Energy and Exergy Analyses of an Integrated Gasification Combined Cycle Power Plant with CO2 Capture Using Hot Potassium Carbonate Solvent
文献类型：期刊论文
| 作者 | Li, Sheng1,2; Jin, Hongguang1; Gao, Lin1; Mumford, Kathryn Anne2; Smith, Kathryn2; Stevens, Geoff2 |
| 刊名 | ENVIRONMENTAL SCIENCE & TECHNOLOGY
 |
| 出版日期 | 2014-12-16 |
| 卷号 | 48期号:24页码:14814-14821 |
| 英文摘要 | Energy and exergy analyses were studied for an integrated gasification combined cycle (IGCC) power plant with CO2 capture using hot potassium carbonate solvent. The study focused on the combined impact of the CO conversion ratio in the water gas shift (WGS) unit and CO2 recovery rate on component exergy destruction, plant efficiency, and energy penalty for CO2 capture. A theoretical limit for the minimal efficiency penalty for CO2 capture was also provided. It was found that total plant exergy destruction increased almost linearly with CO2 recovery rate and CO conversion ratio at low CO conversion ratios, but the exergy destruction from the WGS unit and the whole plant increased sharply when the CO conversion ratio was higher than 98.5% at the design WGS conditions, leading to a significant decrease in plant efficiency and increase in efficiency penalty for CO2 capture. When carbon capture rate was over around 70%, via a combination of around 100% CO2 recovery rate and lower CO conversion ratios, the efficiency penalty for CO2 capture was reduced. The minimal efficiency penalty for CO2 capture was estimated to be around 5.0 percentage points at design conditions in an IGCC plant with 90% carbon capture. Unlike the traditional aim of 100% CO conversion, it was recommended that extremely high CO conversion ratios should not be considered in order to decrease the energy penalty for CO2 capture and increase plant efficiency. |
| WOS标题词 | Science & Technology ; Technology ; Life Sciences & Biomedicine |
| 类目[WOS] | Engineering, Environmental ; Environmental Sciences |
| 研究领域[WOS] | Engineering ; Environmental Sciences & Ecology |
| 关键词[WOS] | PRE-COMBUSTION CAPTURE ; DIOXIDE ABSORPTION ; RATE PROMOTERS ; NATURAL-GAS ; BORIC-ACID ; IGCC-CCS ; SYSTEM ; COAL ; COGENERATION ; TECHNOLOGIES |
| 收录类别 | SCI |
| 语种 | 英语 |
| WOS记录号 | WOS:000346686100090 |
| 公开日期 | 2015-12-22 |
| 源URL | [http://ir.etp.ac.cn/handle/311046/105992]  |
| 专题 | 工程热物理研究所_中国科学院工程热物理所（论文库）_期刊论文（SCI） |
| 作者单位 | 1.Chinese Acad Sci, Inst Engn Thermophys, Lab Distributed Energy Syst & Renewable Energy, Beijing 100190, Peoples R China 2.Univ Melbourne, Dept Chem & Biomol Engn, Cooperat Res Ctr Greenhouse Gas Technol CO2CRC, Melbourne, Vic 3010, Australia |
| 推荐引用方式 GB/T 7714 | Li, Sheng,Jin, Hongguang,Gao, Lin,et al. Energy and Exergy Analyses of an Integrated Gasification Combined Cycle Power Plant with CO2 Capture Using Hot Potassium Carbonate Solvent[J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY,2014,48(24):14814-14821. |
| APA | Li, Sheng,Jin, Hongguang,Gao, Lin,Mumford, Kathryn Anne,Smith, Kathryn,&Stevens, Geoff.(2014).Energy and Exergy Analyses of an Integrated Gasification Combined Cycle Power Plant with CO2 Capture Using Hot Potassium Carbonate Solvent.ENVIRONMENTAL SCIENCE & TECHNOLOGY,48(24),14814-14821. |
| MLA | Li, Sheng,et al."Energy and Exergy Analyses of an Integrated Gasification Combined Cycle Power Plant with CO2 Capture Using Hot Potassium Carbonate Solvent".ENVIRONMENTAL SCIENCE & TECHNOLOGY 48.24(2014):14814-14821. |
入库方式： OAI收割
来源：工程热物理研究所
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