2014
DOI: 10.1016/j.egypro.2014.03.188
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A Typical Solar-coal Hybrid Power Plant in China

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Cited by 34 publications
(8 citation statements)
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“…Hybridization also increased the plant capacity factor slightly from 22.3% to 23.8%. Presumably, the capacity factor would be much higher if the plant were operated in coal-only mode at night [16]. A later study showed solar-to-electricity efficiency as high as 27.3% for the hybrid configuration as compared to 25.9% for a solar-only plant [17], although Zhai et al reported lower solar-to-electric efficiencies of 13.6% in a similar configuration [18].…”
Section: Solar-aided Boiler Feedwater and Air Pre-heatingmentioning
confidence: 98%
“…Hybridization also increased the plant capacity factor slightly from 22.3% to 23.8%. Presumably, the capacity factor would be much higher if the plant were operated in coal-only mode at night [16]. A later study showed solar-to-electricity efficiency as high as 27.3% for the hybrid configuration as compared to 25.9% for a solar-only plant [17], although Zhai et al reported lower solar-to-electric efficiencies of 13.6% in a similar configuration [18].…”
Section: Solar-aided Boiler Feedwater and Air Pre-heatingmentioning
confidence: 98%
“…The investment cost of components of the same type with different power output was calculated using Equation 15 [66,67]. The investment cost of a 1000 MW CO 2 capture unit was calculated based on a 500 MW CO 2 capture unit [66][67][68][69], shown in Appendix C. Table 7 shows the main exergy cost model analysis results of PG-CC, SA-PG-CC and SA-CC-PG systems, with detailed results listed in Appendix D. Table 7. Primary results of exergy analysis for coal-fired power-generation system with MEA-based CO 2 capture (PG-CC), solar-aided coal-fired power generation with CO 2 capture (SA-PG-CC) and solar-aided CO 2 capture coal-fired power generation (SA-CC-PG).…”
Section: Economic Parametersmentioning
confidence: 99%
“…Abbreviations and Components. Investment of Each Component in the MEA-Based CO 2 Capture Subsystem[67][68][69]. Results of Exergy Cost (kW/kW) in the PG-CC, SA-PG-CC and SA-CC-PG Systems.…”
mentioning
confidence: 99%
“…The saturated-rich vapor is expanded to a low pressure P c in the turbine to produce shaft work. In the meantime, after rejecting heat in the high temperature recuperator (5) to the subcooled liquid solution, the weak liquid solution is released to the pressure P c (6) in the throttle. Under pressure P c , the exhaust rich ammonia-water vapor from the turbine (3) is diluted by weak liquid solution (6) at throttle outlet and both streams are fed to mixer to produce the basic solution (7).…”
Section: Schematic Description Of Cpc-kcs Hybrid Systemmentioning
confidence: 99%