NC0024392_Request Alternate Discharge_20150126

' Duke Energy
DUKE McGuire Nuclear Station
ENERGY. Huntaunto Halters Ferry Road
rsvitle,NC 28078
January 26, 2015
McGuire Nuclear Station
12700 Halters Ferry Road RECEIVED/DENR/DWR
Huntersville,NC 28078
Mr. Sergei Chemikov JAN .2.6 2015
North Carolina Department of Water Quality
Environment and Natural Resources Permitting Section
Division of Water Resources
NPDES Unit
1617 Mail Service Center
Raleigh, NC 27699-1617
Subject: Duke Energy Carolinas LLC/McGuire Nuclear Station
NPDES Permit#: NC 0024392
Request for alternate discharge
Certified Mail: 7010 2780 0000 7412 4021
Duke Energy Carolinas, LLC, (Duke Energy) McGuire Nuclear Station submitted an NPDES permit
renewal application for NPDES Permit Number NC 0024392 on August 14, 2014.
OIC In addition to the requests made in our renewal application, we would like to request an additional
change in allowable discharges for Outfall 005 (WWCB - Waste Water Collection Basin).
Our current permit does not allow us to discharge from the plant's turbine building sumps to Outfall 005.
We would like to request that in the event of a turbine building flooding event that we could discharge
the turbine building sumps to Outfall 005. The discharge would be via storm drain piping to either the
WWCB (Waste Water Collection Basin) for Unit 1 or the SNSWP (Standby Nuclear Service Water
Pond) for Unit 2. Both the WWCB and SNSWP are discharged through Outfall 005.
The turbine building sumps normally discharge waste water to the WC (Conventional Waste Water
Collection System) System and discharge through outfall 002.
In a turbine building flooding event scenario, the predominant makeup of the turbine building sumps
would be lake water. In the event of a turbine building flooding event, supplemental pumps are used to
discharge the predominately lake water to yard drains that go to the WWCB or SNSWP to keep water
from impacting essential plant equipment. The turbine building sumps are not able to keep up with the
volume of water that a turbine building flooding event would generate, so supplement pumps are used to
handle the additional volume of water.
I

APPENDIX I
FLOW DIAGRAM
Page 4 of 11

Standby Nuclear Appendix I
Service Water Pond ~—FtormDrains McGuire Nuclear Station
SNSWP _ NPDES Flow Diagram
A NCO02439
10 Normal Flowpath
LAKE NORMAN Nuclear Service 22.2 MGD
� ---110. Alternate Flowpath
Water RN
1 +
'
i Low Level Intake Condenser Cooling 2,604 MGD 2,626 Total MGD LAKE NORMAN
i ( LLI ) �_ _ ♦ Water RC 10 DISCHARGE
WW001
0.0079 MGD
' Low Pressure
Fire Protection i i
i Service Water RL i
L------------_--i! Rad este
i i I Reverse PrimarySystem ! I i System
i Filtered Water I Demineralized
i Osmosis Unit --lo. Coolant Drainage i♦ (WM)
Water YM r j
RO and Leakage i WWO04
U) i
-v Ventilation Unit i
-, on i Garage Vehicle j
n 1 ° Condensate Drain
Water Treatment Wash Area
Secondary System y Tanks (VUCDT) i ' 'Landfill Leachate
i Room Sump Drainage and
0.0015 MGD
Leakage
i 'NDE Photographic 3 i - r Conventional
(Waste G7 p Waste Treatment
"Island Lab Waste
System
iIsland HVAC Turbine (WC)
(Cooling Towers Building Sump WWO02
i Oil Water I -- ----
� � Storm Drains 0.3485 MGD �
Separators
i
Waste Water �---J CATAWBA
Collection Basin RIVER
(WWCB) Total: 0.9819 MGD
-------- -------------► WWO05
0.6334 MGD �
i
Last Revised
July 10, 2014 '------------- ---------------------
�

APPENDIX II
SUPPLEMENTAL INFORMATION FOR
McGUIRE NUCLEAR STATION
Page 5 of 11

Please print or type in the unshaded areas only
tf11 in areas are aced for elite type,i.e., 12 charactersrnch . For Approved. OMB No. 2040-0086. Approval expires 5-31-92
FORM U.S.ENVIRONMENTAL PROTECTION AGENCY I, EPA I.D. NUMBER
1 ♦CEPA GENERAL INFORMATION S T/A C
,r F NCO024392 D
Consolidated Permits Program
GENERAL Read the "General_Instructions"before starting.) 1 2 13 14 15
LABEL ITEMS GENERAL INSTRUCTIONS
If a preprinted label has been provided,
i. EPA I.D. NUMBER affix It in the designated space.Review the
information carefully; if any of it is
incorrect cross through it and enter the
correct data in the appropnate fill-in area
III. FACILITY NAME below.Also,if any of the preprinted data is
absent the area to the left of the label
V. FACILITY PLEASE PLACE LABEL IN THIS SPACE space fists the information that should
appear) please provide it in the proper fill-
in MAILING LIST nd rece recti you nlf the label eed not complete Items
1,111, V, and VI(except VI-B which must be
completed regardless). Complete all items
VI. FACILITY if no label has been proved. Refer to the
instructions for detailed item descriptions
LOCATION and for the legal authorization under which
this data is collected.
II. POLLUTANT CHARACTERISTICS
INSTRUCTIONS: Complete A through J to determine whether you need to submit any permit application forms to the EPA. If you answer"yes"to any
questions,you must submit this form and the supplemental from listed in the parenthesis following the question.Mark"X"in the box in the third column if
the supplemental form is attached. If you answer"no"to each question,you need not submit any of these forms. You may answer"no"if your activity is
excluded from permit requirements;see Section C of the instructions.See also,Section D of the instructions for definitions of bold-faced terms.
MARK"X" MARK"X"
SPECIFIC QUESTIONS FORM SPECIFIC QUESTIONS YES NO FORM
YES NO ATTACHED ATTACHED
A. Is this facility a publicly owned treatment works B Does or will this acility (either existing or
which results in a discharge to waters of the El ® 1:1 proposed) include a concentrated animal ❑ ® ElU.S.?(FORM 2A) feeding operation or aquatic animal
production facility which results in a discharge
16 17 18 to waters of the U.S.?(FORM 2B) 19 20 21
Is this facility which currently results in D is this proposal acility(other than those described
discharges to waters of the U.S. other than in A or B above)which will result in a discharge
El E 1 11
those described in A or B above? FORM 2C 22 23 24 to waters of the U.S.? FORM 2D 25 26 27
E. Does or will this acility treat,store, or dispose o Do you or will you inject at this acility industrial or ❑ ® ❑
hazardous wastes?(FORM 3) ❑ ® ❑ municipal effluent below the lowermost stratum
containing, within one quarter mile of the well
tore, underground sources of drinking water?
28 29 30 FORM 4L31 cili31 32 33
Do you or will you inject at this facility any H. Do you or will you inject at lhisTaty fluids or
produced water other fluids which are brought to special processes such as mining of suffer by the 11 ® E]the surface in connection with conventional oil or ❑ ® ❑ Frasch process,solution mining of minerals,in
natural gas production, inject fluids used for situ combustion of fossil fuel,or recovery of
enhanced recovery of oil or natural gas,or inject geothermal energy?(FORM 4)
fluids for storage of liquid hydrocarbons?
FORM 4 34 35 36 37 38 39
1. Is this facility a proposed stationary source S Is this acility a proposed stationary source
which is one of the 28 industrial categories listedwhich is NOT one of the 28 industrial categories 11in the instructions and which will potentially emit ❑ ® E] listed in the instructions and which will potentially Z El
100 tons per year of any air pollutant regulated emit 250 tons per year of any air pollutant
under the Clean Air Act and may affect or beregulated under the Clean Air Act and may affect
located in an attainment area? FORM 5 40 41 a2 or be located in an attainment are? FORM 5 43 44 45
III. NAME OF FACILITY
c SKIP McGuire Nuclear Station
1
15 1 16-29 1 30 69
IV. FACILITY CONTACT
A.NAME&TITLE last O st,&title B.PHONE area code&no.
C Williamson, John C. Lead EHS Professional, McGuire 980 875 5894
2
15 16 45 46 48 49 51 52 55
V. FACILITY MAILING ADDRESS
A.STREET OR P.O.BOX
C 12700 Hagers Ferry Road, Mailcode: MG01EM
15 16 45
B.CITY OR TOWN C.STATE I D.ZIP CODE
a
Hunte,sville NC 28078
15 16 40 1 1 41 42 1 47 51
VI. FACILITY LOCATION
A.STREET,ROUTE NO.OR OTHER SPECIFIC IDENTIFIER
C 12700 Hagers Ferry Road A U G 2 8 2014
5
15 1 16 45
B.COUNTY NAME Water Quality
Mecklenburg Permitting Section
46 70
C.CITY OR TOWN D.STATE E.ZIP CODE F.COUNTY CODE
C Huntersviile NC 28078 �NA
6
15 1 16 _ 40 41 42 47 51 52 54
EPA FORM 3510-1(8-90) CONTINUED ON REVERSE

CONTINUED FROM THE FRONT
VII. SIC CODES (4-digit, in order of riorit B.SECOND
A.FIRST
C 4911 (specify) 7 (specify)
Electric Services
15 16 17 15 16 19
C.THIRD D.FOURTH
c (specify)
(
7 specify)
7
15 16 17 15 18 19
VIII. OPERATOR INFORMATION B.Is the name listed in Item
A.NAME
VIII-A also the owner?
C Duke Energy Carolinas, LLC
ti ® YES [:]NO
18 1 19
C.STATUS OF OPERATOR Enter the gppropriate letter into the answer box;if'Other's ci D.PHONE area codeno.
F=FEDERAL M=PUBLIC(other than federal or state) P (specify) A 704 875 5894
S=STATE O=OTHER(specify) 15 16 18 19 21 22 25
P=PRIVATE
E.STREET OR PO BOX
526 South Church Street
ss
26 F.CITY OR TOWN G.STATE H.ZIP CODE IX. INDIAN LAND
c Charlotte NC 28201 Is the facility located on Indian lands?
B ❑YES ® NO
15 16 40 42 42 47 51
X. EXISTING ENVIRONMENTAL PERMITS
A.NPDES Discha es to Surface Water D.PSD Air Emissions from Proposed Sources
c T 1 NCO024392 c T °
9 N 9 P
15 16 17 18 30 15 18 17 18 �
B.UIC(Underground In'ection o/Fluids E.OTHER s ci (Specify)
c T , C T ° NC000020-Storm Water 60-04 INDUS- Landfill
9 U 930
15 16 17 18 30 15 16 17 18
C.RCRA Hazardous Wastes E.OTHER s eci (Specify)
c T I NCD 108 706 029 s T ° 08-065-269-Air Permit
9 R 30 it
15 16 17 18 30 15 18 17 18
XI. MAP
Attach to this application a topographic map of the area extending to at least one mile beyond property boundaries. The map must
show the outline of the facility, the location of each of its existing and proposed intake and discharge structures, each of its
hazardous waste treatment, storage, or disposal facilities, and each well where it injects fluids underground. Include all springs,
rivers and other surface water bodies in the map area. See instructions for precise requirements.
XII. NATURE OF BUSINESS rovide a brief descri tion
Steam Electric Generating Facility using Nuclear Fuel.
XIII. CERTIFICATION see instructions
I certify under penalty of law that 1 have personally examined and am familiar with the information submitted in this application and
all attachments and that, based on my inquiry of those persons immediately responsible for obtaining the information contained in
the application, i believe that the information is true, accurate and complete. t am aware that there are significant penalties for
submittin false information, including the ossibili of fine and im risonment. C. DATE SIGNED
A. NAME&OFFICIAL TITLE(type or print) B.SIGN URE
Steven D. Capps, McGuire Nuclear Station g1414
Site Vice President
COMMENTS FOR OFFICIAL USE ONLY
c
C 55
15 1 ---
EPA FORM 3510-1(8-90)

Form Approved:
EPA I.D.NUMBER NCO024392 OMB No.2040-0086
Please print or type in the unshaded areas only. Approval expires 8-31-98
FORM U.S.ENVIRONMENTAL PROTECTION AGENCY
APPLICATION FOR PERMIT TO
ISCHARGE AST
2CEPA EXISTING MANUFACTURING,COMMERCIAL,MINING AND SILV CU TUTRAL OPERATIONS
NPDES Consolidated Permits Program
I Outfall Location
For each outfall,list the latitude and longitude of its location to the nearest 15 seconds and the name of the receiving water.
A. Outfall B. Latitude C. Longitude
Number 1. DEG. 2. MIN 3. SEC 1. DEG. 2. MIN 3. SEC D. Receiving Water(name)
001 35 26 03 80 56 50 Lake Norman
002 35 25 57 80 57 20 Catawba River
004 35 26 03 80 56 50 Lake Norman Via Outfall 001
005 35 25 57 80 57 20 Catawba River
006 Lake Norman/Catawba River via any outfall
Il. Flows,Sources of pollution,and treatment technologies
A Attach a line drawing showing the water flow through the facility. Indicate sources of intake water,operations contributing wastwater to the effluent,
and treatment units labeled to correspond to the most detailed descriptions in Item B. Construct a water balance on the line drawing by showing average
flows between Intakes,operations,treatment units,and outfalls. If a water balance cannot be determined,(e.g.,for certain mining activities),provide a
pictorial description of the nature and amount of any sources of water and any collection or treatment measures.
B. For each outfall,provide a description of: (1) All operations contributing wastewater to the effluent,including process wastewater,sanitary
wastewater,cooling water,and storm water runoff; (2) The average flow contributed by each operation; (3) The treatment received by the wastewater.
Continue on additional sheets if necessary.
1. Outfall No. 2. Operation's)Contributing Flow 3. Treatment
(List) a. Operation list b. Average Flow d. List Codes From
p (list) (including units) c.Description Table 2C-I
001 Once Through Cooling Water 2630 MGD 4-A
Inputs:
Condenser Cooling Water(RC) 2604 MGD Once through cooling water for plant use from
Lake Norman
Low Pressure Service Water(RL) Drawn from RC. Once through component cooling water for
See above Service Building Drawn off of the RC System
Crossover lines
Nuclear Service Water(RN) 25.2 Once through component cooling water for
Reactor and Aux Buildings. From Lake
Norman LLI
Liquid Radwaste(WM) 0.0093 MGD See Outfall 004
Low Level Intake(LLI) 118 MGD Once through cooling water Used during
hottest summer months to meet discharge temp
limit Only used an average of 5 days per
year.
Ventilation Unit Condensate Drain Tank 0.0015 MGD Ventilation Unit condensate from Reactor
(VUCDT) Building ventilation
RN System Back flushing with CA water Variable RN lines are periodically back flushed with CA
water to reduce fouling of piping due to silt/
mud buildup during certain times of the year.
Storm Drains Unknown Stormwater runoff from discharge canal storm
drains. Covered under Stormwater Permit
NCS000020
Page I of 5

CONTINUED FROM PREVIOUS PAGE
1. Outfall No. 2. Operation's)ContributiFlow 3. Treatment
b. Average Flow d. List Codes From
(List) a. Operation(rest) VnckA*V Units) c.Description Table 2C-1
002 Waste Treatment System 0.252 MGD 1-U
Inputs: Waste Treatment Ponds Waste Treatment Ponds for Physical Chemical 2-K
Treatment
Turbine Building Sumps Variable Sumps(2)in Turbine Buildings. See 4-A
supplemental info for inputs into the
sumps.
Floor Drains Variable Floor Drains(various in plant)to WC 2-B
System. See supplemental info for inputs
Water Treatment Room Sump Variable Sump in Water Treatment Room(TB 1-0
Basement)to WC. See supplemental info
for a description of inputs
Demineralizer Regan Waste , Variable Regan Waste From Demineralizers
(sulfuric acid and sodium hydroxide) See
supplemental info for more details
Lab Drains Variable Inputs from Lab Sinks in plant
Steam Generator Blowdown 4. Variable Steam Generator Blowdown at 200 gpm.
See supplemental info for more details.
Wet Lay-up Solutions a Variable Wet Lay-up Solutions(for Steam
Generators) See supplemental info
Closed Cooling Water Systems Variable Closed Cooling Water Systems. Contain
corrosion inhibitors. See supplemental into
for more details.
Landfill Leachate Variable Rainwater runoff to the leachate pond from
the Landfill. Goes to WC.
Oil Water Separators Variable Water from Oil Water Separators in MOC,
OSF,Garage
Standby Shutdown Facility Variable Standby Shutdown Facility Sump
Island Lab Waste . Variable Lab sink discharges from Island Labs
NDE Photographic Waste Variable NDE Photographic Waste(from
Radiography). See Supplemental Info for
more details.
Island HVAC Cooling Towers Variable Discharges from Island HVAC Cooling
Towers. Normally condensate but may
contain some corrosion inhibitors.
Filter Backwash Variable From YF system. See supplemental info
under Outfall 002,Filtered Water System.
Lincoln CT Turbine Blade Wash Variable Lincoln CT Turbine Blade Wash(about
once every 5 years)
Page 2 of 5

CONTINUED FROM PREVIOUS PAGE
1. Outfall No. 2. Operation's)Contributing Flow 3. Treatment
(List) a. Operation(fist) c.Description b. Average Flow d. List Codes From
(including units) Table 2C-1
002 Low Volume Chemical Cleaning Variable Low Volume Chemical Cleaning of Heat
(Continued) Exchangers. Potential of 8,000 gallons to
WC during each outage(max twice a year)
This process is not currently being used.
004 Radwaste System
Inputs: To Waste Monitor Tank .0093 MGD Radioactive waste water releases occur from 4-A
this tank in batch. All radioactive limits per
NRC licensing requirements.
Chemical Volume&Control Tank Variable See supplemental info Outfall 004 24
Waste Evaporator Feed Tank Variable See supplemental info Outfall 004 1 Q
Floor Drain Tank Variable See supplemental info Outfall 004
Hot Lab Sinks Variable See supplemental info Outfall 004
Auxiliary Building Floor&Equipment Drains Variable See supplemental info Outfall 004
Floor and Equipment Sump Variable See supplemental info Outfall 004
Laundry and Hot Shower Tank Variable See supplemental info Outfall 004
Ineore Instrument Room Sump Variable See supplemental info Outfall 004
Auxiliary Floor Drain Tank Variable See supplemental info Outfall 004
Auxiliary Waste Evaporator Feed Tank Variable See supplemental info Outfall 004
005 Waste Water Collection Basin 1.2598 MGD 4-A
Inputs: 1-0
HVAC Unit Drains Variable See supplemental info Outfall 005 I-U
Storm Drains Variable Stormwater runoff from plant/MOC yard drains
and parking lots.
Reverse Osmosis Unit Reject Water 0.216 MGD Reject water from RO system
RC System Un-Watering Variable Un-Watering of the RC during re-fueling
outages. See supplemental info for more
details.
SNSWP Chemical Treatments and Flow .110 MGD When SNSWP Chemical Treatments are
Balances performed the WWCB level is lowed to-5 feet
below overflow and the SNSWP is lowered 4
inches. This is a total flow of about 9 million
gallons per treatment. Historically we have
treated about 5 times per year. Going forward
the plan is treat about the same amount
although there will be fewer Rotenone
treatments(planned 2 times per year.
Hydrothol only treatment 3 times per year.
Filter Water Storage Tank Flushing Variable See supplemental info Outfall 002 under
Filtered Water System. Reject water from the
RO system goes to Outfali 005. Periodic
flushing of the filtered water storage tank to the
W WCB. See Supplemental info under Outfall
002,Filtered Water System for more details.
008 Chemical Cleaning 0 MGD This outfall has never been used,but should the need arise to clean the
Steam Generators this outfall would be utilized.
Official Use Only(effluent guidelines sub-categories)
EPA Form 3510-2C (8-60)
Page 3 of 5

Continued From The Front
C. Except for storm runoff,leaks,or spills,are any of the discharges described in Items II-A or B Intermittent or seasonal?
Yes, Outfalls 002 and 004 are batch releases. LLI usage is seasonal. Some years no
3. Frequency 4. Flow
1. Outfall a. Flow Rate b. Total Volume
a. Days Per b. Months in m d (spedwfth units
Number 2. Operation(s)Contributing Flow(list) Week Per Year
(list) c. Duration
($P��h (sP�ffY 1. Long 2. 1. Long 2.
average) average) Term Maximum Term Maximum
Average Daily Average Daily
001 Low Level Intake 0.035616 1.083 .95 MGD 1.184 MGD .95 MGD 1.184 MGD 24 hrs
'Only operated in summer months to maintain
compliance with dicharge temperature limit.
Operated on average 13 days per year
5 year average)
RN backflush with CA water
Performed about once per year
Ventilation Unit Condensate Drain Tank 0.006 12 0.001607 0.00367 1607 Gals 2580 Gals 16 Days
'Batch release
002 Turbine Building Sumps
Floor Drains
Water Treatment Room Sum
Demineralizer R22en Waste
Lab Drains
Steam Generator Biowdown The frequency and duration of these discharges can not be predicted. The
Wet Lay-up Solutions operation of this equipment and the subsequent releases are based on plant
Closed Cooling Water Systems thermal,hydraulic,environmental and equipment operational conditions.
Landfill Leachate These systems may be drained or taken out of service individually or all
Oil Water Seperators together for routine or non-routine maintenance at various times during the
Standby Shutdown Facility year.
Island Lab Waste
NDE Photographic Waste
Island HVAC Cooling Towers
Filtered Backwash
Lincoln CT Turbine Blade Wash
Low Volume Chemical Cleaning
004 Waste Monitor Tank 0.0113 12 0.0078 0.1764 5207 Gals 5834 Gals 167 Da
ys
Chemical Volume&Control Tank
Waste Evaporator Feed Tank The frequency and duration of these discharges can not be predicted. The
Floor Drain Tank operation of this equipment and the subsequent releases are based on plant
Hot Lab Sinks thermal,hydraulic,environmental and equipment operational conditions.
AuAlary Building Floor&Equipment Drains These systems may be drained or taken out of service individually or all
Floor and Equipment Sump together for routine or non-routine maintenance at various times during the
Laundry and Hot Shower Tank year.
Incore Instrument Room Sump
Auxilary Floor Drain Tank
Auyjlary Waste Evaporator Feed Tank
005 HVAC Unit Drains Unknown-performed on an as needed bases
RCS stem Un-Watering 2.88 1 2.88 12.88 MGD 1 2.88 MGD 5 Days
Filter Water Storage Tank Flushing Periodically based on system performance and plant operating conditions.
Page 4 of 5

III. Production
A. Does an effuent guideline limitation promulgated by EPA under Section 304 of the Clear Water Act apply to your facility?
Yes (complete Item III-B) No(go to Section IV)
B. Are the limitations in the applicable effluent guideline expressed in terms of production(or other measure of operation)?
Yes (complete Item 111-C) No (go to section IV)
C. If you answered"yes"to Item III-B,list the quantity which represents an actual measurement of your level of production,expressed in the terms and units
used in the applicable effluent guideline,and indicate the affected outfalls.
1. Average Daily Production 2. Affected Outfalls(list
a. Quantity Per Day b.Units of Measure c. Operation,Product,Material,etc.(specify) outfall numbers)
NA NA NA NA
IV, Improvements
A. Are you now required by any Federal,State or local authority to meet any implementation schedule for the construction,upgrading or operation of waste
water treatment equipment or practices or any other environmental programs which may affect the discharge described in this applicaiton? This includes,but
is not limited to,permit conditions,administrative or enforcement orders,enforcement compliance schedule letters,stipulations,court orders,and grant or loan
conditions.
Yes(complete the following table) No(go to Item 1V B)
2. Affected Outfalls 4. Final Compliance Date
1. Identification of Condition,Agreement,etc. 3. Brief Description of Project
a. No b. Source of Discharge a. Required b. Projected
NA NA NA NA NA NA
B. OPTIONAL: You many attach additional sheets describing any additional water pollutions control programs(or other environmental projects which may
affect your discharges)you now have underway or which you plan. Indicate whether each program is not underway or planned,and indicate your actual or
planned schedule for construction. a Mark"X"If description of additional control program is attached.
EPA FORM 3510-2C(Rev.2-65)
Page 5 of 5

PLEASE PRINT OR TYPE IN THE UNSHADED AREAS ONLY. You may report some or all of EPA I.D.NUMBER(copy from Item 1 of Form 1)
this information on separate sheets(use the same format)instead of completing these pages. EPA Facility Name:
SEE INSTRUCTIONS NCO024392 McGuire Nuclear Station
OUTFALL NO.
FART
TAKE AND EFFLUENT CHARACTERISTICS(continued from page 3 of Form 2-C) 001 DQ e�
A-You must provide the results of at least one analysis for every pollutant in this table. Complete one table for each outfall. See instructions for additional details.
2.EFFLUENT 3.UNITS 4.INTAKE al
1.POLLUTANT a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
Cdavarbu> of avaiabu) d.NO.OF a.Concert- b.Mass b.NO.OF
(1)Concentration (2)Masa (1)concentration (2)Man (1)Concentration (2)Man ANALYSES tration (1)Concentration (2)Mess ANALYSES
LT-
wnieal oxygen < 2.0 < 41725.0 1 mgA lb/Day < 2 < 43894.42 1
(am failed GGA failed GGA
ical oxygen < 20 c 417250.0 1 mgA lb/Day < 20 < 438944.2 1
(COD)
organic 1.9 39838.8 1
mgA lb/Day 1.9 41509.899 1
-roc)
1.Total susparwad 13 271212.5 1 mg/l lb/Day < 5 < 109236.05 1
( )
Ammonia(as M 0.038 792.8 1 mgA b/Day 0.08 1223.44376 1
Flow VALUE VALUE VALUE VALUE
25M 2500 1825 MGD WA 2618 1825
I.Tenperadre VALUE VALUE VALUE VALUE
1 1 DEGREES CELSIUS 14 1
i.Temperature VALUE VALUE VALUE VALUE
summer) 1 DEGREES CELSIUS 1
pH MINIMUM MAXIMUM MINIMUM MAXIMUM
8. 1 STANDARD UNITS 7.35
ART B-Mark"X"in column 2a for each pollutant you know or have reason to believe is present.Mark"X"in column 2b for each pollutant you believe to be absent.If you mark column 2a for any
pollutant which is limited either directly or indirectly but expressly in an effluent limitations guideline,you must provide the results of at least one analysis for that pollutant.For other pollutants
for which you mark Column 2a,you must provide quantitative data or an explanation of their presence in your discharge.Complete one table for each outfall.See the instructions
for additional details and requirements.
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
D CAS NO. sw rad a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
revaiable) a.pre- b.ab- (davaeabte) INsvaiutlle) d.NO.OF a.Goner- b.Mass b.NO.OF
sent sent (1)Concentration (2)Men (1)Concentration (2)Mess (1)Concentration (2)Mas ANALYSES tratbn (1)Concentration (2)Mess ANALYSES
a.Bromide X < 0.10 < 2086.3 1 mgA b/Day < 0.10 < 2184.721 1
[4m"T-Q)ns. X < 0.05 < 1043.1 1 mg/I b/Day < 0.05 < 1092.3605 1
I
X 5.00 WA WA WA 1 Std.units WA 15.00 WA 1
X 1.00 WA WA WA 1 CokxYes WA < 1.00 WA 1
/100 ml
de X < 0.10 < 2086.3 1 m9A b/Day < 0.10 < 2184.721 1
- X 0.23 4798.4 1 mgA b/Day 0.22 4718.99736 1
s Fq --
EPA Form 3610-2C(Rev.246) PAGE V-1 CONTINUE ON PAGE V-2

EPA I.O.NUMBER(copyfrom Mem 1 of Form 1) OUTFALL NUMBER
I Qui mcrsuireNti oarQ#�fl
2.MARK'P (optional)
D CAS NO. e.e.yee a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
eYa a) aPre- b•'a (K avalleme) (e avairbb) d.NO.OF a.CMoen- b.Mass b.NO.OF
sam sat (1)coneemmtion (2)Mas (1)conwmrallon (2)Maw (1)conwmrsfim (z)Mas ANALYSES nation (1)Concemstion C2)Mw ANALYSES
onIOrem X 0.22 4589.8 1 mgA b/Day 0.19 4150.9699 1
m N)
X < 5.00 < 104312.5 1 mow b/Day < 5.00 < 109238.05 1
a P).Total X 0.012 250.4 1 nVA b/Day 0.01 174.77788 1
14-0)
Ww
)A X < 5.00 WA WA WA 1 pCiA WA < 5.00 WA 1
BOW
4.81 WA WA WA 1 Pon WA 1.74 WA 1
otaI X < 1.00 WA WA WA 1 pCiA WA < 1.00 WA 1
adkin
.Tow X 0.42 WA WA WA 1 Pco WA < 1.00 WA 1
a SO4) X 3.40 70932.5 1pmgA
lb/Day 3.40 74280.514 1
1490&74 8)
as 8) X < 1.00 < 20882.5 1 b/Day < 1.00 < 21847.21 1
SUM
a sm) X < 2.00 < 41725.0 1b/Day < 2.00 < 43694.42 1
14265.45.3)
Surfactents
X 0.210 4381.1 1 mob/Day < 0.05 < 1092.3605 1
o1u X
9D5) 0.073 1523.0 1 mg/l b/Day 0.099 2162.67379 1
429
out �-34s) X 0.013 271.2 1 moll b/Day 0.014 305.86094 1
44o-
a
aa441 -8) X < 0.050 < 1043.1 1 mon Ib/Day < 0.050 < 1092.3605 1
owl
) X < 0.001 < 20.9 1 mgA b/Day < 0.001 < 21.84721 1
TOW
I\f'y u X 0.088 1835.9 1 m9A &/Day 0.112 2448.88752 1
ofal X 1.700 35486.3 1 moll bA]sy 1.750 38232.6175 1
43446•.x)
ow X < 0,001 < 20.9
4saas-7) 1 rTWn bfDaY < 0.001 < 21.84721 1
43446.5) X 0.010 208.8 1 m9A b/Day 0.012 282.16652 1
Tk%Total
440.31 X < 0.010 < 208,8 1 moll b/Day < 0.010 < 216.4721 1
ow X < 0.005 1 < 104.3 1 MOA &/Day < 0.005 < 108.23805 1
44032-s)
EPA Form 351062C(Rev.2415) PAGE W2 CONTINUE ON PAGE V3

EPA I.D.NUMBER(copyfrom Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE 3 OF FORM 2-C NCO024392 001 McGuire Nuclear Station
ART C-If you are a primary industry and this outfaA contains process wastewater,refer to Table 2c-2 in the instructions to determine which of the GC/MS fractions you must test for.Mark"X"in
column 2-a for all such GC/MS fractions that apply to your industry and for ALL toxic metals,cyanides,and total phenols.If you are not required to mark column 2-a(secondary industries,
nonprocess wastewater outfalls,and nonrequired GC/MS fractions),mark"X"in column 2-b for each pollutant you know or have reason to believe is present.Mark"X"in column 2c for each
pollutant you believe is absent.If you mark column 2a for any pollutant,you must provide the results of at least one analysis for that pollutant.If you mark column 2b for any pollutant,you
must provide the results of at least one analysis for that pollutant if you know or have reason to believe it will be discharged in concentrations of 10 ppb or greater.If you mark column 2b for
acrolein,acxylonifile,2,4 dinitrophenol,or 2-mathyh4,6 dinitrophenol,you must provide the results of at least one analysis for each of these pollutants which you know or have reason to
believe that you discharge in concentrations of 100 ppb or greater.Otherwise,for pollutants for which you mark column 2b,you must either submit at least one analysis or briefly describe the
reasons the pollutant is expected to be discharged.Note that there are 7 pages to this part;please review each carefully.Complete one table(all 7 pages)for each outfall.See instructions
for additional details and requirements.
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(opt onal
D CAS NO. are- I Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C.LONGTERM AVG.VALUE a.LONG TERM AVG.VALUE
s avatiable) qur- b.pm- c.ab- I IN avaMable) (ti avauabla) I d.NO.OF a.Concen- b.Mass I d.NO.OF
ad sem sant (1)Concenrnuon (2)Maas (1)concentmuon (2)Mass 1)concentration (2)Masa ANALYSES tratkm (t)Concenration (2)Mus ANALYSE
METALS,CYANIDE,AND TOTAL PHENOLS
M.Antimony. X < 1 < 20.86 1 ugA Ib/Day < 1 < 21.85 1
oral(7440-360)
Arsenic,Total X < 1 < 20,86 1 u9A Ib/Day < 1 c 21.85 1
440 362)
BerYk-. X < 1 < 20.86 1 ugA Ib/Day < 1 < 21.85 1
oW(7440.41-7)
CadrNum. X < 0.1 < 2.09 1 ugA Ib/Day < 0.1 < 2.18 1
oW 440.43A)
Chmmkm, X < 1 < 20.86 1 u9A b/Day < 1 < 21.85 1
oW(74/0-47-3)
Copper.Total X < 0.005 < 104.31 1 M9A blDay < 0,005 < 109.24 1
444s4a>
LOW,Total X < t < 20,86 1 ugA b/Day < 1 < 21.85 1
43tia2-1)
Merowy,TOW X < � 5 < 1.04 1 ugA b/Day < 0.05 < 1.09 1
¢97e1
Pa".TOW X < 1 < 20.86 1 ugA b/Day It 1 < 21.85 1
440-oz-0►
OM.selenium, X < 1 < 20.86 1 ugA b(Day < 1 < 21.85 1
etal(778249-2)
144.Suver,Taal X < 1 < 20,86 1 ugA b/Day < 1 < 21.85 1
444224)
2M.TAaaun. X - 0.00049 10.2 1 m9A blDay < 0.0002 < 4.37 1
eel
(?4410-15-0)
3M.2iw.TOW X 0.006 125.18 1 mgA b/Day < 0.005 < 109.24 1
440-06 6)
4M.Cyanma, X < 0.010 < 208.63 1 mgA blDay < 0.010 < 218.47 1
Total(S7.12-5)
SM.Prwrwts, X c 0.005 1 < 104.3 1 MVA b/Day < 0.005 < 109.24 1
ffrotw
TOXIN
E
DESCRIBE RESULTS
P X c 0.480 < 9598.8 1 pgA b(Day < 0.347 < 7580.96 14)
EPA Form 351420(Rev.245) PAGE V-3 CONTINUE ON PAGE V4

EPA I.D.NUMBER(omfrom Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-3 NCO024392 001 McGuire Nuclear Station
1.POLLUTANT 2.MARK*X* 3.EFFLUENT 4.UNITS 5.INTAKE o tiorlal
D CAS NO. e.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
e,rgsbis) qrr- b.PM- c.ab- (N smuble) (a availabis) d.NO.OF a.Concen- b.Maas d.NO.OF
ed sanl aerM (,) (2)M� (1) „ (21 Mass (1)Con�rwrat on (2)Mass ANALYSES 11at)on (,)Corwentratiaf (2)Mass ANALYSES
CIMS FRACTION-VOLATILE COMPOUNDS
< 104.31 1 ugA b1Day < 5 < 109.24 1
IV.Aeroieln X < 5
107-32-1)
< S < 104.31 1 ugA bA)ay < S < 109.24
AaOorft. X
107-13-1) b/Day -. 2 < 43.69 1
V.Benans x < 2 c 41.73
143.2)
.Bis(Clroro-
EWw X
542416-1) 1 ugA bADay < 2 < 43.69 1
.oro"fam X < 2 < 41.73
&25.2)
.Cwbon
obadlimms X < 2 < 41.73 1 ugll bA]ay < 43.89 1
2 <
56.23.5)
.Ctftmber m* X < 2 < 41.73 1 ugA bA)ay < 2 < 43.69 1
106-90.7)
CMorod 1 u9A bMay < 2 < 43.69 1
X < 2 < 41.73
124-48-1) 1 ugA bMay < 2 < 43.69 1
Ch OWI" X < 2 < 41.73
3
OV.2-Chbro-
Eem X c S < 104.31 1 ugA b/Day < 5 < 109.24 1
1,0.76-3)
,V.Chkroferm x < 2 < 41.73 1 ugA b/Day < 2 < 43.69 1
7-W3)
2V.Dkhlorc-
X [ 2 < 41.73 1 ugA b/Day < 2 < 43.69 1
5.27-4
13V.DkWro-
X < 2 < 41.73 1 ugA b/Day c 2 < 43.69 1
aV,,14)khWo- X c 2 < 41.73 1 tv b/Oay < 2 < 43.89 1
5343) 1 ugA b/Day < 2 < 43.69 1
16V 1.24 knkro. X < 2 < 41.73
(107 1 uqA bfDay < 2 < 43.69 1
6V.1.14AChWo- X < 2 < 41.73
(75-3&4)
7V 124YA*kro- X < 2 < 41.73 1 ugA &/Day < 2 < 43.69 1
7-3)
6v,,3-akWoro- X < 2 < 41.73 1 ugA b/Day < 2 < 43.69 1
(542-76-0)
VV.Eny �xebe X e 2 < 41.73 1 ugA &/Day < 2 < 43.89 1
le.
100,41.4)
mwro X < 2 < 41.T3 1 ugA b/Day e 43.89 1
2 <
IV.mwdo X < 2 < 41.73 1 ugA b/Day < 43.69 1
2 <
(74-67-3)
EPA Fo3610.20(Rev.2.65) PAGE V-4 CONTINUE ON PAGE V3
rm

EPA 1.D.NUMBER(copy from nem 1 of Form 1) OUTFALL NUMBER
NCO024392 001 McGuire Nuclear Station
CONTINUED FROM PAGE V-4 4.UNITS 5.INTAKE(optional)
1.POLLUTANT 2.MARK"X" 3.EFFLUENT �LONG TERM AVG.VALUED CAS NO. are- BWWwed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C LOrNeG RM AVG.VALUE d.NO.OF a.Corn- b.Masad.N0.OF
avai e) �- b.pn- O.ab- ww mm) AAess ANALYSES
ed soot sent (tj COncerraation (2)r�hse (1)Conoenbrelbn (Z)Mese (t)conewwation (2)AAeuANALY5ES uatfbn Concentrebfon (2)
IMS FRACTION-VOLATILE COMPOUNDS continued 1 ugA b/Day < 2 ` 43.89 1
Mme X c 2 < 41.73
(f509.2)
V.1•1.2,2-Taut 1 ugA b/Day < 2 < 43.89 1
X < 2 < 41.73
34 ugA bb/Day < 2 < 43.89
1 1
ay.Tevadibro- X < 2 < 41.73
(t27-t84) 1 ugA bA)ay < 2 < 43.89 1
Tokmw X c 2 < 41.73
tobaa s)
.t,2-Trw- 1 rugAb/Day < 2 X < 2 < 41.731 b/Day < 2 < 43.89 1
X < 2 < 41.73
t S58)
ay.t,1 2-Tr4 1 ugA b/Day < 2 < 43.69 i
X < 2 < 41.73
1 broay < 2 < 43.69 1
Tdchbao- X < 2
V"1-m1 bb/Day c 2 < 43.69
X < 2 1
7 < 41.73
1 bb/Day
Vfrryl < 2 < 43.89 1
1V.
X < 2 < 41.n
Dods(7501-4)
"I,""",,,"",',,,"I'l""I'll""I'll'll""I'll""I'll",'ll""I'll,'ll""I'll""I'll",,'ll""IlI J------------
/MS,FRACTION-ACID COMPOUNDS 1 uyl b/Dsy < t0 ` 21847 1
A.2.04WOO-W X < 10 < 208.63
1 ugA bb/Day < 10 < 218.47 1
Z44)khW*- X < 10 < 208.83
(120-03.2) 1 ugA bA)ay < 10 < 218.47 1
2.4-Dinod* X c 10 < 208.63
(10647-9) U911 blDay < 10 < 218.47 1
4o-0bNOo4 X c-1 0 < 208.63
(5s4-02-1) 1 bb/Day < 81 < 1114.21 1
2.44>Akro- X < 50 < 1043.13
(St-2a� 1 ugA lb/Day s 10 < 218.47 1
2 Neioprwnob X < 10 < 208.83
W75-5) 1 ugA b/Day < 10 < 218.47 1
A,444*Whonob X < 10 < 208.83
100-02-7) 1 ,pA b/Day < 10 < 218.47 1
P-0hbro-hF X c 10 < 208.83
(W50-7) 1 u9A bA)ay < 10 < 218.41 1
PeMadowc- X < 10 < 208.63
(e7-" 1 ugA b/Day < 10 < 218.47 1
Qk Phenol X c 10 < 208.83
106-96.2)
IA.2.4.646- 1 ugA b/Day < 10 < 218.47 1
X � 10 < 208.63
Ba-08.2) CONTINUE ON PAGE V-0
PAGE V-5
EPA Form 3510-20(Rev.2415)

EPA I.D.NUMBER(oopyfrom lam t of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-5 NCO024392 001 McGuire Nuclear Station
1.POLLUTANT 12.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(options
D CAS NO, e.nF I eewvad A.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
ra&%We) qulr b.pro- c.ab (NavalhWa (itavaiebb) d.NO.OF a.Conan b.Maas d.N]YSE
ed sam sem (1)Calanbtli0n (2)Yass (1)Cloombs" (2)Mass (1)Concamr ion (2)Max ANALYSES Nation (1)Concenaason (2)Mess ANA
C/MS FRACTION-BASE NEUTRAL COMPOUNDS
B.AmwphVmw X < 10 < 208,83 1 U911 DIDay < 10 < 218.47
83 32-9)
9.Aoanaphlo- X < 10 -< 205.63 1
20696•x) ugA Ib/Day < 10 c 218.47 1
Ard reane X t 10 < 208.63
12x12-7) 1 "88aY < 10 < 218.47 1
8arviAna X t 100 < 2088.25 1 ugA b/Day < 100 < 2184.72 1
Benso(a)
X < 10 < 208.63 1 U9A b/Day < 10 < 218.47 1
Benso(a) X < 10 < 206,63 1 ug/I b/Day < 10 < 218.47 1
(50-32-8)
X c 10 < 208.63 1 u9A b/Day < 10 < 218.47 1
os-99-2)
.B.-am X < 10 < 208.63 1 UgA May < 10 < 218.47 1
(191-24•Z)
Benso(k)
7 9) X c 10 < 208.63 1 UP May t 10 c 218.47 1
-08-
OB.Bis(2CNoro-
oxy0 Meawn X t 10 < 208.83
t t t-91.1) 1 uqA b/DeY < 10 < 218.47 1
18.Bb(2CNoro-
E6rsr X < 10 < 208,63 1 u9A Ib/Day < 10 <
111-44 218.47 1
.4)
26 ft(2-CN«aao-
E9nr X t 10 < 208.63 1 UgA bA)ay t 10 < 218.47 1
t09.eo-t)
315.Bb(rayl.
1naPhOmWe X < 10 < 208.63 1 U9A b/Day < 10 < 218.47 1
71
19.4-a�ano-
p1mr X < 10 < 206,63
(10745-9) 1 UgA b/Day < 10 < 218.47 1
6B BUM BWO X c 10 < 208,63 1
(88.88.7) ugA b/Day < 10 < 218.47 1
68.2CM0ro
X t 10 < 208,63 1 ug/I b/Day < 10 < 218.47 1
t.s6-n
78.4•Chbro-
Marts X t 10 < 208,83 1 UgA b/DaY t /0 < 218.47 1
(7005-72.3)
6B.Chrysene X < 10 < 208.63 1 UgA b/Day < 10 A218.471
1601
98.Dbarao(a.h)
X t 10 < 208,83
�.70.g) 1 USIA b/Day t 10 1.24NCeoro- X c 2 < 41.73 1 ugA May a 2 X < 2 c 41.73
i � M A)ay < 2
EPA Form 3610.20(Rev.2.85) PAGE V-6 CONTINUE ON PAGE V-7

EPA I.D.NUMBER(Copy from Rom 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-6 INI:UUL4;j UUl McUulr@ IVUCI®ar,Lanon
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(o tlonal
D CAS NO. an aeft ed a.MAXIMUMC. a.L L
Havailable) qulr- b.pw c.ob- I Ofevebbie) (Hev.11eble) d.NO.OF a.Concen- b.Mass d.NO.OF
ed sent aunt (1)ConcentrN on (2)mass (1)cono.nwnon (2)man (l)Concenketion (2)mass ANALYSES ItaWn 11.1 comm - (2)mass ANALYSES
CIMS FRACTION-BASE/NEUTRAL COMPOUNDS continued
1.4-Dkbkro- X c 2 < 41.73 1 U911 b/Day -c 2 < 43.89 1
(10546-7)
3.3-0khkro-
X c 10 < 208,83 1 ugA b/Day -Z-1 0 < 218.47 1
et44-1)
4a.Olew
e X c 10 < 208.83 1 ugA blDay a 10 < 218.47 1
81-08 2)
Sas DYnMry1
X < 10 < 208.63 1 U9A b/Day < 10 < 218.47 1
131-11-3)
.Di-fFBulyl
X < 10 < 208.63 1 ugA b/Day < 10 < 218.47 1
84-74,2)
.2.4431000- X < 10 < 208.63 1 u9A b/Day < 10 < 218.47 1
(121-14.2)
2.6)kAm- X < 10 < 208,83 1 ugA b/Day < 10 < 218.47 1
20.2)
Oi-►FOcryl
X < 10 < 208.83 1 ugA b/Day < 10 < 218.47 1
t t 7dM0)
.1.2-Djphwn+
(as Aso- X < 10 < 208.83 1 u9A May < 10 < 218.47 1
(122667)
t6.FItiamlww X < 10 < 208.63 1 UP b/Day < /0 < 218.47 1
Obs4-D)
a.Fluorerw X c 10 c 208.83 1 ugA b/Day < 10 < 218.47 1
8673-7)
Ne ocillm X < 10 < 208.63 1 ug/I PUB-y- < 10 < 218.47 1
(11674.1)
a.Flex►
X < 10 < 208,83 1 u9A b/Day < 10 < 218.47 1
7-x63)
X e 10 < 208.63 1 ugA b/Day < 10 < 218.47 1
Flexed*xo- X c 10 < 208.63 1 ugA b/Day < 10 < 218.47 1
(67-72-1)
78.Indww
12.3-0 Pyrene X < 10 < 208.63 1 ugA blDay < 10 < 218.47 1
IDS'"
Isoplwrone X < 10 < 208.63 1 u9A 064 < 10 < 218.47 1
1)
N%**WA-w X < 10 < 208.63 1 ugA b/Day < 10 < 218.47 1
91.203)
rakabemNw X < 10 < 208.63 1 u9A b/Day < 10 < 218.47 1
19.N-Nlro-
X < 10 < 208.63 1 ugA blDay < 10 < 218.47 1
8.N-Nemo F
t141,14)141,14) X < 10 < 208.63 1 u9A b/Day < 10 < 218.47 1
EPA Form 35162C(Rev.245) PAGE V-7 CONTINUE ON PAGE V-0

EPA I.D.NUMBER(oopyfrom item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-7 NCO024392 001 McGuire Nuclear Station
fC/MS
POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE al)
ND CAS NO. a.nr Bs4wad a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE LONG TERM AVG.VALUE
b'pw daatnsasl („+ w) d.NO.OF a.Corlcr> b.Mass d.NO.OFsd '."t Bard (1)CoroconCOMP bn (2)Mau 0)Corw�wbwon f21 + (1)Co�Mr+ua+ (2)Mau ANALYSES 1rawn m Cwcormation (2)Mus ANALYSES FRACTION-BASEAVEUTRAL COMPOUNDS continued
N-Nbo-
X < 10 < 208,83 1 ugA
b/Day < 10 < 218.47 1
PMnanuwam X < 10 < 208.83 1 ugA lb/Day < 10
6 < 218.47 1
6-01-6)
%rsna X < 10 < 208.83
724.60.0 1 UgA Ib/Day < 10 < 216.47 1
.1,2.4-TA-
XL1 < 2 < 41.73
120-62.1) i UP WDaY < 2 < 43.89 1
C/MS FRACTION-PESTICIDES
P.Adrin X < 0.05 <
30"0.2) ugA b/Day < 0.05
P.&WWBHC X < 0.05 <
3144146) u9A b/Day < 0.05
bot"HC X < 0.05 <
15657) ugA b/Day < 0.05
9ma-aHC X < 0.05 < ug/I May < 0.05
58-&4)-
aslt�orlc X < 0.05 < u9A N)/Day < 0.05
14668)
P.Chardww X < 0.5 <
57-74-4) ugA Ib/Day < 0.5
.4,4'- x < 0.05
50.24-y)) < ugA b/Day -4-0,06
P.4.4'-DDE X < 0.05 <
-56.9 ugA b/Day < 0.05
.4,4'-ODO X < 0.05 < USIAbA)ay < 0.05
-4-6)
OP.D MM X < 0.05 < u911 Ib/Day < 0.05
-1)
1P.aWwEndosufhn X < 0.05 < u9/1 b/Da < 0.05
116$4.7) Y
2P.bWfEndostMan X < 0.05 <
115,267) u9A bfDaY < 0.05
3P.EndosuUsn
mme X < 0.05 <
1031-07.6 ugA b/Day < 0.05
4P Endrin X < 0.05 <
-20.6) ugA b/Day < 0.05
SP.En*fn
X <
421.431) 0.05 < LigA b/Day < 0.05
6P.Hepbwhlw X s 0.05 < U9A b/Day < 0.05
EPA Form 3610-2C(Rev.2.86) PAGE V-8 CONTINUE ON PAGE V-B

EPA I.D.NUMBER(copy from Item 1 of Farm 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-8 NCO024392 001 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
D CAS NO. a.rr I Oa9aved a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
0-1") guir- b.pre- 0•� (h"aw"s) Cdavalsm) d.NO.OF a.Conan- b.Mass d.NO.OF
ed aad aanl (1)cwmrftson (2)Mass (1)conarnra9on (2)Mau (1)Cion (2)Maas ANALYSES bation (1)cw wwation (z)Maas ANALYSES
CIMS FRACTION-PESTICIDES Continued
7P.hNpladYor
X < 0.05 u911 Ib/Day < 0.05
1024.57-3)
OR PCS-1242 X < 0.5 <
ugA array < o.s
5345621-9)
9P.Pca-1254 X < 0.5 < ugA b1Day < 0.5
11097-061)
PCB-1221 X < 0.5 < ugA b/Day < 0.5
11104262)
1P.PC&1232 X < 0.5 < ugA b/Day < 0.5
11141-1"
P.PCO-1248 X < 0.5 <
ugA b/Day < 0.5
12572-2941)
P.PCB-1200 X s 0.5 < u9A b/Day -c 0.5
1109652
.PCs-1016 X 4 0.5 <
ugA b/Day < 0.5
12674-11-2)
.Toxop is 0 X < 0.5 < ugA b/Day < 0.5
6001-35.2)
EPA Form 3610.20(Rev.2.65) PAGE V-9

PLEASE PRINT OR TYPE IN THE UNSHADED AREAS ONLY. You may report some or all of EPA I.D.NUMBER(copy from Item 1 of Form 1)
this information on separate sheets(use the same format)instead of completing these pages. EPA Facility Name:
SEE INSTRUCTIONS NCO024392 McGuire Nuclear Station
OUTFALL N
V. INTAKE AND EFFLUENT CHARACTERISTICS(continued from page 3 of Form 2-C) 002
PART A-You must provide the results of at least one analysis for every pollutant in this table. Complete one table for each outfall. See instructions for additional details.
2.EFFLUENT 3. UNITS 4. INTAKE(optional)
1.POLLUTANT a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c. LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(itavailable) (if available) d.NO.OF a.Concern- b.Mass b.NO.OF
(1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
a.Biochemical Oxygen 4.9 0 16.4 0 0.0 0 0.0 1 mg/I Ib/Day 0
Demand(BOD) failed GGA
Chemical Oxygen < 20 < 66.8 0 0.0 0 0.0 1 mg/I Ib/Day 0
Demand(COD)
Total Organic 2.9 0 9.7 0 0.0 0 0.0 1 mg/I Ib/Day 0
arbon(TOC)
Total Suspended 6.3 0 21.0 0 0.0 0 0.0 1 mg/I Ib/Day 0
Solids(TSS)
e.Ammonia(as N) 7.90 0 26.4 0 0.0 0 0.0 1 mg/I Ib/Day 0
Flow VALUE VALUE VALUE VALUE
0.4 0.589 0.252 1825 MGD N/A
g.Temperature VALUE VALUE VALUE VALUE
winter) 1 DEGREES CELSIUS
i.Temperature VALUE VALUE VALUE VALUE
summer) 1 DEGREES CELSIUS
.pH MINIMUM MAXIMUM MINIMUM MAXIMUM
1 STANDARD UNITS
PART B-Mark"X"in column 2a for each pollutant you know or have reason to believe is present. Mark"X"in column 2b for each pollutant you believe to be absent.If you mark column 2a for any
pollutant which is limited either directly or indirectly but expressly in an effluent limitations guideline,you must provide the results of at least one analysis for that pollutant.For other pollutants
for which you mark column 2a,you must provide quantitative data or an explanation of their presence in your discharge.Complete one table for each outfall.See the instructions
for additional details and requirements.
1.POLLUTANT 2.MARK°x' 3. EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) a.pre- b-ab- (if available) (if available) d.NO.OF a.Concen- b.Mass b. NO.OF
sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
a.Bromide X < 0.10 < 0.3 0 0.0 0 0.0 1 mg/I Ib/Day 0
24959-67-9)
o Chlorine, X < 0.05 < 0.2 0 0.0 0 0.0 1 mg/I Ib/Day 0
Total Residual
Color X 5.00 N/A N/A N/A 1 Std.Units N/A N/A
J.Fecal X 1.00 N/A N/A N/A 1 Colonies N/A N/A
oliform /100 ml
Fluoride X < 0.10 < 0.3 0 0.0 0 0.0 1 mg/I Ib/Day 0
16964-48-8)
Nitrate- X 1.00 0 3.3 0 0.0 0 0.0 1 mg/I Ib/Day 0

htnte(as N) _
EPA Form 3510-2C(Rev.2-85) PAGE V-1 CONTINUE ON PAGE V-2
EPA I.D. NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
ITEM V-B CONTINUED FROM FRONT NCO024392 002 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) a.pre- b.ab- (if available) (if available) d.NO.OF a.Concen- b.Mass b.NO.OF
sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
.Nitrogen,
otal Organic X 9.00 0 30.0 0 0.0 0 0.0 1 mg/I Ib/Day 0
as N)
Oil and
rease X < 5.00 < 16.7 0 0.0 0 0.0 1 mg/I Ib/Day 0
Phosphorous
as P),Total X 0.04 0 0.1 0 0.0 0 0.0 1 mg/I Ib/Day 0
7723-14-0)
.Radioactivity
1)Alpha,
Total X < 5.00 NIA N/A N/A 1
pCi/I N/A N/A
2)Beta,
Total X 3.72 N/A N/A N/A 1 pCi/I N/A N/A
3)Radium,
Total X <,> 1.00 NIA N/A N/A 1 pCi/I N/A N/A
4)Radium
26,Total X < 1.00 N/A N/A N/A 1
pCiA N/A NIA
Sulfate
as Soo) X 8.80 0 29.4 0 0.0 0 0.0 1 mgA Ib/Day 0
14808-79-8)
Sulfide
as S) X < 1.00 < 3.3 0 0.0 0 0.0 1 mg/1 Ib/Day 0
m.Sulfite
as S03) X < 2.00 < 6.7 0 0.0 0 0.0 1 mgA Ib/Day 0
14265-45-3)
.Surfactants
X 0.840 0 2.8 0 0.0 0 0.0 1 mg/1 Ib/Day 0
.Aluminum,
oral X 0.074 0 0.2 0 0.0 0 0.0 1 mg/1 Ib/Day 0
742&90-5)

p.Barium,
Total X 0.009 0 0.0 0 0.0 0 0.0 1 mg/I Ib/Day 0
7440-39-3)
q.Boron,
Total X < 0.050 < 0.2 0 0.0 0 0.0 1 mg/l Ib/Day 0
7440-42-8)
Cobalt,
Total X < 0.001 < 0.0 0 0.0 0 0.0 1 mg/l Ib/Day 0
7440-48-4)
.Iron,Total
7439-89-6) X 0.167 0 0.6 0 0.0 0 0.0 1 mg/l Ib/Day 0
.Magnesium,
Total X 1.720 0 5.7 0 0.0 0 0.0 1 mg/I Ib/Day 0
7439-95-4)
.Molybdenum,
Total X 0.096 0 0.3 0 0.0 0 0.0 1 mg/I Ib/Day 0
7439-98-7)
.Manganese,
Total �, X 0.049 0 0.2 0 0.0 0 0.0 1 mg/I Ib/Day 0
7439-96-5)
.Tin,Total
7440-31-5) X < 0.010 < 0.0 0 0.0 0 0.0 1 mgA Ib/Day 0
x.Titanium,
Total X < 0.005 < 0.0 0 0.0 0 0.0 1 mg/I Ib/Day 0
7"0-32-6)
EPA Form 3510-2C(Rev.2-85) PAGE V-2 CONTINUE ON PAGE V-3
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE 3 OF FORM 2-C NCO024392 002 McGuire Nuclear Station
PART C-If you are a primary industry and this outfall contains process wastewater,refer to Table 2c-2 in the instructions to determine which of the GC/MS fractions you must test for.Mark"X"in
column 2-a for all such GC/MS fractions that apply to your industry and for ALL toxic metals,cyanides,and total phenols.If you are not required to mark column 2-a(secondary industries,
nonprocess wastewater outfalls,and nonrequired GC/MS fractions),mark"X"in column 2-b for each pollutant you know or have reason to believe is present.Mark"X"in column 2-c for each
pollutant you believe is absent.If you mark column 2a for any pollutant,you must provide the results of at least one analysis for that pollutant.If you mark column 2b for any pollutant,you
must provide the results of at least one analysis for that pollutant if you know or have reason to believe it will be discharged in concentrations of 10 ppb or greater.If you mark column 2b for
acrolein,acrylonitrile,2,4 dinitrophenol,or 2-methyl-4,6 dinitrophenol,you must provide the results of at least one analysis for each of these pollutants which you know or have reason to
believe that you discharge in concentrations of 100 ppb or greater. Otherwise,for pollutants for which you mark column 2b,you must either submit at least one analysis or briefly describe the
reasons the pollutant is expected to be discharged.Note that there are 7 pages to this part;please review each carefully.Complete one table(all 7 pages)for each outfall.See instructions
for additional details and requirements.
1. POLLUTANT 2.MARK"X" 3. EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) quit- b.pre- c.ab- (if available) (d available) d.NO.OF a.Conten- b.Mass d.NO.OF
ed sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration I( )mass Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
METALS,CYANIDE,AND TOTAL PHENOLS
1 M.Antimony. X1 117�7 1 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00

Total(7440-36-0)
M.Arsenic,Total X < 1 < 0.00 0 0.00 0 0.00 1 ug;I Ib/Day 0.00
7440-38-2)
M.Beryllium, X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Total(7440-41-7)
M.Cadmium, X 0.1 0 0.00 0 0.00 0 0 00 1 ug;l Ib/Day 0 00
Total(7440-43-9)
M.Chromium, X < 1 < 0.00 0 0.00 0 0.00 1 ugil Ib/Day 0.00
Total(7440-47-3)
M.Copper,Total X 0.005 0 0.02 0 0.00 0 0 00 1 mg/I Ib/Day 0.00
(7440-50-8)
M Lead,Total X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(7439-92-1)
M.Mercury,Total X < 0.05 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(7439-97-6)
M Nickel,Total X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
7440-02-0)
10M.Selenium, X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Total(778249-2)
11M Silver.Total X < 1 < 0 00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
7440-22-4)
12M.Thallium, X 0-00043 0 0.0 0 0.0 0 0.0 1 mg/I Ib/Day 0.00
Total(7440-28-0)\'
13M Zinc,Total X 0.012 0 0.04 0 0.00 0 0 00 1 mg/I Ib/Day 0.00
(7440-66-6)
14M.Cyanide, X < 0.010 < 0.03 0 0.00 0 0.00 1 mg/I Ib/Day 0.00
Total(57-12-5)
15M.Phenols, X < 0.005 < 0,0 0 0.0 0 0 0 1 mg/I Ib/Day 0 00
Total
DIOXIN
3,7,8 Tetra DESCRIBE RESULTS
hlorodibenzo P X < 0.410 1 < 1.4 0 0.0 0 0.0 1 1 pg/I Ib/Day 0.00
Dioxin(1764-01-6)
EPA Form 3510-2C(Rev.2-85) PAGE V-3 CONTINUE ON PAGE V-4
EPA I.D. NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-3 N00024392 002 McGuire Nuclear Station
1. POLLUTANT 2.MARK"X" 3. EFFLUENT 4. UNITS 5. INTAKE(optional)
AND CAS NO. are- Believed a. MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C. LONG TERM AVG.VALUE a. LONG TERM AVG.VALUE
if available) quir- b.pre- c.ab- (if available) (if available) d. NO.OF a.Concen- b.Mass d.NO.OF
ed sent sent (1)Concentration (2)Mass Im Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-VOLATILE COMPOUNDS
tV.Acrolein X < 5 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0 00
107-02-8)
V.Acrylonit le X < 5 < 0.02 0 0.00 0 0.00 1 ug;I Ib/Day 0 0C
107-13-1)

methyl)Ether X 0 0 0 0
(542-88-1)
5V.Bromoform X < 2 < 0.01 0 0.00 0 000 1 ug/l b/Day 000
(75-25-2)
V Carbon
Tetrachloride X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(56-23-5)
7V.Chlorobenzene X < 2 < 0.01 0 0.00 0 000 1 uc/1 Ib/Day 0.00
(108-90.7)
V.Chlorodi-
bromomethane X < 2 < 0.01 0 0.00 0 0.00 1 ua/1 lb/Day 0.00
(124-48-1)
V.Chloroethane X < 2 < 0.01 0 0.00 0 000 1 ugil Ib/Day 0 00
(75-00-3)
10V.2-Chloro-
thylvinyl Ether X < 5 C.02 0 0.00 0 0.00 1 ug/I Ib/Day coo
(110-75-6)
11V.Chloroform X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0 00
(67-66-3)
12V.Dichloro-
bromomethane X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(75-27-4)
13V.Dichloro-
difluoromethane X < 2 < 0.01 0 0.00 0 0.00 1 ug/l Ib/Day 0 00
(75-71-8)
14V.1,1-Dichloro- X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
thane(75-34-3)
15V.1,2-Dichloro- X < 2 < 0 01 0 0.00 0 0.00 1 ug/l Ib/Day 0 00
thane(107-06-2)
16V.1,1-Dichloro- X < 2 < 0.01 0 0.00 C 000 ug/I Ib/Day 000
ethylene(75-35-4)
17V_1,2-Dichloro- X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
propane(78-87-5)
18V.1,3-Dichloro- X < 2 - 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
propylene(542-75-6)
19V.Ethylbenzene X < 2 < 0.01 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
(100-41-4)
oV.Methyl X 2 0.01 0 0.00 0 0.00 1 ugll Ib/Day 0.00
Bromide(74-83-9)
IV.Methyl X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
hionde(74-87-3)
EPA Form 3510-2C(Rev.2-85) PAGE V-a
CONTINUE ON PAGE V-5
EPA I.D.NUMBER(copy from Item 1 of For 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-4 NCO024392 002 McGuire Nuclear Station
1. POLLUTANT 12.MARK"X" 3.EFFLUENT 7 4. UNITS 5. INTAKE(optional)
AND CAS NO. are- I Believed a.MAXIMUM DAILY VALUE lb.MAXIMUM 30 DAY VALUE 1C.LONG TERM AVG.VALUE I I Ia.LONG TERM AVG.VALUE

(if available) quir- b.pre-�.ab- (if available) (if available) d.NO.OF a.Concen- b.Mass d.NO.OF
led sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass JANALYSES�tration
(1)Concentration (2)Mass JANALYSES
GC/MS FRACTION-VOLATILE COMPOUNDS(continued)
2V.Methylene X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Chloride(75-09.2)
3V.1,1,2,2-Tetra-
chloroethane X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(79-34-5)
4V.Tetrachloro- X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
ethylene(127.18-4)
SV.Toluene X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(108-88-3)
6V.1,2-Trans-
Dichloroethylene X < 2 < 0.01 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
(156-60-5)
7V.1,1,1-Tri-
chloroethane X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
71-55-6)
BV.1,1,2-Tri-
chloroethane X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
79-00-5)
9V.Trichloro- X < 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
thylene(79-01-6)
OV.Thchloro-
uoromethane X
2 < 0.01 0 0.00 0 0.00 1 ugll lb/Day 0.00
75-69-4)
1V.Vinyl X 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Chloride(75-01-4)
GC/MS FRACTION-ACID COMPOUNDS
1A.2-Chlorophenol X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
95-57-8) •
A.2,4-Dichloro- X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
henol(120-83-2)
A.2,4-Dimethyl- X < 10 < 0.03 0 0.00 0 0.00 1 ug/l lb/Day 0.00
henol(105-67-9)
A.4,6-Dinitro-0- X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
resol(534-52-1)
A.2,4-Dinitro- X < $0 < 0.17 0 0.00 0 0.00 1 ug/l lb/Day 0.00
phenol(51-28-5)
A.2-Nitrophenol X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
88-75-5)
A.4-Nitrophenol X =, 10 < 0.03 0 0.00 0 0.00 1 ug/l lb/Day 0.00
100-02-7)
A.P-Chloro-M- X +a;"' 10 < 0.03 0 0.00 0 0.00 1 ug/I lb/Day 0.00
resol(59-50-7)
A.Pentachloro- X < 10 < 0.03 0 0.00 0 0.00 1 ug/l b/Day 0.00
phenol(87-86-5)
1oA.Phenol X < ' 10 < 0.03 0 0.00 0 0.00 1 ugll lb/Day 0.00
(108-95-2)

181A.8 2,4,6-Tri-
hlorophenol X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
( 06-2)
EPA Form 3510-2C(Rev.2-85) PAGE V-5 CONTINUE ON PAGE V-6
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-5 NCO024392 002 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUEC.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(d available) quir- b.pre- c.ab- (ifavailable) (if available) d.NO.OF a.Concen- b.Mass d.NO.OF
ed sent I sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (i)Concentration (2)Mass ANALYSES
GC/MS FRACTION-BASE NEUTRAL COMPOUNDS
1B.Acenaphthene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
83-32-9)
B.Acenaphtylene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
208-96-8)
e.Anthracene X < 10 < 0.03 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
120-12-7)
e.Benzidine X < 100 < 0.33 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(92-87-5)
513.Benzo(a)
Anthracene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(56-553)
e.Benzo(a) X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Pyrene(50-32-8)
6.3,4-Benzo-
uoranthene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(205-99-2) 11
e.Benzo(ghi) X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Perylene(191-24-2)
B.Benzo(k)
Fluoranthene X < 10 < 0.03 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
(207-08-9)
108.Bis(2-Chloro-
thoxyl)Methane X < 10 < 0.03 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
(111-91-1)
11 B.Bis(2-Chloro-
ethyl)Ether X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(111-44-4)
12B.Bis(2-Chloroiso-
propyl)Ether X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(108-60-1)
138.Bis(2-Ethyl-
hexyl)Phthalate X < 10 < 0.03 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
(117-81-7) _
148.4-Bromo-
henyl Phenyl X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00

Ether(101-55-3)
15B.Butyl Benzyl X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Phthalate(85-68-7)
168.2-Chloro-
naphthalene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(91-58-7)
178.4-Chloro-
phenyl Phenyl X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Ether(7005-72-3)
188.Chrysene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(218-01-9)
196.Dibenzo(a,h)
Anthracene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(53-70-3)
06.1,2-Dichloro- X < ' 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
benzene(95-50-1)
16.1,3-Dichloro- X <' 2 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
benzene(541-73-1)
EPA Form 3510-2C(Rev.2-85) PAGE V-6 CONTINUE ON PAGE V-7
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-6 NCO024392 002 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUEC.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(if available) quir- b.pre- c.ab- (if available) (if available) d.NO.OF a.Concen- b.Mass d.NO.OF
ed sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-BASE/NEUTRAL COMPOUNDS(continued)
26.1,4-Dichloro- X < 2 < 0.01 0 0.00 0 0.00 1 Ug/I Ib/Day 0.00
benzene(106-46-7)
3B.3,3-Dichloro-
benzidine X < 10 < 0.03 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
(91-94-1)
4B.Diethyl
Phthalate X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(84-66-2)
5B.Dimethyl
Phthalate X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(131-11-3)
6B.Di-N-Butyl
Phthalate X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(84-74-2)
78.2,4-Dinitro- X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
toluene(121-14-2)
BB.2,6-Dinitro- X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
toluene(606-20-2)
9B.Di-N-Octyl
Phthalate X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(117-84-0)

OB.1,2-Diphenyl-
hydrazine(as Azo- X < 10 < 0.03 0 0.00 D 0.00 1 ug/I Ib/Day 0.00
benzene)(122-66-7)
1B.Fluoranthene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(2064-0)
2B.Fluorene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(86-73.7)
33B.Hexachloro- X < 10 < 0.03 0 0.00 0 0.00 1 Ug/I Ib/Day 0.00
benzene(118-74-1)
B.Hexa-
hlorobutadiene X < 10 < 0.03 0 0.00 0 0.00 1 Ug/I Ib/Day 0.00
(87-68-3)
5B.Hexachloro-
yclopentadiene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
77-47-4)
36B.Hexachloro- X < 10 < 0.03 0 000 0 0.00 1 ug/I Ib/Day 0.00
thane(67-72-1)
378.Indeno
(1,2,3-cd)Pyrene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(193-39-5)
8B.Isophorone X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(78-59-1)
9B.Naphthalene X < 10 < 0.03 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
(91-20-3)
OB.Nitrobenzene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(98-95-3)
1 B.N-Nitro-
sodimethylamine X < 10 < 0.03 0 0.00 0 0.00 1 Ug/I Ib/Day 0.00
(62-75-9)
2B.N-Nitrosodi-
N-Propylamine X < 10 < 0.03 0 0.00 0 0.00 1 ug/l lb/Day 0.00
621-64-7)
EPA Form 3510-2C(Rev.2-85) PAGE V-7 CONTINUE ON PAGE V-8
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-7 NCO024392 002 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
AND CAS NO. a.re- Beliednt
a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(if available) quir- b.pre- (if available) (if available) d.NO.OF a.Concen- b.Mass d.NO.OF
ed sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-BASE/NEUTRAL COMPOUNDS(continued)
3B.N-Nitro-
sodiphenylamine X < 10 < 0.03 0 0.00 0 0.00 1 Ug/I Ib/Day 0.00
(86-30-6)
4B.Phenanthrene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(85-01-8)
5B.Pyrene X < 10 < 0.03 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(129-00-0)

468,1.2,4-Td-
hlorobenzene X < 2 < 0.01 pro
0.00 0 0.00 1 ugll Ib/Day 0.00
120-82-1)
GC/MS FRACTION-PESTICIDES
1P.Aldrin X < 0.05 < ug/I Ib/Day
(309-00-2)
P.alpha-BHC X < 0.05 < Ug/I lb/Day
319-84-6)
P.beta-BHC X < 0.05 < Ug/I Ib/Day
31585-7)
P.gamma-BHC X < 0.05 < ug/I lb/Day
58-89-9)
P.delta-BHC X < 0.05 < ug/I Ib/Day
(319-86-8)
P.Chlordane X < 0.5 < ug/1 Ib/Day
57-74-9)
P.4,4'-DDT X < 0.05 < Ug/I Ib/Day -
(50-29-3)
P.4,4'-DDE X < 0.05 < ug/I lb/Day
72-559)
P.4,4'-DDD X < 0.05 < ug/I Ib/Day
72-54-8)
10P.Dieldrin X < 0.05 < ug/I lb/Day
(60-57-1)
11 P.alpha-Endosulfan X < 0.05 < ug/I Ib/Day -
11529-7)
12P,beta-Endosulfan X < 0.05 < Ug/I Ib/Day
(11529-7)
13P.Endosulfan
Sulfate X < 0.05 < ug/I Ib/Day
(1031-07-8)
14P.Endrin X < 0.05 < Ug/I Ib/Day
72-20-8)
15P.Endrin
Aldehyde X < 0.05 < Ug/I Ib/Day
(7421-93,-4)
16P.Heptachlor X < 0.05 < Ug/1 Ib/Day
76-44-8)
EPA Form 3510-2C(Rev.2-85) PAGE V-8 CONTINUE ON PAGE V-9
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-8 NCO024392 002 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUEC.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
rfavailable) quir- b.pre- c.ab- (rfavailable) (if available) d.NO.OF a.Concen- b.Mass �d.NO.OF
ed I sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass 1ANALYSES trat ion (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-PESTICIDES(continued)

17P Heptachlor
Epoxide X < 0.05 0 ugll Ib/Day
(1024-57-3)
18P.PCB-1242 X < 0.5 < ug/l Ib/Day
(53469-21-9)
19P.PCB-1254 X < 0.5 <
ug/I lb/Day
(11097-69-1)
OP.PCB-1221 X < 0.5 < ug/l Ib/Day
(11104-28-2)
1P.PCB-1232 X < 0.5 <
ugll Ib/Day
(11141-16-5)
2P.PCB-1248 X < 0.5 - ug/I lb/Day
(12672-29-6)
3P PCB-1260 X < 0.5 ug/l lb/Day
(11096-82-5)
4P.PCB-1016 X < 0.5 < ug/l Ib/Day
(12674-11-2)
SP.Toxaphene X < 0.5 < Ug/l Ib/Day
(8001-35-2)
EPA Form 3510-2C(Rev.2-85) PAGE V-9

PLEASE PRINT OR TYPE IN THE UNSHADED AREAS ONLY. You may report some or all of EPA I.D.NUMBER(copy from Item 1 of Form 1)
this information on separate sheets(use the same format)instead of completing these pages. EPA Facility Name:
SEE INSTRUCTIONS NCO024392 McGuire ear Station
OUTFALL
V. INTAKE AND EFFLUENT CHARACTERISTICS(continued from page 3 of Form 2-C)
PART A-You must provide the results of at least one analysis for every pollutant in this table. Complete one table for each outfall. See instructions for additional details.
2.EFFLUENT 3. UNITS 4. INTAKE(optional)
1.POLLUTANT a. MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(if available) (if available) d.NO.OF a.Concen- b.Mass b. NO.OF
(1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
a.Biochemical Oxygen < 2 < 4.9 0 0.0 0 0.0 1 mg/I Ib/Day 0
Demand(BOD) failed GGA
b.Chemical Oxygen < 20 < 49.2 0 0.0 0 0.0 1 mg/1 Ib/Day 0
Demand(COD)
c.Total Organic 2.7 0 6.6 0 0.0 0 0.0 1 mg/I Ib/Day 0
Carbon(TOC)
d.Total Suspended 1.4 0 3.4 0 0.0 0 0.0 1 mg/I Ib/Day 0
Solids(TSS)
a.Ammonia(as N) 0.07 0 0.2 0 0.0 0 0.0 1 mg/I Ib/Day 0
f.Flow VALUE VALUE VALUE VALUE
0.295 9.141 1.261 1825 MGD N/A
g.Temperature VALUE VALUE VALUE VALUE
(winter) 1 DEGREES CELSIUS
h.Temperature VALUE VALUE VALUE VALUE
(summer) I DEGREES CELSIUS
i.pH MINIMUM IMAXIMUM IMINIMUM MAXIMUM
1 1 STANDARD UNITS
PART B-Mark"X"in column 2a for each pollutant you know or have reason to believe is present.Mark"X"in column 2b for each pollutant you believe to be absent.If you mark column 2a for any
pollutant which is limited either directly or indirectly but expressly in an effluent limitations guideline,you must provide the results of at least one analysis for that pollutant.For other pollutants
for which you mark column 2a,you must provide quantitative data or an explanation of their presence in your discharge.Complete one table for each outfall.See the instructions
for additional details and requirements.
1. POLLUTANT 2.MARK°X' 3. EFFLUENT 4. UNITS 5.INTAKE(optional)
AND CAS NO. Believed a.MAXIMUM DAILY VALUE b. MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(if available) a.pre- b.ab- (if available) (if available) d.NO.OF a.Concen- b.Mass b.NO.OF
sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
a.Bromide X < 0.10 < 0.2 0 0.0 0 0.0 1 mg/1 Ib/Day 0
(24959-67-9)
b.Chlorine, X < 0.05 < 0.1 0 0.0 0 0.0 1 mg/1 Ib/Day 0
Total Residual
c.Color X 10.00 N/A N/A N/A 1 Std.Units N/A N/A
d.Feral X 1.0 N/A N/A N/A 1 Colonies N/A N/A
oliform /100 ml
Fluo de X < 0.10 < 0.2 0 0.0 0 0.0 1 mg/I Ib/Day 0
16984-48-6)
Nitrate- X 0.047 0 0.1 0 0.0 0 0.0 1 mg/I Ib/Day 0

Itnte(as N)
EPA Form 3510-2C(Rev.2-85) PAGE V-1 CONTINUE ON PAGE V-2
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
ITEM V-B CONTINUED FROM FRONT NCO024392 005 McGuire Nuclear Station
1.POLLUTANT 2.MARK X' 3.EFFLUENT 4. UNITS 5. INTAKE(optional)
AND CAS NO. Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
rf available) a.pre- b.ab- (if available) (if available) d. NO.OF a.Concert- b.Mass b.NO.OF
sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
.Nitrogen,
Total Organic X 0.20 0 0.5 0 0.0 0 0.0 1 mg/I Ib/Day 0
as N)
h.Oil and
Grease X < 5.00 < 12.3 0 00 0 0.0 1 mg/I Ib/Day 0
i.Phosphorous
as P),Total X 0.018 0 0.0 0 0.0 0 0.0 1 mg/I Ib/Day 0
7723-14-0)
j. Radioactivity
i)Alpha,
Total X < 5.00 N/A N/A N/A 1
pCi/I N/A N/A
2)Beta,
Total X < 5.00 N/A N/A N/A 1
pCi/I N/A N/A
3)Radium,
Total X < 1.00 N/A N/A N/A 1
pCi/I NIA N/A
4)Radium
26,Total X 2.49 N/A N/A N/A 1 PDA N/A N/A
k.Sulfate
as SO4) X 3.90 0 9.6 0 0.0 0 0.0 1 mg/I Ib/Day 0
14808-79-8)
1.Sulfide
as S) X e 1.00 < 2.5 0 0.0 0 0.0 1 mg/I Ib/Day 0
Sufte
as S03) X < 2.00 < 4.9 0 0.0 0 0.0 1 mg/I Ib/Day 0
14265-45-3)
.Surfactants
X 0.190 0 0.5 0 0.0 0 0.0 1 mg/I Ib/Day 0
.Aluminum,
otal X 0.083 0 0.2 0 0.0 0 0.0 1 mg/I Ib/Day 0 -
7429-90-5)

Barium.
Total X 0.009 0 0.0 0 0.0 0 0.0 1 mg/I IbDay 0
(7440-39-3)
q.Boron,
Total X < 0.050 < 0.1 0 0 0 0 0.0 1 mgt Ib/Day 0
7440-42-8)
r.Cobalt,
Total X < 0.001 < 0.0 0 0 0 0 0.0 1 mg/I Ib/Day 0
7440-4")
s.Iron,Total
7439-89-6) X 0.155 0 0 4 0 0 0 0 00 1 mg/I Ib/Day 0
I
Magnesium,
Total X 2.040 0 5.0 0 0.0 0 0.0 1 mg/I Ib/Day 0
7439-95-4)
Molybdenum,
Total X 0.0038 0 0.0 0 0.0 0 0.0 1 mg'I Ib/Day 0
7439-98-7)
.Manganese,
Total X 0.115 0 0.3 0 0 0 0 0.0 1 mg2,1 Ib/Day C
7439-96-5)
.Tin,Total
7440.31-5) X < 0.010 < 0.0 0 0 0 0 0 0 1 mg'I b/Day C
.Titanium,
Total X < 0.005 < 0.0 0 0.0 0 0 0 1 mg/1 Ib/Day 0
7440-32F)
EPA Forth 3510-2C(Rev.2-85) PAGE V-2 CONTINUE ON PAGE V-3
EPA I.D. NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE 3 OF FORM 2-C NCO024392 005 McGuire Nuclear Station
PART C-If you are a primary industry and this outfall contains process wastewater,refer to Table 2c-2 in the instructions to determine which of the GC/MS fractions you must test for. Mark"X"in
column 2-a for all such GC/MS fractions that apply to your industry and for ALL toxic metals,cyanides,and total phenols. If you are not required to mark column 2-a(secondary industries,
nonprocess wastewater outfalls..and nonrequired GC/MS fractions),mark"X"in column 2-b for each pollutant you know or have reason to believe is present. Mark"X"in column 2-c for each
pollutant you believe is absent. If you mark column 2a for any pollutant,you must provide the results of at least one analysis for that pollutant. If you mark column 2b for any pollutant,you
must provide the results of at least one analysis for that pollutant if you know or have reason to believe it will be discharged in concentrations of 10 ppb or greater. If you mark column 2b for
acrolein,acrylonitrile,2,4 dinitrophenol,or 2-methyl-4,6 dinitrophenol,you must provide the results of at least one analysis for each of these pollutants which you know or have reason to
believe that you discharge in concentrations of 100 ppb or greater.Otherwise,for pollutants for which you mark column 2b,you must either submit at least one analysis or briefly describe the
reasons the pollutant is expected to be discharged.Note that there are 7 pages to this part,please review each carefully.Complete one table(all 7 pages)for each outfall.See instructions
for additional details and requirements.
1.POLLUTANT 2.MARK"X" 3. EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. a re- Believed a. MAXIMUM DAILY VALUE b. MAXIMUM 30 DAY VALUE c. LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) quir- b.pre- c.alb (if available) (if available) d. NO.OF a.Concen- b.Mass d.NO.OF
ed sent sent 0)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration I(1)Concentration (2)Mass ANALYSES
METALS,CYANIDE,AND TOTAL PHENOLS
1 M.Antimony, X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00

Total(7440-36-0)
M.Arsenic,Total X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
7440-38-2)
M.Beryllium, X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Total(7440-41-7)
M.Cadmium, X < 0.1 < 0.00 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
Total(744G-43-9)
M.Chromium, X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Total(7440-47-3)
M.Copper,Total X <; 0.005 < 0.01 0 0.00 0 0.00 1 mg/I Ib/Day 0.00
(7440-50-8)
M.Lead,Total X c_ 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
7439-92-1)
M.Mercury,Total X < 0.05 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
7439-97-6)
M.Nickel,Total X < 1 < 0.00 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
(7440-02-0)
10M.Selenium, X < 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Total(778249-2)
11 M.Silver,Total Xf 1 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(7440-22-4)
12M.Thallium, X < 0.0002 < 0.0 0 0.0 0 0.0 1 mg/l Ib/Day 0.00
Total(7440-28-0)
13M.Zinc,Total X 0.010 0 0.02 0 0.00 0 0.00 1 mg/I Ib/Day 0.00
(7440-66-6)
14M.Cyanide, X <, 0.010 < 0.02 0 0.00 0 0.00 1 mg/I Ib/Day 0.00
Total(57-12-5)
15M.Phenols, X < 0.005 < 0.0 0 0.0 0 0.0 1 mg/I Ib/Day 0.00
Total
DIOXIN
3,7,8 Tetra DESCRIBE RESULTS
hlorodibenzo P X < 0.439 1 < 1.1 0 0.0 0 0.0 1 pg/l Ib/Day 0.00
Dioxin(1764-01-6)
EPA Form 3510-2C(Rev.2-85) PAGE V-3 CONTINUE ON PAGE V-4
EPA I.D.NUMBER(copy from Item 1 of For 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-3 NCO024392 005 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3. EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE C.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) quir- b.pre- c.ab- (if available) (if available) d.NO.OF a.Concen- 1b.Mass d.NO.OF
ed sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-VOLATILE COMPOUNDS
1V.Acrolein X < 5 < 0.01 0 0.00 0 0.00 1 ug/I Ib/Day - 0.00
(107-02-8)
V.Acrylonitr le X < 5 < 0.01 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
107-13-1)

V.Benzene X < 2 < 0.00 0 0 00 0 0 00 1 ug(I Ib,+Day 0.00
(71-43-2)
V.Bis(Chloro-
ethyl)Ether X 0 0 0 0
542-88-1)
v.Bromoforrn X < 2 0 00 0 0.00 0 0.00 1 ug%I IbiDay 0.00
75-25-2)
V.Carbon
etrachlonde X < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
56-23-5)
.Chlorobenzene X < 2 < 0 00 0 0.00 0 0.00 1 ugfl Ib/Day - 0.00
108-90-7)
V.Chlorodi-
romomethane X < 2 < 0.00 0 0 00 0 0.00 1 ug/I Ib-Day 0.00
124-48-1)
V.Chloroethane X < 2 < 0 00 0 0 00 0 0.00 1 ug/I Ib.!Day 0 00
75.00.3)
1 OV.2-Chloro-
thylvinyl Ether X < 5 < 0.01 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
110-75-8)
11 V.Chloroform X < 2 < 0.00 0 0 00 0 0.00 1 ug/I Ib/Day 0.00
67-66-3)
12V.Dichloro-
romomethane X < 2 < 0.00 0 0.00 0 0.00 1 ug'l Ib/Day 0.00
75-27-4)
13V.Dichloro-
difluoromethane X < 2 < 0.00 0 0 00 0 0.00 1 ug/l Ib/Day 0.00
75-71-8)
14V.1,1-Dichloro- X < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
thane(75-34-3)
15V.1,2-Dichloro- X < 2 < 0.00 0 0 00 0 0.00 1 ug/l Ib/Day 0.00
thane(107-06.2)
16V.1,1-Dichloro- X < 2 < 0.00 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
ethylene(75-35-4)
17V.1,2-Dichloro- X < 2 < 0.00 0 0 00 0 0.00 1 ug/I Ib/Day 0.00
propane(78-87-5)
18V.1,3-Dichloro- X < 2 < 0.00 0 0 00 0 0 00 1 ug/I Ib/Day 0.00
propylene(542-75-6)
19V.Ethylbenzene X < 2 - 0 00 0 0 00 0 0.00 1 ug/I Ib/Day 0.00
100-41-4)
oV.Methyl X < 2 - 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Bromide(74.83-9)
iV.Methyl X < 2 < 0.00 0 0.00 0 0.00 1 ug/l b.!Day 0.00
hloride(74-87-3)
EPA Form 3510-2C(Rev.2-85) PAGE V-4 CONTINUE ON PAGE V-5
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER

CONTINUED FROM PAGE V-4 NCO024392 005 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a. LONG TERM AVG.VALUE
if available) quir- b.pre- c.ab- I (if available) (if available) d.NO.OF a.Concen- b.Mass Id.NO.OF
ed sent sent 1(1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-VOLATILE COMPOUNDS(continued)
2V.Methylene X < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Chloride(75-09-2)
3V.1,1,2,2-Tetra-
chloroethane X < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
79-34-5)
4V.Tetrachloro- X 4 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
thylene(127-18-4)
5V.Toluene X < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
106-88-3)
6V.1,2-Trans-
Dichloroethylene X < 2 < 0.00 0 0.00 0 0.00 1 ugA Ib/Day 0.00
156-60-5)
7V.1,1,1-Tri-
hloroethaneX < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
71-55-6)
BV.1,1,2-Th-
hloroethane X < 2 < 0.00 0 0.00 0 0.00 1 ugA Ib/Day 0.00
79-00-5)
9V.Trichloro- x < 2 < 0.00 0 0.00 0 0.00 1 ugA Ib/Day 0.00
Nylene(79-01-6)
OV.Trichloro-
uoromethane X c 2 < 0.00 0 0.00 0 0.00 1 ug/1 Ib/Day - 0.00
75-69-4)
1V.Vinyl X < 2 < 0.00 0 0.00 0 0.00 1 ugA Ib/Day 0.00
hloride(75-01-4)
GC/MS FRACTION-ACID COMPOUNDS
1A.2-Chlorophenol X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
95-57-8)
A.2,4-Dichloro- X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
phenol(120-83-2)
A.2,4-Dimethyl- X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
henol(105-67-9)
A.4,6-Dinitro-0- X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day _ 0.00
resol(534-52-1)
A.2,4-Dinitro- X < 50 < 0.12 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
henol(51-28-5)
A.2-Nitrophenol X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
88-75-5)
A.4-Nitrophenol X - < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day - 0.00
100.02-7)
A.P-Chloro-M- X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day - - 0.00

resol(59-50-7)
A.Pentachloro- X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
henol(87-86-5)
10A.Phenol X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
108-95-2)
11A.2,4,6.Tn-
hlorophenol X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
88-06-2)
EPA Form 3510-2C(Rev.2-85) PAGE V-5 CONTINUE ON PAGE V-6
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-5 NCO024392 005 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. a.re- Believed a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) quir- b.pre- c.ab- (if available) (if available) d.NO.OF a.Concen- �b.Mass d.NO.OF
ed sent sent (t)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-BASE NEUTRAL COMPOUNDS
1 B.Acenaphthene X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
8332-9)
e.Acenaphtylene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
208.96.8)
B.Anthracene X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
120-12-7)
B.Benzidine X < ' 100 < 0.25 0 0.00 0 0.00 1 ugA Ib/Day 0.00
92-87-5)
B.Benzo(a)
Anthracene X -c 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
56-55-3)
B.Benzo(a) X < ' 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
yrene(50-32-8)
8.3,4-Benzo-
uoranthene X t 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
205-99-2)
B,Benzo(ghi) X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
Perylene(191-24-2)
B.Benzo(k)
Fluoranthene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
207-08-9)
10B.Bis(2-Chloro-
thoxyp Methane X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
111-91-1)
11 B.Bis(2-Chloro-
thyl)Ether x < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
12B.Bis(2-Chlorois0-
ropyl)Ether X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00

108-60-1)
13B.Bis(2-Ethyl-
hexyl)Phthalate X < 10 < 0.02 0 0.00 0 0.00 1 ug/I lb/Day a.�} 0.00
117-81-7)
14B.4-Bromo-
henyl Phenyl X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
Ether(101-55-3)
15B.Butyl Benzyl X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
hthalate(85-68-7)
16B.2-Chloro-
aphthalene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
91-58-7)
17B.4-Chloro-
henyl Phenyl X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
ther(7005.72-3)
188.Chrysene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
218.01-9)
19B.Dibenzo(a,h)
Anthracene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
53-70-3)
L.n,ene
-Dchloro, X < 2 < 0.00 0 0.00 0 0.00 1 ug/1 Ib/Day0.00
(95-50-1)chloro- X < 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day0.00
(541-73.1)
EPA Form 3510-2C(Rev.2-85) PAGE V-6 CONTINUE ON PAGE V-7
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-6 NCO024392 005 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3. EFFLUENT 4.UNITS 5. INTAKE(optional)
AND CAS NO. !e-rBelieved a.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
if available) ur- cab- (I available) (ifavailable) d.NO.OF a.Concen- b.Mass d.NO.OF
d sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-BASE/NEUTRAL COMPOUNDS(continued)
28.1,4-Dichloro- X r 2 < 0.00 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
enzene(106-46-7)
313.3,3-Dichloro-
enzidine X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
91-94-1)
413.Diethyl
Phthalate X < 10 < 0.02 0 0.00 0 0.00 1 ug/l Ib/Day 0.00
84-66-2)
58.Dimethyl
hthalateX < 10 < 0.02 0 0.00 0 0.00 1 ug(I Ib/Day 0.00
131-11-3)
6B.Di-N-Butyl
hthalate X < 10 < 0.02 0 0.00 0 0.00 1 ugll IbJDay 0.00

78.2,4-Dinitro- X < 10 < 0.02 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
oluene(121-14-2)
88.2,6-Dinitro- X < 10 < 0.02 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
oluene(606-20-2)
913.Di-N-Octyl
Phthalate X < 10 < 0.02 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
117-84-0)
OB.1,2-Diphenyl-
hydrazine(as Azo- X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day - 0.00
benzene)(122-66-7)
1 B.Fluoranthene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day _ 0.00
206-44-0)
2B.Fluorene X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
86-73-7)
38.Hexachloro- X t 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
enzene(118-74-1)
B.Hexa-
hlorobutadiene X .4 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
87-68-3)
SB.Hexachloro-
yclopentadiene X `< 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
77-47-4)
B.Hexachloro- X < 10 < 0.02 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
thane(67-72-1)
76.Indeno
1,2,3-cd)Pyrene X < 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day 0.00
193-39-5)
BB.Isophorone X �t_, 10 < 0.02 0 0.00 0 0.00 1 ug/1 Ib/Day 0.00
78-59.1)
9B.Naphthalene X <: 10 < 0.02 0 0.00 0 0.00 1 ugA Ib/Day ;,-_i 0.00
91-20-3)
OB.Nitrobenzene X '<. 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 77 77, 0.00
98-95-3)
18.N-Nitro-
odimethylamine X <: 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
L
-9)-Nitrosodi-
pylamine X < O.D2 0 0.00 0 0.00 1 ugfl Ib/Day - 0.00
4-7)
EPA Form 3510-2C(Rev.2-85) PAGE V-7 CONTINUE ON PAGE V-8
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-7 NCO024392 005 McGuire Nuclear Station
1.POLLUTANT 2.MARK"X" 3.EFFLUENT 4.UNITS 5.INTAKE(optional)
AND CAS NO. a.re- �b.p
elietsent (l)
.MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
"rf available) quit- e- (if available) (rf available) d.N0.OF a.Concen- b.Mass d.N0.OF
ad t Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES

GC/MS FRACTION-BASE/NEUTRAL COMPOUNDS(continued)
3B.N-Nitro-
sodiphenylamine X < 10 < 0.02 0 0 00 0 0 00 1 ug;l b/Day 0.00
(86-30-6)
4B Phenanthrene X < 10 < 0.02 0 0.00 0 0.00 1 ug/I Ib/Day 0.00
(85-01-8)
5B.Pyrene X < 10 < 0.02 0 0 00 0 0.00 1 ug`I Ib'Day 0.00
(129-00-0)
6B.1,2,4-Tri-
hlorobenzene X < 2 < 0.00 0 0.00 0 0 110 1 ugIbDay 0 00
(120-82-1)
GC/MS FRACTION-PESTICIDES
I P.Aldrin X < 0.05 - ug/I Ib/Day
309-00-2)
P alpha-BHC X < 0.05 < -gig,I Ib/Day
319-84-6)
P beta-BHC X < 0.05 < ug/I Ib/Day
315-85-7)
P.gamma-BHC X < 0.05 < ugl Ib/Day
(58-89-9)
5P.delta-BHC X < 0.05 < ug/I Ib/Day
319-86-8)
P Chlordane X < 0.5 < ug/1 Ib/Day
57-74-9)
P 4,4'-DDT X < 0.05 < ug/I Ib/Day
50-29-3)
P 4,4'-DDE X < 0.05 - ug/I Ib/Day
72-55-9)
P 4,4'-DDD X < 0.05 < ug/1 Ib/Day
72-54-8)
10P.Dieldrin X < 0.05 < ug/1 Ib/Day
s0-57-1)
11 P.alpha-Endosulfan X < 0.05 < ug/1 Ib/Day
15-29-7)
12P.beta-Endosulfan X < 0.05 < ug/1 Ib/Day
15-29-7)
13P.Endosulfan
Sulfate X < 0.05 < ug,l Ib../Day
(1031-07-8)
14P.Endrin X < 0.05 < ug/1 Ib/Day
(72-20-8)
15P.Endrin
L2 �,3-,,.1),;,j:
X < 0.05 < ugll Ib1Day
X < 0.05 < uql brDay
EPA Form 3510-2C(Rev.2-85) -AGE V-° CONTINUE ON PAGE V-9

,
EPA I.D.NUMBER(copy from Item 1 of Form 1) OUTFALL NUMBER
CONTINUED FROM PAGE V-8 NCO024392 005 McGuire Nuclear Station
1. POLLUTANT 2. MARK"X" 3.EFFLUENT 4. UNITS 5. INTAKE(optional)
AND CAS NO. a.re- Believed a. MAXIMUM DAILY VALUE b.MAXIMUM 30 DAY VALUE c.LONG TERM AVG.VALUE a.LONG TERM AVG.VALUE
(if available) quir- b.pre- c.ab- (if available) (if available) d.NO.OF a.Concen- b.Mass d. NO.OF
ed sent sent (1)Concentration (2)Mass (1)Concentration (2)Mass (1)Concentration (2)Mass ANALYSES tration (1)Concentration (2)Mass ANALYSES
GC/MS FRACTION-PESTICIDES(continued)
17P.Heptachlor
Epoxide X < 0.05 0 ug/I Ib/Day
1024-57-3)
18P.PCB-1242 X < 0.5 < ugfl Ib/Day
(53469-21-9)
19P.PCB-1254 X < 0.5 <
ugll Ib/Day
(11097-69-1)
oP.PCB-1221 X < 0.5 < ug/I Ib/Day
(11104-28-2)
21 P.PCB-1232 X < 0.5 < ug/I Ib/Day
11141-16-5)
2P.PCB-1248 X < 0.5 <
ug/l lb/Day
12672-29-6)
3P,PCB-1260 X < 0.5 < ug/I Ib/Day
11096-82-5)
4P.PCB-1016 X < 0.5 < ug/I Ib/Day
12674-11-2)
SP.Toxaphene X < 0.5 < ug/I Ib/Day
8001-35-2)
EPA Form 3510-2C(Rev_2-85) PAGE V-9

SUPPLEMENTAL INFORMATION
FOR
MCGUIRE NUCLEAR STATION
NPDES PERMIT
# NCO0243 92
Revision 7
7/10/2014
For Use With NPDES Permit Renewal Application 8-2014

r
TABLE OF CONTENTS
OVERVIEW 4
STATION INTAKE 4
Surface Intake 4
Subsurface Intake _. _ 4 _
NUCLEAR SERVICE WATER _ _ 5
Containment Spray Heat Exchangers 5
CONVENTIONAL LOW PRFSSURE SERVICE WATER 6 —
FIRE PROTECTION SYSTEM 6
OUTFALL 001
Condenser Cooling Water 6
Ventilation Unit Condensate Drain Tank(VUCDTl 7
316(al Study and Thermal Variance 8
OUTFALL 002
Water Treatment Room Sump 9
_Filtered Water System _ — 10
Drinking Water System — 10
Demineralized Water System 10
Turbine Building Sumps _ _ 10
Diesel Generator Room_ Sumas 11
Lab Drains 12
Condensate Polisher Backwash 12
Steam Generator Blowdown12
Wet Lam ------ — 13
_Auxiliary Electric Boiler Blowdown _ _ 13
Groundwater Drainage System 13
RC System Unwatering 13
Closed Cooling Systems 14
Sia by Shutdown Facility _ _ 14
e-ss�
Steam Generator Cleaning —__ 14
Miscellaneous System/Comgonent Cleaning 14
Alkaline Boilout Solutions _ __ _ __— _—`-- _ 15 _
_Acid Solutions _---- ----._..._-.. ------ 15
Acid Solution Additives15
EDTA Compounds and HED_TA —�_ _ _— 15
Miscellaneous Compounds _ --- -----------—- -------------- ---- ----- 15 —
�Landfill Leachate_�-___—_---_-�_-_ —_-_ ——__--- 16
McGuire Garage_ ---------------------- --- ___------ 16 -
Page 2 of 24
i

• 1
McGuire Office Complex 16
Nondestructive Examination _ 17
Ice Condenser 18
OUTFALL 003
OUTFALL 004
Floor. Eauiument, and Laundry Drains _ 19
Ventilation Unit Drains _ 19
Chemical Volume and Control System 19
Chemical Treatment in WM System 19
OUTFALL 005
Standby Nuclear Service Water Pond _ 20
Administrative BuildingDrains 20
RC System Unwaterin 21
Filtered Water T 21
HVAC Unit Drains 21
Yard Drains 21
OUTFALL 006 22
APPENDIX 1 -----� �~
Water Use Diagram _ 24
Page 3 of 24

OVERVIEW
McGuire Nuclear Station is a two unit nuclear steam electric generating station. It is owned and
operated by Duke Energy Carolinas LLC . Each unit has a four loop pressurized water reactor.
Reactor fuel consists of uranium oxide pellets clad in zirconium alloy fuel rods. Reactor heat
absorbed by the Reactor Coolant System(primary side)is transferred to four steam generators to
produce steam(secondary side) sufficient enough to drive a turbine generator with a design net
electrical rating of 1180 megawatts.
The nuclear reaction is controlled by control rods and chemical neutron absorption. Boric acid is
used as a chemical neutron absorber and to provide borated water for emergency safety injection.
During reactor operation, changes are made in the reactor coolant boron concentration.
A schematic diagram of water use and waste water discharges for McGuire Nuclear Station is
attached as Appendix 1. It is possible for any of the discharges to contain low levels of
radioactivity. All discharges of radioactivity are regulated by the Nuclear Regulatory
Commission in accordance with 10 CFR Part 20 and 10 CFR Part 50. The following is a brief
description of the major systems.
STATION INTAKE
All water for McGuire Nuclear Station is withdrawn from Lake Norman through a dual intake
system, a surface and a subsurface system. These systems supply the Main Condenser Cooling
Water(RC), Conventional Low Pressure Service Water(RL),Nuclear Service Water(RN),Fire
Protection System (RF/RY),and Containment Ventilation Cooling Water System(RV).
Surface Intake
McGuire Nuclear Station has two power generating units with four Condenser Cooling Water
(RC)pumps per unit. There are two intake screens per pump for a total of l 6 screens. The
intake screens are back washed on an intermittent basis to prevent differential pressure buildup
across the intake screens. The frequency of cleaning is determined by the amount of debris on
the screens. Approximately 8,500 gallons of water is used to backwash each screen. The water
is returned to Lake Norman at the intake bay. The backwash water is raw lake water. No
chemicals are used in the backwash water.
Subsurface Intake
The subsurface intake(Low Level Intake) is located near the bottom of Lake Norman at Cowans
Ford Dam. There are six low-level intake pumps with a capacity of 150,000 GPM each.
Currently only 3 pumps are operational. The Unit 2 pumps have been taken out of service.
During certain times of the year,this system pumps cooler water from the bottom of the lake
(hypolimnion- perpetually colder water in the lower part of the lake) and mixes it with the
warmer water in the surface intake structure during times of high lake surface water
temperatures. At all times of the year,the Low Level Intake(LLI) supplies water to the RV and
RN Systems.
Page 4 of 24

The LLI lines are periodically drained to the Catawba River just below the Cowan's Ford Dam
for inspection.
NUCLEAR SERVICE WATER
The Nuclear Service Water (RN) System is a safety related, once-through, non-contact Cooling
water system. The RN System supplies cooling water to various herat loads in both the primary — 0-)(—
and
0-)(—
and secondary portions of each unit. There are two pumps per unit (four pumps total) that are
capable of delivering 17,500 GPM per pump. The water supply for this system is from Lake
Norman or the Standby Nuclear Service Water Pond (SNSWP). Water from Lake Norman is
supplied by the RC system from the surface intake or by the Low Level Intake (LLI). The
normal source of water is the LLI system. The normal discharge is to Lake Norman through
Outfall 001.
The SNSWP is a 34.9 acre pond designed to provide cooling water for the safe shutdown of the
station in the unlikely event that Lake Norman becomes unavailable. The level in the pond is
maintained,per requirements of the McGuire Nuclear Station Technical Specifications,by
pumping water from Lake Norman into the pond. The pond overflows to the Catawba River via
the Wastewater Collection Basin(WWCB), Outfall 005. The pond also receives storm water
runoff from a drainage area of approximately 100 acres. At times,the RN System is aligned to
take suction from the SNSWP and discharge back to the SNSWP. This recirculation mode is
used for testing purposes of the RN system and flow balances.
As a result of accelerated corrosion of RN System components, some components have corrosion
inhibitors added. Corrosion inhibitors may contain nitrites, borates, carbonates, silicates,
hydroxides,triazoles, and azoles. Low levels of one or more of these corrosion inhibitors would
be discharged at environmentally acceptable levels.
Macrofouling by Corbicula(Asiatic clams) and Dreissena(Zebra Mussels) can impact the safe
operation of the station. Zebra Mussels have not been problematic to date in Lake Norman but
other utilities have experienced macrofouling with Zebra Mussels. Microbial influenced
corrosion(MIC)has caused failures of piping and heat exchanger tubing due to pitting. Non-
oxidizing biocides,chlorine,or sodium hypochlorite may be used at concentrations,which will
not impact the environment to address macrofouling and MIC. Surfactants,which act as
biopenetrants may be added along with biocides to improve their efficacy. To prevent mud
fouling of components cooled by the RN System,dispersants are added.
CONTAINMENT SPRAY HEAT EXCHANGERS
In order to mitigate corrosion of carbon steel, a wet lay-up system is being used on the
Containment Spray Heat Exchangers(NS). Various corrosion inhibitor solutions containing
nitrites,borates, azoles, and triazoles may be used. The corrosion inhibitor solution is released 5
to 10 times per year per heat exchanger(2 heat exchangers per unit) to either the SNSWP or
Lake Norman via Outfall 001, during the flow balance and heat exchanger performance testing.
Each heat exchanger has a capacity of 3600 gallons. Organic biocides are added for biofouling
control.
Page 5 of 24

CONVENTIONAL LOW PRESSURE SERVICE WATER
The Low Pressure Cooling System(RL) supplies cooling water for various functions on the
secondary(steam) side of the station. The system takes suction from the RC crossover lines and
supplies cooling water to various motor bearings, seals, lube oil coolers,vacuum breaker valves,
and a blowdown separator. Discharge is normally back through the RC System. RL is the
supply for the plant's Outsourced Water Treatment System(OWTS).
FIRE PROTECTION SYSTEM
The Fire Protection Systems(RF/RY)provides the plant with fire protection water. The system
is equipped with two 200 GPM jockey pumps which take suction from the RC_System. One
pump is capable of maintaining system pressure. However,the second pump is used to
supplement the jockey pump system capacity. In the event the jockey pumps can no longer
supply enough water to maintain system pressure,there are three 2,500 GPM main fire pumps
that will start as necessary to maintain system pressure. The fire protection system is treated
with an oxidizing biocide,when water temperatures are greater than 620 F,to a concentration of
approximately 1-4 ppm total residual oxidant,to control bio-growth in the system's
piping. The fire protection system uses sodium silicates for corrosion control. The fire
protection system is used as the back-up source of water for bearing lubrication and gland seal on
the low level intake pumps. System operability is demonstrated by periodically testing of the
system. A summary of the current testing schedule follows:
Monthly, the main fire pumps are started, then stopped,to assure operability. Pump Suction is
taken from Lake Norman and discharged directly back into the lake. The water used for this
testing is un-treated lake water.
Each valve on each hydrant is stroked semiannually to assure proper operation. At this same
time,each hydrant is opened and flushed to verify flow. Very little water is discharged. Any
water discharged during testing is discharged to yard drains which discharge to the SNSWP or
WWCB.
Other routine tests are performed periodically to ensure operability of the RF/RY System. These
tests include pump head curve and pump starts in which the water is recirculated back into Lake
Norman at the Intake Structure. Water is also pumped through the system to ensure there are no
obstructions in the lines.
OUTFALL 001
Inputs to Outfall 001 include discharges from the RC, RL, and RN systems. Outfall 004
combines with Outfall 001 before discharging into Lake Norman. Storm drains along the
discharge canal also discharge to Outfall 001.
Condenser Cooling Water
The RC System is a once through, non-contact cooling water system that removes heat rejected
from the main and feedwater pump turbine condensers and other miscellaneous heat exchangers.
Page 6 of 24

Each of the two power generating units has four RC pumps for a total of eight(8)pumps. The
flow for each unit depends on the number of pumps operating as shown by the following table:
Number of Pumps Operating Total Flow/Unit GPM
1 254,000
2 640,000
3 1 867,000
4 1 1,016,000
The operational schedule of the pumps of each unit is a function of the intake water temperature
and the unit load. At 100%load and with the intake temperature near its summer high four RC
pumps per unit are used. During winter when intake temperatures are lower,three pumps may
be used.
Condenser cleaning is accomplished by mechanical means using the "Amertap� " system. This
system circulates small sponge rubber balls through the condenser continuously. There are 8
AmertapTM pumps per unit, 16 altogether. Each system(2 systems per unit,one for main
condenser and one for the FWPTs(Feedwater Pump Turbines)has a capacity of approximately
1240 balls. The balls are injected on the inlet side of the condenser and are retrieved on screens
on the discharge side of the condenser. Periodically some balls escape the retrieval system and
are discharged through Outfall 001. Efforts are made to minimize the loss of balls within the
system.
It may become necessary at times to institute chemical control for macroinvertebrate infestation,
general corrosion, and microbiologically induced corrosion(MIC). Chemicals anticipated to be
added include chlorine(sodium or calcium hypochlorite), organic biocides, dispersants, and —
corrosion inhibitors. The corrosion inhibitors include nitrites,carbonates,triazoles,borates,
triazoles, and azoles. Discharge concentrations are maintained below permitted discharge levels.
MNS has identified the need to treat for Asiatic clams in a section of the RC system. The site
has determined that clams are present in a"crossover pipe"that connects the U1 and U2 RC
systems. The clams have caused fouling of plant components. It is planned to periodically
perform localized injections of a clamicide, EVAC, into the crossover pipe section. The
injection concentrations will be kept at a level to prevent toxic conditions at the plant discharge.
Discharge concentrations of any treatment chemicals will be maintained below permitted
discharge levels.
Ventilation Unit Drains
The Ventilation Unit Condensate Drain Tanks (VUCDT) collects condensate from air handling
units from each reactor building. Each VUCDT(1 per unit)has a volume of 4,000 gallons.
This condensate typically has little radionuclide contamination. The condensate is sampler -
radionuclide contamination before being released. If the results of this sampling indicates the
need, the VUCDT contents are transferred to the Floor Drain Tank(FDT) for processing through
Page 7 of 24

Outfall 004. If no processing is needed,the condensate is released from the VUCDT via the RC
System piping to Lake Norman(Outfall 001).
Note: Outfall 004 and the VUCDTs discharge through the same piping to Lake Norman through
Outfall 001.
During refueling outages, a portion of the ice in the ice condenser is melted. The ice melt is
normally routed to the WC system via the Turbine Building Sumps,however on occasion the ice
melt may be routed through the VUCDT. This drainage contains small amounts of boron. Boron
is used as a neutron absorber in the ice to control reactivity.
During outages the KC Heat Exchangers may be drained to the VUCDT as well. Permission was
granted for this discharge in a permit modification approved by NCDENR on April 11, 2002.
316(a)Study and Thermal Variance
A 316(a) study was submitted to the state on August 9, 1985 and a 316(a)variance was granted
on October 18, 1985. Plant operating conditions and load factors remain unchanged and are
expected to remain so for the term of the permit. An annual Lake Norman aquatic environment
maintenance monitoring program was implemented on July 8, 1987. A copy of this report is
submitted annually to the Environmental Sciences Section of the Division of Water Resources at
NCDENR and to the NC Wildlife Resources Commission(NCWRC). No obvious short term or
long term impact of station operations have been observed in water quality,phytoplankton,
zooplankton or fish communities since the inception of this program. Additionally,Duke Energy
is not aware of any changes to plant discharges or other discharges in the plant site area which
would negatively impact the thermal discharge or biological habitat of Lake Norman. The
annual reports show that Lake Norman continues to have a balanced indigenous population of
fish and other aquatic organisms.
There were multiple fish kills in the vicinity of the McGuire Nuclear Station Intake during the
current permit period,most recently in 2� 012. The NCWRC)and Duke Energy Fisheries
Personnel have investigated the fish kills and have determined they were due to natural lake —
conditions and not associated with McGuire Plant operation. The NCWRC summarized the
2012 event`.
Investigators witnessed the reoccurrence of a striped bass kill on Lake Norman
(Mecklenburg County)during July 2012. Nearly 1000 dead fish were recorded near the
dam. Striped bass kills in North Carolina reservoirs are not unusual in summer months as
high temperatures deplete oxygen in the middle and lower levels of the lakes,trapping
bass that appear to be feeding or seeking refuge in lower depths. Lake Norman also
experienced a similar kill of various catfish species in the same location in early August
2012 (1200 fish). Based on underwater camera footage and recent lake testing, Duke
Energy investigators suspected catfish encountered low dissolved oxygen water while
chasing and feeding on prey.
North Carolina Department of Environment and Natural Resources(NCDENR). 2012. North Carolina Division of
Water Quality(DWQ)Annual Report of Fish Kill Events—2012. NCDENR-DWQ. Raleigh,NC.
Page 8 of 24

OUTFALL 002
Outfall 002 discharges treated wastewater from the Conventional Wastewater Treatment(WC)
System through a Parshall flume to the Catawba River below Cowans Ford Dam. The WC
System consists of a polyurethane coated concrete Initial Holdup Pond(200,000 gallon
capacity), two parallel PolyflexTm Textured HDPE geomembrane-lined Settling Ponds (2.5
million gallons each), and a concrete based Geothane Lined Final Holdup Pond(1 million gallon
capacity). Normally, inputs are received in the Initial Holdup Pond (IHP)but can be routed
directly to an in-service Settling Pond if needed. The IHP serves as a common mixing point for
all wastewater, a surge dampening function to the remainder of the system, and also allows
heavy solids to settle for periodic removal. Retention time in the IHP is 12 to 24 hours. Solids
removed from the IHP are dewatered and disposed of in a permitted landfill.
Flow is directed from the IHP to the in service Settling Pond. Caustic, acid, and/or other
chemicals may be added as necessary. Sulfuric acid and sodium hydroxide may be added for pH
control or to precipitate various chemical compounds. Coagulants may be added to facilitate the
settling of lighter solids. Additional treatment may include chemical oxidation with hypochlorite
(calcium or sodium) or catalyzed hydrogen peroxide. Retention time for each of the settling
ponds ranges between 6 and 12 days. The Settling Ponds can discharge to the FHP or directly to
the Catawba River. Treatment-and discharge are normally on a batch basis. During normal
operations,the FHP is bypassed.
The FHP can be aerated and may be used to remove any persistent oxygen demand or provide
additional holdup capacity. The capability is available for recirculation intra- or inter-basin.
aDischarge to the Catawba River is being modified in the summer of 2014 to be a gravity only
discharge with an approximate flow rate between 600 and 1100 GPM determined by pond level.
The pH_of the discharge from the WC System is adjusted to within permitted limits by the Y('Y
automatically controlled addition of CO2 (carbon dioxide). y mcg
The WC System accepts all conventional plant wastes except sanitary sewage. Inputs to the
system are from the Turbine Building Sumps, Water Treatment Room Sump,Closed Cooling
Systems,the Standby Shutdown Facility, Diesel Generator Room Sumps, Laboratory Drains,
Landfill Leachate. Steam Generator Blowdown, Wet Layup Drains, and the Unwatering Pump
discharges may occasionally be routed through this system as well. Several other buildings also
have inputs to the WC system, including the Vehicle Maintenance Facility, McGuire Office
Complex, Nondestructive Examination Lab, Island Labs, and the McGuire Medical Facility.
These systems typically contain low levels of radioactive hydrogen (tritium). The activity is
monitored and accounted for as part of the radioactive release process.
Water Treatment Room Sump
The demineralized water system(YM) for the plant is produced in a separate building located to
the southwest of the Administration Building. Inputs to the Water Treatment Room Sump are
minimal and may consist of rinsate of empty hydrazine, ammonia, carbohydrazide,
dimethylamine containers and backflow preventer drains. In addition, floor wash and sample
Page 9 of 24

line flush water are routed to this sump. Antifoaming agents and wax strippers are routinely
present in this waste stream. Rinsate from empty microbiocide containers(used in the closed
cooling systems)are periodically added to this sump. The drains in the plant Auxiliary Electric
Boiler Room also route to this sump. Additionally, inputs from the McGuire Island Industrial
Waste System are routed to the sump. See the Island Industrial Waste section for additional
details on these inputs. The Water Treatment Room Sump discharges to the WC System via the
Initial Holdup Pond.
Filtered Water System
The filtered water system has been abandoned in place and is no longer used.
Drinkiny-Water
Drinking Water for the McGuire Site is supplied by the Charlotte/Mecklenburg Utility
Department.
Demineralized Water Svstem
Outsourced Water Treatment Building(OWTS)
The site has replaced the plant water treatment system with a vendor operated system. While the
process is similar, there are some changes to waste streams. The treatment process consist of
chlorination, filtration, dechlorination,reverse osmosis,electrodeionization(EDI) and ion
exchange.
Sodium hypochlorite is used for chlorination. Instead of diatomaceous earth filters,
ultrafiltration(UF) is used. This eliminates the waste filter media(DE)that was previously
produced. The OF filters are backwashed periodically to remove accumulated lake solids. At
times cleaning cycles are combined with backwashes for the OF filters. Sodium hypochlorite,
oo� hydrochloric acid and sodium hydroxide may be used to clean the OF fibers. Backwash and
cleaning waste water is routed to the WC system Initial Holdup Pond for treatment. OF filtered
water is pumped to a 25,000 gallon storage tank at the new building.
The new process does not use carbon filtration, eliminating carbon filter backwash wastewater
and the need to dispose of waste carbon. Sodium bisulfite is used to dechlorinate filtered water
before it is pumped to the reverse osmosis units and OF Filter backwash water prior to it being
discharged to the Initial Holdup Pond.
Reverse osmosis is performed with reject flow,approximately 100 gpm max flowrate, routed to
the Wastewater Collection Basin. Antiscalents are injected into the RO feed. The RO system
requires periodic cleaning using surfactants, acids or caustic chemicals. Any spent cleaning
solutions are routed to the WC system for treatment.
The new system employs an electrodeionization(EDI)unit to remove dissolved minerals from
the water. Reject water from the EDI unit is sent back to the OF filtered water storage tank for
reprocessing. The EDI unit is also cleaned periodically with the same cleaning system used for
RO.
Page 10 of 24

The demineralization system consist of modular,replaceable mixed ion exchange resin beds.
When the resin beds are exhausted,they are replaced with new resin beds and transported off site
for regeneration. This eliminates the demineralizer waste streams including the 75,000+ gallons
of regenerant wastes previously sent to WC.
Turbine Building Sumas
The Turbine Building Sumps(TBS),one for each unit,receive inputs from leakage,drainage,
and liquid wastes from equipment and floor drains located in the Turbine Building. Inputs
include Groundwater Drainage Sumps(WZ),Auxiliary Electric Boiler Blowdown, Steam
Generator Blowdown, air handling units,Diesel Generator Room Sumps, lab drains, floor
washes,normal condensate system leakage,and condensate polisher backwashes. Other possible
inputs may include RC Un-watering, closed cooling system drainage,and steam generator wet
lay-up/drain down. Periodically, condensate from air compressors is processed through an oil
water separator and routed to the TBS then to the WC Initial Holdup Pond. The TBS's pump out
to the WC Initial Holdup Pond. If radioactivity limits are exceeded,theses sumps may be routed
through the Radwaste Liquid Waste Monitoring(WM) System(Outfall 004)or directly to RC
(Outfall 001)depending on the treatment needed. All radioactive releases are controlled and
regulated by the Nuclear Regulatory Commission(NRC). Discharges from the TBS may also be
routed to RC (Outfall 001)if system inventory is high or for periodic testing.
Chemicals that may be present in the TBS include the following:
• ammonia
• hydrazine
• carbohydrazide
• 3-methoxypropylamine(MPA)
• dimethylamine(DMA)
• Glycol (standby diesel coolant)
• microbiocides
• corrosion inhibitors(examples include: molybdate,nitrite,tolyltriazole, etc.)
• janitorial cleaning products
• ethylene glycol(from ice melt)
• Boric Acid/Borax (from ice melt)
• miscellaneous system/component cleaning products(low—volume wastes not associated
with chemical metal cleaning)
• laboratory chemicals
• poly acrylic acid(PAA)
• surfactants
• dispersants
During refueling outages, a portion of the ice in the ice condenser is melted. The ice melt is
routed to WC via the Turbine Building Sumps. This drainage contains small amounts of boron.
Boron is used as a neutron absorber in the ice to control reactivity.
Additionally, small amounts of oil have also been found to accumulate on the ice in the ice
condensers. The source of the oil is from pneumatic tools used to vibrate the ice from the
condenser's ice baskets.
Page 11 of 24

Diesel Generator Room Sums
The Diesel Generator Room Sumps(WN),receive inputs from the leakage or drainage of the
four,diesel generator engine cooling water, fuel oil,and lubrication systems. Each diesel
generator room has two sumps. The smaller sump has a volume of 600 gallons and one pump
with a capacity of 25 GPM. The larger sump has a volume of approximately 4,000 gallons and
contains two pumps with a rated capacity of 450 GPM each, and a third pump,with a rated
capacity of 50 GPM. Fuel oil and lube oil is collected in the"drip tank" which is then pumped to
the Waste Oil Storage Tank(WOST).
Each of the four engine cooling water systems has a volume of 800 gallons. The systems may be
treated with various corrosion inhibitors which may contain molybdate,hydroxides,borates,
silicates,triazoles and azoles. Miscellaneous biocides and dispersants may also be added. Each
cooling system is drained and the coolant is recovered , approximately once per year.
Additionally,the fuel oil used in the diesels contains fuel stabilizers and a biocide which is added
to reduce bacterial breakdown of the oil during storage.
Lab Drains
There are several analytical laboratories on site which discharge to the WC System. These
discharges contain small quantities of typical laboratory chemicals used in analytical procedures.
The island environmental labs discharge to the WC System as well. Further discussion of this
waste stream is provided in the Island Industrial Waste section on page 16.
The lab sinks in the Island Technical Services Center(TSC),building 7406, drain to CMUD.
There are signs on all of the TSC lab sinks telling lab personnel not to dispose of any chemicals
down the lab sink drains. There is very little chemical use in these labs. The TSC labs perform
weight calibration, and sound and vibration analysis.
Condensate Polisher Backwash
Over time,trace impurities in the condensate system increase in concentration. In order to
maintain the integrity of the condensate system,the condensate is processed through condensate
polishing vessels. Each unit has4 vessels. Condensate polishers act as filters and if chemistry
conditions require it,an overlay o ion-exchange resin is added over the filter elements. The
resin allows for the capture of soluble contaminants. On average,the vessels are backwashed on
a monthly basis. If conditions require,backwashes are performed more frequently. Each
backwash requires approximately 10,000 gallons of condensate or YM water. When ion
exchange resin is used, the backwash will also contain 15-20 cubic feet of resin and 120
milliliters of polymer. Backwash water is discharged to the WC system. When resin is used,the
backwash is routed to a decant tank where the resin is captured. Normally,the spent resin is
pumped into a liner, de-watered and shipped to a low level radioactive waste disposal site. This
resin may also be discharged to the WC System or to the Liquid Waste Monitoring System
(WM)depending on levels of radioactivity and volume.
Page 12 of 24

Steam Generator Blowdown
There are four steam generators(SG)per unit at McGuire for a total of eight steam generators.
Each has an operating volume of 16,000 gallons. Each unit is provided with a Steam Generator
Blowdown Recycle System. Steam generator blowdown is continuous at a rate of approximately
200 gallons per minute per unit. Normally,the blowdown is directed to either the condensate
1 ' polishing demineralizers or to the steam generator blowdown demineralizers. SG Blowdown can
be routed to the WC System via the Turbine Building Sumps if needed.
During normal operation,hydrazine is added to the condensate system for oxygen scavenging.
The hydrazine concentration is maintained within a range of 25-200 ppb. 3-methoxypropylamine
is added for pH control. The steam generators and hotwell are placed in wet lay-up if a unit is to
be in extended shutdown or per management direction. Each unit is normally shutdown every 12
— 18 months for refueling and maintenance.
Dispersants may be used in the plants Steam Generators to control corrosion and sediment
buildup, therefore the potential exists that rejected blowdown waste water may contain small
amounts of the dispersant.
Steam Generator Wet Lay-up
Wet lay-up is the method used for protecting the steam generators against corrosion during
inactive periods. Typically,this will only be performed 1-2 times during a unit outage.
Chemical additions are made up in a 150 gallon addition tank. Normally, 40 gallons of 12%
Carbohydrazide and 20 gallons of 40%3-methoxypropylamine(MPA) are made up for transfer
to the steam generators. Any remaining chemical solution is drained to the WC System via the
Turbine Building Sump. Prior to returning the unit to operation,the wet layup solution in the
steam generators may be drained to the WC System or WM System via the TBS.
The hotwell on each unit has a volume of approximately 250,000 gallons. During each unit
shutdown or per chemistry management direction, the hotwell is placed in wet layup.
Approximately 300 gallons of carbohydrazide are added to achieve a target concentration of 100
ppm carbohydrazide with the pH adjusted with MPA. If Carbohydrazide is not available,
sufficient hydrazine is added to achieve a target concentration of 75 ppm. Prior to returning the
unit to operation, this wet layup solution is discharged to the WC System or WM System via the
TBS.
Auxiliary Electric Boller Blowdown
The Auxiliary Electric Boiler is supplied feedwater from the condensate system. Trisodium
phosphate is added as an electrolyte. The blowdown from the boiler may contain these
chemicals and approximately 1-2 ppm suspended solids. Blowdown is routed to the WC System
via the TBS.
Page 13 of 24

Groundwater Drainaze System
The Groundwater Drainage System(WZ)is designed to relieve hydrostatic pressure from the
Reactor and Auxiliary Buildings by discharging groundwater collected in sumps to either a yard
drain or the TBS. There are three groundwater sumps with two 250 GPM sump pumps each.
Two of the sumps discharge to the TBS while the third sump discharges to a yard drain that is
routed to the Standby Nuclear Service Water Pond(SNSWP).
RC System Unwaterins
The RC System piping for each of the two units has a total volume of approximately 2 million
gallons. Whenever a unit is scheduled for refueling,periodically during other shutdowns, and
for condenser tube leaks, the system must be un-watered for purposes of maintenance. Un-
watering must continue while maintenance is performed because of leakage by the valves in the
approximately I 1 foot diameter RC piping. The maximum un-watering rate is approximately
2,000 GPM and the water is essentially untreated lake water. Treated liquid radioactive waste
effluent(Outfall 004)discharges into a crossover line between the RC System of the two
units. During un-watering,the possibility exists for trace amounts of radioactivity to be released
into the water from the un-watering process because of isolation valve leak-by. All radioactivity
is accounted for and regulated by the NRC. The principle discharge route of the un-watering is
through the WWCB. However,it may be routed through the WC System for short periods of
time.
Closed Cooline Systems
There are several closed cooling systems within the station. The largest system has a volume of
approximately 30,000 gallons. The main components of these systems are constructed of carbon
steel. In order to mitigate corrosion of the carbon steel, various corrosion inhibitor solutions
which may contain nitrite,borate, carbonate, azole,triazole, silicate,phosphate, and molybdate
compounds are used. Dispersants may also be used to control corrosion and reduce fouling.
Biocides such as gluteraldehyde,isothiazolin and DBNPA can be used to prevent microfouling.
Surfactants which act as biopenetrants may be added to improve efficacy. The systems may need
to be drained, individually, for non-routine maintenance. Should this occur,these systems would
be drained to the RC discharge,WC System,or WM System, if contaminated with radioactivity.
Standby Shutdown Facility
The Standby Shutdown Facility(SSF)is an alternate and independent means to shutdown the
station during emergencies should the need arise. The independent power supply for the SSF is a
diesel generator system. The SSF contains a sump to collect system leakage, floor wash, and
drainage of the equipment for maintenance. The closed cooling system for the diesel generator
uses corrosion inhibitors which may contain nitrite,borate, carbonate, azole,triazole, silicate,
phosphate. glycol and molybdate compounds. Biocides such as gluteraldehyde, isothiazolin and
DBNPA can be used to prevent microfouling. Surfactants which act as biopenetrants may be
added to improve efficacy. Based on maintenance requirements and/or system chemistry
monitoring, system coolant is drained and captured for re-use or recycling.
Page 14 of 24

Steam Generator Cleaning
Each electrical generating unit contains four steam generators that have a capacity of
approximately 25,000 gallons each. There has been no chemical cleaning of the steam
generators to date,but the possibility exists that cleaning may be required. The actual chemicals
used for cleaning will depend on the type of fouling, and may include use of the chemicals listed
below.
Miscellaneous System/Component Cleaning
Other systems/components(such as strainers,piping,HVAC heat exchangers, etc.) are cleaned
periodically because of scaling or plugging. Some cleanings are done by rinsing or by high
pressure washdown with water only(hydrolasing). Other times additives may be used to
improve cleaning efficiency. Solutions utilized are dilute acids, caustics, detergents or other
cleaning agents that do not attack the base metal. Typically only small volumes of waste are
generated. Chemicals utilized by these methodologies, alone or in combination,may include the
following:
Alkaline Boilout Solutions
non-ionic surfactants
anionic surfactants
cationic surfactants
sodium hydroxide
soda ash
trisodium phosphate
disodium phosphate
monosodium phosphate
sodium bicarbonate
Acid Solutions
hydrochloric acid
sulfiiric acid
phosphoric acid
formic acid
hydroxyacetic acid
sulfuric acid
citric acid
nitric acid
Acid Solution Additives
thiourea
ammonium bifluoride
oxalic acid
Page 15 of 24

EDTA Compounds and HEDTA
pH adjusted tetra-ammonium EDTA
tetra-ammonium EDTA
di-ammonium EDTA
hydroxyethylenediaminetriacetic acid
tetrasodium EDTA
Miscellaneous Compounds
chlorothene
sodium chloride
potassium permanganate
aqua ammonia
ammonium persulfate
antifoam
sodium sulfite
chlorine
The wastes from these cleanings are analyzed to determine proper waste disposal. These
cleaning solutions are released through the WC System or WM System depending on levels of
radioactivity.
Island Industrial Waste
Industrial Waste from the McGuire Island is collected and routed to the plant Water Treatment
Room Sump and eventually to the WC System through a dedicated discharge pipe. Industrial
Waste consists of small quantities of lab chemicals from analysis in the Duke Energy Corporate
Labs in Building 7405 and Building 7403 (McGuire Technical Training Building), and some low
level radioactive liquid waste. The radioactive waste is accounted for through McGuire's
radioactive effluent license.
Landfill Leachate
The McGuire Site operates a synthetically lined landfill(Permit 60-04 Indus), which is located
on Duke Energy property, across Highway 73, from the McGuire Plant. The landfill began
operation in January 1992. The area of the landfill is approximately 5 acres.. The landfill
accepts only non-hazardous solid wastes, which contain no free liquids.
The leachate collection system is designed to collect rainwater that falls directly onto the landfill.
In the landfill cells, a perforated pipe collects the leachate which is then routed to the leachate
collection pond. The leachate system is designed to collect a maximum of 68,000 gallons. From
the leachate collection pond, the leachate is pumped to the WC System Initial Holdup Pond. The
Leachate also contains pump seal water which comes from a well at the landfill. The estimated
average flow from the landfill leachate system is 200 GPD. This will vary according to rainfall
amounts. The leachate is sampled semi-annually. The results are submitted to the N.C.
Department of Environment, Health, and Natural Resources, Solid Waste Section, per the
Landfill permit requirements.
Page 16 of 24

McGuire Garage
The McGuire Garage conducts maintenance on a variety of vehicles and heavy equipment.
Examples include cars,trucks,boats, fork lifts,cranes, etc. All industrial waste generated at this
facility is routed through an oil water separator to the WC System via the Initial Holdup Pond
(IHP). To add weight to some equipment,water is added to the tires. To prevent the water from
freezing,calcium chloride is added. Approximately 500 gallons of this solution is generated
each year. Some of this solution is reused. Portions that are not reused are disposed of in the
Initial Holdup Pond.
McGuire Office Complex
All industrial waste generated in this building is routed to the WC system via the Initial Holdup
Pond. Waste from an oil water separator is also routed to the WC system. The average daily
flow has not been be estimated due to the highly intermittent nature of the flow but it is expected
to be less than 5 GPD (Gallons Per Day).
Office Shop Facility
All industrial waste generated in this building is routed to the WC system via the Initial Holdup
Pond. Waste from an oil water separator is also routed to the WC system. The average daily
flow has not been estimated due to the highly intermittent nature of the flow but it is expected to
be less than 5 GPD(Gallons Per Day).
Nondestructive Examination
Current trend is the use of computed radiography(CR)which uses a plate to capture the image
and the image is scanned directly into the computer. This method does not produce a waste
stream. The method described below may be used as an alternate process backup and as the
process to support other Stations.
Nondestructive Examination(NDE)includes X-ray testing of various components. The
photographic waste from X-raying is routed to the WC system via the IHP. NDE is usually
conducted in a building inside the protected area. If this X-ray processing unit is unavailable,
then a trailer which has the same type of equipment is utilized. The trailer also discharges the
photographic waste to the WC System via the IHP. When operating, the X-ray processing unit
has a waste stream which consists of approximately 0.0059 GPM developer replenisher working
solution, 0.0297 GPM fixer and replenisher working solution and 4.0 GPM water. The
developer replenisher working solution contains hydroquinone, glutaraldehyde, and potassium
acetate. The fixer and replenisher working solution contains ammonium thiosulfate and sodium
sulfate. Other developer working solutions and/or fixer replenisher working solutions with other
constituents may be substituted in the future. Silver is recovered from the process unit flow
before it enters the waste stream. The developing process can be operated a maximum of 30
hours per week (4.3 hours/day)but averages only 6 hours per week(1.2 hours/day). Operation
of the developing process results in a maximum of approximately 1040 GPD, with an average of
290 GPD of photographic waste discharging to the WC System.
Page 17 of 24

Ice Condenser
During refueling outages, ice melt from the plants ice condenser is routed to WC. Potential
chemicals in ice melt include:
• Borax
• Boric Acid
• Trace amount of oil from ice removal pneumatic tools
• Ethylene Glycol from spills from the ice making equipment. The amount of Ethylene
Glycol in the ice melt would be<55 gallons total.
OUTFALL 003
Outfall 003 was eliminated as of June 28, 1998. All sanitary wastewater is now discharged to
the Charlotte/Mecklenburg Utilities Department(CMUD).
OUTFALL 004
Outfall 004 discharges wastewater from the Radwaste Liquid Waste Monitoring System(WM).
This discharge combines with RC water before discharging through the concrete discharge
structure(Outfall 001)into Lake Norman as a batch discharge. All radioactive and potentially
radioactive liquids are collected, segregated, sampled and processed as needed prior to release.
These effluents are classified as recyclable or non-recyclable liquids. Recyclable liquids are
recirculated back to their process streams. Non-recyclable liquids are collected and processed to
Nuclear Regulatory Commission(NRC)requirements per 10 CFR Part 20 and 10 CFR Part 50
requirements prior to release. The type of processing depends on the type of waste. The
maximum discharge rate from WM is 120 GPM. The batt sce flow for a Waste Monitor
Tank Release is a function of activity level,the number of RC pumps in operation, and the
resultant boron concentration in Lake Norman.
The WM llects waste in three subsystems; floor andeq P ui meth drains laundryLwaZste, and
ventila ' n unit drains. Chemicals that may be present in the WM System include:
boric acid
borax
nitrate
ammonia
carbohydrazide
Dimethylamine(DMA)
3-methoxypropylamine(MPA)
coagulants (example: Nalco 71259
lithium hydroxide
ethylene glycol (from ice melt)
corrosion inhibitors(examples include: molybdate,nitrite, tolyltriazole, etc.)
hydrazine
chlorine/hypochlorite
hydrogen peroxide
pump bearing cleaning chemicals
laboratory chemicals
Page 18 of 24

surfactants
polyelectrolytes
miscellaneous system/component cleaning waste(low volume waste not associated with
chemical metals cleaning)
microbiocides
tool and component decontamination waste
janitorial cleaning products.
The TBS can become contaminated with radioactivity. When this occurs,it can be pumped to
the Floor Drain Tank(FDT)or to the WM release point in the RC crossover line. Any chemicals
listed as being in the TBS have the potential to be present in the Waste Monitor Tank(WMT)
when the sump is routed to WM. Any solids generated in the treatment process are de-watered
and transported to a State licensed low level radioactive waste disposal facility.
Floor, Eauiament.and Laundry Drains
Floor drains in the Auxiliary Building,drainage from all equipment(pumps,tanks,heat
exchangers,etc.)which process radioactive waste, waste from showers in the change rooms and
washing equipment which is used to decontaminate protective clothing, and waste from the Unit
1 and Unit 2 Containment Floor and Equipment Sumps are routed to the Floor Drain Tank
(FDT), Waste Evaporator Feed Tank (WEFT),Auxiliary Floor Drain Tank(AFDT),Auxiliary
Waste Evaporator Feed Tank(AWEFT), and/or Laundry and Hot Shower Tank(LHST). The
total tank volume is 125,000 gallons. These collection tanks are used interchangeably and/or as
backup and surge capacity for waste collection upstream of processing.
Radioactive waste from these collection tanks are processed using filters and/or demineralizers
based on content. The processed effluent is collected in the Waste Monitor Tanks for sampling
and analysis prior to release. Release is to Lake Norman via the RC crossover line.
Chemical Volume and Control System
The Chemical Volume and Control System(NV)regulates the concentration of chemical neutron
absorber in the Reactor Coolant System(NC)to control reactivity changes and maintain the
required water inventory in the NC System. Boron, as boric acid is used as the chemical neutron
absorber.
Other control elements introduced into the NC System by the NV System include lithium and/or
carbohydrazide or hydrazine. Approximately 120 pounds of lithium hydroxide monohydrate is
used in each unit per year for pH control. The lithium is removed by demineralizers in the NC
System. Zinc acetate dihydrate is added to the NC system to achieve a concentration of 10 ppb
as zinc. This is done to reduce radiation exposure to plant personnel. Zinc will be removed by
demineralization in the NC system and by uptake into NC system piping oxide layers and
corrosion product deposits on fuel cladding During start-up, carbohydrazide or hydrazine is used
as an oxygen scavenging agent. It is consumed upon unit heat-up, and is not used at any other
time. During shutdown, hydrogen peroxide is added to the NC System to facilitate the removal
of activated corrosion products.
Page 19 of 24

Chemical Treatment in WM System
If it becomes necessary to oxidize sodium nitrite in a Waste Monitor Tank, hypochlorite—'
(calcium or sodium) or catalyzed hydrogen peroxide would be used. When this treatment is
performed, the Waste Monitor Tank is isolated, recirculated, and mixed. The tank is sampled to
ensure that the nitrite has been oxidized. The addition of the oxidation chemicals should result in)
a small residual of nitrite in the tank, since the oxidation chemicals will not be added in
stoicheometrical excess.
OUTFALL 005
Outfall 005 discharges flow from the Waste Water Collection Basin (WWCB). The WWCB is a
13.4 acre collection b_asin,having a total capacity of approximately 40 million gallons with a
maximum drawdown capacity of approximately 11.1 million gallons. Discharge from the basin
ranges from 0 to 20,000 GPM. If the Standby Nuclear Service Water Pond (SNSWP) is being
flushed, no holdup of the WWCB is possible. Otherwise,holdup is minimal. The WWCB
provides sedimentation, natural neutralization, and skimming. The overflow from the WWCB
mixes with discharge fi-om the WC System(Outfall-00) in a concrete apron and is discharged to
the Catawba River downstream of Cowans For Dam
Inputs to the basin include overflow from the SNSWP, yard drains, RO reject flow,
miscellaneous Administrative Building drains, and RC System un-watering.
--;-RO reject flow from the Water Treatment Building(OWTS) is routed to the WWCB through an
approximate 3 inch line.
Standby Nuclear Service Water Pond
The SNSWP is a 34.9 acre pond designed to provide water for the safe shutdown of the station in
the unlikely event that Cowans Ford Dam is damaged and Lake Norman becomes unavailable.
The level in the pond is maintained,per requirements of the McGuire Nuclear Station Technical
Specifications (NRC requirements),by pumping water from Lake Norman into the pond. The
pond receives runoff from a drainage area of 100 acres. The containment spray heat exchanger
cleaning solutions(NS System)may occasionally be routed to the SNSWP. Overflow of the
SNSWP is routed to the WWCB.
Macrofouling sources (fish, algae, weeds, etc.) are removed from the SNSWP through the use of
chemical treatments. Rotenone is used to remove fish at a frequency of approximately twice per
year. Rotenone is added at approximately 2 ppm for these treatments. The rotenone is
neutralized through the use of Potassium Permanganate at no more than 4 ppm. Aquatic weeds
and algae are removed using Hydrothol 191 in the shallow areas of the SNSWP at depths of 10 ft
in depth or less. Hydrothol treatments are conducted approximately 3 times a year in the late
spring, summer and early fall.
To ensure that the treatment chemicals are not released to the Catawba River prior to being non-
toxic, the WWCB is lowered approximately 5 feet below overflow. Additionally, the SNSWP is
lowered approximately 4 inches under overflow. In order to lower the pond levels, temporary
pumps may be used to pump water to the WWCB and Catawba River via the overflow pipe at
Page 20 of 24

the permitted Outfall 005 . Treatments are controlled by procedure. Per agreement with
NCDENR toxicity tests are performed on the ponds before water is released to the Catawba
River.
Administrative Building Drains
The Administrative Building drains include an HVAC sump, floor drains,janitorial sink,hot
water boiler, and chiller water system discharge. Any chemicals in the drains would include the
typical commercial products used to clean and maintain the floors as well as closed cooling
corrosion inhibitors and microbicides from leakage/drainage of the HVAC Systems. The
corrosion inhibitors may contain nitrite,borate, carbonate,triazole, azole, and glycol compounds.
Additionally, HVAC cooling units are periodically cleaned using dilute coil cleaning solutions.
These cleaning solutions are typically flushed to storm drains near the building which drain to
the SNSWP or the WWCB. Volumes are less than 55 gallons. The coil cleaning solutions are
typically Phosphoric Acid or Hydrofluoric Acid based.
RC Svstem Un-waterin¢
The RC System piping for each of the two units has a total volume of approximately 2 million
gallons. Whenever a unit is scheduled for refueling,periodically during other shutdowns, and
for condenser tube leaks,the system must be un-watered for purposes of maintenance. Un-
watering must continue while maintenance is performed because of leakage by the valves in the
approximately 11 foot diameter RC piping. The maximum un-watering rate is approximately
2,000 GPM and the water is essentially raw lake water. Treated liquid radioactive waste effluent
(Outfall 004) discharges into a crossover line between the RC System of the two units. During
un-watering,the possibility exists for trace amounts of radioactivity to be released into the water
from the un-watering process because of isolation valve leak-by. All radioactivity is accounted
for and regulated by the NRC. The principle discharge route of the un-watering is through the
WWCB. However, it may be routed through the WC System for short periods of time.
Filtered Water
The Filtered Water(YF) storage tanks on the service building roof have been converted to
demineralized water(YM) storage tanks. Periodic flushes of the tanks are no longer performed.
,The Filtered Water system has been removed or recon i,wed.
HVAC Unit Drains �,a ��,, �_�� ✓�
Several HVAC units have once through non- contact cooling water drains which discharge to
yard drains on the east and west sides of the Administrative Building. The flow from each of
these units is 10 GPM. These HVAC units are supplied by RL.
Additionally, HVAC cooling units are periodically cleaned using dilute coil cleaning solutions.
These cleaning solutions are typically flushed to storm drains near the building which drain to
the SNSWP or the WWCB. Volumes are less than 55 gallons. The coil cleaning solutions are
typically Phosphoric Acid or Hydrofluoric Acid based.
Page 21 of 24

Yard Drains
Most yard drains discharge to the WWCB or SNSWP. The drainage area for the plant site is
approximately 250 acres. The yard drain system is described in McGuire's Stormwater
Supplemental Information and the sites Storm Water Pollution Prevention Plan(SWPPP).
Turbine Building
There is a small pit in each unit's turbine building that gravity drains to the WWCB. These pits
are part of the drainage grid under the turbine building; no plant waste streams are routed to
these pits.
OUTFALL 006
System performance standards may require that certain metal components be periodically
cleaned using an acid or caustic solution. This cleaning process can be reactive with the base
metal of the component. The waste metal cleaning solutions which are generated will be
neutralized. The other compounds will be mixed,oxidized, and/or precipitated as necessary for
treatment. The wastes from these cleanings will be sampled and analyzed to determine proper
waste disposal. If the wastewater is in specification it will be released through the WC System
or WM System. If the waste solution exceeds the permitted discharge limits, it will either be
treated further or sent off-site to an approved disposal facility.
Page 22 of 24
I

APPENDIX 1
Water Use Diagram
Page 23 of 24

� r
Shndby Nuelear AppmmftI
Sw%ft&VWMW Pond �— Sbmr Drams Motitdn Ibelgr BYllan
SUB" Nth Row DMWM
♦ NCON439
LAKE NORMAN Nuclear Service 22.2 MCD Nw.. FbRWM
Wyw RN -----♦ Alleerale Flowpalb
' t F i
i Low Level We Il_, Condenu►COD" 2.904 MGD 2,929 Total MOD LAKE NORMAN
i (LU) _._.♦ °' DISCHARGE
i
------ i 0.0079 MOD WW001
' - Fire Prolecdon i Low Pressure
i Servloa Water RL
-------------ti
Ftitered Waler I
Osmosis ItRO
�� i BysEem
VJaterYM � �e —T� IWMI
i
and Lsakaps i W WO04
r i-----
Ca i
i n
Vmdbtkm Unit i •Gaspe Vehlda
Water Treatrrbnt CorWensab Drain Mlaah Area
i Room Sump SeODXlwy SY*Am Tanks(V IMM 'LWWM Leachate
Drainage and`--_-- A � 0.0016 MOD 1
'NDEPbotopaplic w ----- -----------� ConverWonal
wow
i INrrd Lab Waste i v -- Waeb TnNlvem
i
Island HVAC >h� '_--
Codit Towers Turbine (WC) i
9 Stow Sloan DramsW WO02
seperabors
0.7186 MOD i
i r
Wash CATAMA
]'. r
(YVWCB � Total:0.9919 MGD RIVER
�-------- -------------► r
i 0.8371 MGD �
� r
---------------- r
Page 24 of 24
i

APPENDIX IV
TOPOGRAPHIC MAP
Page 7of11

UNITED STATES STATE Of NORTH CAROLINA
DEPARTMHNT OF THE INTERIOR OU
AaTM[NT O!XNv1.ONM[NT.11[AtTN LAKE NORMAN SOUTH OUADRAVOLE t�
AMD NANRAI.[130U1f[S nONTN CANOIJnI fr
OEOLODICAL SURVEY RALl K:X.NORTN CAROLINA !d wNUTE 6RRIEE(TOPIX)RAONIGI
3t [
7P k
�` y _ ..�• ro
L A R B �.� N O R Y A N
14,
a _ s� 1 � Vii, � ��' J^• ,�i
r ^�
1
f:
k
l:•w � -r, -�:...,.:
Roacw M nR sw[f Gfom[Ks� xKc I nmo neo aA[aR�[Anov`
' O[Wwo�Nb:NwA4pv mNww.y.ww W=wr--u-L=v:.- ^' he.bylywf
0.+wn„wb.r,.il .. w 1Wa�M[.[N 10�f,i •a.M. ���Wywf�f ......
le IOOOwr1Y..lrw.rnrr K[�,n..i. '� Or rrrl[.aru [i a.r. USr.N Lw rn i
n.rw.rr sn N.x..ou n.N noa H,
LAKE NORMAN SOUTH.NC ;
s....NAvcw,rr.v. ..w.e.o.�Ra rn ..MwfsnuvwwawwKrrc uvlw "r,•':•,•
N.ru[rus.aaaen[Rur[+ a•••..a..•.1rt....•.....+r.r „.�oo'n W.
p[��WWiO`[Y►�1Mf�gfr.�[ALi ��:w.a:l�.lr✓Nlw.+rl..Y./
.rw.. NUNu a.arn ,.+ri4..rte.'.TrN«,arf:>A Wsa rnw IB9! E-
N.o.a.d row.

APPENDIX V
SITE MAP
Page 8 of 11

MIX,;R.
Lake Norman South Quad
AV'
03-08-33
pz
"A
71
001, 004
002
005
...... ----
'�411Lf111� OQI- atr!i� r(_ � '� �.•r! '! � i � ��K•G• �}'
Ow-fa
__]S'76'03 03
%!-W,
002
gy
'vin Sftegnt, Corporatio
'25
35 'S W& [G 02430
North
-57-20-
McO Nuclear Station,

APPENDIX VI
SLUDGE MANAGEMENT
Page 9 of 11

DUKE ENERGY
McGUIRE NUCLEAR STATION
SLUDGE MANAGEMENT PLAN
Conventional Waste Water System (WC)sludge is disposed of in the site's permitted
landfill. The landfill is a Subtitle D, Solid Waste Lined Landfill which only accepts non-
hazardous waste. Prior to disposal,the sludge is sampled,then removed and de-watered.
The old water treatment system that used diatomaceous earth has been replaced with a
new system that uses different types of filtration which is housed in the Outsourced
Water Treatment building
Settleable solids from the plants waste systems are routed to the WC system and these
solids settle in the Initial Holdup Pond(IHP). This sludge includes solids from the filter
backwash process used in the Outsourced Water Treatment building. Other sources of
sludge are accumulation of dusts and silts from plant operation and the areas surrounding
the ponds. The site no longer uses diatomaceous earth filtration which was the major
contributor to sludge accumulation during previous operation. This will greatly reduce
the frequency of sludge removals from the IHP. It's estimated that sludge removals from
the IHP will not occur more often than 5-7 years.
Along with sludge removed from the IHP,it may become necessary to remove and
dewater solids from the two settling ponds or the Final Holdup Pond. Any removals from
the two settling ponds or the Final Holdup Pond (FHP)will be very infrequent.
Any radioactive contaminated sludge is disposed of per the sites NRC license and is
permitted by Mecklenburg County Solid Waste Department and the State of NC for
disposal in our landfill.
Sources of radioactivity in the sludge come from various sumps in the auxiliary and
turbine buildings.

APPENDIX VII
HISTORICAL SULFATE ANALYSIS TREND
Page 10 of 11

MNS WC Discharge Sulfate MR
'Hill Vf vt"Idol
Water Treatment
:JU
1"0
l;al
I11/94 1/1/96 12/31/97 :2/31199 12/30/01 12130/o3 12/29/05 12/29/07 12/28/09 12/28/11 12/27/13 11,7 7.:S
Page 11 of 11

APPENDIX III
SECTION 311 LIST
Page 6 of 11

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