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THE APPLICATION OF KENTUCKY POWER

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THE APPLICATION OF KENTUCKY POWER ( the-application-kentucky-power )

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Table 8 Gas CC Units Installed by Turbine Type in the U.S. Since 2002 Turbine Model - GeneralElechic Co-MS7001FA GT SieinensPower GenerationInc-501FD Mitsubisli Heavy Indushies-MSO 1G Siemens Power GenerationInc-SGT6-6000G GeneralElechic Co-MS7001FB Mitsubishi Heavy Indushies-M501F GeneralElechic Co-MS700 1EA SieinensPower GenerationInc-V84.2 GeneralElechic Co-LM6000PC Splint GeneralElechic Co-LM6000PD Splint Soiirces atid Notes Installed MW by turbine tnodcl from Ventyx (201I). Cost Jy) $473 $499 $504 da $466 $537 $524 $459 da da This database is not completely comprehensive in identifying turbine model, with 35% of the total MW installed since 2002 being identified by turbine type. Unit cost (including steam turbine but excluding balance of plant) assumes a typical configuration and steam turbine, from Gas TirrDiire World (2010). E. COMBINED-CYCLOEOLINGSYSTEM For the reference combined-cycle plant, we assumed a closed-loop circulating water cooling system with a multiple-cell mechanical draft cooling tower, based on the predominance of cooling towers among new CCs and CH2M HILL’S recommendation. Among the 15 CC units installed in PJM since 2002 and reporting cooling system data, 13 have cooling towers while 2 have air cooling or once-through cooling systems.l4 F. DUCTFIRINGAND POWER AUGMENTATION For the reference CC plant, we included duct firing capability, consistent with predominant practice among prqjects in PJM and elsewhere. We determined that a cost-effective amount of duct firing to include was 74 MW at 92 OF (76 MW at 59 O F ) based on guidance from CH2M HILL,, and consultation with GE representatives. According to CH2M and GE, this quantity of duct firing is consistent with 7FA.05 2x1 projects cui-rently being developed. For CCs and CTs, we also evaluated additional power augmentation options by comparing the capital costs and incremental output available if investing in each option. Table 9 and Table 10 compare inlet evaporative cooling to inlet chilling and to no power augmentation for both gas CT andCCplants. ThesecostandperformancemetricswerecalculatedbyCH2MWILLusingGE software, and while self-consistent, represent rough approximations of equipment and balance of plant (“BOP”) cost components without considering detailed locational, materials escalation, or other engineering cost factors. 11 Installed Since 2002 (m) (Cotlnt) 180 54 22 5 7 925 5 765 9 452 4 204 4 172 4 ($IC 32,940 I 1,232 5,874 1,335 1,260

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