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dc.contributor.author김우승-
dc.date.accessioned2018-02-28T01:54:45Z-
dc.date.available2018-02-28T01:54:45Z-
dc.date.issued2015-11-
dc.identifier.citationFUEL, v. 160, Page. 513-524en_US
dc.identifier.issn0016-2361-
dc.identifier.issn1873-7153-
dc.identifier.urihttps://www.sciencedirect.com/science/article/pii/S001623611500808X-
dc.identifier.urihttp://hdl.handle.net/20.500.11754/40967-
dc.description.abstractIGCC is an emerging clean coal technology with the potential to produce electricity without damaging the ecosystem. However, efficiency enhancement of the IGCC when pollutant emissions are included in the system is a critical issue that should be evaluated further. In this paper, a large-scale IGCC system is modeled and simulated in three configurations: IGCC without CO2 capture, IGCC with pre-combustion capture, and IGCC with post-combustion capture. The validated model of CO2 capture based on a blended solution of ammonia and AMP is integrated with the IGCC to evaluate system performance in terms of net power produced, efficiency penalty due to CO2 capture, and energy losses in various sections of the IGCC. Moreover, an exergy analysis is carried out to investigate the loss of useful work in major sections of the IGCC for three cases (IGCC without capture, IGCC with pre-capture and IGCC with post-capture). The results indicated that the chemical absorption-based blended solution of AMP and NH3 is an attractive option due to its high CO2 loading capacity and low heat duty requirement; it can also be applied to both the IGCC with pre-combustion capture and IGCC with post-combustion capture. However, IGCC with post-combustion capture is more efficient because the net power produced from IGCC with post-combustion capture (561 MW) is greater than the power obtained from IGCC with pre-combustion capture (518 MW). The efficiency loss due to CO2 was 1.1% for post-combustion capture and 4.3% for pre-combustion capture. Furthermore, about 65% of the total exergy loss was observed in the gasifier and gas turbine combustor only, whereas 41.5% of the total power produced was consumed in the gas turbine compressor and air separation unit. (C) 2015 Elsevier Ltd. All rights reserved.en_US
dc.description.sponsorshipThis work was supported by a National Research Foundation of Korea (NRF) Grant funded by the Korean government (MEST) (No. NRF-2011-0017220). We would like to thank the Higher education Commission of (HEC) Pakistan for the scholarship under title "HRD Initiative-MS leading to PhD program of Faculty development for UESTP" Hanyang University Korea.en_US
dc.language.isoen_USen_US
dc.publisherELSEVIER SCI LTDen_US
dc.subjectCoalen_US
dc.subjectClimate changeen_US
dc.subjectCO2 captureen_US
dc.subjectGasificationen_US
dc.subjectIGCCen_US
dc.subjectGAS SHIFT REACTIONen_US
dc.subjectCARBON-DIOXIDE CAPTUREen_US
dc.subjectCOAL-WATER SLURRIESen_US
dc.subjectPOWER-PLANTen_US
dc.subjectPROCESS SIMULATIONen_US
dc.subjectREACTION-KINETICSen_US
dc.subjectSYSTEMSen_US
dc.subjectHEATen_US
dc.subjectOPTIMIZATIONen_US
dc.subjectGENERATIONen_US
dc.titlePerformance evaluation of integrated gasification combined cycle (IGCC) utilizing a blended solution of ammonia and 2-amino-2-methyl-1-propanol (AMP) for CO2 captureen_US
dc.typeArticleen_US
dc.relation.volume160-
dc.identifier.doi10.1016/j.fuel.2015.08.008-
dc.relation.page513-524-
dc.relation.journalFUEL-
dc.contributor.googleauthorAsif, Muhammad-
dc.contributor.googleauthorBak, Chul-u-
dc.contributor.googleauthorSaleem, Muhammad Wajid-
dc.contributor.googleauthorKim, Woo-Seung-
dc.relation.code2015001837-
dc.sector.campusE-
dc.sector.daehakCOLLEGE OF ENGINEERING SCIENCES[E]-
dc.sector.departmentDEPARTMENT OF MECHANICAL ENGINEERING-
dc.identifier.pidwskim-
Appears in Collections:
COLLEGE OF ENGINEERING SCIENCES[E](공학대학) > MECHANICAL ENGINEERING(기계공학과) > Articles
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