TY - JOUR
T1 - Novel design of integrated gasification combined cycle (IGCC) power plants with CO2 capture
AU - Shi, Bin
AU - Xu, Wen
AU - Wu, Erdorng
AU - Wu, Wei
AU - Kuo, Po Chih
N1 - Funding Information:
The authors gratefully acknowledge the financial support received from the Fundamental Research Funds for the Central Universities (WUT: 185220007 ) and also thank the Ministry of Science and Technology, Taiwan for its partial financial support of this research under grant MOST 106-2211-E-006-239 .
Publisher Copyright:
© 2018 Elsevier Ltd
PY - 2018/9/10
Y1 - 2018/9/10
N2 - To develop the new integrated gasification combined cycle (IGCC) power plants with CO2 capture, first the integrated intermittent chemical looping air separation (IICLAS) unit is added to improve the coal gasification and carries out the oxy-fuel combustion, second the CO2 compression and sequestration (CCS) unit is added to achieve deep reductions in emissions of CO2 to the atmosphere. Compared to the conventional cryogenic air separation (CAS) unit, the IICLAS unit continuously produces the high-purity oxygen without the solid looping cycles and it also generates the additional electricity by virtue of the heating jacket for the oxy-fuel combustion of methane (OCM) and the waste heat recovery mechanism. A few comparisons show that the IICLAS-based IGCC + CCS power system (Design 2) can effectively increase 12.2% of the gross power compared to the CAS-based IGCC + CCS power system (Design 1). For the dual IICLAS-based IGCC + CCS power system (Design 3), the OCM units are removed and the flue gas is split to reduce the circulated steam/water. Finally, Design 3 can ensure the lowest oxygen supply rate by 50.67 kg/s, the highest net efficiency by 40.25%, and the largest KCC factor by 0.58.
AB - To develop the new integrated gasification combined cycle (IGCC) power plants with CO2 capture, first the integrated intermittent chemical looping air separation (IICLAS) unit is added to improve the coal gasification and carries out the oxy-fuel combustion, second the CO2 compression and sequestration (CCS) unit is added to achieve deep reductions in emissions of CO2 to the atmosphere. Compared to the conventional cryogenic air separation (CAS) unit, the IICLAS unit continuously produces the high-purity oxygen without the solid looping cycles and it also generates the additional electricity by virtue of the heating jacket for the oxy-fuel combustion of methane (OCM) and the waste heat recovery mechanism. A few comparisons show that the IICLAS-based IGCC + CCS power system (Design 2) can effectively increase 12.2% of the gross power compared to the CAS-based IGCC + CCS power system (Design 1). For the dual IICLAS-based IGCC + CCS power system (Design 3), the OCM units are removed and the flue gas is split to reduce the circulated steam/water. Finally, Design 3 can ensure the lowest oxygen supply rate by 50.67 kg/s, the highest net efficiency by 40.25%, and the largest KCC factor by 0.58.
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U2 - 10.1016/j.jclepro.2018.05.152
DO - 10.1016/j.jclepro.2018.05.152
M3 - Article
AN - SCOPUS:85048575100
SN - 0959-6526
VL - 195
SP - 176
EP - 186
JO - Journal of Cleaner Production
JF - Journal of Cleaner Production
ER -