IGCC Precombustion CO2 Capture Using K2CO3 Solvent and Utilizing the Intercooling Heat Recovered From CO2 Compressors for CO2 Regeneration

被引:9
作者
Li, Sheng [1 ]
Jin, Hongguang [1 ]
Mumford, Kathryn Anne [2 ]
Smith, Kathryn [2 ]
Stevens, Geoff [2 ]
机构
[1] Chinese Acad Sci, Inst Engn Thermophys, Beijing 100190, Peoples R China
[2] Univ Melbourne, Dept Chem & Biomol Engn, Cooperat Res Ctr Greenhouse Gas Technol CO2CRC, Melbourne, Vic 3010, Australia
来源
JOURNAL OF ENERGY RESOURCES TECHNOLOGY-TRANSACTIONS OF THE ASME | 2015年 / 137卷 / 04期
基金
中国国家自然科学基金;
关键词
IGCC precombustion; potassium carbonate solvent; CO2; capture; modeling; exergy analysis; HOT POTASSIUM CARBONATE; PRE-COMBUSTION CAPTURE; EXERGY ANALYSIS; MASS-TRANSFER; NATURAL-GAS; ABSORPTION; DIOXIDE; POWER; ENERGY; COGENERATION;
D O I
10.1115/1.4029964
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
CO2 capture (CC) using hot K2CO3 solvent in integrated gasification combined cycle (IGCC) plant is a promising technology for CO2 emission reduction. Based on pilot scale trials, an innovative IGCC system with CC using hot K2CO3 solvent is proposed, in which the intercooling heat between CO2 compressors is recovered for CO2 regeneration (IGCC_CC_HR). Thermodynamic performance and exergy and energy utilization diagram (EUD) analysis are presented. Results show that recovery of the intercooling heat between CO2 compressors reduces the steam extraction requirement from turbines for CO2 regeneration by around 18% and enhances the efficiency of IGCC with CO2 capture (IGCC_CC) plant by 0.3-0.7 percentage points. With 90% CC, the efficiency of the IGCC_CC_HR plant is around 35.4% which is higher than IGCC_CC plant using Selexol technology. Compared to IGCC, the energy penalty for CC in IGCC_CC_HR plant is mainly caused by the exergy losses in CO2 separation (45.2%), water gas shift (WGS) (28.5%), combined cycle (20.7%) and CO2 compression units (5.6%). EUD analysis shows that the IGCC_CC_HR plant realizes good match of the energy levels between the intercooling heat and the recovered steam for CO2 regeneration, thereby obviously reducing the exergy losses in CO2 compression and separation units and improving the plant efficiency. The results presented in this paper confirm the sources causing the energy penalty for CC in IGCC power plant and the new IGCC_CC_HR system helps to reduce the energy penalty for CC in IGCC power plant based on solvent technologies.
引用
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页数:9
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