water quality standards.
d. Samples analyzed in accordance with the terms of this permit shall be submitted on forms
approved by the Director no later than January 31 for the previous year in which sampling was
required to be performed.
Analytical results from sampling during the final year of the permit term shall be submitted
with the permit renewal application.
This permit regulates stormwater discharges associated with industrial activity. Non-
stormwater discharges which shall be allowed in the stormwater conveyance system are:
(1) All other discharges that are authorized by an NPDES permit.
(2) Foundation drains, air -conditioner condensate without added chemicals, springs,
waterline and fire hydrant, water from footing drains, flows from riparian habits and
wetlands, fire -fighting training and fire system testing, wash down water without added
chemicals.
(3) Discharges resulting from fire -fighting
g. If the storm event monitored and reported in accordance with this permit coincides with a non-
stormwater discharge, the permittee shall separately monitor and report all parameters as
required under the non-stormwater portion of this permit and provide this information with the
stormwater discharge monitoring report.
No analytical monitoring is required by the permit.
A. (13) FISH TISSUE SAMPLING:
Progress Energy shall conduct fish tissue sampling for Arsenic on an annual basis. The fish tissue
sampling plan shall be approved by the Division's Environmental Sciences Section prior to
commencement of sampling.
Mayo Permit Update
Subject: Mayo Pernut Update
From: "Cahoon, Steve" <Steve.Cahoon@pgnmail.com>
Date: Thu, 6 Dec 2007 08.54:18 -0500
To: <toya.fields@ncmail.net>
Toya,
I wanted to get an update on when the final permit for Mayo may be sent to the plant. Do you have any
info I can forward to plant folks as well as our construction folks?
Also, we are going to add a truck wheel wash to wash gypsum and limestone off truck wheels before it
leaves the site, that wash water will go to an oil water separator and then to the ash pond We presently
have an oil water separator onsite that goes to low volume waste and then to the ash pond. Will the
additional oil water separator change our permit limits at the ash pond?
Please let me know Thanks for your help
Steve Cahoon
Environmental, Health and Safety Services
Mail Code PEB4
Vnet - 770-7457
Bell - 919-546-7457
1 of 1 12/17/2007 8 10 AM
Mayo NPDES Permitting Options
Subject: Mayo NPDES Permitting Options
From: "Cahoon, Steve" <Steve. Cahoon@ pgnmail.com>
Date: Mon, 19 Nov 2007 15:36:52 -0500
To: <toya.fields@ncmail.net>
CC: "Enzor, Earl" <kenneth.enzor@pgnmail.com>, "Hatcher, Larry" <Larry.Hatcher@pgnmail.com>,
"Holt, Fred" <fred holt@pgnmail.com>, "Madewell, Alan" <Alan.Madewell@pgnmatl.com>
Toya,
As a follow up to our earlier phone conversation we have selected an option to proceed with our NPDES
permit for the Mayo facility. We would like our permit to reflect the addition of 4 parameters (Antimony,
Boron, Cobalt and Molybdenum) without a minimum flow limit, we also request that these parameters have
a two year compliance period associated with them as well, to be consistent with other parameters
currently in our permit We also request that at this time the permit limit for Beryllium be changed to
reflect the current water quality standard of 6 5 ug/I, instead of the current weekly average limit in the draft
permit of 0.0068 ug/I The plant requests that the Division proceed with these changes and finalize our
permit as soon as possible A formal response selecting the above referenced permit option from the
Mayo Plant signatory (Larry Hatcher) will be forthcoming
Also, an updated Flow Diagram will be sent with the letter, the updated flow diagram will reflect the
proposed future addition of a side stream from the FGD intake pumps to the cooing towers This addition
was discussed with the Division in a meeting on November 9, 2007
Please contact me if you have any questions
Steve Cahoon
Environmental, Health and Safety Services
Mail Code PEB4
Vnet - 770-7457
Bell - 919-546-7457
1 of 1 12/17/2007 8 10 AM
Mayo FGD & Cooling Tower Make Up Water Balance
Ash Pond
Ash Sluice
" 3,300 GPM
Condensers
* 3,300 GPM
GP
2,000 GPM
FGD
Heat Exchangers
7,700 GPM
4,300 GPM
Mayo Lake Intake:
Avg. = 3,800 GPM (FGD MU) + 7,700 (1 CT MU Pump)
= 11,500 GPM = 16.6 MGD
258.000 GPM
MU CT MU
Avg. 1,800 GPM
Make Up Water for Basin Level
6,200 GPM
Evaporation
Cooling Towers
* Can utilize either flow path
Progress Energy
Mayo FGD & Cooling Tower Make Up Water Balance
Ash Pond
Ash Sluice
' 3,300 GPM
Condensers
* 3,300 GPM
M
2,000 GPM
FGD
Heat Exchangers
7,700 GPM
4,300 GPM
Mayo Lake Intake:
Avg. = 3,800 GPM (FGD MU) + 7,700 (1 CT MU Pump)
= 11,500 GPM = 16.6 MGD
258,000 GPM
D MU CT MU
Avg. 1,800 GPM
Make Up Water for Basin Level
6,200 GPM
Evaporation
Cooling Towers
* Can utilize either flow path �j+� Progress Energy
Progress Energy Carolinas, Inc Attachment 1 b for Fact Sheet
Mayo Electric Generating Plant
NCO038377
Parameter Estimated FGD (C Waters) Allowable Estimated Effluent Acute Maximum Predicted
Blowdown Conc ' WQ standard EPA Criteria\llowat uq/L conc uq/L ^^ Values uq/L conc for RPA # Limit or Monitor?
Antimony
440
56
5 6
041
541
Monitor
Arsenic
390
10
10
1000
13200
Monitor
Barium
25190
1000
1000
8438
111382
Limit
Beryllium
250
00068
00068
084
11 09
Limit
Boron
790
750
750
265
3498
Monitor
Cadmium
80
2
2
027
15
356
Limit
Chloride (mg/L)
160000
230 mg/L (AL)
230000
535945 98
7074486 94
Limit
Chromium
121 0
50
50
405
1022
5346
Limit
Cobalt
770
65
1 65
028
370
Monitor
Copper
720
7 (AL)
7
017
224
Monitor
Fluoride
184000
1 8 mg/L
1800
61634
8135.69
Limit
Lead
790
25
25
265
338
3498
Limit
Manganese
14500
200
200
4857
64112
Limit
Mercury
380
0 012
0.012
061
805
Limit
Molybdenum
12900
170
170
1 90
2508
Monitor
Nickel
5760
25
25
079
261
1043
Monitor
Selenium
54800
5
5
2500
56
330 00
Keep Limit
Thallium
8 0
035
035
005
066
Limit
Vanadium
650
24
24
218
2878
Limit
Zinc
36900
50 (AL)
50
742
67
9794
Monitor (AL)
Concentrations are in ug/L unless otherwise noted
^^ The concentration output is based on the flow from the ash pond (7 3 MGD) + flow from FGD (0 253) = 7 553 MGD
= mass (lbs/day)/ (7 553 ' 8 34)
= conc mg/L
# Estimated effluent conc ' 13 2
IWC = 100% (assumed, since discharge is into the Lake and no modeling was conducted)
Limit or monitor determined by one data point (the estimated concentration from the ash pond effluent). As defined in EPA TSD
for one data point, CV = 0.6 and the multiplier is 13.2
c Progress Ener
9 9Y
LeToya Fields
NC Division of Water Quality
1617 Mail Service Center
Raleigh, NC 27699-1617
R� -crcc---- - --
LSEP22007
DENR - WATER QUALITY
POINT SOURCE BRANCH
SEP 2 4 2007,
Subject: Carolina Power & Light Company d/b/a Progress Energy Carolina, Inc.
Mayo Electric Generating Plant
NPDES Permit No. NCO038377
Comments on Draft Permit
Dear Ms. Fields:
Thank you for working with us through this permit modification. We have evaluated the
two options presented to us by the Division. These options are: 1) keeping the minimum
flow requirement for Outfall 002 as proposed in the draft permit or 2) accepting
additional permit limits for antimony, boron, cobalt and molybdenum with no minimum
flow requirement. After evaluating both options we accept the draft permit with a
minimum flow requirement of 7.3 MGD, with some qualification as presented below.
We believe the Division recognizes that the proposed minimum flow requirement is
associated with reducing the level of chlorides in the future FGD wastewater and is a
design factor an the mixing zone model. It as our understanding that the proposed
minimum flow requirement is expressed as a daily minimum that is proposed to be met at
all times, i.e. 24 hours a day/seven days a week/365 days a year. Progress Energy intends
to ensure compliance with the proposed limitation by providing supplemental flow by the
installation of additional intake capacity with redundancy. However it must be
recognized that there will be occasions when ensuring a minimum flow is not needed
from a permitting standpoint and to require such without qualification as an unnecessary
use of water and power and would mflact unnecessary wear on materials Also at must be
recognized that there may be unexpected events such as pump malfunctions, power
interruption, etc. that may render the site unable to provide the prescribed continuous
flows The intent of the following proposed special condition or note as to attempt to
recognize these situations and to provide a qualification that would allow us to have a
waiver from the minimum flow requirement during these situations
We propose the following language, associated with the minimum flow, be added an a
footnote to paragraph A. (4) of our draft NPDES permit -
Progress Energy Carolinas, Inc
Mayo Steam Plant
10660 Boston Road
Roxboro, NC 27574
SEP x 4 2007
The minimum flow requirement is not applicable during the following events.
1) Power failures or other physical or mechanical events unpreventable by the
reliability requirements at 15A NCAC 2H .0124.
2) Periods of time when there is no discharge of FGD wastewater through the
bioreactor.
3) Maintenance of pumps, or associated conveyance structures that requires the item
to be out of service
Also, because of the supplemental water required to ensure compliance with the
minimum flow requirements, we would like to establish a new Outfall (0 10) at a point
beyond (downstream) where the supplemental water is proposed to enter the discharge
canal to Mayo Lake. The supplemental water is proposed to be routed to the discharge
canal to avoid any conflicts with the technology-based limits for the ash pond discharge.
We also request that the compliance point for flow monitoring and the metals monitoring
requirements and limits in paragraph A. (4) of the current draft permit be moved from the
Ash Pond Discharge (Outfall 002) to the new Outfall (010) Please modify our existing
application of record accordingly with the enclosed schematic.
We also recommend that the flows at Outfall 010 be determined by summing the flows
from Outfall 002, (Instantaneous), Outfall 009 (Instantaneous) and the new supplemental
water flow (Pump logs or similar)
Also Note 2 of paragraph A. (4) states that the limit becomes effective 24 months after
the commencement of the FGD system. We would like that note to read as follows. the
limit becomes effective 24 months after the discharge of treated FGD wastewater through
Outfall 009
If you have any questions regarding this submittal please contact Steve Cahoon at (919)
546-7457.
I certify, under penalty of law, that this document and all attachments were prepared under my
direction or supervision in accordance with a system designed to assure that qualified personnel
properly gather and evaluate the information submitted Based on my inquiry of the person or
persons who manage the system, or those persons directly responsible for gathering the
information, the information submitted is, to the best of my knowledge and belief, true, accurate,
and complete I am aware that there are significant penalties for submitting false information,
including the possibility of fines and imprisonment for knowing violations
Sincerely,
Larry E. Hatcher — Plant Manager
Mayo Electric Generating Plant
Re Draft permit status update
Subject: Re: Draft permit status update
From: Toya Fields <toya.fields@ncmail.net>
Date: Wed, 08 Aug 2007 16:32:57 -0400
To: "Cahoon, Steve" <Steve. Cahoon@ pgnmail.com>
CC: "Enzor, Earl" <kenneth.enzor@pgnmatl.com>
Steve,
We've taken a look at your comments. We can remove the flow minimum, but since we
can't do a true reasonable potential analysis without that information, we'd have to
add limits for nearly all parameters of concern for the FGD system. The draft permit
you reviewed had limits for nearly everything predicted to be in the FGD wastewater
except antimony, boron, cobalt, and molybdenum. So if you want to remove the flow
minimum, we'd just have to add in limits for those four parameters. As always, once
the system gets up and running and we have more data to review, you guys will be able
to request a re-evaluation of some of these limits.
Also, instream monitoring will need to remain in the permit. The requirement is
consistent for all other facilities throughout the state that have limits based on
dilution models. Its fine if you sample at the boat ramp.
I think those were your biggest concerns. Let me know how to proceed.
Toya
Cahoon, Steve wrote:
Sergei was also given worst case scenario parameters in 2005. I believe
arsenic was one of the parameters Sergei was concerned about (we are
required by permit to conduct biological sampling for arsenic in the
Lake for the past two years) in addition we have been monitoring the
lake for many parameters including metals since the plant began
operation in the mid 1980's. Our biological monitoring team continues
to report that we are not seeing any accumulation of arsenic in fish
tissue.
In my absence please contact Earl Enzor copied on this response or by
phone at 546-2136.
Thanks'
Steve Cahoon
Progress Energy Carolinas, Inc.
Environmental, Health and Safety Services - POG
Vnet 770-7457
Bell (919) 546-7457
steve.cahoon@pgnmail.com
-----Original Message -----
From: Toya Fields [mailto:toya.fields@ncmail.net] Sent: Wednesday, August 08, 2007
12:09 PM
To: Cahoon, Steve
Subject: Re: Draft permit status update
Its really not the chlorides we were concerned about, its the other parameters
that Sergei added in 2005. I think some of those were based on the 7.3 MGD
assumption. Thats what we're taking another look at.
Is there anyone that I should direct questions to while you are on
vacation?
1 of 2 10/10/2007 1 21 PM
Re Draft permit status update
Cahoon, Steve wrote:
Hey Toya,
Keep in mind while you're looking at the permit that the model was set
up using worst case scenario numbers for example a worst case input of
20,000 ppm of chlorides from coal versus the expected 15,0Oppm
chlorides
Ifrom coal and drought conditions in the lake, which are much worse than
7Q10 conditions. We do not expect to see either of these worst case
scenario conditions.
Let me know if you have questions.
Steve Cahoon
Progress Energy Carolinas, Inc.
Environmental, Health and Safety Services - POG
Vnet 770-7457
Bell (919) 546-7457
steve.cahoon@pgnmail.com
-----Original Message -----
From: Toya Fields[mai.lto:toya.fields@ncmail.net] Sent: Wednesday, August 08,
2007 11:26 AM
To: Cahoon, Steve
Subject: Draft permit status update
Hi Steve,
We're working on your draft modification. We're looking into the flow minimum
and trying to determine whether or not changing that 7.3 MGD assumption would
have an effect on any of the other permit conditions.
I'll let you know when I have more information.
Toya
Toya Fields - toya.f?elds@:cmail.net
Environmental Engineer I
Western NPDES Program
Division of Water Quality
Tel: 919-733-5083 x 551
Fax: 919-733-0719
2 of 2 10/10/2007 1 21 PM
Progress Energy
LeToya Fields
NC Division of Water Quality
1617 Mail Service Center
Raleigh, NC 27699-1617
File: 12520 B-1
J U L i 1 2007
J U L 0 6 2007
f
Subject: Carolina Power & Light Company d/b/a Progress Energy Carolina, Inc.
Mayo Electric Generating Plant
NPDES Permit No NCO038377
Comments on Draft NPDES Permit
Dear Toya:
Enclosed are our comments on the subject draft NPDES permit sent to us by your letter
of June 6, 2007. We appreciate the opportunity to comment.
If you have any questions please contact Steve Cahoon at (919) 546-7457.
I certify, under penalty of law, that this document and all attachments were prepared under my
direction or supervision in accordance with a system designed to assure that qualified personnel
properly gather and evaluate the information submitted Based on my inquiry of the person or
persons who manage the system, or those persons directly responsible for gathering the
information, the information submitted is, to the best of my knowledge and belief, true, accurate,
and complete I am aware that there are significant penalties for submitting false information,
including the possibility of fines and imprisonment for knowing violations
Sincerely,
Z" E . lam
Larry E. Hatcher
Plant Manager
Mayo Electric Generating Plant
Progress Energy Carolinas, Inc
Mayo Steam Plant
10660 Boston Road
Roxboro NC 27574
Mayo Electric Generating Plant
Draft NPDES Permit Comments
• Sampling Frequencies
r J U L 1 1 2007 9
,u 4
It is our understanding that the draft permit requires twice monthly monitoring
(with no limit) for the parameters referenced by Note 2 until 24 months after the
FGD treatment system comes online. After the FGD treatment system has been
operational for 24 months then the monitoring frequency for those parameters
referenced by Note 2 becomes weekly. Please confirm our understanding.
• In -stream monitoring for chlorides has been added at the boundary of the nuxing
zone. Additionally it appears that there are limits for chlorides at this boundary.
KO'd "& -11
First, Progress Energy requests that the permit be clarified so that the permit
cannot be interpreted to have chloride limits at the edge of the mixing zone as this
would defeat the purpose of having the same permit limits at the outfall.
• A minimum flow limit of 7.3 MGD has been added to Outfall 002. This limit
becomes applicable 24 months after the commencement of the FGD system.
Consistent with 40 CFR §122 45(f)(1) for water quality based effluent limits, and
the Total Maximum Daily Load concept, Progress Energy believes that a mass
limitation is more appropriate than a minimum flow requirement for controlling
the discharge from outfall 002 Receiving water concentrations are a function of
Secondly, Progress Energy requests that this sampling requirement be deleted.
0� ��✓
The mixing zone model developed by Progress Energy and submitted to the DWQ
was based on a worst case scenario of high chloride coal and drought conditions
in the lake. The drought conditions reflect a modeling constant that is more
1� 'v
conservative than a 7Q10 condition The model produced certain end -of -pipe
values that reflected the conservative nature of the model. Consistent with the
model, it is our viewpoint that if we are meeting the end -of -pipe limit for
then be the the the
chlorides we will meeting water quality standard at edge of
`
mixing zone Furthermore, sampling for sampling sake when the lake is not
0 �� ;�V,
approaching drought conditions appears to be excessive.
k� r cryo
A weekly sampling requirement at the boundary of the mixing zone will be very
burdensome on staff resources as well as dangerous if staff must conduct weekly
sampling regardless of weather conditions. If sampling is desired to ascertain
chloride levels in the lake near the mixing zone boundary then a less onerous
sampling spot would be at the boat ramp (shown on the enclosed attachment).
Therefore if the in -stream sampling conditions cannot be deleted, Progress Energy
requests the location be switched to the one presented above and the sampling be
conducted only when the lake conditions approach drought conditions.
• A minimum flow limit of 7.3 MGD has been added to Outfall 002. This limit
becomes applicable 24 months after the commencement of the FGD system.
Consistent with 40 CFR §122 45(f)(1) for water quality based effluent limits, and
the Total Maximum Daily Load concept, Progress Energy believes that a mass
limitation is more appropriate than a minimum flow requirement for controlling
the discharge from outfall 002 Receiving water concentrations are a function of
both discharge flow and discharge concentration mixed with the receiving water
constant flow. In other words the discharge can have a low concentration with a
larger flow and maintain in -stream standards. Also the discharge can have a
higher concentration with lower flow and maintain in -stream standards due to
G- mixing caused by wind, and gradient diffusion. In order to control both flow and
concentration through a permit limit it is recognized that a mass limit based on
modeling conditions is the most appropriate. Also a mass limit helps to
encourage water conservation and pollution prevention practices.
discharge e uirement of 3 MGD
Furthermore, in order to meet the minimum requirement 7
r (J� under normal operating conditions the company would be forced to install extra
pumping capacity to pump water from the lake, through the plant and back to the
lake to satisfy the permit limit. We believe this is unnecessary when the matter
can be better controlled by a mass limit.
Consequently Progress Energy requests that the minimum flow limit be replaced
by mass limits calculated by the concentration limits and the design 7.3 MGD
flow
Progress Energy recognizes that past discussions with the Division have indicated
that a mass limit is not feasible, but we must request that the Division reconsider
this position. If the Division cannot remove the minimum flow requirement from
the permit then Progress Energy requests a meeting before the permit is issued to
discuss the issues and the following permit language: "The flow limit shall only
apply when the plant is in operation or the Bioreactor discharge averages greater
than 18,000 ppm chloride with the water level in Mayo Lake below the 407 foot
level (lake level at which Mayo's Drought Contingency Plan is activated); normal
operating conditions for the plant are at lake level 434 feet."
• Total Mercury Limitation
f ,y„ The limit for Total Mercury is referenced by Note 2 and 4. We interpret the notes
to mean we must monitor for mercury twice a month for 12 months after
commencement of the FGD system. For this 12 month period there is no limit.
After the 12 month period the limit becomes effective and the monitoring
frequency increases to weekly. Please confirm our understanding.
Total Beryllium Limitation
The present concentration limit for Beryllium of 0.0068 µg/L was based on a
currently outdated human health criterion. Recent (May 2007) modifications to
f the Division's Water Quality Standards present the only criterion for Beryllium
1. as 6.5 pg/L Progress Energy requests that the Division take this opportunity to
revise the weekly average limit for Beryllium to 6.5 pg/L.
N� N
SOW
s
!,�sh Pond Discharge Approximate Edge of Mixing Zone
..
T
Mixing
Zone
Mayo Dock (Proposed Sampling Point)
Proposed Sampling Point
Approximate
Edge of Mixing Zone
"' Progress Energy
Mayo Dock (Proposed Sampling Point)
Approximate Edge
of Mixing Zone
Mixing Zone Cove
Proposed-
-
- Sampling Point
-sem. __ •�... �' _ �^`� •—_ _ ..-���s. __ _' _ ' .
1-
r
�� Progress Energy
Mayo Dock (Proposed Sampling Point)
Sample from Dock
Progress Energy
RE: Your message
i.
Subject: RE: Your message
From: "Cahoon, Steve" <Steve.Cahoon@pgnmail.com>
Date: Mon, 25 Jun 2007 14:05:20 -0400
To: "Toya Fields" <toya. fields@ ncmail. net>
Toya,
Outages are easy to deal with, our concerns are more with operational
issues such as trips offline that cause the units to be down for hours
or days, the unit offline because of demand, the unit not running at
100% of load. The 7.3 MGD used in the model was a worst case scenario,
if the unit is not running at 100%, or the chloride concentration in the
coal is not 20000 ppm as described in the model then the plant won't
need to discharge 7.3 MGD to meet the concentration limit at the end of
the pipe. We'll be pumping water from the lake just to satisfy the
limit.
We'll go ahead and send you written comments ( by our 30 day clock they
are due to you by July 11, 2007) in our comments we'll try and
incorporate language that will satisfy both of our needs. If the
Division is unable to incorporate these suggestions into the permit then
we do request a face to face meeting to discuss the issue before the
final permit is issued to the plant.
Steve Cahoon
Progress Energy Carolinas, Inc.
Environmental, Health and Safety Services - POG
Vnet 770-7457
Bell (919) 546-7457
steve.cahoon@pgnmail.com
-----Original Message -----
From: Toya Fields [mailto:toya.fields@ncmail.net]
Sent: Monday, June 25, 2007 1:31 PM
To: Cahoon, Steve
Subject: Re: Your message
Steve,
The flow limit was simply based on our understanding that Progress could
meet a 7.3 MGD discharge from the ash pond. If that can't happen during
outages then the solution may be as simple as a footnote explaining that
the limit doesn't apply during outages (of course other limits based on
that 7.3 MGD assumption would still apply). The flow issue may be
complicated, but if the solution is that simple then we won't need to
devote significant staff hours to meeting on that issue. If the
solution is not going to be that simple, then perhaps we will need to
meet.
I need you to give me some idea of what your full concerns are. If a
letter won't suffice, then feel free to give me a call.
Toya
Cahoon, Steve wrote:
Toya,
We can send the comments in by letter, but we feel we will still need
1 of 2 10/10/2007 1:19 PM
RE: Your. message
to
meet. The flow issue is somewhat complicated and will be better
understood if we can meet face to face. I'm not sure we can explain
the
Iissue well enough in a letter so that DWQ will be able understand the
full impact of the flow limit.
Let me know when you can schedule a meeting.
Steve Cahoon
Progress Energy Carolinas, Inc.
Environmental, Health and Safety Services - POG
Vnet 770-7457
Bell (919) 546-7457
steve.cahoon@pgnmail.com
-----Original Message -----
From: Toya Fields [mailto:toya.fields@ncmail.net]
Sent: Friday, June 22, 2007 11:05 AM
To: Cahoon, Steve
Subject: Your message
Hi Steve,
I got your message yesterday. The easiest thing to do would probably
ne
for you guys to submit your written comments and we can schedule a
meeting if there are still any outstanding concerns. If there is
something that you don't want to put in a letter you can give me a
call. I'd rather not schedule a meeting unless there is a significant
issue to discuss that we can't come to an agreement on.
Thanks,
Toya
Toya Fields - toy- fields@ncmall.net
Environmental Engineer I
Western NPDES Program
Division of Water Quality
Tel: 919-733-5083 x 551
Fax: 919-733-0719
2 of 2 10/10/2007 1:19 PM
STATE OF NORTH CAROLINA,
PERSON COUNTY
PRINTER'S AFFIDAVIT
Vickie F. Carver, being duly sworn,
deposes and says: That she is Office Manager of
The Courier -Times, with its principle place of business
located in the city of Roxboro, County of Person, State
of North Carolina; that the foregoing or attached
newspaper notice was published in The Courier -Times,
once a week for I successive weeks, beginning with
its issue of 9hay of l"k, 20 � ,
and ending with its issue of4_ day of
r
'20 y I ; that The Courier -Times, is
the sole owner and publisher of said newspaper,
The C ourier-T
1
Affiant)
Sworn to and subscribed before me,
r
this the day of 20��
ki
(Notary Public)
My commission expires them day of�..,ll�' f N�i20�
(Publication Fee $ t n
(Notarial Seal)
PUBLIC NOTICE
STATE OF NORTH CAROLINA
ENVIRONMENTAL MANAGEMENT
COMMISSION/NPDES UNIT
1617 MAIL SERVICE CENTER
RALEIGH, NC 27699-1617
NOTIFICATION OF INTENT
TO ISSUE A NPDES
WASTEWATER PERMIT
On the basis of thorough staff
review and application of NC General
Statute 143.21. Public law 92.500 and
other lawful standards and regulations,
the North Carolina Environmental
Management Commission proposes
to issue a National Pollutant Discharge
Elimination System (NPDES)
wastewater discharge permit to the
person(s) listed below effective 45
days from the publish date of this
notice.
Written comments regarding the
Proposed permit will be accepted until
30 days after the publish date of this
notice. All comments received priorto
that date are considered in the final
determinations regarding the
proposed permit. The Director of the
NC Division of Water Quality may
decide to hold a public meeting forthe
proposed permit should the Division
receive a significant degree of public
interest.
Copies of.the draft permit and
other supporting information on file
used to determine conditions present
in the draft permit are available upon
request and payment of the costs of
reproduction. Mail comments and/or
requests for information to the NC
Division of Water Quality at the above
address or call Ms. Frances
Candelaria at (919) 733-5083.
extension 520 at the Point Source
Branch. Please include the NPDES
permit number in any communication.
Interested persons may also visit the
Division of Water Quality at 512 N.
Salisbury Street. Raleigh, NC 27604-
1148 between the hours of 8:00 a.m.
and 5:00 p.m. to review information
on file.
Progress Energy, 10660 Boston
Road, Roxboro, NC 27344 has applied
for a modificiation of its NPDES
discharge permit for Mayo Electric
Generating Plant (number
NC0038377). discharging to the Mayo
Reservoir in the Roanoke River
Basin.This modification would allow a
mixing zone for chlorides in Mayo
Lake. This facility operates two
outfalls, 001 (recrculated cooling
water), and 002 (low volume waste,
ash sluice water, cooling tower
blowdown, coal pile runoff, FGD
blowdown, etc). Currently total
selenium, oil and rease, and TSS are
water quaility limited. This discharge
may affect future allocations in this
portion of the Roanoke River Basin.
June 9
7
Mayo-long3.mdb Salinity, ppt 07130!:
N
Salinity, ppt
1.00
0.23
0.00
Maximum Length = 120 meters
Surface Area = 18900 square meters
Bottom Area = 13400 square meters
Volume = 36320 cubic: meters
500 m
Progress Energy
Mayo-long3_mdb Salinity, ppt 08/19/2002 00:01
Salinity
Maximum Length = 180 met(
Surface Area = 21400 squar
Bottom Area =15820 square
Volume = 43800 cubic mete
N
A
500 m
Progress Energy
tf' Start 11 CORMIX-GI << 41 A 4;16 PM
ERM Surfacewater Modeling
Group
A
F. s T,
F.- 3
Grace Lake, Michigan 3-D Thermal Discharge Modeling
Services Include:
Study Design and Field Program Layout
Model Development and Application
NPDES Permit Applications
Public Presentations and Testimony
Software Development (FORTRAN, VB, ArcGIS)
Training for GEMSS and CE -QUAL -W2
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CE -QUAL -W2 Model Application to Lake Mohave, CA
ERM's Surfacewater Modeling Group (SMG) is an
internationally -recognized group of surface water
professionals supporting clients since 1976. The group
specializes in modeling and analysis of watersheds, rivers,
lakes, reservoirs, estuaries and coastal waterbodies. Model
applications are made in support of thermal plume
investigations, point source discharge permits, optimization
of cooling water facilities, oil spill damage assessments, PRP
litigation, reservoir water quality studies, water supply
development, and TMDL studies.
Expertise of the SMG team includes hydrodynamics,
computational fluid dynamics, hydrology, limnology,
oceanography, water chemistry, aquatic ecology, and
information technology. These disciplines are essential to
developing and applying mathematical models for
watershed, waterbody, and ecosystem -scale simulation.
Selection of Clients
• Electric utilities
• Public agencies
• Petroleum industry
• Paper mills
• Mining industry
• Harbor and waterway authorities
• Marine insurance firms
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Delivering sustainable solutions in a more competitive world
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GEMSS Software Interface
GEMSS - SMG's Comprehensive Modeling Software
SMG has encapsulated many of its analysis techniques in
the software system GEMSS (Generalized Environmental
Modeling System for Surfacewaters). At the heart of the
system are four hydrodynamic modules: the 3-D model
GLLVHT, the 2-1) longitudinal -vertical model
CE -QUAL -W2, the 1-D model GLHT, and the
fully -mixed model RTC.
Specialized fate modules include:
• Hydrodynamic and Transport - HDM
• Water Quality Module - WQM
• Toxics Module - TOX
• Sediment Transport Module - STM
• Particle Tracking Module - FTM
• Chemical and Oil and Spill Module - COSIM
• Entrainment Module - ENM
• 1D Module -1DM
• CE -QUAL -W2 Module - W2M
• Generalized Bacteria Module - GBM
• User Constituent Module - UCM
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12 71 /9 9 r 7 1 6 5 J ] t 1
Connecticut Yankee Thermal Plume Modeling
GEMSS has had extensive application experience and has
been accepted by many regulatory agencies including the
NRC, EPA, the World Bank, and state agencies such as
NJDEP and DNREC and others.
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GEMSS Output Data Visualizer
GEMSS itself is a graphical user interface that supports these
modules and provides additional capabilities, including: Contact: Venkat S. Kolluru at 610-524-3654
• Grid generation Email: Venkat.Kolluru@erm.com
• Geographic information systems (GIS)
• Field data importing and visualization
• Boundary condition data preprocessors '004
• Post -processors for model output visualization
• 3-1) Visualizer
Coldwater Plume Discharging at Depth Zo
ERM consulting services worldwide www.erm.com ERM
Generalized Environmental Modeling System for Surface Waters (GEMSS)
TECHNICAL DETAILS
GEMSS is an integrated system of 3-D hydrodynamic and transport models embedded in a
geographic information and environmental data system. GEMSS includes a grid generator and
editor, control file generator, 2-D and 3-D post processing viewers, and an animation tool. It uses
a database approach to store and access model results. The database approach is also used for
field data; as a result, the GEMSS viewers can be used to display model results, field data or
both, a capability useful for understanding the behavior of the prototype as well as for calibrating
the model. The field data capability can be used independently of the model application. GEMSS
was developed in the mid -80s as a hydrodynamic platform for transport and fate modeling. The
hydrodynamic platform ("kernel") provides 3-D flow fields from which the distribution of various
constituents can be computed. The constituent transport and fate computations are grouped into
modules. GEMSS modules include hydrodynamics, water quality, sediment transport, particle
tracking, oil and chemical spills (the Chemical / Oil Spill Impact Module, COSIM), entrainment,
and toxics.
The theoretical basis of the hydrodynamic kernel of GEMSS is the three-dimensional Generalized,
Longitudinal -Lateral -Vertical Hydrodynamic and Transport (GLLVHT) model which was first
presented in Edinger and Buchak (1980) and subsequently in Edinger and Buchak (1985). The
GLLVHT computation has been peer reviewed and published (Edinger and Buchak, 1995; Edinger,
et al., 1994 and 1997). The kernel is an extension of the well known longitudinal -vertical transport
model written by Buchak and Edinger (1984) that forms the hydrodynamic and transport basis of
the Corps of Engineers' water quality model CE -QUAL -W2 (U. S. Army Engineer Waterways
Experiment Station, 1986). The constituent modules as well as the GIS interoperability, the
visualization tools, the graphical user interface (GUI), and the post -processors have been
developed by Kolluru et al. (1998; 1999; 2003a; 2003b).
VALIDATION
COSIM was recently used during a major U.S. oil spill in Buzzards Bay, Massachusetts. During a
Natural Resource Damage Assessment (NRDA) to assess potential impacts resulting from a
release of No.6 Fuel Oil from a fuel barge, COSIM was used on behalf of the responsible party in a
cooperative assessment with the U.S. National Oceanic and Atmospheric Agency (NOAA). NOAA
is one of the world's leading agencies for managing oil spill responses and assessing spill -related
impacts. When use of one of NOAA's in-house models, NRDAM/CME, was rejected by NOAA in
response to demands for the best state-of-the-art oil spill model be implemented, NOAA agreed to
allow SIMAP (by the trustees) and COSIM (by the responsible party) to be run in parallel. Thus the
aquatic injury assessment was performed concurrently with COSIM and SIMAP to form a
consensus model, facilitating the cooperative process. The model was successfully calibrated to
field observations, shoreline oiling was delineated and potential aquatic injuries associated with the
oil's dissolved aromatic hydrocarbons in the water column and nearshore were assessed. COSIM
results have been verified through comparisons to field observations for use in other major oil spills
including a rupture in a river in Maryland and a barge leak off the coast of California.
GEMSS and its component modules have met agency approval in the U.S. and Canada many
times since 1981. GEMSS-based studies have been accepted by the U.S. Environmental
Protection Agency (EPA), several U.S. state agencies including California, Massachusetts,
Pennsylvania, Louisiana, Texas and Delaware. Washington State's Department of Ecology has
adopted GEMSS as their standard tool for estuarine and water quality modeling. Most recently
GEMSS has been published as a recommended three-dimensional hydrodynamic and water quality
model in studies funded by EPA (HGL and Aqua Terra, 1999) and by the Water Environment
Research Foundation (Water Environment Federation, 2001). It is the sole hydrodynamic model
listed in its WERF model selection tool database for hydrodynamic and chemical fate models that
can do 1-D, 2-D, and 3-D time -variable modeling for most waterbody types, all state variables, for
J
near field and far field simulations, with GUIs, grid generation, GIS linkage, and strong
documentation.
Outside the U.S., GEMSS and its various software modules have been approved by many
regulatory agencies as well. Studies conducted using the hydrodynamic (GEMSS-HDM) and
thermal analysis (GEMSS-TAM) modules were approved by the regulatory agency in the State of
Bahamas. Similar studies using the same modules were also approved by the regulatory agency in
the State of Qatar. Spill impact studies conducted using the COSIM module of GEMSS were also
approved by the regulatory agency in the State of Qatar. Studies conducted using the water quality
(GEMSS-WQM) module of GEMSS was approved by the overseeing regulatory agency in India.
GEMSS-HDM and GEMSS-WQM modules were recently applied to study the hydrodynamic mixing
and water quality of the confluence of the Nottawasaga River with Nottawasaga Bay in Ontario,
Canada. The model results were accepted by the Lake Simcoe Region Conservation Authority of
Ontario, Canada.
Buchak, E. M. and J. E. Edinger. 1984. Generalized, Longitudinal -Vertical Hydrodynamics and
Transport: Development, Programming and Applications. Prepared for U.S. Army Corps of
Engineers Waterways Experiment Station, Vicksburg, Miss. Contract No. DACW39-84-M-1636.
Prepared by J. E. Edinger Associates Wayne, PA. Document No. 84-18-R. June.
Edinger J.E., J. Wu and E.M. Buchak. 1997. Hydrodynamic and Hydrothermal Analyses of the
Once -through Cooling Water System at Hudson Generating Station. Prepared for Public Service
Electric and Gas (PSE&G). Prepared by J. E. Edinger Associates, Inc., June 1997.
Edinger, J. E. and E. M. Buchak. 1980. Numerical Hydrodynamics of Estuaries in Estuarine and
Wetland Processes with Emphasis on Modeling, (P. Hamilton and K. B. Macdonald, eds.). Plenum
Press, New York, New York, pp. 115-146.
Edinger, J. E. and E. M. Buchak. 1995. Numerical Intermediate and Far Field Dilution Modelling.
Journal Water, Air and Soil Pollution 83: 147-160,1995. Kluwer Academic Publishers, The
Netherlands.
Edinger, J. E., and E. M. Buchak. 1985. Numerical Waterbody Dynamics and Small Computers.
Proceedings of ASCE 1985 Hydraulic Division Specialty Conference on Hydraulics and Hydrology
in the Small Computer Age. American Society of Civil Engineers, Lake Buena Vista, FL. Aug. 13-
16.
Edinger, J. E., E. M. Buchak, and M. D. McGurk. 1994. Analyzing Larval Distributions Using
Hydrodynamic and Transport Modelling. Estuarine and Coastal Modeling III. American Society of
Civil Engineers, New York.
HGL and Aqua Terra. 1999. Selection of Water Quality Components for Eutrophication-Related
Total Maximum Daily Load Assessments. Task 4: Documentation of Review and Evaluation of
Eutrophication Models and Components EPA Contract Number 68-C6-0020 Work Assignment No.
2-04. Prepared by HydroGeoLogic, Inc. Herndon, VA 20170 and AQUA TERRA Consultants,
Mountain View, CA. June.
Kolluru, V. S., E. M. Buchak and J. E. Edinger, 1998. "Integrated Model to Simulate the Transport
and Fate of Mine Tailings in Deep Waters," in the Proceedings of the Tailings and Mine Waste'98
Conference, Fort Collins, Colorado, USA, January 26-29.
Kolluru, V. S., E. M. Buchak, J. Wu, 1999. "Use of Membrane Boundaries to Simulate Fixed and
Floating Structures in GLLVHT." In Spaulding, M.L, H.L. Butler (eds.). Proceedings of the 6th
International Conference on Estuarine and Coastal Modeling. pp. 485 — 500.
Kolluru, V. S., J. E. Edinger, E. M. Buchak and P. Brinkmann 2003. "Hydrodynamic Modeling of
Coastal LNG Cooling Water Discharge." Journal of Energy Engineering. Vol. 129, No. 1, April 1,
2003. pp 16 — 31.
Kolluru, V.S. and Mike Fichera, 2003. "Development and Application of Combined 1-D and 3-D
Modeling System for TMDL Studies." Proceedings of the Eighth International Conference on
Estuarine and Coastal Modeling. American Society of Civil Engineers. pp. 108-127, 2003.
U. S. Army Engineer Waterways Experiment Station, Environmental Laboratory, Hydraulics
Laboratory. 1986. CE-QUAL-W2: A Numerical Two -Dimensional, Laterally Averaged Model of
Hydrodynamics and Water Quality; User's Manual. Instruction Report E-86-5. Prepared for
Department of the Army, U.S. Army Corps of Engineers, Washington, DC. Final Report. August.
Water Environment Federation. 2001. Water Quality Models: A Survey and Assessment. Order No.:
D13209WW (Electronic Media).
A Cross Section, Vertical Slice through the cove across the entire Mayo Reservoir (West to East)
Database: Mayo7010-73.mdb Slice: Slice 1 Date 07/30/2002 00-01
Conc. of Salinity ppt
1
8
It
1.30
�+1.0
16
} 0,6
0
Z 2t OA
a
0.3
0.23
a 26 0.2
01
005
1 31 0.00
36
41
13 18 23 28 33 38 43 48 53
7 Index Along the Slice in East Direction
Database: Mayo7010-549.mdb Slice: Slice 1 Date: 07/30/2002 00:01
Conc. of salinity ppt
1
6
n
N 1.30
1.0
0.8
16 0.6
21 0.4
7.z
0.3
0 3
02
2fi 0.1
a 0.05
31 0.00
36
41
13 1a 23 28 33 3B 43 48 53
I Index Along the Slice in East Direction
Database- Maya 7010-349.mdb Slice: Slice 1 Date: 07/30j2002 0001
Conc. of Salinity ppt
1
6
tt
01 30
LO'Q
21 0.4
0.3
0.23
0126- 0.2
ZI 0.05
37 0.00
35-
41:
13 18 23 2B 33 38 43 48 53
1 Index Along the Slice in East Direction
Same cross sections as above, but zoomed into the first 900 meters
Database: Meyo7O1B-73.mdb Slice: Slice1 Date: 07/30/2002 00:01
Database: Mayo7C!10-549.mdb Slice: Slice 1 Date: 07/30/2002 00:01
Core. of Salinity ppt
132.89
129.72
126-55-
Mi
1.30
10
127.36
11.30
08 .8
0-6
w 120.21
0.4
0.3
023
Q 117.04
0.2
0.11
0.05
113.87:
0.00
110-7-
10 7107.53
107-534
0
375.3 750.6
Distance, m
Database: Mayo7C!10-549.mdb Slice: Slice 1 Date: 07/30/2002 00:01
Database: Mayo7O10-349.mdb Slice: Slice 1 Date: 07/30/2002 00:01
Conc. of Salinity ppt
132.89
129.7?
126.55
1.30
10
123.38
0.6
0.6
120.21
0.4
0.3
023
Q 117.04
'
0.2
01.1
0.05
11397
0.00
110.7-
107,531
0
375.3 750.fi
Distance, m
Database: Mayo7O10-349.mdb Slice: Slice 1 Date: 07/30/2002 00:01
Com. of Salinity ppt
13299
129.72
126.55
1.30
1.0
123.38
0.8
0.6
'r 120.21
0.4
0.3
023
Q 117.04
0.2
0.11
0.05
113.87
0'00
1107
107.53
0
375.3 750.6
Distance. m
.40
Y
V7
7 Ash Pond &
Bioreactor
Discharge
-'U--I
t
qb
•
4r
Mayo
Lake
Mayo Steam Generating Plant
NCO0038377
"4
L Progress Energy
Mayo Steam Generating Plant Progress Energy
NC00038377
Mayo Steam Generating Plant Progress pro Ener
NC00038377 g 9V
Calculated monthly averages - ash pond flows
Permit
-- -
NC0038377
Facility
----------------------------------------------------- --- - ----
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
Outfall
- - - -
002
Date
- ' --
Jan -04
Param Class Sample
- -- -- ----
Flow Recorder
UoM
----
mgd
Value
- -- - -------------
6.72
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Feb -04
Flow
Recorder
mgd
8.13
N00038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Mar -04
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Apr -04
Flow
Recorder
mgd
6.51
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
May -04
Flow
Recorder
mgd
6.32
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jun -04
Flow
Recorder
mgd
5.90
NC0038377
------
N00038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
-------------------------- --- ---- ----- ------------ -------------- -----------
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
-------
002
Jul -04
--
Aug -04
Flow
------
Flow
Recorder
------
Recorder
mgd
------
mgd
7.12
- -------
8.14
N00038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Sep -04
Flow
Recorder
mgd
8.01
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Oct -04
Flow
Recorder
mgd
5.91
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Nov -04
Flow
Recorder
mgd
7.01
N00038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Dec -04
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jan -05
Flow
Recorder
mgd
7.40
NC0038377
- -------------------
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
--------------------------------------------- - ' - - ------------ ----------
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
- --- ------------------------------------------------
002
Feb -05
Mar -05
Flow
I Flow
Recorder
---------------
Recorder
mgd
----------------
mgd
7.30
---------- -----------------------------------------..
8.03
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Apr -05
Flow
Recorder
mgd
6.31
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
May -06
Flow
Recorder
mgd
5.91
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jun -05
Flow
Recorder
mgd
6.41
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jul -05
Flow
Recorder
mgd
6.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Aug -05
Flow
Recorder
mgd
6.15
NC0038377
--
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
--------------------------------------------------------------------------------------
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
-----
002
Sep -05
---------------------
Oct -05
Flow
------
Flow
Recorder
----- ----
Recorder
mgd
--------
mgd
5.70
-- - - ---
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Nov -05
Flow
Recorder
mgd
7.69
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Dec -05
Flow
Recorder
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jan -06
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Feb -06
Flow
Recorder
I mgd
6.62
NCo038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Mar -06
Flow
Recorder
mgd
4.15
NC0038377
---------------
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
------- - -- -- -- - - - - - -------------- ------------
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
-----------
002
Apr -06
-----------
May -06
Flow
-----------------
Flow
Recorder
---------------
Recorder
mgd
-------------
mgd
6.22
- - - - - - - -
5.70
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jun -06
Flow
Recorder
mgd
5.66
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Jul -06
I Flow
Recorder
mgd
8.80
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Aug -06
Flow
Recorder
mgd
5.66
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Sep -06
Flow
Recorder
mgd
7.96
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
Oct -06
Flow
Recorder
mgd
6.96
NC0038377
-----------------
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
---- ------ - - - -- ---' - - -- - -- --- ---- ---- -----
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
-
002
Nov -06
----
Dec -06
Flow
------------
Flow
Recorder
- -- -
Recorder
mgd
- -
mgd
6.80
-- ----------------------------- -
6.12
Average
6.77
Median
6.76
Max
8.80,
Min
4.15
Percentiles
95th i
8.13 stn r 5.66
99th i
8.57 1 st i 4.68
Re Red 'dei ' flows from ash pond (weekly mon@orin r
wired
Penni
Facility
Outfall
Date
Param Cie.
Sample
1JoM
Value
1400038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/8/2004
Flow
Recorder
mgd
6.33
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/16/2004
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/19/2004
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
129/2004
Flow
Recorder
mgtl
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
2/3x2004
iFlow
Recorder
mgd
9.63
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Elecac Power Plant
002
2/112004
Flow
Recorder
mgd
7.88
NC0038377
I Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
2/19/2004
Fbw
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electrc.Powsr Plant
002
224/2004
Flow
Recorder
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
3x2/2004
Flow
Record.
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
&12/2004
Flow-
Record.
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
&11/2004
Flow
Recorder
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
3262004
Flow
Recordw
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
lW3Ot2OO4
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
4/6/2004
Flow
Recorder
mgd
5.49
NC0038377
Progreso Energy Carolinas Inc - Mayo Steam Electric Pows, Plant
002
4/15x2004
Flow
Record.
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
4/20/2004
Flow
Record.
mgtl
6.33
1400038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
4/30/2004
Flow
Record.
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
5/3/2004
Flow-
Recorder
mgd
8.79
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Elactric Power Plant
002
5x122004
Flow
Recorder
jm9d
5.49
NC0038377
Progreso Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
5/18/2004
IFIw
Record.
mgd
5.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
5/25/2004
Flow
Record.
mgd
5.49
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
6/12004
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - May. Steam Electro Power Plant
002
6x10/2004
Flow-
Record.
mgd
6.33
NC0038377
Progress Energy Gamines Inc - Mayo Steam Electric Power Plant
002
8/15/2004
Flow-
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/23/2004
Flow
Recordw
mgd
4.65
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8x292004
Fbw
Record.
mgd
5.10
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7/8/2004
Fbw
Recordw
mgd
5.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7/14/2004
Flow
Record.
mgtl
5.94
14C0035377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7/192004
Flow
Recorder
lmgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam EMetric Power Plant
002
728/2004
Flow-
Recorder
mgtl
9.17
NC0038377
Progrese Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
8/3/2004
Flow
Recorder
mgd
7.11
NC0039377
Progrees Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/12/2004
Flow
Record.
mgd
7.89
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
811612004
Flow
Recorder
mgd
10.47
NC0038377
Progress Enwgy Carolinas Inc - Mayo Steam Electro Poww Plant
002
825x2004
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
9/2/2004
Fbw
Recorder
mgtl
9.17
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
9/72004
lFbw
Record.
mgd
7.11
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
9/15/2004
Flow
Recorder
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
9/212004
Fbw
Record.
mgd
8.79
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
9292004
Flow-
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/5x2004
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/13/2004
Flow
Recorder
mgd
4.65
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/192004
Flow
Record.
mgtl
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Pows, Plant
002
101282004
Flow
Recorder
mgtl
6.33
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
11/12004
Flow
Recorder
mgd
7.11
NC0038377
Progreas Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
11/9/2004
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
11/162004
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Elactric Power Plant
002
11232004
Flow
Record.
mgd
7.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
12/12004
Fbw
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
1277/2004
Flow
Record.
mgd
7.89
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
12/15/2004
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
12212004
Flow
Record.
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Maya Steam Electric Power Plant
002
12/30/2004
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/4/2005
Fbw
Recorder
mgtl
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
1/12/2005
Fbw
Recorder
mgd
7.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/18/2005
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
126x2005
Fbw
Recorder
mgd
7.11
NC00383n
Progreas Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
2/12005
Flow
Recorder
mgd
7.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Poww Plant
002
2/82005
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Maya Steam Elacifb Power Plant
002
2/15/2005
Flow
Recordw
mgtl
7.49
NC0038377
Pmgress Energy Carolinas Inc - Mayo Steam Electric Poww Plant
002
2212005
Flow
Record.
mgtl
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
3112005
Flow
Record.
mgtl
8.79
1400038377
Pmgreu Energy Carolinas Inc - Mayo Steam Electric Poww Plant
002
3/8/2005
Flow
Recorder
mgd
7.48
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
3/152005
Flow
Recorder
mgtl
7.11
1400038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
322/2005
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
3/292005
Flow
Recorder
mgtl
9.63
NC0038377
Progress Energy Carolinas Ino - Mayo Steam Electric Power Plant
002
4/12005
Flow
Recorder
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002S
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
4/122005
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
4/19/2005
Flow
Recorder
mgd
6.72
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Powe, Plant
002
420121105
Fbw
Record.
mgd
3.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
5/3x2005
Fbw
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
5/10/2005
Flow
Recorder
mgtl
4.65
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
5/16/2005
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
5/242005
Flow
Recorder
mgd
6.33
NC0038377
Progreaa Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
6/12005
Flow
Record.
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
6/8/2005
Flow
Recorder
mgd
6.33
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
61142005
Flow
Record.
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8x202005
Flow
Recorder
mgd
6.33
NCDO38377
Progress Energy Carolinas Inc - Mayo Steam Electrc Power Plant
002
6/272005
Flow
Record.
mgd
5.94
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7/5/2005
Flow
Recorder
mgd
7.11
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Poww Plant
002
7/132005
Flow
lRecord.
mgd
6.33
NG0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7/18/2005
Flow
Record.
jmgd
5.49
NC0038377
Pmgress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7272005
Flow
Recorder
mgtl
5.49
NC0038377
I Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8x2/2005
Fbw
Recorder
mgtl
7.11
NC0038377
I Progress Energy Carolinas Inc - Mayo Steam Electric Pcww Plant
1002
8/9/2005
Flow
Recorder
jmgd
6.33
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
6/15/2005
Flow
Recorder
mgd
5.48
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/24/2005
Flow
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/312005
Flout
Recorder
mgd
5.49
NC0038377
Progress Energy Camlinas Inc - Mayo Steam Electric Power Plant
002
WWW5
Flow
Recorder
mgd
5.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
9/14/2005
Flow
Recorder
mgd
5.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Elecirc Power Plant
002
9/19/2005
Flow
Recorder
mgd
5.49
N00038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
9/27/2005
Flow
Recorder
mgtl
6.33
KC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/4/2005
IFIlev
Recorder
lmgd
6.33
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/13/2005
Flow
Recorder
mgd
7.88
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/18/2005
Flow
Record.
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10/27/2005
Flow
Recorder
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
11/1/2005
Flow
Recorder
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1192005
Flow-
Recorder
mgd
7.11
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
11/152005
Flow
Recorder
mgd
6.33
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1122/2005
Flow
Recorder
mgd
10.01
NC003S377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
11292005
Flow
Record.
mgd
7.88
N00038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
12/8/2005
Flow
Record.
mgd
11.76
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Pow. Plant
002
12/142005
Flow
Record.
mgtl
6.33
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Pow. Plant
002
12202005
Flow
Recorder
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
1228/2005
Flow
Recorder
mgd
6.33
NCO038377
Programs Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
IIWOO6
Flow
Recorder
mgd
7.88
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/122008
Flow
Recorder
mgd
7.88
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/172006
Flow
Recorder
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1282006
Flow
Recorder
mgd
6.33
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1/312006
Flow
Record.
mgtl
6.33
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
2/72006
Flow
Record.
mgtl
6.33
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
2/152006
Flow
Record.
mgd
6.33
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
2232006
Flow
Record.
mgd
7.11
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
2282006
Flow
Recorder
mgd
6.72
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
3/6/2006
Flow
Recorder
mgd
1.91
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
392006
Flow
Recorder
mgd
2.38
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Pcww Plant
002
3/18/2006
Flow
Recorder
mgd
5.49
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
3/212008
Flow
Record.
mgtl
4.65
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
3902006
Flow
Recorder
lmgd
6.33
r4com377
Progress Energy CaroAnas Inc - Mayo Steam Electric Power Plant
002
4/42006
Flow
Record.
mgtl
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
4/122006
Flow
Recorder
mgd
5.94
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
4/18/2006
Flow
Record.
mgd
5.49
NCO038377
Progress Energy Carolinas Inc - Maya Steam Electric Power Plant
002
426/2008
IFIDW
Record.
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
5/32006
Flow
Record.
mgd
5.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
5/70/2006
Flow
Record.
mgtl
6.33
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
5/16/2006
Flow
Record.
mgtl
6.33
NCO038377
Progress Energy CaroAnas Inc - Mayo Steam Electro Power Plant
002
5/23/2006
Flow
Recorder
mgd
4.65
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
82/2006
Flow
Record.
mgtl
5.49
NCO038377
Progress Energy Card Inc - Mayo Steam Electric Pow. Plant
002
8/6/2006
Flow
Record.
mgtl
4.65
NC0038377
Progress Energy Cana Inc - Mayo Steam Electric Power Plant
002
8/142006
Flow
Record.
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
6202006
Flow
Recorder
mgd
5.49
NCD038377
Progress Energy Carolinas Inc - Mayo Steam Electric Pow. Plant
002
628/2008
Flow
Record.
mgd
6.33
NC0039377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
7/82008
Flow
Recorder
mgd
17.12
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
7/102006
Flow
Record.
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
7/19/2006
Flow
Recorder
mgd
5.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
725/2008
Flow
Recorder
5.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/42008
Flow
Recorder
5.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/8/2006
Fbw
Recorder
5.49
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
8/16/2006
Fbw
Recorder
Vmgd
5.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
8/22/2006
Fbw
Record.
5A9
NCG038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
8/302006
Fbw
Record.
6.33
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
9/7/2006
Fbw
Recorder
6.33
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
9/142006
Flow
Recorder
mgd
11.31
NCO038377
jProgress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
9212006
Flow
Record.
1.9d
6.33
NC0038377
Progress Energy Carolnes Inc - Mayo Steam Electric Power Plant
002
926/2006
Flow
Record.
mgd
7.88
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
1032006
Flow
Recorder
mgd
7.88
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
10102006
Flow
Recorder
mgd
8.79
NC0038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
10172006
jFbW
Recorder
mgd
6.33
NC0038377
Progress Energy Carolinas Inc - Mayo Staam Electric Power Plant
002
10282006
Flow
Record.
mgtl
6.33
NCO039377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
10312006
Flow
Recorder
mgd
5.49
NC003B377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
11/72006
Flow
Recorder
mgd
5.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Paw. Plant
002
11/14/2006
Flow
Recorder
mgd
7.49
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Pow. Plant
002
11212006
Flow
Record.
mgd
7.11
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
11/302006
Flow
Recorder
mgd
7.71
NC0038377
Progress Energy Carolinas Inc- Mayo Steam Electric Power Plant
002
12/72006
Fbw
Recorder
mgd
6.33
NCO038377
Progress Energy Carolinas Inc- Mayo Steam Electro PowerPlant
002
12/14/2006
Flow
Recorder
mgd
6.33
NCO038377
Progress Energy Carolinas Inc - Mayo Steam Electro Power Plant
002
12/21/2006
Flow
Recorder
mgd
5.49
1,100035377
Progress Energy Carolinas Inc - Mayo Steam Electric Power Plant
002
1229/2006
Flow
Recorder
mgtl
6.33
Average,
6,75
Median
6.33
Maximum
17.12
Minimum
1.91
Percentiles
95th x 1
9.17 4,65
991h %
11.50 1. x 3.02
���� V'Or �
Progress Energy
LeToya D. Fields
NC Division of Water Quality
1617 Mail Service Center
Raleigh, NC 27699-1617
MAR 2 1 2107
2007
Subject: Carolina Power & Light Company d/b/a Progress Energy Carolina, Inc.
Mayo Electric Generating Plant
NPDES Permit No. NCO038377
Mixing Zone Submittal — Response to Request for Additional Information
Dear Toya:
Progress Energy Carolinas, Inc. is in receipt of your request for additional information
dated March 6, 2007, regarding the Mayo mixing zone submittal. We would like to
schedule a meeting with the appropriate Division staff to discuss the mixing zone
submittal, particularly Item 1 below, before the final end of pipe limit for the mixing zone
is established. Please contact Mr. Steve Cahoon, at (919) 546-7457, to schedule the
meeting. The following items are provided to address your request for additional
information.
• The submittal states that the ash pond flow rate used for the model was 7.3 MGD.
How was this estimate determined? What is the range of discharge rates that
might be expected from the ash pond?
Response: The average discharge estimate of 7.3 MGD was provided by
reviewing long term data from past NPDES permit applications. The mixing zone
is dependent upon two factors, in stream flow of the reservoir and the ash pond
discharge. In order to reduce model variability we maintained one of the
variables constant (ash pond discharge @ 7.3 MGD) which maintained the mixing
zone to a small size, but requires the use of mass based limits to account for the
variation in flow from the ash pond. We felt this would be the best option for
regulatory approval of a mixing zone because it greatly reduced the size of the
mixing zone with an end of pipe concentration of 672 ppm.
Modeling low flow conditions in the reservoir and low flow conditions of the ash
pond (3.49 MGD monthly average for the ash pond) results in an end of pipe
concentration of 1353.7 ppm, and more than doubles the size of the requested
mixing zone for chlorides. Internally, we felt representing the mixing zone in this
manner would be more acceptable to the Division along with the mass based limit
to account for the variability of flow in the ash pond discharge. However, if
Division policy requires concentration based limits for the chloride mixing zone,
we request the Division consider the additional information provided with this
Progress Energy Carolinas, Inc.
Mayo Steam Plant
10660 Boston Road
Roxboro, NC 27574
MAR 21 2007
submittal which describes the low flow conditions in both the ash pond and the
reservoir and predicts an end of pipe concentration of 1353.7 ppm at these low
flow conditions. The Division would then develop an end of pipe concentration
limit for the mixing zone based on the low flow conditions in both the ash pond
and reservoir; which will yield a larger mixing zone in the lake to accommodate
the variation in the ash pond discharge. The monthly average variation in the ash
pond discharge over the last two years ranges from 3.49 MGD to 17.12 MGD.
• The document characterizes the discharge plume during low flow conditions.
Please include a similar characterization for periods of "normal " and "high "
flows. What size plume might be expected to exceed water quality standards
during those conditions? If possible, please provide graphics similar to Figure 2
to characterize the plume during these conditions.
Response: Please see Attachment 1, which includes a characterization of
flows for "low" "normal" and "high flows.
• In September 2006, Progress Energy was able to provide salinity surface
contours for the entire reservoir (similar to Figure 9) depicting concentrations in
increments of 0.2 ppt. If possible, please provide similar representative graphics
for "low", "normal", and "high" periods of flow.
Response: Please see Attachment 2, which provides salinity surface contours
for low, normal and high flows. These graphics were depicted in 0.01 ppt for
your convenience.
• Please verify that Progress Energy is only requesting a mixing zone for chlorides.
Response: At this time Progress Energy is only seeking a mixing zone for
chlorides. At some point in time there may be a need to request additional mixing
zones for other parameters based on the actual performance of the bioreactor. In
our response to the Mayo Draft NPDES permit dated, February 26, 2007, our
response indicated a need for a compliance period for several parameters, in part
that compliance period would allow for time to assess the performance of the
bioreactor and allow us to petition the Division for mixing zones for additional
parameters if needed.
• Please provide a map indicating the location of the dam discharge (to the creek).
Response: Please see Attachment 3 for the map.
Enclosed with this submittal is a check for $860.00 for a major permit modification
associated with the mixing zone request. If you have any questions relating to this
submittal please contact Steve Cahoon.
MAR 2 12007
1 certify, under penalty of law, that this document and all attachments were prepared under my
direction or supervision in accordance with a system designed to assure that qualified personnel
properly gather and evaluate the information submitted. Based on my inquiry of the person or
persons who manage the system, or those persons directly responsible for gathering the
information, the information submitted is, to the best of my knowledge and belief, true, accurate,
and complete. I am aware that there are significant penalties for submitting false information,
including the possibility of fines and imprisonment for knowing violations.
Sincerely,
J c W-�--
Larry E. Hatcher
Plant Manager
Mayo Electric Generating Plant
Attachment 1
Mayo Reservoir simulation from 2001 to 2003 uses the outflow from the dam as observed at
USGS gage #02077670 shown below. Average flow rate for that station is 40 cfs.
In the simulation, the scrubber discharges a constant 0.253 mgd at 20,000 ppm of chloride. The
Ash Pond recirculates a constant 7.3 mgd at 2 ppm of chloride.
1000
:11
600
V
3
O
LL 400
200
[I]
Mayo Creek d/s of Dam
USGS #02077670
High Flow
945 cfs 4/11/03
Normal Flow
40 cfs 2/07/03
Low Flow
3.5 cfs 8/19/02
1/1/00 5/31 /00 10/29/00 3/29/01 8/27/01 1/25/02 6/25/02 11/23102 4/23/03
Date
Attachment 1 Page 1
Low Flow Condition - August 19, 2002
— ----
Mayo-long3-mdb Salinity. pt OBASnOO2 00:01
Mayo-long3.mdb Salinity, ppt 08/19/2002 00:01
Attachment 1 Page 2
Normal Flow Condition - February 7, 2003
Mayo-longlmdb Salinity. ppt 02/07/2003 00:01
Mayo-long3_mdb Salinity. ppt 02/07/2003 00:01
Attachment 1 Page 3
High Flow Condition - April 10, 2003
Mayo-long3.mdb Salinity. ppt 04/10/2003 00:00
Mayo-long3_mdb Salinity. ppt 04/10/2003 00:00
Attachment 1 Page 4
Attachment 2
Attachment 2: Mixing Zone depictions of the combined ash pond and FGD blowdown
based on GEMSS modeling results during low, normal, and high reservoir
flows.
Osefearge Cove
\
100.
i50m
f
f
t
!
400 mg.L '_ , - t
t ,
325 mgL C!
0
Low Flow 3o mgL CI -
r -130,
130,
t
80m t00m �
ZOOrr'r Of
t r
! f
Discharge
Myo Lake overview
f
400 mgL cr - !
Cove
!
325 mgt- Cf - !
130 mgL C,
Normal Flow
67m 85. 110m
7 40D mgL cr -
Legend
325 .OL Cr -
Depth (ft)
230 .gL Cr
=OD -29
-3D-59
6D-89
_ 9D- 11.9
- 12D -1JJ
High Flow
& D9.1 -Y Pout
D o.x 0.5 1.5 ks
Attachment 2: Mixing Zone depictions of the combined ash pond and FGD blowdown
based on GEMSS modeling results during low, normal, and high reservoir
flows.
Attachment 3
4
Mayo Creek
rge Cove
'A - :.,.)
Low- Level
Release Discharge
Structure
,r
L 4-1
Spi