unrr - texas

PUC Docket No. 46449 Schedule H-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY ARSENAL HILL *5 GENERATING uNrr CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION .3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs -

6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10, TYPE OF EXCITATION

BOILER 1. OESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5, BOILER MANUFACTURER 8. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2, MANUFACTURER Of PART. CONTROL 3. MANUFACTURER OF SOK CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF Nflx CONTROL a CURRENT LEVEL OF PARTICULATES a CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS

DESCRIPTION / RESPONSE

General Electric Company Two casing, tandem cornpound, two flow exhaust. condensing. non-reheat 1000T / 1450 ask; Four 213 / 3600 RPM General Electric Company 147,059 KVA, 0.85 PF, 15,500 volts 100 MW Hydrogen DC exciter

Natural gas None Not Applicable Natural gas Combustion Engineering Pressurized furnace, natural circulation, non-reheat Not Applicable Corner fired

Louisiana Department of Environmental Quality regulations Not Appficable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable '0.0006 LbsiMillion Btu *0.1036 Lbs/KIlion Blii Not Applicable Not kr/Plicate Not Applicable Louisiana Department of Erwironrnental Quality regulations Louisiana Department of Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable

Not AOgficabtle Not Applicable

'Based on 201 3-201 5 EPA kir Ma ts Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF LoDuLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER I- ttOPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8, MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Cooling pond with mist sprayS Marley (spray system) 0.9 MW (circulating water purnps) (2) motor driven boiler feed pumps Pacific Pumps (pumps), Allis Chalmers (motors) 2.2 PAW (2) forced draft tans Westin9house (tarts). Allis Chalmers (mo(ors) 1.0 MW (2) Ljuogstrom regeneratve Air Preheater Corporation 0.0/ MW Pressurized gas piping Not Applicable

Not AOPficable

Sponsored by: Paul Franklin

3000

PUC Docket No. 46449 Schedule H-123b

of 25

SOUTHWESTERN ELECTR/C POWER COMPANY Stall Plant (ARSENAL. HILL #6) GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GDIERATOR J. TURBINE MANUFACTURER

2, TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs e GENERATOR MANUFACTURER

7. NAMEPLATE RATINGS B. NOMINAL GROSS MW OUTPUT 9. rePE OF COOUNG 10. TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2 DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5, BOILER MANUFACTURER 6. TYPE OF BOILER 7 TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL

7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12 PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUf OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4, DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTUFIER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS


6A & 6B Combustion Tubines (CT): Siemens, 6S Steam Thrbine: GE CT: 6A & 6B Siemens 501FD2-Class, 63: GE Dll Two casing, tandem compound flow, two flow exhaust condensing, reheat Stearn Turbine: 6S 1050F l 1882 psi design Not Applicable 6A & 6B: 25.0* - 3600 rpm 6S: 33.5- 3600 rpm 6A & 6B: Siemens AreoPac II 6S: GE 6A & 6B CTs: 217 MVA, ass PF, 15,000 VAC. SS: 301.2 MVA, .85 PF. 18,000 VAC 500 MW 6A & 6B - Closed loop air 6S: Hydrogen 6A & 6B Brushless Rotating Rectifier - DC Exciter 65: Static DC Exciter

Not Applicable Nat Applicable Not Applicable Not Applicable 65A & 68: Nooter-Eriksen 6A & 68 Heat Recovery Stearn Generator 6A & 6B: Natural Gas 6A & 6B: DLN Combustion Turbine - Natural Gas

Louisiana Department of Environmental Ouality regulations Not Applicable Not Applicable 6A & 613: Peerless Mfg Company - Cormetech SCR Not Applicable No1 Applicable

6A & 6f3: SCR with 19% aqueous ammonia and DIN Combustion Fuel Nozzles Not Applicable `6A & 68 0.0006 Lbs/Million Btu 1 •6A 0.0110 Lbs/Millian Btu & 68 0.0108 LbsNillion Btu Not Applicable Not Amlicable 6A & 613: 0.2 tilw Nat APPIicable Not Applicable Not Applicable Not Applicable Not Aoplicable Not APPlicable Not Applicable Not Applicable

Mechanical Draft Cooling Tower - 10 Cells, 2 Circ Water Pumps SPX 4.7 Mw 6A & 68: Motor Driven Boiler Feed Pump 6S: Not Applic:able 6A & 68: Motor - GE. Purnp - Sulzer 6A 1.1 Mw 613: 1.1 Mw, (combined 0 2.2Mw) Not APPlicabla Not APPlicabie Not Applicable Not Applicable Not Applicable Not Applicable Natural Gas - Pipe Line Quality (dual suppliers) BA & 68: Texas Systern Nal APPlicable

Sponsored by: Paul Franldin

3001

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

PUC Docket No. 46449 Schedule H-123b

01 25

SOUTHWESTERN ELECTRIC POWER COMPANY FLINT CREEK #1 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOLING 10. TYPE OF EXCITATION


General Electric Company Three casing. tandem compound, four flow exhaust, condensing, reheat 1000`F / 1000°F / 2400 psig Seven 26 / 3600 RPM General Electric Company 620 MVA, 0.90 PF. 22.000 volts 511 MW Water cooled stator AC exciter

Western Coal None Not Applicable No. 2 fuel oil Babcock & Wilcox Balanced draft, natural circulation. reheat Pulverized Opposed

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13, PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE 1NATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE D1SP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2 MANUFACTURER OF COOLING WATER SYS 3. PEAK NIW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COM8UST1ON AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PFIEHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Arkansas Pollution Conirol and Ecology Cornmission regulations Research-Cottrell GE (Aistorn) Babcock & Wilcox Hot side electrostatic precipitator/Pulse Jet Faoric Fitter NID Dry Scrubber Low NOx burners 0.0024 lbs./million Btu (filterable portion only 7/20/2016 test) 0.057 lbs/million Btu (July & Aughust 2016 avg) 0.2755 Lbs/Million Btu

2.2 MW 7.0 MW Not Applicable Arkansas Pollution Control and Ecology Commission regulations Arkansas Pollution Control and Ecology Commission regulations Not Applicable Not Applicable Not Applicable Landfill for combustion by-products .

Not APeficab4e Not Applicabie

Lake Not Applicable 3.4 MW (circufating water pumps) (1) turbine driven BFP; (1) motor driven BFP wfth hydraulic coupling DeLaval (pumps), Westinghouse (turbine). General Electric (motors) 13 MW (equivalent electrical load of auxiliary steam turbine output) Two (2) forced draft farts Westinghouse (FD fans) and General Electric (motors) 2.6 MW (2) LrUngstrom regenerative tri-sector air heaters Air Preheater Corporation 0.06 MW Belt conveyors. coal feeders, pulverizers, and primary air fans J.B. Webb (corweyors). Stock (feeders), B&W (pulv.), Westinghouse (PA fans) 10.0 MW


3002

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. NIW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY DOLET HILLS V GENERATING UNIT CHARACTERISTICS

CATEGORY

TURB1NE-GENERATOR 1, TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3, INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLAD1NG SIZE / RPMs 6. GENERATOR MANUFACTURER 7, NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION


Westinghouse Electric Corporation Four casing. tandem compound, tour flow exhaust. condensing, reheat 1000°F / 1000°F / 2400 psig Seven 28-1/2' / 3600 RPNI Westinghouse Electric Corporation 775 MVA, 0.93 PF, 24,000 volts 660 NM Water cooled stator Brushless AC exciter

Lignite None Not Applicable Natural gas Babcock & Wilcox Balanced draft, natural circulation, reheat Pulverized Opposed firing

LLUT1ON CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 5. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK hilW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG /6. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUNIP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTPON AIR SYS & MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Louisiana Department of Environmental Quality Regulations Hamon Research Cottrell United Oil Products Air Correction Division Advanced Burner Technotogies /Fuel Tech Pulse Jet Fabnc Filter (Baghouse) Limestone Absorption Low Nox Burners/ SNCR 0.013 tblmrrBTU (Cleo° guarterty testing) 0.910 lloimmBTU (Cleco GEMS 2016 YID) 0.198 lbfmmBTU (Cleco GEMS 2016 YTD) 1.0 MW 5.0 MW 0.3 MW Louisiana Department of Environmental Quality reoulations Louisiana Department of Environmental Quality regulations Ecodyne-Graver Water Divison Lime treatment for solidsprecïpitalion Not Applicable Landflll for combustion by-products and FGD sludge System not used Not Applicable

Coding tower with makaup and biowdown ponds . Ceramic Cooling Tower Company 10.0 MW (circulating water pumps, cooling tower fans, rnisc, pumps) (1) turbine driven BM; (1) motor driven BFP with hydraulic coupllng PaOrlic Pumps (pumps), Westinghouse (turbine), General Electric (motors) 16.8 MW (equivalent electrical load of auxiliary steam turbine output) Two (2) forced draft fans Westinghouse (fans) and General Electric (motors) 4,5 MW (1) primary and (2) secondary, Rornemuhle bisector regenerative Babcock & Wilcox 0.05 MW Belt conveyors, fuel feeders, pulverizers, and primary air fans FMC (conveyors), Westinghouse (PA fans), eavi (putvenzers), Stock (feeders) 15:8 MW

Sponsored by: Paul Franldin

3003

am Data

SYSTEM 1. DESCRIPTION OF COOLIC/WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEECRUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Lake Not ApplicaDre 0.15 (circulating wider pumps) (1) turbine driven BFP (1) mc4or driven BFP worthincecn (Pumps). Westinghouse (turbine). Allis Chalmers (motor) 0.45 MW (1) forced dralt fan, (1) induced draft fan Westinghouse 0.45 MW (1) tubular type Baba,* & Wilcox Not applicable Pressurized gas piping Not Applicable Not Applicable

'Based


c4 25

SOUTHWESTERN ELECTRIC POWER COMPANY LIEBERMAN #1 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURß!4E.GENERATOR 1. TURBINE MANUFAC TURER 2_ TURBINE DESCRIPTION 3. INLET TEMPERATURES 1 PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE 1 RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9, TYPE OF COOUNG 10. TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW CERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7, TYPE OF FUEL FIRING B. DESCRIPTION OF BURNER LAYOUT

poumnoN CONTROL 1. APPUCABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5, TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL. OF PARTICULATES 9. CURRENT LEVEL OF SOx ' TC:i. CURRENT LEVEL OF NOx 11. PERK MW LOAD Of PART, SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM ... 14. APPLICABLE WATER POLLUTION R 1,-- 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF OF WASTE WATER SY ••• - 17. TY?E OF WASTE WATER SY 18. MANUF OF WASTE DISPOSA 19. TYPE OF WASTE DISPOSA 20. PEAK MW LOAD OF WAST YS 21. PERK MW LOAD OF - s


General Eletlric Compan S,n e casin , condertsini , non-reheat 900"F / 850 • '1 Four 20" / 3600 RPM General Electrk Co • 31 250 KVA, 0 80 PF, 13,800 rods

Natural • as N e Not A!,;•lica le A .:. Natural gas

abcock & W PCŒS

B lanced d a , na. tcn. non-reh ea Not Applicable _ Front firing

Louis p t of Envlranmental Qualityegul U s Net Nct

.i.,

Applieabla 11 . Ap,pllcoble' ....,

ot AvaiIab *NotAvalI. N

ot +Ng' A ca

Louislana ment of Environmentaled aIity repulations orals lane Depmeni af Environmerttal Q a ity regulaticns

Not AppIlcabte Not Applicable Not App(icable Not Appficable Net Applicabie Nat abie


3004

Natural gas

Not APPlicabio Natural gas Babcock & WtIcox Balanced draft. natural circulation, non-reheat Not Applicable Front firing


General Electric ComPany Single casing, condensing. non-reheat 900*F / aso psig Four 20' .I 3600 RPM General EleCtric Company 31,250 KVA. 0,80 PF, 13,800 volts 20 MW Hydrogen DC exciter

Louisiana Department of Environmental Quality regulations Not Applicable Not APplicable Nc4 Applicable Not Applicable Not Apolicabie Not Applicable Not Applicable 'Not Available 'Not Available Not Applicable Not Applicable

Not ADOlicable Louisiana Department 01 Erwironmental Quality regutations Louisiana Department of Environmental Quality regulations

Not AOPliffahle Not Applicable 404 Appocable

Not Applicable Not Applicable Not Applicable

PUC Docket No. 46449 Schedule I-1-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY LIEBERMAN *2 GENERATING UNIT CHARACTERISTICS

CATEGORY

BI E-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE I RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION

BOILER 1. DESCIRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING • ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING B. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTRO 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8, CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13, PEAK MW LOAD OF NOx SYSTEM 14. APPUCABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS *Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6_ PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCFIIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12, PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFAC1URER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Lake Not Applicable 0.15 (circulating water pumps) (1) turbine driven BFP; (1) motor driven 8FP Worthington (pumps). Westinghouse (turbine), Allis Chalmers (motor) 0.45 MW (1) forced draft Ian, (1) induced draft Ian Westinghouse 0.45 MW (1) tubular type Babcock & Wilcox Not aPPlicable Pressurized gas piping Not Applicable Not Applicable


= 3005

RUC Docket No. 46449 Schedule H-12.31)

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY UEBERMAN 63 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES 1 PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SVE / RPMs 6. GENERATOR MANUFACTUREF1 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOLING 10, TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3, MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT


Westinghouse Electric Corporation Two casing, tandem compound, two flow exhaust. condensing, reheat 1000FF / 1000°F / 1450 psig Five 23 / 3600 RPM Westinghouse Electric Corporation 133,689 KVA, 0.85 PF, 13.800 volts 100 MW

Hydrogen DC exciter

Natural gas Fuel oil 30 MW reduction Natural gas Combustion Engineering Pressurized furnace. natural circulation, reheat Not Applicable Corner firing

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL B. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW 1.0A0 OF PART. SYSTEM 12, PEAK MW LOAD OF SOx SYSTEM • 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17, TYPE OF WASTE WATER SYSTEM 18, MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS

Louisiana Department of Environmental Duality regulations Not Applicable

Not Applicable Not Applicable Nol Applicable Not Applicable

Not Applicable Not Appricabte 0.0006 Las/Million Btu

0.1202 Lbs/Milfion Btu Not Apolicabfe Not Appficable Nol Applicable Louisiana Department of Environmental Quality regulations Louisiana Department of Environmental Ouality reoulations Not Applicable Not Applicabie Not Applicable Not Applicable Not Applicable Not Applicable

'Based on 2013-2015 EPA Air Ma ts Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FELUPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Lake Not Applicable 0.4 MW (circulating water pumps) (2) motor driven boiler teed pumps with hydraulic cowlings pacific Pumps (pumps), Allis Chalmers (motors) 1.9 MW (2) forced draft fans Buffalo Forge (fans), Allis Chalmers (motors) 1.0 MW

(2) Liunastrnin regenerative air heaters Air Preheater Corporation 0.01 MW Pressurized gasjiginri, oìl Plaine Not Applicable 0.06 MW (fuel oil pump)

Sponsored by Paul Franklin

!-• 3006 _ _


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY LIEBERMAN #4 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURB1NE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLAD1NG St2E i RPtiils 6, GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCiTATION

BOILER


Westinghousa Electric Corporation Two casing, tandem compound, two flow exhaust, condensing, reheat 1000°F 1 1000°F / 1450 psig Five 23 I 3600 RPM Westinghouse Electric Corporation 133,689 KVA, 0.85 PF, 13,800 votts 100 MW Hydrogen DC exciter

NaturN gas Fuel oil 30 MW reduction Naturai gas Combustion Engineering Pressurized lurnace, natural circulation, reheat Not Applicable Corner tiring

1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3, MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5 BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

PowynoN CONTROL 1. APPLICABLE AIR POLLUTION REG 2 MANUFACTURER OF PART. CONTROL & MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL . 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL B. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12 PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE Of WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2. MANUFACTURER OF COOLING WATER SYS & PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. -MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF OOMBUSTK)N AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER • 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Louisiana Department of Environmental Quality regulations Not Applicable Nol Applicable Not Applicable Not Appticable , Not Applicable Not Applicable Not Applicable 0.0008 LbsiMillion Btu 0.1175 Lbs414illion Btu

Not Applicable Nol Applicable Not Applicable Louisiana Department of Erwironmental Quality regulations Louisiana Department of Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable

Lake Not Applicable 0.4 MW (c(rculating water pumps) 2) motor driven boiler feed pumps with hydraulic couplings ,(

Pacrfic Pumps (pumps), Elliot CornPany (meters) 1.9 MW (2) forced draft fans Buffalo Forge (fans), Elliot Company (motors) 1.0 MW (2) Ljunqstrom regenerative air heaters Air Preheater Corporation 0.01 MW Pressurized gas Piolog. 08 RiPina Not Applicable 0.06 MW (fuel oil pumP)


3007


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY KNOX LEE #2 GENERATING UNIT CHARACTEFIISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FttUWATER HEATERS 5. LAST ROW Of BLADING StZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATtNGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOLING 10. TYPE OF EXCITATION

BOILER 1 DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3, MW DERAT1NG - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTUP.ER 8. TYPE OF BOILER 7. TYPE OF FUEL FIRING a DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2 MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTFIOL 5. TYPE OF PARTICULATE CONTROL .. 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx tO. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12, PEAK MW LO.AD OF SOx SYSTEM 13. PEAK NW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 13a on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOUNG WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUS110N AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTTON OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS , 15. PEAK MW LOAD OF FUEL FEED SYS


Westinahouse Electric Corporation . Single casínp. condensing, non-reheat 900F / 850 psig Four 20* / 3600 RPM Westinghouse Electric Corporation 44,118 KVA, 0.85 PF. 13,800 volts 30 MW Hydrogen DC exciter

Natural gas None Not Applicable Natural gas Babcock & Wilcox Pressurized furnace, natural circulation, non-reheat Not Applicable Front firing

Texas Commission on Environmenlal Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable 0.0006 Lbs/Million Btu 03734 Lbs/Miltion Btu

Not Applicable Not Applicable Not Applicable Texas Commission en Environmental Quality regulations Texas Corrimission on Environmental Oual4y regulations Not Applicable Not Applicable Not Applicable Not APPiicable Not Applicable Not Applicable

Lake Not APP6cable 0.3 MW (circulating water pumps) (2) motor driven boiler feed pumps Worthington (pumps). General Electric (motors) 0.6 MW (1) forced draft tan Westinghouse (tar). General Eiectric (motor) 0.3 MW (1) tubular tyPe Babcock & Wilcox Not Applicable Pressunzed gas piping Not Applicable Not Appiicable


3008


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY KNOX LEE it3 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1, TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS S. LAST ROW OF BLADING SUM / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL. GROSS MW OUTPUT . 9. TYPE OF COOLING 10. TYPE OF EXCITATION

BOILER


Westinghouse Electnc Corporation Single casing, condensing. non-reheat 900*F11350 osig Four 20' / 3600 RPM Westinghouse Bectdc Corporation 44,118 KVA. 0.85 PF, 13,800 votts 30 MW Hydrogen DC exciter

Natural gas None Not Applicable Natural gas Babcock & Wilcox Pressurized furnace, natural circulation, non-reneat Not Applicable ' Front firing

1. DESCRIPTION OF PRIMARY FUEL 2 DESCRIPTION OF ALTERNATE FUEL

MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1_ APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4, MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7, TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM ao. PEAK !VW LOAD OF WASTE WATER SYS 21, PEAK tAW LOAD OF WASTE DISP SYS -

on 2013-2015 EPA Air Markets Program Data

AU IES & COOUNG WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER Of BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS Et MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS RO. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AtR PREHEATER : 12, PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Texas Commission on Environmental Qualrty regulations Not Applicable Not Applicable Not Applicable Nat Applicable Not Applicable Not Applicable Not Applicable 0.0008 Lbs/Million Btu

*0.4470 Lbs/Million Btu

Not Applicable Not Applicable Not Applicable Texas Commission on Environmental Quality regulations Texas Commission on Environmental Qualltir regulations Not Applicable Not Applicable Not Applicable Not Applicable Nol Applicable

Not APPlicable

Lakø Not Applicable 0.3 MW (circulating water pumps) (2) motor driven borler feed pumps .

Worttdifu w (pumps), General Electric (rnotors) 0.6 MW (1) forced draft fan Westinghouse (fan), General Electric (motor) 0.4 MW (1) tubular type Babcock & Wilcox Not APOlicable Pressurized gas piping Not Applicable Not Applicable

Sponsored by: Pau) Franklin

3009

PUC Docket No. 46449 Schedule I-1-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY KNOX LEE #4 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE NERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES./ P1RESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF SLAMS SIZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMtNAL GROSS MW OUTPUT 9. TYPE OF COOLING 10 TYPE OF EXCITATION

BOILiR 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERt4ATE FUEL 3. MW DERATING • ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx . 12. PEAK MW LOAD OF PART, SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15, APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM .. 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MIN LOAD OF WASTE D1SP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM


General Electric Company Two casing, taridern compound, two flow exhaust, condensing, non-reheat 1000°F / 850 psig Five 20' / 3600 RPM General Etectric Company 91,875 KVA, 0.80 PF, 13,800 volts 75 MW Hydrogen DC exciter . .

Natural gas None Not Applicable Natural gas Riley Stoker - . Pressuiized furnace, rktural circulation, non-reheat Not Applicable Front firing

-Texas Commission on Emrironmental Quality regulations Not ApplicaMe Not Applicable - Not Applicable Not Applicable Not APIA:able Not Applicable Not Applicable . '0.0006 LbsiMillion Btu 0.2549 Lbs(Mil6on Btu

Not Applicable Not Applicable Not Applicable Texas Commission on Environmental Quality regulations Texas Commission on Environmental Quality regulations Nol Applicable Net AOOlicable Nol Applicable Not Applicable Not Applicable Not Aptgicable

1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS EL MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. - PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Lake Not Applicable 0.6 kW (cimulating water pumps) (3) motor driven pumps Worthinoton (pumps), Allis Chalmers (=tors) 1.2 MW (2) forced draft tans American Mower Corporation (tans), Allis Chalmers (motors) 1.0 MW (2) Llungstrom regeneradve Air Preheater Corporation Negligible Pressurized gas piping Not Applicable Not Applicable


577f 3010


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY KNOX LEE #5 GENERATING UNIT CHARACTERISTICS

CATEGORY

. TURBINE-GENERATOR 1. TURBINE MANUFACTURER • 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING StZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS a NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION

BOILER


General Electric Company Too casing, tandem compound. two flow exhaust, condensing. reheat 1000°F / 100TF 1 2000 psig Six 30 1 3600 RPM General Electric Compariy 390 MVA, 0.90 PF, 22,000 volts 323 MW Water cooled stator AC exciter

Natural gas Fuel oil 100 MW reduction Natural cas Combustion Enqineering Pressurized furnace, natural circulation. reheat Not Applicable Comer fired

1. DESCRIPTION OF PRIMARY FUEL Z DESCRIPTION OF ALTERNATE FUEL. 3. MW DERATING • ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1, APPLICABLE AIR POLLUTION REG , 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL. OF NOx 11. PEAK ktW LOAD OF PART. SYSTEM 12. PEAK PAW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. NIANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM. 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK WM LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS 3. PEAK NIW LOAD OF COOLING WATER SYS ' 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDRIMP SYS 6. PEAK IOW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8, MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD Of AIR PREHEATER 13. DESCRIPTPON OF FUEL. FEED SYS 14. MANUFACTURER OF FUEL. FEED SYS 15. PEAK MW LOAD OF RJEL FEE() SYS

Texas Commission on Environmental Quality regulations Not Applicable Not Applicable RJM Coif/. Not Applicable Not Applicable Burner water injection Not Applicable 0.0006 Lbs/Mdlion Btu 0.1224 Lbs/Million Btu Not Applicable Not Applicable ' Not Applicable Texas Commission on Environmental Quality regulations Texas Commission on Environmental Duality regulations Not Applicable Nol Applicable Not Applicable Plot Applicable Not Applicable Not Applicable

Lake Not Applicable 2.0 MW (circulating water Pumps) (I ) tuthine driven BFP. (1) motor driven BFP with hydraulic coupling Pacific Pumps (pumps), General Electric (turbine and motor) 7.3 MW (equivalent electrical load of auxiliary steam tudyne output) (2) forced draft fanS Green Fuel Econorrrrzer Company (fans), General Electric (motors) 5.2 MW (1) Liungstrom regenerative air heater Air Preheater Corporation 0.02 MW Pressurized gas piping, oil piping Not Applicable 0.09 MW (fuel oil pumps)


30H


of 25

SOUTHWESTERN Fl FCTR1C POWER COMPANY LONE STAR 81 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS S. LAST ROW OF BLADING SIZE/ RPMs & GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS & NOMMIAL GROSS MW OUTPUT 9. TYPE OF COOUNG Q. TYPE OF EXCITATION

BOILER I. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER . 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROt. 1. APPLICABLE AIR POU.UTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL • 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 1 I. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POWITION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS *Based on 2013-2015 EPA Ak Markets Program Data.

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF tX1OUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS 3, PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 5. PEAK MW LOAD OF BOILER FEEDPUMP SYS . 7. DESCRIPTION OF COMBUSTION AIR SYS & MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13, DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS • 15. PEAK MW LOAD OF FUEL FEED SYS


General Electric Oompany Two casing, tandem compound, two flow exhaust, condensing, non-reheat 900°F / 850 psig Four 16-1/2. / 3600 RPM General Electric Company 58,823 KVA, 0.85 PF, 1&800 volts • 40 MW Hydrogen DC exciter

Natural gas Fuel 011 None Natural gas Babcock & Wilcox Pressurized lumace, natural circulation. non-reheat Not Applicable Front tiring

Texas Commisslon on Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable 0.0006 Us/Million Btu 0.1078 Lbs/Million Btu

Not Applicable Not Applicable Not Applicable Texas Commission on Environmental Quality regulations Texas Comrnission on Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable

Lake Not Applicable 0.45 MW (circulating water pumps) (2) motor driven boiler feed pumps Pacific Pumps (pumps), Allis Chalmers (motors) 0.75 MW (1) forced draft fan Westinghouse 0.52 MW (1) tubular type Babcock & Wilcox Not Applicable Pressurized gas Ming, oil piping Not Applicable Not Applicable

Sponsored by: Faul Franklin

3012

PUC Docket NO. 46449 Schedule H-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY MATTISON et GENERATING UNIT CHARACTERISTICS

CATEGORY

COMBUSTION TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TUFIBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / FIPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS B. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG . 10. TYPE OF EXCITATION


POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL. 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8, CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx . 11. PEAK NW/ LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APFLICABI F WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS *Baseclon 2013-2015 EPA Air Markets P

AUXIUARIES & COOUNG WATER SYSTEM


Gerieral Electric, Co. Frarne 7, Model 7121 EA Combustion Turbine Ambient Not Applicable 3600 RPM Elio, Austria 102540 KVA, 0.85 PF, 13800 Volts 85 MW Air Electric Machinery Co Brushless Exciter

Not Applicable Not Applicable Not Applicable ..

Not Applicable Not Applicable - Not Applicable Not Applicable Not Applicable

Arkansas Pollution Control and Ecology CommIssion regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable '0.0036 Lbs/Million Btu 0.1080 Lbs/MOlion Btu

Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable

1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Part of Combustion Turbine System Part of Combustion Turbine System Not Applicable • Not Appficable Not Applicable Not Appficable Not APPlicalle Not Applicable Not Applicable Not Applicable Not APPlicable Not APplicabte

Not Applicable Not Apt:Citable


'3013


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY MATTISON li2 GENERATING UNfT CHARACTERISTICS

CATEGORY

COMBUSTION TURBINE-GENERATOR 1. TUR BINE MANUFACTUR ER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL. GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION i

BOILER 1. DESCRIPTION OF PRIMARY FUEL. 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL. 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL. 1. APPUCABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3 MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL B. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF sox la CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATEFI POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM la MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK NIW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS *Based on 413-2015 EPA Air Markets Program Data

AUXIUARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS a DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTON AIR SYS 10. DESCRIPTION OF AIR PREHEATER lt. MANUFACTURER OF AIR PREHEAI EH 12. PEAK PAW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14, MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS


General Electric, Co. Frame 7, Model 7121 EA Ccxnbuslion Turbine Ambient NW Applicable 3600 RPM Elio. Austria 102540 KVA, 0.85 PF, 13800 Volts 85 MW - Air . Electric Machinery Co Brushless Exciter _

Not Applicable Not APPIicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable

Arkansas Pollution Controt and Ecology Commission regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable . Not Applicable Not APPlicable 0.0006 LbstNlillion Btu 0.0972 LbsfMalion Btu

Not Applicable Not Applicable Not Applicable ' Not Applicable Not Applicable Not Applicable Not Apolicable Not Applicable Nat Applicabte Not Applicable Not App5cable

Part of Combustion Turbine System Part of Combustion Turbine System Not APplicable Not Applicable Not Applicable Not Applicable Net Applicable Not Applicable Not APPlicable Not APPlicable Not Applicable Not Applicable Not Applicable Not APOlicable Not Applicable


3014

PUC Docket No. 46449 Schedule 1412.3b

of 25

' SOUTHWESTERN ELECTRICPOWER COMPANY MATRSON*3 GENERATING UNIT CHARACTERISTICS

CATEGORY

COMBUSTION TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION a INLET TEMPERATURES I PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE I RPMs

GENERATOR MANUFACTURER ..6. 7. NAMEPLATE RATINGS 8 NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER p. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL -1, APPUCABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL a MANUFACTURER OF SOx CONTROL

MANUFACTURER OF NOx CONTROL ,4. 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx • 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPUCABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASI t DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXIUARIES & COOUNG WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEOPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPULIIP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTUREFI OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

DESCRIPTION/ RESPONSE

General Electric. Co Frame 7, Model 7121 EA Combustion Turbine Ambient Not Applicable 3600 RPM General Electric, Co. 101800 KVA, 0.85 PF. 13800 Volts 85 MW . Air Kato Bnishiess Exciter

Not Applicable Nal APPlicable NO APPlicable Not Applicabki Not Applicable Not Applicable Not Applicable Not Applicable

Arkansas Pollution Control and Ecoiogy Commission regulations Not Applicable Not Applicable Not Applicable .

Not Applicable Not Applicable Not Applicable -

Not APPlicable , 0.6006 LbsIMIllion Btu 0.0834 LbstMillion Btu

Not APPlicabie Not Applicable Not Applicable Not Applicable Not Applicable .

Not Applicable Not APPlizable Not APPlicabie Not Applicable Not ApPlIcable Not Applicable

Part of Combustion Turbine System Part of Combustion Turbine System Not Applicable Not Applicable Not APPtic-able Not Applicable Not Applicable Not Applicable Not Applicable' Not Appricable Not Applicable Not Applicable ' Not APPlicable Not Applicable Not AppRcable


3015


ot 25

SOUTHWESTERN ELECTRIC POWER COMPANY mArnsoN #4 GENERATING tirgrr CHARACTERISTICS

CATEGORY

COMBUSTION TURBINE-GENERATOR 1. TURBINE MANUFACTURER .

2. TURBINE DESCRIPTION 3. INLET TEMPERATURES 1 PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE I RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT ' 9. TYPE OF COOUNG 10. TYPE OF EXCITATION

BOILER I. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL . 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx , 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYS i EM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WAsn DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MIN LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Air Martts Program Data

AUXILIARIES & COOUNG WATER SYSTEM


General Electric. Co. .

Frarne 7, Model 7121 EA Combustion Turbine Ambient Not Applicable 3600 RPM General Electric, Co. 101800 KVA, 0.85 PF, 13800 Volts 85 MW Air Kato Brustiless Exciter

Not APPlicable • Not Applicable Not Applicabte Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable

Arkansas Pollution Control and Ecology Commission regulatbns Not Applicable Not Applicable N9i Applicable Not Applicable . Not Applicable . Not Appliosble Not Applicable *0.0006 Lbs/Milion Btu 0.0928 Lbs/Mithon Btu Not Applicable Not Applicable ' Not Applicable Not Applicable Not Applicable Nat Applicable Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable

1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS a PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AHR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Part of Cornbustiori Turbine System Part of Combustion Turbine System Not Applicable Not Applicable Not Applicable Nat Ariplicable Not Applicable Not Applicable . Not Applicable Not Applicable Nat APPlicable Not Applicable Not Applicable .

Not APPItable Not Applicable

Sponsored by. Paul Franklin

3016

PUC Docket No. 48.449 Schedule H-12.3b

Page 16 of 25

SOUTHWESTERN ELECTRIC POWER COMPANY JOHN W. TURK PIJINT GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR

t . TURBINE IAANU FACTURER

2. TURBINE DESCRIPTION

3. INLET TEMPERATURES / PRESSURES

4. NUMBER OF FEEDWATER HEATERS

5. LAST ROW OF BLADING sae / RPMs

& GENERATOR MAI4UFACTURER

7. NAMEPLATE FIATINGS

8. NOMINAL GROSS MW OUTPUT

9. TYPE OF COOLING

10. TYPE OF EXCITATION

BOILER

1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL

3. MW DEBATING • ALTER FUEL USE

4. STARTUP FUEL

5. SOLER MANUFACTURER

6. TYPE OF BOILER

7. TYPE OF FUEL FIRING B. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL

1 APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL

3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER CP NOx CONTROL

5. TYPE OF PARTICULATE CONTROL

8. TYPE OF SOx CONTROL

7. TYPE OF NOx CONTROL . 6. CUR RENT LEVEL OF PARTICULATES

9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NON

11. PEAK TAW LOAD OF PART. SYSTEM

12. PEAK MW LOAD OF SOx SYSTEM

13. PEAK MW LOAD OF NOx SYST94

14. APPLICARI F IIYATER POLLUTION REG

15. APPLICABLE WASTE DISPOSAL REG

16. NAMUR OF WASTE WATER SYSTEM

17. TYPE OF WASTE WATER SYSTEM

18. MANUF OF WASTE DISPOSAL SYSTEM

19. TYPE OF WASTE DISPOSAL SYSTEM

20, PEAK MW LO.AD OF WASTE WATER SYS

21. PEAK MW LOAD OF WASTE DISP SYS

'Based on 2013-2015 EPA Ae easels Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS

2. MANUFACTURER OF COOLING WATER SYS

3. PEAK MW LOAD OF COOUNG WATER SYS

4. DESCRIPTION OF SOLER FEEDPUMP SYS

5. MANUFACTURER OF BOLLER FEEDPUMP SYS

8. PEAK MW LOAD OF BOILER FEEDPUMP SYS

7. DESCRIPTION OF comatisnoN AIR SYS

B. MANUFACTURER OF COMBUSTION AIR SYS

9. PEAK MW LOAD OF COMBUSTION AIR SYS

10. DESCRIPTION OF AIR PREHEATER

11, MANUFACTURER OF AIR PREHEATER

12, PEAK MW LOAD Of AIR PREHEATER

13. DESCRIPTION OF FUEL FEED SYS

14. MANUFACTURER OF FUEL SYS

15. PEAK MW LOAD Of FUEL FEED SYS



Alstorn Alstom steam tub:le-generator is a fax casing. 3600-rpn. tandem compound, single reheat. saideneell) machete. The keine consists of semis flow high-pressons (HP) turbine section, a doultie how ireeenedate-rxesatre (IP) turbine section end too double flow kw pressure (LP) turbine sectlons Mai down exhausts (a Gar few LP tudWW). SH: 1115F/3515 Psi RH: 1125T/750. Psi

34 Irich 3600 rpm Alstorn

840 MVA Rating. 085 Power Faclor. 2 Pole, 3 phase

682 Direct Hydrccen cookie field and stator core. Direct weter cooled stator windings

Static ExCtif -

Low Stilts Powder River Basin docv , le/A NIA

Nahsal Gas

Babcock &Moos Ptimerlaed coal feed Spiral Would Universal Presstre (SWUM uttra staler ertical boiler

Poexiet River Basin (PRB) 30 low NOx burners ,3 levet omosed firing 10 low nox pans

ADEO Tile V *2123-A0P-R2

B&W

B&W B&W

Bagtkruse Spray Oni At:ember

Selezlive Catatelc Reducbon MIll 19% NH3

Lima s 10%, CUllefit OS%

0.0553 Lbs/Mtlion Btu 0.0103 Lbs/Mrilon Btu

N/A 1 mw N/A ADEO AR0051136 ADEO Class 3N soficl waste SHAW/CBI

settling Pend watt caste

UCC

Solid Landlit N/A .

NIA

Mechanical drat 16 cells. Z 3400 Hp circ temps SPX Coo5mTechnologitet 3.6 MW 1 turbine teettptsnp. 1 motor feedptinp

Turtine: Attar. Portz Floweerve. Motor: TECO Westingtimee. PunPl Flowserve Ttrblne: 10.5 MW Motor 3.7 MW

Belarced Draft

11.2 MW (ED, ID & PA fare)

Trisector lisigstnin

Alstom ,

0.09 MW

Nat Gast pipefre Ned Coak 613SW-98N PuèeerLat

Nal Gni B&W CoatB&W

Nat Gas: NAA Coat 1.8Mw

3017

Lignite

Not Applicable Natural gas 'Babcock & Wilcox Balanced draft, natural circulation, reheat Pulverized Opposed firirig

1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER -6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

BOILER

OLLUTI CONTROL 1. APPLICABLE AIR POLLUTION REG 2 MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM i 2. PEAK MW LOAD OF SOx SYSTEM 13. PEAK k4W LOAD OF NOX SYSTEM 14. APPUCABLE WATER POLLUTION REG 15. APPLICAR1 F WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE ()GP SYS

'Texas Commission on Environmental Quality reoulations United Oil Products Air Correction Division United Oil Products Air Correclion Division Advanced Burner Technologies Corp. Cold side electrostatšc preciritator Limestone absorption Low NOx burners with overfire air 0,04 M./million Btu *0.1776 Lbs/Million Btu *0.1591 LbstMilfion Btu 4.4 MW 7.5 MW Not Applicable Texas Commission on Environmental Quality regulations Texas Commission on Environmental Quality reoulations Ecodyne-Graver Water Divison Lime treatment for solids precipitation Not Applicable Landfill for combustion by-products and FGD sludge System not used - Not Applicabie

PUC Docket No. 46449 Scheduie 1-1-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY HENRY W. PIRKEY *1 GENERATING UNfT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES I PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF &ACING 417F / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION

DESCRIPTION I RESPONSE

Westinghouse Electric Corporation Four casing, tandem compound, four flow eithaust, condensing, reheat 1000°F 11000•F I 2400 psig Seven ., 28-1/2' / 3600 RPM Westinghouse Electric Corporation 775 MVA, 0.93 PF. 24,000 volts 660 MW Water cooled stator . Brushiess AC exciter

"Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2, MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK INAW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS ,

Lake Not Applicable 4.5 MW (circulaling water_pumPa) sil turbine driven BFP; (1) motor driven BFP with hYdraulic courginfl Pacific Pumps (pixnps), Weslinghouse (turbine), General Electric (motors) 10-8 WM/ (eQuivalent electrical load of auxiliary stearn turbine output) Two (2) forced draft fans Westinobouse (fans) and General Electric (motors) 4.5 k4W , (1) primary and (2) secondary, Rothemuhle bisector 1erierierative Babcock & Wilcox 0.05 MW Bett conveyors, fuel feeders, pulverizers, and primary air fans FMC (conveyors). Westinghouse (PA fans), B&W (pulverizers), Stock (feeders) 17.0 MW


3018,

Natural gas Fuel oil 27 MW reduction Natural gas Combustion Enclineering Pressurized furnace, natural circulation, reheat Nat Applicable Comer fired


General Electric Company Two casing, tandem compound, two flow exhaust, condensing. rebeat 1000T / 1000°F / 1800 Psig Six 23 / 3600 RPM General Electric Company 211,200 KVA. 0.85 PF. 20.000 volts , 160 MW Oil cooled stator DC exciter

Texas Commission on Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable Not APPIitable Not Appficabte Net Applicable 0.0007 Lbs/Milffon Btu 0.0939 Lbs/MIllion Btu

Not Applicable Not Applicable Not Applicabie Texas Commission on Environmentat Quality regulations Texas Commission on Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable • Not Applicable Not Applicable


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY WILKES #1 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE fiAANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs 6 GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOLING 10. TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL - 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POU.UTION CONTROL. 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL. 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SQx CONTROL 7 TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPUCABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16 MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM ..

20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYSTEM 1. DESCRIPTION OF COOLING WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPLAAP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER - 11. MANUFACTUREFI OF AIR PREHEATER . 12. PEAK MW LOAD OF AIR PREHEATER 13.- DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS . 15. PEAK MW LOAD OF FUEL FEED SYS

Lake and cooling tower Not Applicable 0.6 MW (circulating water pumps) (2) motor driven boiler feed pumps Pacific Pumps (pumps), General Electric (motors) 3.7 MW (2) forced draft fans Westinghouse (fans), General Electric (motors) 1.5 MW Teo Liungslrom regenerative air heaters Air Preheater Corporation 0.01 MW Pressurized gas piping, oil piping Not Applicable 0.06 MW (fuel oil pump)


3019

PUG Docket No. 46449 Schedule H-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY WILKES 42 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER . 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF GOOUNG 10. TYPE OF EXCITATION


POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2 MANUFACTURER OF PART, CONTROL 3. MANUFACTURER OF SOx CONTROL 4. M.ANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx it. PEAK MW LOAD OF PART. SYSTEM 12. PEAK Wil LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM • 14. APPLICABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM • 19. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Based on 2013-2015 EPA Nu Markets Program Data

AUXUARIES & COOUNG WATER SYSTEM


General Electric Company . Two casing, tandem compound, two Pow exliaust condensing, reheat 1C,00°F / 1000F / 2000 psig Six 30' / 3600 RPM General Electric Company 390 MVA, 0.90 PF, 22,000 votts 323 MW Water cooled stator AC exciter .

Natural gas None .

Not AKA cable Natural gas Babcock & Wilcox . Pressurized furnace, natured circulation. reheat Not APPlIoable Opposed

Texas Commission on Environmental Quality reoulations Not AloPticable Not Applicable RJM C o ffi. Not Applicable Not Applicable Low NOx bumers Not APplicable 0,0006 Lbs/Milion Btu 0.1511 Lbs/MPlion Btu Not Applicable Not Appficatie Not Applicable Texas Commission on Environmental Orally regulations .

Texas Commission on Environmental Quality regulations No: Aloolicable Not AoVicable Not Applicable Not Applicable Not Applicable Not Applicable

1. DESCRIPTION OF GOOUNG WATER SYS 2. MANUFACTURER OF COOUNG WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4, DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6, PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATEFI 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPT/ON OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Lake and cooling tower No( Applicable 1.2 MW (circulating wafer pumas) . 11) turbine driven BFR, (1) motor drrven BFP with hydraulic coupling Pacific Pumps (pumas), General Electric (turbine and motors) 7.3 MW (equivalent electrical load ot auidliary steam turbine outPut) (2) forced draft tans Air Preheater Company (fans), General Electric (motors) 4.5 MW (1) Ljunostrom regenerative Air Preheat& Corporation 0.02 MW Pressurized oas piping Not Applicable Not Applicable

Sponsored Oy: Paul Franklin

30(k

PUC Docket No. 464-49 Schedule H-12.3b

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY WILKES #3 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES -4. NUMBER OF FEEDWATER HEATERS 5, LAST ROW OF BLADING SIZE if RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG -W. TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE PJEL 3, MW DERAT1NG - ALTER FUEL USE ' 4. STARTUP FUEL 5. BOR_ER MAMUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

DESCRIPTION/ RESPONSE

General Electric ComParly . Two casing, tandem compound, two flow exhaust, condensing, reheat 1000°F / 1000°F / 2000 Psig Six 30' / 3600 RPM General Electric Company 390 MVA, 0.90 PF, 2Z000 volts 323 MW Water cooled stator AC exciter

Natural gas None Not Applicable Nalural gas Babcock & Wilcox Pressurized furnace, natural circulation, reheat Not Applicable Opposed

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM O. MANUF OF WASTE DISPOSAL SYSTEM

19_ TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS

Texas Commission on Environmental Qualty regulations Not Applicable Not Apphcable , RJM Corp. Not Applicable Not Applicable Low NOx burners Not Applicable • *0.0006 Lbs/Million Btu -0.0908 Lbs/Million Btu Not Applïcabte Not Applirahl•i Not Applicable Texas Commission on Environmental Ouality reoulations Texas Commission cm Environmental Quality regulations Not Applicable Not Applicable Not Applicable Not Applicable Not Applicable Noi Applicable

*Based on 203-2015 EPA Air ets Program Data

AUXILIARIES & COOUNG WATER SYSTEM 1. DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF corvisus-noN AIR SYS 8. MANUFACTURER OF comsusnoN AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER

I. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Lake and cooling tower MeneY (cooling tower) _ 33 MW (circulating water pumps and cooling tower) (1) turbine driven BFP; (1) motor driven BFP with hydraufic coupling Pacific Pumps (pumps), General Electric (turbine and motors) 7.3 MW (equivalent electrical load of auxiliary steam turbine output) (2) forced draft fans Westinghouse (fans), General Electric (rnotors) 4.5 MW (1) Uungstrom regenerative Air Preheater Corporation 0.02 MW Pressurized gas Piping Not Applicable Not Applicable

Sponsored by: • Paul Franklin

3021

PUC Docket No. 46449 Schedule H-12.31,

of 25

SOUTHWESTERN ELECTRIC POWER COMPANY WELSH 41 GENERATING UNIT CHARACTERISTICS

CATEGORY

TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATEFIS 5. LAST ROW OF BLADING SIZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOUNG 10. TYPE OF EXCITATION


Westinghouse Electric Corporation Three casing, tandem compound, four flow exhaust, condensing, reheat 1000°F / 1000°F 1 2400 psig Seven 25' / 3600 RPM Westinohouse Electric Comoany 620 MVA. 0.90 PF. 18,000 volts 512 MW • Hydrogen Brushless AC exciter

Western coal None Not Applicable No. 2 fuel oil Babcock & Wilcox Balanced draft, natural circulation, reheat Pulverized Opposed

BOILER 1. DESCRIPTION OF FRIMARY FUEL . 2. DESCRIPTION OF ALTERNATE FUEL 3, MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CONTROL 1. APPLICABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPLICABLE WASTE DISPOSAL REG 16, MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19. TYPE OF WASTE DtSPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS . 21. PEAK MW LOAD OF WASTE DISP SYS `Based on 2013-2015 EPA Air Markets Program Data

AUXILIAFIIES & COOUNG WATER SYSTEM 1. DESCRIPTION OF COOLING WA I tH SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOUNG WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS . 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

Texas Commission on Environmental Quality regulations Research-Cottrell Not Applicable Advanced Burner Technologies Corp. Hot side electrostatic precipitator/Pulse Jet Fatiric Fitter None Low NOx burners with overtre air 0.0028 LbsiMillion Btu T.4276 LbstMon Btu 0.1819 Lbs/MIltion Btu

2.7 MW '

Not Applicable Not Applicable Texas Commission on Environmental Quality regulations Texas Commission on Environmental Quality regulations Not Applicable Not Applicabte Not APPlioat4e Landfill for combustion by-products ' Not Applicable No1 Applicable

Lake and cooling tower Not applicable 3.4 MW (circulating water pumlds) (1) turbine driven BFP; (1) motor driven BFP with hydraulic coupling DeLaval (TDBFP), Pacific (MDBFP), Westinghouse (turbine), GE (motor) 13 MW (equivalent electrical toad ol auxiliary stearn turbine output) Two (2) forced draft fans Westinghouse (FD fans) and General Electric (rnotors) 2.6 MW (2) Liuriastrom regenerative 41-sector air heaters Air Preheater Corporation 0.06 MW Belt conveyors. coal feeders. Pulverizers. and Pnmerv air fans J.B. Webb (corweyors), Stock (feeders), B&W fpuly.), Westinghouse (PA fans) 9.8 MW


3022

Western coa i.• 'one 04 .ticable

No. 2 fuel o11 Babcock & 1. loos Balaaced dratt, n atu a rehea Ptilverízed •Opposed

POLLUTION CONTROL 1. APPUCABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL. 4. MANUFACTURER OF NOx CONTROL 5. TYPE OF PARTICULATE CONTROL 6. TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL 8, CURRENT LEVEL. OF PARTICULATES 9, CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD oF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 13. PEAK MW LOAD OF NOx SYSTEM Ia, APPUCABLE WATER POLLUTION REG 15. APPLICABLE WASTE (ISPOSAL REG. 16. MANUF. OF WASTE WATER SYST 17. TYPE OF WASTE WATER SYSTE 18. MANUF OF WASTE DISPOSALSYST 19. TYPE OF WASTE DISPOSAL Q,, . E 20. PEAK MW LOAD OF WAS t YS 21. PEAK MW LOAD OF WAS

rners

Texas C Res earc N Apptica

vironmental Quality regulations

Btu LbsiMition BTU

••0.1666 Lbs/Mdlion BTU .9 MW

Not Applicable Not Applicabie Texas Commission on Environmental Quanty regulations Texas Commission on Environmental Qualty regulations Not Apocabie Not APolicade Not Applicable Landfill Ice combustion by-products Not Appficable Not Applicabie

1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION OF ALTERNATE FUEL 3. MW DERATING • ALTER FUEL USE 4, STARTUP FUEL S. BOILER MANUFACTURER 6. TYPE OF BOILER 7. TYPE OF FUEL FIRING 8. DESCRIPTiON OF BURNER LAYOUT


of 25

SOUTHWESTERN ELECTRIC POWER COMPANY WELSH a2 GENERATING UNIT CHARACTERISTICS

CATEGORY 1


TURBINE-GENERATOR 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES / PRESSURES 4. NUMBER OF FEEDWATER HEATERS S. LAST ROW OF BLADING SIZE i RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOLING 10. TYPE OF EXCITATION

BOILER

Wesagttouse Electrlc Corporation Tlireo caslng. tandealccmpound, four liow exhat,st. Londensing, reheat 000 1300eF 2400 psiç

Seven 25/3$OGRPM Westinghouse Electric Company :.-?.. 620 t1A 0.90 PF. 18,000 vdts 512 MW H dr. • BrushlessACexciter

1, DESCRIPTION OF TER SYS 2. MANUFftTURE ,:t.,.„ ATER SYS 3. PEAK MW LOAD ''.:" - • G WATER SYS • 4. DESCRIPTION OF : • FEEDPUMP SYS 5. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7. DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12. PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS . 15. PEAK MW LOAD OF FUEL FEED SYS

Lake and cooling tower Not applicable 3.4 MW (circulating water pumps) (1) turbine drivers 8FP: (1 ) motor drNen BFP with hydraulic coupling Pacific Pumps (pumps), Westinghouse (turbine), General Beane (mdors) 13 MW (equivalent electrical load of auxiliary steam turbine output) Two (2) forced draft fans Westinghouse (FD fans) and General Electric (motors) 3.0 MW (2) Llungstrom regenerafive VI-sector alr heaters Air Preheater Corporafion 0.06 MW . Coat feeders, puiverizers, and Prirrialy air fans - Stock (feeders), Babcock & Wilcox (pulverizers), and Westinghouse (PA fans) 8.7 MW

/


3023

PUC Docket No, 46449 Schedule H-12_3b

of 25

SOUTI-IWESTERN ELECTRIC POWER COMPANY WELSH n GENERATING UNIT CHARACTERISTICS

CATEGORY

'TURBIHE-GENERAT 1. TURBINE MANUFACTURER 2. TURBINE DESCRIPTION 3. INLET TEMPERATURES 1 PRESSURES 4. NUMBER OF FEEDWATER HEATERS 5. LAST ROW OF BLADING SIZE / RPMs 6. GENERATOR MANUFACTURER 7. NAMEPLATE RATINGS 8. NOMINAL GROSS MW OUTPUT 9. TYPE OF COOLING 10. TYPE OF EXCITATION

BOILER 1. DESCRIPTION OF PRIMARY FUEL 2. DESCRIPTION! OF ALTERNATE FUEL 3. MW DERATING - ALTER FUEL USE 4. STARTUP FUEL 5. BOILER MANUFACTURER 6. TYPE OF BOILER 7, TYPE OF FUEL FIRING 8. DESCRIPTION OF BURNER LAYOUT

POLLUTION CO 1. APPUCABLE AIR POLLUTION REG 2. MANUFACTURER OF PART. CONTROL 3. MANUFACTURER OF SOx CONTROL 4. MANUFACTURER OF NOx CONTROL S. TYPE OF PARTICULATE CONTROL 6, TYPE OF SOx CONTROL 7. TYPE OF NOx CONTROL fl. CURRENT LEVEL OF PARTICULATES 9. CURRENT LEVEL OF SOx 10. CURRENT LEVEL OF NOx 11. PEAK MW LOAD OF PART. SYSTEM 12. PEAK MW LOAD OF SOx SYSTEM 11 PEAK MW LOAD OF NOx SYSTEM 14. APPLICABLE WATER POLLUTION REG 15. APPUCABLE WASTE DISPOSAL REG 16. MANUF. OF WASTE WATER SYSTEM 17. TYPE OF WASTE WATER SYSTEM 18. MANUF OF WASTE DISPOSAL SYSTEM 19, TYPE OF WASTE DISPOSAL SYSTEM 20. PEAK MW LOAD OF WASTE WATER SYS 21. PEAK MW LOAD OF WASTE DISP SYS 'Data Obtained hom EPA Air Markets Program Data

AUXILIARIES & COOLING WATER SYST 1, DESCRIPTION OF COOUNG WATER SYS 2. MANUFACTURER OF COOLING WATER SYS 3. PEAK MW LOAD OF COOLING WATER SYS 4. DESCRIPTION OF BOILER FEEDPUMP SYS S. MANUFACTURER OF BOILER FEEDPUMP SYS 6. PEAK MW LOAD OF BOILER FEEDPUMP SYS 7, DESCRIPTION OF COMBUSTION AIR SYS 8. MANUFACTURER OF COMBUSTION AIR SYS 9. PEAK MW LOAD OF COMBUSTION AIR SYS 10. DESCRIPTION OF AIR PREHEATER 11. MANUFACTURER OF AIR PREHEATER 12 PEAK MW LOAD OF AIR PREHEATER 13. DESCRIPTION OF FUEL FEED SYS 14. MANUFACTURER OF FUEL FEED SYS 15. PEAK MW LOAD OF FUEL FEED SYS

DESCRIPTION f RESPONSE

Westinghouse Electric CorPoration Three casing, tandem compound, four flow exhaust, condensing, reheat 1000`F / 1000°F / 2400 Osiq Seven 25 I 3600 RPM Westinghouse Electric ComPany 620 MVA, 0.90 PF, 18,000 volts 512 MW Hydrogen Brushless AC exciter

Westem coal None Not Applicable No. 2 fuel oil Babcock & Wilcox Balanced draft, natural circulation. reheat Pulverized Opposed

Texas Commission on Environmental Quality regulations Research-Cottrell Not Applicable Babcock & Wilcox Hot side electrostatic precipitator/Pulse Jet Fabric Filter None Low NOx burners with overfire air 0.0041 Lbs/Million Btu 0.4260 Lbs/Million Btu 0.1846 Lbs/M4lion Btu

2.7 MW Not Applicable Not Applicable Texas Commission on Environmental Quality regulations Texas Commission on Environmental Quality regulations Not Applicable Not Applicable Not Applicable Landfill for combustion by-Products Not Applicable Not Applicab/e

Lake and cooling tower Research CttJl (cooling tower) 6.2 MW (circulating water pumps and cooling tower fanstpurnPs) (1) turbine driven SEP; (1) motor driven BFP with hydraulic coupling Pacific Pumps (pumps), Westinghouse (turbine). General Electric (motors) 13 MW (equivalent electrical load of auxiliary steam turbine output) Two (2) forced draft tans Westinghouse (FD fans) and General Electric (motors) 3.0 MW (2) Uungstrom regenerative tri-sector air heaters Air Preheater Corporation 0.06 MW Coal feeders, Pulverizers, and primary air fans Stock (feeders), Babcock & Witcox (pulverizers). and Westinghouse (PA fans) 8.7 MW


3024

SOUTHWESTERN ELECTFtIC POWER COMPANY EFFICIENCY AND CONTROL SYSTEMS

PUC Docket No. 46449 Schedule H-12.3c

Page 1 of 26

This schedule contains Non-Confidential and Highly Sensitive information. For the Highly Sensitive information, see the High), Sensitive schedule.

Sponsored by: PauI Franklin

3025

CATEGORY

INMIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOUNG WATER S. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7, NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM MW I TOTAL Btus 3. MNIMUM MW / INCREMENTAL Btus PER MW h 4. 1ST STEP MW / INCREMENTAL Btus PER MWh 5. 2ND STEP MW ./ INCREMENTAL Btus PER MWh 6. 3R1) STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8, 5TH STEP MW I INCREMENTAL Eiltus PER MWh

THREE MOST RECENT HEAT RATE TESTS

DATE 1. TEST 1 MW OUTPUT

HEAT RATE INCREMENTAL HEAT RATE

2. TEST 2 kW OUTPUT HEAT RATE

INCREMENTAL HEAT RATE 3. TEST 3 MW OUTPUT


CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 1 a TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY ARSENAL HILL #5 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PUC Docket No. 46449 Schedule H-12.30

Page 2 of 28


842% 11500 psig / 1005•F 8,532 Btu/KWh I 1450 psig / 1000T 98.90%1125 MW : 77.5 WAR 2.50 Hg absolute / 67,200 gpm 10,479 Btu/KWh * 100,000 gross KW 4,000 KW 10,916 Btu/KWh ill 96,000 net KW Not Available

REDACTED

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 LEVEL 6 LEVEL 7 LEVEL 8

REDACTED

Mecharicat - HydrauUc Control . General E.:*ctric 1960: Cost included with turbine-generator Programmable logic controller (PLC) based system. Central & South West - Engineering Servies ' 1998: $319,000 Mechanical positioning of inlet vatves Mechanical positioning of feechvater valve

One None None

NOTES: 0) GROSS HEAT RATE - TOTAL' FUEL CONSUMED (Including Start - up) (in rrirBtu 's)

GROSS ELECTRICAL OUTPUT TOTAL FUEL CONSUME) (rrenStu s)

GROSS ELECTRCAL OUTPUT - STATION SERVICE

Vacate whether Mallon Service hciudes calsurnp6on tor Common Facfrtie


(2) NET HEAT RATE .

3026

STALL (ARSENAL HILL #6) GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS SOUTHWESTERN ELECTRIC POWER COMPANY


Page 3 of 26


99.5% / 1084F / I058F 0 151Ipsi (HRSG Performace Data Case 7) 6,119 Btu/Gross KWh / 1050°F / 1050`F 42 1882 psi design (calcu(ated) 6A & 68: Not Available % / 184.5 Mve I 115 MVAR 65: Not Available % / 256.02 Mw / 160 MVAR 215 Hg Absolute I 166,999 gpm 6,150 Btu/14.M (LHV) @ 537.2 Gross Mw (Case Stuch, 7, 100% load 72F)

15,400 Kw 6,331 BtuiKwh (LHV) 0 521.8 Gross Mw (Case Study 7, 100% load 72F) Not Available

REDACTED

DATE

1

June-10

LEVEL I LEVEL 2 L.EV EL 3 LEVEL 4 LEVEL 5 LEVEL 6 LEVEL 7 LEVEL 8

REDACTED

CATEGORY

TIAL DE IGN EFFICIENCIE 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY I STEAM CONDITIONS

3. GENERATOR EFFICIENCY l MW : MVAR

4. CONDENSOR CONDITIONS / COOUNG WATER S. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EOUATION

"PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCIREMENTAL Btus PER MWh 4. 1ST STEP MW 1 INCREMENTAL Btus PER MWh 5. 2ND STEP MW / INCREMENTAL Btus PER MWh 6. 3RD STEP MW f INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Bars PER MWO 8. ETH STEP MW I INCREMENTAL Btus PER MWh


1. TEST 1 MW OUTPUT HEAT RATE




INCREMENTAL HEAT RATE

CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL. SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTAUATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

Digital Electro Hydraulic / Fuel Combustion CT Control 6A & 68: Siemens T-3000, 65: ABB Symphony Feb 2010, Commercial Operation June 2010 DCS (Distributive Corrtml System tor both HRSG's) ABB Feb 2010, Commercial Operation June 2010 N/A 6A & 6B: Motor Driven Boier Feed Pump. constant &Peed, DOS wivering racirc N/A .., 1- Main Control Romm, (1 Engineering Control Station) N/A

_

NIA

NOTES: (1) GROSS HEAT RATE

(2) mEr HEAT RATE

TOTAL FUEL CONSUMED (iricluebo Sian • up) On =sty 's)

GROSS B.ECIRCAL OUTPUT

TOTAL Fua CONSUMED (=au's)

GROSS ELECTRICAL OUIPUT - STATION SERVCE

Indic:ale whether Slake Service irducles consumption for Common Facilities.

Spcosored by: Paw Franklin

3027 ,

SOUTHWESTERN ELECTRIC POWER COMPANY LIEBERMAN #1 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


Page 4 of 26

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY I STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSCR CONDITIONS / COOLING WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Mils 2. MINIMUM MW / TOTAL Bba 3. MINI 54.1v1 MW 1 INCREMENTAL Bt1 s PER Mihih 4. 1ST STEP MN / INCREMENTAL Btus PER h4Wh 5. 2N0 STEP MIN 1 ;NCREMENTAL Btus PER MWI1 6. 5RD S i MW i NCREMENTAL Btus PER tAvvri 7. 4TH STEP MW /INCREMENTAL Btus PER MINIti 8. 5TH STEP NMI 1 INCREMENTAL. Btus PER MVO

THREE MOST RECENT fitAT RATE TESTS

1. TEST 1 MIN OUTPUT HEAT RATE

INCREMENTAL HEAT RATE 2. TEST 2 MIN-OUTPUT

HEAT RATE INCRevIENTAL HEAT RATE

3. TEST 3 NW/ OUTPUT ' HEAT RATE

I NCRU4ENTAL HEAT RATE

L.LAS l KUL JT 1 CM* 1. DESCRIPTION OF TURBINE CONTROL SYS 2. MANUFACTURER OF TURBINZ CON O 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL 5. MANUFACTURER OF BOILER A 6. DATE& COST OF INSTALLATIO 7.IYPEOFFANCONTROŠ.SYS = 8. TYPE OF FEEDWATER P ROL SYS. 9. TYPEOFSOOT.OW SYS. 10. NUMER OF OPERAT -OL ROOMS 11.D WRIPTION o ON SYS 12 TYPE OF SCRUB -OL SYS.


82.2% / 875 psig / 910T 9.535 Btu/KWh 1 850 psig / 930*F Not Availaidel 25 MW : 1815 MVAR 1.50* Hg abscAute / 35.000 gpm 11,600 Btu/KWh 20000grossKW 600 KW 11.959 Btu/(Wh fp 19.430 net KW Not Available

Mechanical - Hydraulic Control General Eeetrie 1947: Cost included W.th bid:ire-generator C4sfributed costrci system. Central & Scuth West - Engineering Sefvies 1999.. 6310.000 Mechanical positioning of forced and induced draft Ian Inlet valves Speed calve. CrOBFP): mechanical positioning or feechireter valve (MDBFP) None One room commal 10 units 1&2 None None

NOTES : (1) GROSS HEAT RATE

(2) NET HEAT RATE GROSS ELECTRICAL OUTRJT - STATION SWNICE

lecke. whether Station Service inoWes consumption for Common FacTiees.

TOTAL FuEL CONSuM83 (Inclustreg Stott - up) (Si nuriku ' s)

GROSS ELECTRCAL OUTFUT

TOTA L Fua CONSUMS3 (mmtatu's)


3028 .

CATEGORY

INITIAL DESIGN EFFICIENCIES

I. BOILER EFFICIENCY ¿STEAM CONDITIONS 2. TURBINE EFFICIENCY I STEAM CONDITIONS

3, GENERATOR EFFICIENCY / MW : MVAR

4. CONDENSOR CONDITIONS / 000LING WATER

5. GROSS HEAT RATE (1)

6. ORIGINAL STATION LOAD

7. NET HEAT RATE (2)

8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus

2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Blus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER KWh

5. 2ND STEP MW / INCREMENTAL Btus PER MWti 6. 3R0 STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MIN I' INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER MWh


1. TEST 1 MW OUTPUT

HEAT RATE


HEAT RATE , INCREMENTAL HEAT RATE

3. TEST 3 MW OUTPUT

HEAT RATE


CONTROL SYSTEMS

DATE

1995

1994

1989

1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. r(PE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY UEBERMAN #2 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PDC Docket No. 46449 Schedule H-12.3c

Page 6 of 26


82.23s / 875 psig / 910°F .

9,535 Btu/KWh / 850 psis i 900°F Not Available / 25 MW : 18.75 MVAR . 1.50 Hg absolute / 35,000 gpm

11.600 Stu/KWh ti 20,000 gross KW 600 KW

11.959 Btu/KWh ft 19,400 net KW Not Available

REDACTED


REDACTED

Mechanical - Hydraulic Control General Electric

1949; Cost included with turbine-generator Distributed control system.

Central & South West - Engineering Servies

1999: 5297,000

Mechanical positioning of forced and induced dralt fan inlet valves

Speed control (TDBFP); mechanical positioning of feedwater vaIve (MDBFP) Norte

One room common to units 1&2

None

None

NOTES: (1) GROSS HEAT RATE = TOTAL REL. CONS(ME) (Including Sart up) (in innEtu ' s)

GROSS ELECTROAL OUTPUT

(2) NET HEAT RATE = TOTAL FUEL CONSUMED (frrnStu s)

GROSS ELECTRCAL OUTRJT - STATONSERVCE

Ina:ate whether Staiicn Service inckiissecnsumpton for CSrnmon Facildits.

Sponsored by; Paul Frankiin

3029 _

1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOLING WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM AM / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4.1ST STEP tiiIW / INCREMENTAL Btus PER ti,1Wh 5. 2N0 STEP MW 1 INCREMENTAL Btus PER MWh 6. 3RD STEP LON / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER kWh






HEAT RATE INCREMEWAL HEAT RATE

CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS, 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTAUATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9 TYPE OF SOOT BLOWER CONTROL SYS. 10, NUMBER OF OPERATOR CONTROL ROOMS 11, DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY LIEBERMAN #3 GENERATING UNIT EFFICIENCY & CONTROL. SYSTEMS

PUG' Docket No_ 46449 Schedule H-12.3c

Page 6 of 26

CATEGORY


1NrriA DE GN EFRCIENCIES 84.6% t 1575 psig / 1005" / 1005•F 8.105 Btu/KWh / 1450 psig / 1000T / 100OT 98.78% / 113.6 MW : 70.4 MVAR 1.50 Hg absolute / 58,200 gpm 9,563 Btu/KWh @ 103,000 gross KW 4,000 KW 9,961 Btu/(Wh et 96,000 net KW Not Available

REDACTED


REDACTED

Mechanical - Hydraulic Control Westinghouse 1957: Cosi included with turbine-generator Microprocessor based split architecture distributed control system ., Foxboro 1986: $127,000 Mechanical positioning of inlet valves Mech. positioning Of feedwater valve and pump speed control via hyd. coupling None One room common io units 3, 4 None Norte

_ TOTAL FUEL CONSUIVE> Gicluding Start - up) (iri rivretu .5) NOTES: (I) GROSS HEAT RATE -

GROSS ali,..11-rx.AL TOTAL WEL CONSUIVIED (mralitte ' s)

(2) PET HEAT RA TE GROSS ELECTRICAL OUTPUT - STATON SERVICE

Indicate %idlether Station Service noliales consueptico for Common


3030

DESCRIPTION RESPONSE

84.6% / 1575 psig /1005°F I 1005°F 8,105 Btu/KWh 1 1450 psig / 1000°F / 1000°F 98.78% / 113.6 MW : 70,4 MVAR 1.50 Hg absolute / 58,200 apm 9,563 Blu/KWh lit 100,000 gross KW 4,1300 KW 9,961 BIWKWh 40 96,000 net KW Not Available

REDACTED




3. TEST 3 PAW OUTPUT HEAT RATE


CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. Z MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10, NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY LIEBERMAN #4 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


-Page 7 of 26

CATEGORY

NI DESIGN EFFICIENCIE 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR MICTRONS / COOUNG WATER 5. GROSS HEAT RATE cl) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Blus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MIN / INCREMENTAL Btus PER MWh 5. 2NO STEP MW / INCREMENTAL Btus PER MWh 6. 3R0 STEP MIN / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER MW11

THREE MOST RECENT HEAT RATE TESTS DATE

L 1 LEVEL 2 LEVEL 3 LEVEL 4 - LEVEL 5 LEVEL 6 LEVEL 7 LEVEL 8

REDACTED

Mechanical - Hydraulic Control Westinghouse 1957: Cost Included with turbine-generator Microprocessor based spUt architecture distributed control system Foxboro 1992 6146,600 Mechanical positioning of inlet valves Mech. positionlng of feedwater valve and pump speed control via hyd. coupling None One room common to units 3, 4 None None

NOTES: (1) GROSS NEAT - TDTAL FUEL O0NSumED (halo:Nig Start - uP) (kicrraBtu • a)

RATE GROSS aeorRicAt. =cur

TOTAL R.IB_ OONSLEAED (mrrEttu a)

Sponsored by-. Paul Franklin

, (2) !CT HEAT RATE = GROSS ELECTRICAL ou-rpur - STATION SERVCE

Indicate whether Station Service imludes consumption for Common Fealties.

303'1

1996

1991 •

1969

• DATE

SOUTHWESTERN ELECTRIC POWER COMPANY KNOX LEE #2 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PUC Docket No. 46449 Schedule 11-12.3c

Page 8 of 26

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2_ TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOLING WATER S. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATt (2) 8. HEAT RATE CURVE i EQUATION

'PROMOD* TYPE iaATA 1. STARTUP Blus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Stus PER MWh 5. 2N0 STEP MW 1 INCREMENTAL BIus PER MWh 6. 3RD STEP MW / INCREMENTAL Btus PER MWh 7. 4T1-1 STEP MW / INCREMENTAL Efts PER MWh 8. STH STEP MW / INCREMENTAL Btus PER MWh

ThREE MOST RECENT HEAT RATE TESTS





INCREMENTAC HEAT RATE

CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMEIER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12 TYPE OF SCRUBBER CONTROL SYS.


83.1% / 875 psig / 910•F 9,554 Btu/KWh / 850 psig / 900°F 98.30% / 37.5 MW : 232 MVAR 1.50 Hg absolute / 45,000 gum 11553 BtulKWh @I 30,000 gross KW 1,500 KW 12,161 Btu/KWh CI 28.500 net KW Not Available

REDACTED


REDACTED

Mechanicai - Hydraulic Control Westinghouse 1950: Cost included with turbine-generator programmable logic controtler (PLC) based system. Central & South West - Engineering Servies 1997: $184.000 Mechanical posilioning of Inlet valves Mechanical positioning of feedmiter vatve None One room common to units 23,4, & 5 None None

NOTES: (1) GROSS HEAT - TOTAL FUEL CONSUWEI) ( In Including Start - up) rnmBtu's)

RATE GROSS ELECTRCAL OUTPUT

TOTAL FUEL CONSUME) (rnmetu s)


(2) NET HEAT RATE - GROSS ELECTRICAL OUTRJT - STATON EB3V PCE

Inchoate %%tether Station Service 'educes constrnption J Cornmen

3032


83.1% / 875 psig / 910`F 9,554 Btu/KWh /850 psig l 900°F 98.30% / 37.5 MW : 23.2 MVAR 1.50' Hg absolute / 45,000 gpm 11,553 Btuil(Wti 0 30,000 gross KW 1,500 KW - 1Z161 Btu/KWh 0 28.563 net KW Not Available

REDACTED


PUC Docket No.46449 Schedule H-12.3c

Page 9 of 26

' CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY/ STEAM CONDITIONS 2. TURBINE EFFICIENCY / b I hAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOLING WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL. STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

'PROMOD" TYPE DATA 1. STARTUP Bilis ' 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4.'1ST STEP MW / INCREMENTAL Efts PER mW h 5. 2ND STEP MW / INCREMENTAL Btus PER MN/11 6. 3RD STEP MW / INCREMENTAL Btus PER MW11 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER MWh


1. TEST I MW OUTPUT HEAT RATE





CONTROL SYSTEMS

DATE 1996

-1991

1989

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 LEVEL 6 LEVEL 7 LEVEL

REDACTED

1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM & TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

NOTES: (1) GROSS HEAT RATE

(2) NET HEAT RATE

Mechanical - Hydraulic Control Westinghouse . 1952: Cost included with turbine-generator Programmable logic controller (PLC) based system. Central & South West - Engineering Servies 1997: 5184,000 Mechanical positioning of inlet valves Mechanical positioning of feedwater valve None

One room common to units 2,3,4, & 5 Nene

TOTAL RAI CONSumED (Including Start - up) (In rrnetu s)

GROSS ELECTRCAL ourPur

TOTAL FUG. CONSUME) (innetu • s)'

GROSS ELECTRICA L OUTPUT - STATION SERVICE

Indicate %teethes Staten Service includes consuinpten for Cashman Fealties.


3033

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS I 000UNG WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

PROMOCe_TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3, MINIMUM MW I INCREMENTAL Btus PER MW h 4. 1ST STEP MW / INCREMENTAL Btus PER MWh 5. 2N0 STEP MW / INCREMENTAL Btus PER MWh 6. 3R1) STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER MWh


1. TEST 1 mw UTPUT HEAT RATE





CONTROL SYSTEMS

DATE 1995

1993

1989

1. DESCRIPTION OF TURBINE COMTROL SYS. 2, MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS: 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.


PliC Docket No. 46449 Schedule H-12.3c

Page 10 of 26


83.6% / 875 'nig / 1005°F 9,040 Btu/KWh / 850 psig / 11300°F 98.62% I 73.5 MW : 55.1 MVAR 1.50 Hg absolute / 60.000 gem 10,754 Btu/KWh 44 60,000 gross KW 2,1001<W . 11,144 Btu/KWh 6 57.900 net KW Not Available

REDACTED


REDACTED

Mechanical - Hydraulic Contrel General Electric 1956: Cost included with turblne-generator Programmable logic controller (PLC) based system. Rockwall Automation (controllers); AEP Service Corporation (engineering) 2004; Se2,462 Mechanical positioning of inlet vanes Mechanical positioning ot feedwater valve None , One mom common 10 units 2,3,4, & 5 None None

NOTES : (1) GROSS AT RATE - TOTAL FUEL CONSUMED (ticludeig Skirt- up) (in nvratu

eiE GROSS ELECTRICAL OUTPUT

TOTAL FUEL COWSLIP/ED (rreiatu 'e)

Sponsored by Paul Franldin

(2) NET HEAT RATE - GROSS ELECTRICAL ()Limo - STATION S8WICE

Indicate whether Starcin Service Incluies consurnpeco for Common Feeireles.

3034




3, TEST 3 MW OUTPUT HEAT RATE


CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8_ TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.



Page 11 of 26

CATEGORY

ImmAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR

4, CONDENSOR CONDITIONS / COOUNG WATER 5. GROSS HEAT RATE (1) B. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Lillis 2. MNIMUM MW / TOTAL Btus 3, MNIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER MWh 5. 2NCI STEP MW / INCREMENTAL Btus PER MWh 6. 3RD STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP PAW / INCREMENTAL Btus PER 141Wh 8. 5TH STEP MW / INCREMENTAL Btus PER With

THREE MOST RECENT HEAT RATE TESTS DATE


85.5%/ 2100 psig / 1005°F / 1005T 8,088 Btu/KWh / 2000 psig i 1000°F / 1030°F

98.70 / 351 MW : 170 MVAR 2.00 Hg abeclute / 245,500 gprn 9,451 Btu/KWh 6. 322,521 gross KW 10,936 KW 9.793 Litu/KWh e 311.585 net KW Not Available

REDACTED

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 6 LEVEL 6 LEVEL 7 LEVEL

REDACTED

Programmabie logic controller based electronics. Hydraulic field actuators. Central & South West - Engineering Servles 1998: $175,003 Programmable logic controller (PLC) based system. Central & South West • Engineering Servies 1996: $512.000 Mechanical positioning of inlet vanes Speed control: Hydraulic coupling (MDBFP). turbine speed (TDBFP) . None One MOM common to units 2.3,4. & 5 None None

TOTAL FUEL CONSUME) (iciuding Start - up) (in rarreau • s) NOTES : ' (1) GM:WHEAT RATE

(2) NEr HEAT RATE GROSS ELECTRICAL OUTPUT - STATON SERVICE

inckale whether Station Service includes corsumplIco Icf Occrolon Fadilbes.


GROSS SECTRCAL OUTPUT

TOTAL FUEL CONSUIJED (pyrEttu

3035

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR OONDITIONS / COOUNG WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) • 8. HEAT RATE CURVE / EQUATION

'PROMOD• TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER NM 4. 1ST STEP MW t INCREMENTAL Btus PER MWh 5. 2ND STEP MW / INCREMENTAL Btus PER MWh 6. 3RD STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER MWh




HEAT RATE INCREIvIENTAL HEAT RATE



DATE 1995

1993

1989

SOUTHWESTERN ELECTRIC POWER COMPANY LONE STAR #1 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PUC Docket No. 46449 Schedule H-12.30

Page"12 of 26


85.0%! 920 psig / 91(rF 9.410 Btu/KWh i 850 PSIgi 900T 98.54% / 50 MW : 31 MVAR 1.50" Hg absolute / 55,030 gprn • .

11 026 Eitu/KWh 0 40,000 gross KW ; 1,400 KW 11.426 13tufKVih @ 38,600 net KW Not Available

REDACTED


REDACTED

CONTROISYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL vs. a DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10, NUMBER OF OPERATOR CONTROL ROOM

11, DESCRIPTION OF HEATPIATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS. •

no-res: (1) GROSS HEAT RATE

(2) NET HEAT RATE

Mechanical - Hydraulic Control General Electric 1954: Cost incltxled with turbine-generator Microprocessor based split architecture distributed control systern Foxboro ,

1987: $100000 Mechanical positioning of inlet valves ' Mechanical positioning of feedwater valve None One -

None None

TOTAL FUEL CONSUMED (Including Start- up) (in rrIrretU 's)

GROSS ELECIRCAL OUTPUT

TOTAL FUEL CONSUIVE33 (nyristu s)

GROSS ELECTRICAL OUTPUT - STATOR SERVICE

!Falcate *later Station Service inciules ccostoeption ler COMOIQR FaciMes.


. 3036


85.1% / 1875 psig / 1005T / 1005*F 8,058 Btu/KWh 11800 psig / 1000`f 11000T 98.66%1179,5 MW : 111 MVAR 2.00 Hg absolute! 70,000 gpm 9,460 Btu/KWh 14 160.000 gross KW 6,948 KW 9.890 Btu/KWh a 153052 net KW Not Available

REDACTED

SOUTHWESTERN ELECTRIC POWER COMPANY WILKES #1 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


Page 13 of 26

CATEGORY

INITIAL. DESIGN EFFICIENCIES 1, BOILER EFFICIENCY 1 STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS i COOLING WATER 5. GROSS HEAT RATE ( 1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) ' 8. HEAT RATE CURVE / EQUATION

"PROMOD* TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER MWh 5. 2ND STEP MW /INCREMENTAL Blus PER MWh 6, 3R0 STEP MW /INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER WAlh

THREE MOST RECENT HEAT RATE TESTS DATE , LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 LEVEL 6 LEVEL 7 LEVEL 8 ,

1. TEST 1 hAW OUTPUT HEAT RATE





CONTROL SYSTEMS

1997

1996

1992

REDACTED

1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. r(PE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS.' 10. NUMBER OF OPERATOR CON i L ROOMS 11. DESCRIPTION OF HEATRATE DEVIAT/ON SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

Mechanical - 1-lydraulic control . General Electric 1964: Cost included with turbine-generator Programmable logic controller (PLC) based system. Central & South West - Eregineering SeNtes 1996: $463,000 Mechanical positioning of inlet vanes Mechanical positioning of feedwaler valve None One room common to units 1,2,3 None None

TOTAL Fl tR CONSUMED (belucrng Start - up) (in rrwetu 's)

GROSS ELECTRICAL OUTFLTT TOTAL I.UEL CONSUMED (rrrnBtu ' s)

(2) NET HEAT RATE - GROSS azcmcAt. OUTRIT - STATON senvCE

indicate abetter Station Service ercbAes corsunptim far Gornmco Fealties.

NOTES ; .1) GROSS HEAT RATE

Sponsored try: Paul Franklin

3037


85.6% / 2100 Og / 1005°F / 1005.F 8,088 Btu/KWh / 2000 psig / 1000*F / 1000•F 98.70% / 351 MW : 170 MVAR 2.00 Hg absolute / 139,000 gpm 9,451 Ettu/KWh CI 322,521 gross KW 9,370 KW 9,733 Btu/KWh 0! 313,151 net KW . Not Available

REDACTED

SOUTHWESTERN ELECTRIC POWEFI COMPANY WILKES #2 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PLC Docket No. 46449 Schedule H-12.3c

Page 14 of 26

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / P.4W : MVAR 4. CONDENSOR CONDITIONS i COOUNG WATER 5. GROSS HEAT RATE (1) 6, ORIGINAL STATION LOAD 1 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOIY TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL BILIS 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER NiWri 5. 2N13 STEP MW / INCREMENTAL Btus PER MWh 6. 3813 i tP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Baia PER MWti 8. 5TH STEP MW / INCREMENTAL Btus PER MWh


DATE

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 LEVEL 6 LEVEL 7 LEVEL 8 1. TEST 1 MW OUTPUT


2. TEST 2 MIN 01/MUT HEAT RATE -

IN6REMENTAL HEAT RATE 3. TEST 3 MW OUTPUT

HEAT RATE INCREMEhITAL HEAT RATE

CONTROL SYSTEMS

2001

1996

REDACTED

1995

1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. a DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

hCrtES: (1) GROSs HEAT RATE -

(2) NET HEAT RATE

Programmable logic controller based electronics. Hydraulic field actuators. Central & South West - Engineering Sennes 1999: $224,000 Sofid stale electronics and microprocessor based Foxboro 1970, 1992, 1994, 1995: $115,000 Mechanical positioning of inlet vanes Speed control: Hydraulic coupling (MOBFP), turbine speed (TDBFP) None One room common to units 1,2,3 None •

None

TOTAL FUEL OONSAVED (hcludIng Start - up) (ri -rrirrStu a)

GROSS ascmc..AL OUTPUT

TOTAL aim OONSLME33 fmrratrits)

GROSS ascmcm. OUTFUT - STATON seqvIi3E

indicate wheeler Static* Service indides consimption for Common Facilities.


3038 a

CATEGORY

INrTIAL DESIGN 'E FICIENCIES 1. BOILER EFRCIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4, CONDENSOR CONDMONS / COOUNG WATER 5. GROSS 1-SEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EOUAT1ON

PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW 1 INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER MVVh 5. 2N0 STEP MW / INCREMENTAL Btus PER MWh 6. 3R0 STEP MW / INCREMENTAL Btus PER tv1Wh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5T1-1 STEP MW / INCREMENTAL Btus PER MWh





3. TEST 3 MW OUTPUT HEAT FIATE


CONTROL SYSTEMS

DATE 1996

1993

1992

1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6, DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10, NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY WILKES #3 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


Page 16 of 26

DESCRtPTION / RESPONSE

85.6% / 21002sig / 1005°F / 1005•F 8.088 Btu/KWh / 2000 psig / 1000T / 1000•F .

98.70% / 351 MIY1 : 170 MVAR 2.00'' Hg absolute / 139,000 gam 9,451 Btu/KWh 0 322,521 gross KW 9,370 KW 9,733 Btu/KWh 0 313,151 net KW Not Available

REDACTED

LEVEL. 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 LEVEL 8 LEVEL 7 LEVEL 8

REDACTED

Programmable Logic controller based eled-ronics. Hydrautic field actuators. Central & South West - Engineering Servies 1998: 5123,000 Solkl state electronics and microprocessor based Foxboro 1971, 1992, 1995: $123,C00 Mechanical positioning of inlet vanes Speed control: Hydraulic coupling (MDBFP), turbine speed (TDBFP)

One room common to units 1,Z3 None None

NOTES : (1) GROSS HEAT TOTAL FUEL CONSuMED (inducing Start up) On mmatu ' s}

RATE = GROSS aECTRCAL CUTAJT

TOTAL FUEL coNsumso (rr:new • s)


(2) NET NEAT SATE = GROSS ELECTRICAL OUTPUT - STATICtISERVICE

Indicate whether Siam SerftfiCef includes consumption for Common Facilfties,

3039

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDMONS 2, TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS I COOUNG WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Blus 3. MINIMUM MW / INCREMENTAL Eltus PER MWh 4, 1ST STEP MW / INCREMENTAL Btus PER MWh 5. ZNE) STEP MW / INCREMENTAL. Btus PER MWh 6. 3RD STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. STH STEP MW / INCREMENTAL Btus PER MWh





INCREMENTAL HEAT RATE 3, TEST 3 MW OUTPUT


COF1TROL. S ŠTEMS 1, DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10, NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIAllON SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

, SOUTHWESTERN ELECTRIC POWER COMPANY WELSH #1 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

4

PUC Docket No. 46449 Schedule 1-1-12.3c

Page 16 of 26

NOTES (11 GROSS HEAT RATE

DESCRIPTI0N1 RESPONSE

85.8% / 2620 psig I 1005°F I 1005°F , 7,944 BtufKWh I 2400 psig / 1000°F I 1000°F 98.81% / 558 MW : 270 MVAR . 2.50 Hg absolute / 241,300 gpm 9.264 Btu/KWh @ 510.280 gross KW 29,137 KW 9.825 Btu/KWh 0 481,143 net KW Not Available .

REDACTED


REDACTED

4

Digital Electro - Hydraulic control Wood Group 2006: $1,767.000 Distributed control system. Siemens Moore 2001: 52,014,000 Mech. positioning of FD & PA inlet vanes, hyd. positioning of ID tan blades Speed control: Hydraubc coup/ing (MDBFP), turbine speed (TDBFP) N6croprocessor based automatic seq_uencing control One room common to units 1,2.3 Nona None

TYYTAL FUEL coNsumer) (hcludhg Start - up). (in rrniatu 's)

(2) NET HEAT RATE — GROSS Euacmcm. OUTPUT - STATION SERVICE

Incricate wheaitor Station Service includes consmption tor Ccmmon

GROSS ELECTRCAL ourrur 4 TOTAL Rae_ CONSUIWO (rroStu ' a)

Sponsored by: Paul Franklin .

3040


05.6% I 2020 psig / 1007F 1100.7f 7.944 Btu/KWh / 2400 psig 1 1000°F / 1000•F 96.81% ð 558 MW : 270 MVAR 2.50" Hg absciute / 241.300 gpm 9,264 Btu/KWh @ 510,280 gross KA/ 29.137 KW 9.825 Btu/KWh @ 431,143 net KW Not Mailable ...I

SOUTHWESTERN Et:ECTRIC POWER COMPANY WELSH #2 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


Page17 of 26

CATEGORY

INITIAL DESIGN EFFICIENCIE 1, BOILER EFFICIENCY V STEAM CONDITIONS 2 TURBINE EFFICIENCY 1 STEAM CONDMONS 3. GENERATOR EFFICIaNCY 1 MW : MVAR 4. CONDENSCR CONDITIONS / COOLING WATER

S. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE 1 EQUATION

'PROMOD" TYPE DATA I. STARTUP Bhis 2. MINIMUM MW 1 TOTAL Btus 3. MINIMUM MW 1 INC RatENTAL Btus PER MWh 4. IST STEP MIN / INCREMENTAL Btus PER MWh S. 2ND STEP MW / INCREMENTAL Etta PER MWh 6. 3RI3 STEP MW 1 INCREMENTAL Btus PER MWh 7. 4TH STEP MW 1 INCREMENTAL Btus PER MW11 8. 5TH STEP MI INCREMENTAL Btus PER Mit





a TEST 3 MW OUTPUT HEAT RATE


CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONT SYS. 3. DATE & COST OF INSTALLATION e 4. DESCRIPTION OF BOILER CONTROL 5. MANUFACrJRER OF BO LER CM S. 6. DATE & COST OF INSTALLA, 7. TYPE OF FAN CONTRO S 8. TYPE OF I-LtUWATER P ROL SYS. ' 9. TYPE OF SOOT BLOWER CO SYS. 10. NUMBER CF OPERATOR CONTROL ROOMS 11, DESCRIPTION OF I4EATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

NoTES: .(1) GROSS HEAT RATE

(2) NET HEAT RATE —

REDACTED

Digital Etectro - Hydrauk control Wood Group 2008: 81,785,000 Distributed control systarn Siemens Mccce 2005: 53,695.955 Mech. postion'eg of PA fan Wet Vanes. hyd powtioning of FD & ID fan blades Speed ccntrol: Hydraulic =aping (MDEFP), turblne speed (TDBFP) Iificrqxocessor based automatic sequencing coned One room commce to units 1.23 None None

TOTAL FUG, CONSUMED (Including Start- up) (in rrrnBtu 's)

GROSS ELECTRICAL OuTRIT

TOTAL Re. coNsi_fmeo (menu`

GROSS ELECTRCAL OUTFLIT - STATON SERVCE

Inle *nether SMtion Sante incluies consumption tor Common Faailies.


3041

1. STARTUP Eitus Z MINIMUM MW r TOTAL Btus 3. MINIMUM MW I INCREMENTAL BtUs PER MVIII 4. 1ST STEP VW I INCRSMENTAL Btus PER M'Wh 5. 2ND STEP MW / INCREMENTAL 91us PER MAI, 6. 3R0 STEP MW f INCREMENTAL Btus PER MWII 7. 4TH STEP MW / INCREMENTAL Btus PER MVi/h 8. 5TH STEP MW / INCREMENTAL Btus PER MWh

THREE MOST: RECENT HEAT RATE TESTS






CONTROL SYSTEMS 1. DESCRIPTION OF TURENE CONTROL SYS. 2, MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CourRoL SYS. 8. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

StiUTHWESTERN ELECTRIC POWER COMPANY FLINT CREEK #1 GENERATING uNrr EFFICIENCY & CONTROL SYSTEMS

PUC Docket No. 46449 Schedule 1412.3c

Page18 of 26

CATEGORY

NMAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4, CONDENSOR CONDITIONS / COOLING WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATK)N LOAD 7. NM' HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION


85.8% / 2620 psig / 1005°F / 1005°F 7,946 Btu/KWh / 2400 psig / 1000°F i 1000°F 99.69% / %BMW t 270 MVAR Z50 Hg absolute / 241,300 gpm 9,2E3 Btu/KWh 6 509,799 gross KW

._

29,262 KW 9,849 Btu/KWh 6 480.537 net KW Not Available

"PRO OD" TYPE DATA

NOTES: (1) GROSS1-EAT RATE

REDACTED


REDACTED

Electro - Hydraulic control General Electric 1978: Cost included iorith turbine-generator Solid state electronics Leeds & Northrup 1978 $513,000 Mech. positioning of FD & PA inlet vanes, hyd. positioning of ID fan blades Speed contra Hydraulic coupling (MDBFP), turbine Weed (TV:IFP) Microprocessor based automatic sequenciiv correct One Black & Veatch On-Line Performance Monitoring System Ne

TOTAL FUEL CONSUME) (Including Start - up) (in rivr;Stu s)

(2) NET HEAT WOE GROSS alECTRCAL OUTPUT - STATON SERV CE

Indicate wheeler Staten Service itcluciee consuription tor COrnman Faoirttett

GROSS B_ECTRICAL -at/TRH

TOTAL FUEL CONSUM93 (rimBlu•s)


3042

CATEGORY

INITIAL DESIGN EFRCIENCIES I. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM coribmoNs 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONCENSOR CONDITK/NS /COOUNG WATER S. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EOUATION

"PROtilOtr TYPE DATA 1. STARTUP Btus 2. MINIMUM MW l TOTAL Btus 3. MINIMUM MW / INCREMENTAL MIA PER MWh 4. 1ST STEP MW /INCREMENTAL Btus PER MWh 5. 2ND STEP MW / INCREMENTAL Btus PER MWh 6. 3RD STEP MW 1 INCREMENTAL Btus PER fkriNh 7. 4TH STEP MW / INCREMENTAL Btus PER Mei B. 5TH STEP MW I INCREMENTAL Btus PER MWhi



INCREMENTAL HEAT RATE 2. TEST 2 MW OtriPur


3. TEST 3 tAW OUTPUT HEAT RATE


CONTROL SYSTEMS

DATE 2302

2001

1999

1. DESCRIPTION OF TURBINE CONTROL. SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLAIION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF $00T BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY WELSH #3 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

P00 Docket No: 46449 Schedule H-12.30

Page 19 of 26


85.8% l 2620 psig / 1005T / 1005°F 7,944 Blu/KWh I 2400 psig / 1000°F / 1000°F 98.81% / 558 MW : 270 MVAR 2.50 Hg absolute/ 241,300 gpm 9,264 Btu/KWh 6 510,280 gross KW 29,137 KW 9.825 Btu/KWh CI 481,143 net KW Not Available

REDACTED


REDACTED

Digital Electro - Hydraulic control Wood Group 2008: 51.869,000 Distributed control system Siemens Moore 2008: $a440.000 Mech. positioning of PA fan inlet vanes, hyd. positioning of FE) a ID fan blades Speed control: ndraulic coupling (MDBFP), turbine speed (TDBFP) fificroprocessor based automatic sequencing control One mom common to units 1,2,3 . None .

None

NOTES: (1) GROSS NEAT ToTAL FUEL CONSUMED (Including Start - up) (in Irrnlatu ' a)

RATE L GROSS ELECTRICAL OUTPUT

TOTAL FUG_ CONSUME) (mew ' a)


(2) NET HEAT RATE - GROSS ELECTRICAL OUTPUT - STA-TON sERVCE

tralicate %shether Station Service inckides coreumplion for Confront% Facilities.

3043

SOUTHWESTERN ELECTRIC POWER COMPANY H.W. P1RKEY #1 GENERATING UNIT EFFICIENCY & CONTROL. SYSTEMS


Page 20 of 26 .

CATEGORY

INFRAL DESIGN EFF1CIEN.CIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONOITIONS 3. GENERATOR EFF/CIENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOLING WATER 5. GROSS HEAT RATE (1) 6, ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD• TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Ðlus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER MWh 5. 2N0 STEP MW / INCREMENTAL Btus PEFi MWh 6. 3R0 STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Slits PER MWII


1. TEST I MW OUTPUT HEAT RATE


HEAT RATE INCREMENTAL HEAT RATE.




84.1%/ 2600psiq / loo5°F / 1005- F 8,112 8tu/KWh / 2400 psig / 1000°F / 1000°F 98.70% / 72075 MW : 285 MVAR 4.00 Hg absolute i 328.216 gpm 9,636 Btu/KWh 0 647,616 gross KW 52,975 KW 10,495 BtufKWh a 594,641 mit KW Not Available

REDACTED


REDACTED

DATE 2002

1995

1992

CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTIROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9_ TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

NOTES"i (1) GROSS-HEAT RATE =

(2) NETHEAT RATE -

Digital Electro • Hydraulic control Westinghouse 1985: Cost included with turbine-generator Solid state electronics Leeds & Northrup 1985: 51,365,000 Mech. positioning of PA tan inlet vanes, hyd. positioning of FD & 113 fan blades Syeed control: Hydraulic coupling (MDBFP), turbine speed (TDBFP) _ Microprocessor based automatic sequencing control Two . None Solid state electronics

TOTAL FUEL CX)NSUMElft {Including Start - uP) rmau '31

OnosS ELECTRICAL OUTFUT

TOTAL FUEL. cONSUSiED (rniretu9s)

GROSS ELECTRICAL OUTPUT - STATON SERVICE

Incicate whetter Station Service 33:skatea contssn'pecri for Common Faater.


3044,

CATEGORY

NMAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS a GENEFIATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS I COOUNG WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8_ HEAT RATE CURVE / EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Blus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4, 1ST STEP MW /INCREMENTAL Btus PER MWh 5. 2N0 STEP MW ¡INCREMENTAL Btus PER MWh 6. 3FI0 STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MIN /INCREMENTAL Btus PER MWh





INCREMENTAL HEAT RATE 3, TEST 3 MW OUTPUT


CONTROL SYSTEMS I. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION . 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL. SYS. 6. DATE & COST OF INSTAU.ATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY DOLET HILLS #1 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


Page 21 of 26


84.1%! 2600 psig i 100.5`F / 1005°F 8,112 Btu/KWri / 2400 psig / 1000°F / 1000°F 98.70% i 720.75 MW : 255 MVAR 4.00* Hia absolute / 324,720 gpm 9,636 Btu/KWh 0 647,616 gross KW

.. 61,027 KW 10,639 Btu/KWh 0 586.589 net KW Not Available

REDACTED

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4- LEVEL 5 LEVEL. 6 LEVEL 7 LEVEL 8

REDACTED

Digital Electro - Hydraulic control Westinghouse 1986: Cost included with turbine-generator , Distributed control system ABB . 2007: 53,012,000 • Mech. positioning of PA fan inlet vanes, hyd. positioning al FD & ID fan blades Speed control: Hydraulic coupling (MDBFP). turbine speed (TDEIFP) hfcroprossor based automatic sequencing control Two Noae Solid state electronics

TOTAL FUR. coNsumm {Emiuding Start - up) (in mrngto s) TES: (1) GROSS HEAT RATE

(2) NET HEAT RATE - enoss ELECTRICAL OUTPUT - STATION SERVICE

Indicate whether Station Service includes commotion for Common Facades.

Sponsored try: Paul Franklin

GRcLaiS RECTRICAL =FUT

TOTAL RIELr(X)NSUIVED <crnetu

3045

CATEGORY

INrnat. DE I N EFF(CIENCtES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOUNG WATER 5. GROSS HEAT RATE (I) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (21 8, HEAT RATE CURVE / EQUATION

"PROMOD- TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL Btus PER MWh 5. 2N0 STEP MW i INCREMENTAL Btus PER MWh 6. 3R0 STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8. 5TH STEP MW /INCREMENTAL Efts PER MWh

THREE MOST RECENT HeAT RATE TESTS

DATE 1 TEST 1 MW OUTPIJT





CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3 DATE & COST OF INSTALLATION 4, DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. . 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12 TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY MATTISON #1 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PUG Docket No, 46449 Schedule H-12.3C

Page 22 OI 26


NA NA 96.25 / 80 MW. .85 PF NA 10840 Blu/kWh 0 compressor iniet 96F, 54% relative humidity 898 kW per unit 10981 Btu/kWh Not available

REDACTED


REDACTED

Dal GE Mark V wIth turbine control. generator control, motor control and HMI General Elactnc 2007 - Cost included with Turtkne NA NA NA NA NA NA

None NA

TOTAL FUEL CONSUMED (Inckiding Start - up) meets 'S) NOTES (1) GROSS H6kT RATE

GROSS ELECTROCAL OLTIRIT

TOTAL FUEL CONSUMED (irrnetu 'a) .(2) NET HEAT RATE

GROSS exaBICAL OUTPUT - STATON SERVICE

Indicate whetter Station Service incluSea conaunption for Common Facilities.

Sponsored try Paul Franklin

3046

CATEGORY

INITIAL DESIGN EFFICIENCIES 1. BOILER EFFICIENCY /STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY 1 MW : MVAR 4. CONDENSOR CONDITIONS / COOUNG WATER $. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

"PROMOD- TYPE DATA 1. STARTUP Btus 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4 1ST STEP MW 1 INCREMENTAL Btus PER kWh 5. 2ND STEP MW / INCREMENTAL Btus PER kWh 6. 3R0 STEP MW 1 INCREMENTAL Btits PER MWt1 7. 4TH STEP MW / INCREMENTAL Btus PER MWh 8, 5T1-t STEP MW / INCREMENTAL Blus PER MW11


DATE 1. TESTI MIW OUTPUT

HEAT RATE INCREMENTAL HEAT RATE'




CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. B. DATE & COST OF INSTAU.ATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY MATTISON #2 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS


Page 23 of 26


NA NA 98.25 / 80 MW, .85 PF NA 10840 Btu/kWh 0, compressor inlet 96F. 54% relative humidity 898 kW per unit 10981 Btu/kWh Not available

REDACTED

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL S LEVEL 6 LEVEL 7 LEVEL S

REDACTED

Digital GE Mark V with turbine control. generator control, motor control and HMI General Electric 2007 - Cost included with Turbine NA NA NA NA NA

NA

None NA

TOTAL RJEL CONSUMED (Inciuding start - up) Oh rreretu

GROSS ELECTRICAL OUTRTT

(2) NET HEAT RATE - TOTAL FUEL CONSUMED (mats 's)

GROSS ELECTRICAL OUTPUT - STATION SERVICE

Incilcate %that/le-Station Service inctudes consumption tor Common Facellea.

NOTES: 'CO GROSS HEAT RATE -


3047

CATEGORY

INMAL DESIGN EFflCJENCIES 1. BOILER EFFICIENCY / STEAM COND(TIONS 2_ TURBINE EFFICIENCY / STEAM CONDITIONS 3 GENERATOR EFRCIENCY/ MW : MVAR 4. CONDENSOR CONDITIONS ( COOLING WATER 5. GROSS HEAT RATE J1) . 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CUFIVE / EOUAT/ON

"PROIIIIOD" TYPE DATA 1. STARTUP Was 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW / INCREMENTAL Btus PER MWh 4. 1ST STEP MW / INCREMENTAL 8ft:a PER MWh 5. 2ND STEP MW / INCREMENTAL Btus PER MWh 6. 3RD STEP MW / INCREMENTAL Btus PER MWh 7. 4TH STEP MW / INCREMENITAL Btus PER MWh 8. 5TH STEP MW / INCREMENTAL Btus PER kWh


OATE



TEST 2 MW OUTPUT HEAT RATE




CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2, MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST Of INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. 10, NUMBER OF OPERATOR CONTROL, ROOMs 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY MAT11SON #3 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

MC Docket No. 46449 Schedule H-12.3c

Page 24 of 26


NA NA 98.25 1 50 MW..85 PF NA 10840 BtuikYifh CI compressor inlet 96F, 54% relative humidity 898 kW per unit 10981 Blu/kWti ' Not available

REDACTED


REDACTED

Digital GE Mark V with turbine control, generator control, motor control and HMI General Electric 2007 - Cost included with Turbine NA NA NA . NA NA NA

None NA

NOTES : (1) GROSS T RATE = UMED , TOTAL FUEL CONS (Including Start - up) (k1 rrrraiu ' s)

HEA GROSS B-ECTRICAL OUTPUT

TOTAL RJEL CONSUMED (rmetu 's)


(2) NET HEAT RATE - GROSS ELECTRicAL OUTFUT - STATION SERVCE

Indica* whether swan SetviCe InCludeS consurnption tor Common Faciaies.

3048

1. BOILER EFFICIENCY 1 STEAM CONDITIONS 2. TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR FHC1ENCY / MW : MVAR 4. CONDENSOR CONDITIONS / COOLING WATER 5. GROSS HEAT RATE (1) S. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE / EQUATION

`PROMOD" TYPE DATA 1. STARTUP Btus 2 MINIMUM MW / TOTAL Btus & MINIMUM MW / INCREMENTAL Skis PER MWh 4. 1ST STEP MW I INCREMENTAL. Btus PER MWh 5. 2N0 STEP MW / INCREMENTAL Btus PER WWII 6. 3RD STEP MW / INCREMENTAL Btus PER MIMI 7. 4TH STEP MW /INCREMENTAL Btus PER MWh 8. 5TH STEP MIN i INCREMENTAL Btus PER MWh




2 TEST 2 MW OUTPUT HEAT RATE



CONTROL SYSTEMS 1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE CONTROL SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS_ 6. DATE & COST OF INSTALLATION 7. TYPE OF FAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP CONTROL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. O. NUMBER OF OPERATOR CONTROL ROOMS

11_ DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

SOUTHWESTERN ELECTRIC POWER COMPANY MA1TISON #4 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

PUC Docket-No, 46440 Schedule H-12.30

Page 26 of 26

CATEGORY


INMAL DESIGN EFF1C NCIES NA NA 98.25 / 80 MW..85 PF NA 10840 Btu/kWri 0 compressor inlet 06F, 54% relative humidity 890 kW per unit 10981 Btu/kWh Not available

REDACTED

LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 1.11/EL 6 LEVEL 7 LEVEL 8

REDACTED

Digital GE Mark V with turbine control, generator corittol, motor control and HMI General Electric 2007 - Cost included with Turbine NA • . NA NA NA NA NA 1

NA

TOTAL FUEL CONSUIABD (ncluoing Start - up) (in Mat/ 's) NOT15S : (1) `onoss HEAT RATE =

GROSS SACO:CAL ourPur TOTAL FUEL CONSUMED (rnmaiu 's)


(2) NEr HEAT RATE - GROSS ELECTRACAL ourpur - STATION SERYCE

Incricate where(' Station Service iricludee conekingion for Common Faciitiee

3049


MA NA 98.25 1 80 MW, .85 PF NA 10840 Btu/kWh CP cornpressor inlet 96F, 54% relative humidity' 896 kW per unit 10961 Btu/kWh Not available

REDACTED

SOUTHWESTERN ELECTRIC POWER COMPANY MA1TISON #4 GENERATING UNIT EFFICIENCY & CONTROL SYSTEMS

(Non Confidential}

PUC Docket No. 46449 Schedule H-12..3o

Page 28 of 26

CATEGORY

INITIAL DESIGN EFF C ENCIES 1. BOILER EFFICIENCY / STEAM CONDITIONS 2... TURBINE EFFICIENCY / STEAM CONDITIONS 3. GENERATOR EFFICIENCY / MW : MVAR • 4. CONDENSOR CONDITIONS / COOUNG WATER 5. GROSS HEAT RATE (1) 6. ORIGINAL STATION LOAD 7. NET HEAT RATE (2) 8. HEAT RATE CURVE l EQUATION

"PROMOD" TYPE DATA 1. STARTUP Btus . 2. MINIMUM MW / TOTAL Btus 3. MINIMUM MW I INCREMENTAL Btus PER MWh 4. IST bi tP MW / INCREMENTAL Btus PER MWh 5. 2ND STEP MW / INCREMENTAL Btus PER MWh 6. 3R0 o l bP MW 1 INCREMENTAL Btus PER MWh 7. 4TH STEP MW /INCREMENTAL fillus PER MWh 8. 5TH STEP MW / INCREMENTAL &us PER MWt:

TfiREE MOST RECENT HEAT RATE TESTS

DATE LEVEL 1 LEVEL 2 LEVEL 3 LEVEL 4 LEVEL 5 LEVEL 6 LEVEL 7 LEVEL 8 1. TEST 1 MW OUTPUT



, INCREMENTAL HEAT RATE 3, TEST 3 MW OUTPUT


REDAL I ED

CONTROL. SYSTEMS

1. DESCRIPTION OF TURBINE CONTROL SYS. 2. MANUFACTURER OF TURBINE coarsot. SYS. 3. DATE & COST OF INSTALLATION 4. DESCRIPTION OF BOILER CONTROL SYS. 5. MANUFACTURER OF BOILER CONTROL SYS. 6. DATE & COST OF INSTALLATION 7. TYPE OF PAN CONTROL SYSTEM 8. TYPE OF FEEDWATER PUMP courRÕL SYS. 9. TYPE OF SOOT BLOWER CONTROL SYS. ., 10. NUMBER OF OPERATOR CONTROL ROOMS 11. DESCRIPTION OF HEATRATE DEVIATION SYS. 12. TYPE OF SCRUBBER CONTROL SYS.

Digital GE Mark V with turtiine controI, generator control, motor control and HMI General Electric 2007 - Cost included with Turbine NA NA NA NA NA ' NA

None NA

NOTES : (1) GROSS HEAT TOTAL FUR. CONSUMED (raid's.* S(art - up) (in irrnEstu ' s)

RATE GROSS am-1'8cm. otrrpur

TOTAL Fus_ CONSUMED (rnmEttu 's)

GROSS ELECTRICAL OUTRJT • STATION SERVICE

Irldicale whether Stshort Servize includes corm...pt.., tor COMM Fat:Mies.

Sponsored by: Paul Frankrui

(2) NET HEAT RATE -

3050

Sponsored by: Nairn Hakimi

SOUTHWESTERN ELECTRIC POWER COMPANY

PUC Docket No. 46449 SUMMARY OF FIRM PURCHASED POWER (NM MWM

Schedule1-1-12.4a

OUAUFYING FACtUTLIES, BY COMPANY

SWEPCO did not have any Firm Purchased Power MWh for this year.

_

- - - - .

..


-


i

SWEPCO did not have arty Fimn Purchased Power MWh for this iear. -

t

- - - • .

1 '

i 1 i


. . . .. . . . . . .

Jan-13 Feb-13 Mar-13 Apr-1

May-1 Jun-1 Jul-1

Aug-1 Sep-1 Oct-1 Nov-1 Dec-1

Total 2013


May-1 Jun-1 Jui-1


Total 2014

Jan-1 Feb-1 Mar-1 APr-1

May-1 Jun-1 Jul-1


Total 2015


May-1 Jun-1

Total TY Total RP

RECONCIUATION PERIOD R Jan-12 Feb-12 Mar-12 APr-12

May-12 Jun-12 Jul-12


Total 2012

3051

PDC Docket No: 46449 Schedule 11- 1 2.4b

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY FTRIVI PURCHASED POWER ENERGY COSTS

SWEPCO ha.s not filed a fuel reconciliation with its current base rate case; therefore, this schedule is not applicable.

3052

3053

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Sponsored by: Naim Haldint

SOUTHWESTERN ELECTRIC POWER COMPANY

PUC Docket No. 46449 SUMMARY OF FIRM PURCHASED POWER ENEFIGY COSTS PER NET ki1Wh

Schedule H-12.4d

($0.001MWh)

QUALIFYING FACIUTLIES, BY COMPANY

SWEPCO crld not have any Rrm Purchased Power MWh for this year.

- . . . . .

SWEPCO did not have any Firm Purchased Power MWh tor this year.

SWEPCO did not have any Finn Purchased Power MWh for this year.


,




Aug-13 Sep-13 Oct-13

Nov-13 Dec-13

Total 2013


May-14 Jun-1 Jul-14

Aug-1 Sep-14 Oct-1

Nov-1 Dec-14

Total 2014


May-1 Jun-15 Jul-1


Total 2015

Jan-1 Feb-1 Mar-1 APr'l

May-1 Jun-1

Total TY Total RP

RECONCILIATION PERIOD RP Jan-12 Feb-12 Mar-12 Apr-12



Total 2012

3054

PUC Docket No. 46449 Schedule H- I 2.4e

Page 1 of 1

. SOUTHWESTERN ELECTRIC POWER COMPANY NON FIRM PURCHASED POWER

SWEPCO has not filed a fuel reconciliation with its current base rate case; therefore, this schedule is not applicable.

3055

PDC Docket No. 46449 Schedule 11,12.4f

Page 1 of 1

_SOUTHWESTERN ELECTRIC POWER COMPANY NON FIRM PURCHASED POWER ENERGY COSTS


3056

PL/C Docket No. 46449 Schedule H- I 2.4g

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY NON FIRM PURCHASED POWER ENERGY COSTS PER MWH


3057

PUC Docket No. 46449 Schedule H- I 2.5a

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY LINE LOSSES AND SYSTEM'S OWN USE


3058

Plic Docket No. 46449 Schedule 11-12.5b

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY OFF-SYSTEM SALES (ECONOMY & FIRM)

SWtPCO has not filed a fuel reconciliation with its current base rate case; therefore, this schedule is not applicable.

3059.


Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY OFF-SYSTEM SALES REVENUE (ENERGY CHARGE COMPONENT)


3060

PUC Docket No. 46449 Schedule II-123d

Pap I of I

SOUTHWESTERN ELECTRIC POWER COMPANY OFF-SYSTEM SALES REVENUE (FIXED CHARGE COMPONENT)

SWEPCO has not filed a fuel reconciliation with its current base rate case; therefore, this gchedule is not applicable.

ITC Docket No. 46449 Schedule /I-12.5e

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY OFF-SYSTEM SALES REVENUE (ENERGY CHARGE KWH)

SWEPCO has not filed a fuel reconciliation with its current base rate case; therefore; this schedule is not applicable.

3062

PUC Docket No. 46449 Schedule H-12.5f

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY ON-SYSTEM SALES (WHOLESALE AND RETAIL)


3063 "

PUC Docket No. 46449 Schedule H-12.6a

Page 1 of 1

SOUTHWESTERN ELECTRIC POWER COMPANY MONTHLY MINIMUM AND PEAK DEMAND

JULY 2012 -JUNE 2016

Month Peak

Demand Minimum Demand

Peak Month Demand

Minimum Demand

Jul-2014 4793 2036 Jul-2015 5023 2202 Aug-2014 4836 2138 A4-2015 5149 2175 Sep-2014 4651 1891 Sep-2015 4643 1886 Oct-2014 4070 '" 1835 Oct-2015 3928 1725 Nov-2014 4131 1824 Nov-2015 3381 1770 Dec-2014 3711 1911 Dec-2015 3469 1758 Jan-2015 4708 2011 Jan-2016 4051 1877 Feb-2015 4248 2018 Feb-2016 3929 1796 Mar-2015 4389 1847 Mar-2016 3475 1739 Apr-2015 3147 1733 Apr-2016 3321 1740

May-2015 3708 1728 May-2016 3845 1755 Jun-2015 4664 1936 Jun-2016 4623 ' 1914

* Peak Minimum Peak Minimum Month Demand Demand Month Demand Demand

Jul-2012 5205 2234 Jul-2013 4880 2106 Aug-2012 5121 2232 Aug-2013 5049 2109 Sep-2012 5036 1945 Sep-2013 4774 1892 Oct-2012 3382 1849 Oct-2013 3917 1787 Nov-2012 3412 1703 Nov-2013 3880 1893 Dec-2012 3993 1723 Dec-2013 4279 1988 Jan-2013 4178 1859 Jan-2014 4919 2059 Feb-2013 3673 1985 Feb-2014 4517 1941 , Mar-2013 3803 1771 Mar-2014 4358 1960 Apr-2013 3489 1797 Apr-2014 3331 1789

May-2013 4137 1839 May-2014 3887 1779 Jun-2013 4887 2018 Jun-2014 4454 2126

Sponsored By: Nora Williams

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