“…A heat rate of 7188 Btu/kWh was estimated from the Fluor report based on pressurized gas fuel and a turbine firing temperature (Chandra et al 1978b). This is comparable with estimates for liquid-fueled combined cycles of 8345 Btu/kWh for 2000°F firing temperature, 7300 Btu/kWh for 2200°F firing temperature and 6679 Btu/kWh for 3000°F firing temperature (EPRI 1979;NRC 1977b).…”
Section: Combined-cycle Plants Not Co-sited With a Gasification Plantsupporting
confidence: 58%
“…By integrating a GCC system with a coal gasification plant, cost savings can be made and overall thermal efficiency can be improved compared to separate gasification and power plants. Several studies have been published on these systems; th~ general conclusions reached in these studies are that integrated gasification combined-cycle systems (IGCC) can potentially produce electric power at lower cost and higher thermal efficiency than conventional coal-fired systems with stack gas scrubbers (Chandra et al 1978b;Jones and Donahue 1977;Robson, Belcher and Colton 1976). The IGCC systems are also expected to have lower air emissions and water requirements.…”
Section: Power Production With Integrated Coal Gasification Combined-mentioning
confidence: 99%
“…Among the various design studies that have been published, those published by Fluor Engineers. and Constructors under EPRI sponsorship appear to be the most up-to-date (Chandra 1978a(Chandra , 1978bColeman et ale 1979)~ The results of the Fluor-EPRI studies are also well suited for use in this study because important assumptions are clearly spelled out and process designs and cost breakdowns are given in sufficient detail to allow comparison among this study and others.…”
Section: 27mentioning
confidence: 99%
“…The Fluor reports cited previously give separate cost estimates for gasification plants producing either intermediate Btu gas or electric power using the BGC slagging gasifier (Chandra et ale 1978a(Chandra et ale , 1978b. Adding the combinedcycle power production equipment increased the plant capital cost by an amount equivalent to $259/kW (mid-1976 dollars not including contingency).…”
Section: Combined-cycle Plants Not Co-sited With a Gasification Plantmentioning
confidence: 99%
“…If the more conservative contingency (20%) is used, the capital cost, including contingency, is 4.32 $485/kW (1981 dollars). Estimated construction times range from 24 to 36 months (Bechtel 1977;EPRI 1979;Chandra et al 1978b). The total capital required includes capital cost ($485/kW); land, inventory and startup costs (~$24/kW); escalation during construction (EDC); and interest during construction (IDC).…”
Section: Combined-cycle Plants Not Co-sited With a Gasification Plantmentioning
PNL-3277 UC-97 PNL's assessment consists of two parts. The first part, which is the subject of this document, is a detailed description of the technical, cost, resource and environmental characteristics of each system component and technologies available for these components. The second part is a computer-based model that PNL has developed to simulate construction and operation of alternative system configurations and to compare the performance of these systems under a variety of economic and technical conditions. This document consists of six chapters and two appendices. A more thorough description of coal-based electric energ~ systems is presented in the Introduction and Chapter 1. Each of the subsequent chapters descrihes technologies for five system components: Western coal resources (Chapter 2), coal vii transportation (Chapter 3), coal gasification and gas transmission (Chapter 4),
“…A heat rate of 7188 Btu/kWh was estimated from the Fluor report based on pressurized gas fuel and a turbine firing temperature (Chandra et al 1978b). This is comparable with estimates for liquid-fueled combined cycles of 8345 Btu/kWh for 2000°F firing temperature, 7300 Btu/kWh for 2200°F firing temperature and 6679 Btu/kWh for 3000°F firing temperature (EPRI 1979;NRC 1977b).…”
Section: Combined-cycle Plants Not Co-sited With a Gasification Plantsupporting
confidence: 58%
“…By integrating a GCC system with a coal gasification plant, cost savings can be made and overall thermal efficiency can be improved compared to separate gasification and power plants. Several studies have been published on these systems; th~ general conclusions reached in these studies are that integrated gasification combined-cycle systems (IGCC) can potentially produce electric power at lower cost and higher thermal efficiency than conventional coal-fired systems with stack gas scrubbers (Chandra et al 1978b;Jones and Donahue 1977;Robson, Belcher and Colton 1976). The IGCC systems are also expected to have lower air emissions and water requirements.…”
Section: Power Production With Integrated Coal Gasification Combined-mentioning
confidence: 99%
“…Among the various design studies that have been published, those published by Fluor Engineers. and Constructors under EPRI sponsorship appear to be the most up-to-date (Chandra 1978a(Chandra , 1978bColeman et ale 1979)~ The results of the Fluor-EPRI studies are also well suited for use in this study because important assumptions are clearly spelled out and process designs and cost breakdowns are given in sufficient detail to allow comparison among this study and others.…”
Section: 27mentioning
confidence: 99%
“…The Fluor reports cited previously give separate cost estimates for gasification plants producing either intermediate Btu gas or electric power using the BGC slagging gasifier (Chandra et ale 1978a(Chandra et ale , 1978b. Adding the combinedcycle power production equipment increased the plant capital cost by an amount equivalent to $259/kW (mid-1976 dollars not including contingency).…”
Section: Combined-cycle Plants Not Co-sited With a Gasification Plantmentioning
confidence: 99%
“…If the more conservative contingency (20%) is used, the capital cost, including contingency, is 4.32 $485/kW (1981 dollars). Estimated construction times range from 24 to 36 months (Bechtel 1977;EPRI 1979;Chandra et al 1978b). The total capital required includes capital cost ($485/kW); land, inventory and startup costs (~$24/kW); escalation during construction (EDC); and interest during construction (IDC).…”
Section: Combined-cycle Plants Not Co-sited With a Gasification Plantmentioning
PNL-3277 UC-97 PNL's assessment consists of two parts. The first part, which is the subject of this document, is a detailed description of the technical, cost, resource and environmental characteristics of each system component and technologies available for these components. The second part is a computer-based model that PNL has developed to simulate construction and operation of alternative system configurations and to compare the performance of these systems under a variety of economic and technical conditions. This document consists of six chapters and two appendices. A more thorough description of coal-based electric energ~ systems is presented in the Introduction and Chapter 1. Each of the subsequent chapters descrihes technologies for five system components: Western coal resources (Chapter 2), coal vii transportation (Chapter 3), coal gasification and gas transmission (Chapter 4),
scite is a Brooklyn-based organization that helps researchers better discover and understand research articles through Smart Citations–citations that display the context of the citation and describe whether the article provides supporting or contrasting evidence. scite is used by students and researchers from around the world and is funded in part by the National Science Foundation and the National Institute on Drug Abuse of the National Institutes of Health.