2008
DOI: 10.1016/j.rser.2007.06.010
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Assessment of integrated gasification combined cycle technology competitiveness

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Cited by 46 publications
(23 citation statements)
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“…The raw syngas from the gasification process mainly consisted of carbon monoxide (CO) and hydrogen (H 2 ), and a small quantity of contaminant compounds such as hydrogen-sulfide (H 2 S) and carbonyl sulfide (COS), oxides of carbon and sulfur such as carbon dioxide (CO 2 ) and sulfur dioxide (SO 2 ), nitrogen compounds such as ammonia (NH 3 ), hydrogen cyanine (HCN), Hg, and particulates from the mineral fraction of the coal such as unconverted carbon and ash [32]. Some of the corrosive components such as sulfide, nitride, and dust were removed in this cleaning section.…”
Section: Acid Gas Removal and Sulfur Recovery Processmentioning
confidence: 99%
See 1 more Smart Citation
“…The raw syngas from the gasification process mainly consisted of carbon monoxide (CO) and hydrogen (H 2 ), and a small quantity of contaminant compounds such as hydrogen-sulfide (H 2 S) and carbonyl sulfide (COS), oxides of carbon and sulfur such as carbon dioxide (CO 2 ) and sulfur dioxide (SO 2 ), nitrogen compounds such as ammonia (NH 3 ), hydrogen cyanine (HCN), Hg, and particulates from the mineral fraction of the coal such as unconverted carbon and ash [32]. Some of the corrosive components such as sulfide, nitride, and dust were removed in this cleaning section.…”
Section: Acid Gas Removal and Sulfur Recovery Processmentioning
confidence: 99%
“…The shift reaction was repeated in the second reactor with a lower temperature than the first reactor. The syngas that left the WGS reactor had a much higher H 2 composition than the raw syngas with the CO conversion of 90% [32,33].…”
Section: Water Gas Shift and Co 2 Removal Unitmentioning
confidence: 99%
“…In the same study a BIGCC plant with CCS and net generation of 123 MW el might present a lower HHV efficiency ($28%), higher capital costs (approximately 1730 $/kW) while its COE could be as high as 0.082 $/kWh due to the high CCS costs. In a more recent study [9], higher net efficiencies are envisaged for the close future due to ongoing improvements on IGCC technology and some interesting data for IGCC plants already installed are listed within a capacity range 100-545 MW el . The assumptions for IGCC technology indicate capital costs $1450 $/kW, and net HHV efficiency in the range 40-50% provided that a CCS system is not installed.…”
Section: Business Interest and Competitive Technologiesmentioning
confidence: 99%
“…IGCC pilot plants and industrial-scale demonstrations plants have shown potential for this technology to be implemented in commercial-scale; however; this technology still requires improvement in terms of process economics to become fully competitive [5]. Also, reliability and availability have challenged the development and commercialization of IGCC power plants in terms Pre-combustion technology [14] Lignite coal Units to be completed in the first half of 2013, non-slagging transport reactor integrated gasifier (TRIG) & two Siemens SGT6-5000F gas turbine Nakoso (Japan) 2014 500-600…”
Section: Introductionmentioning
confidence: 99%