Title of article :
Integration of the steam cycle and CO2 capture process in a decarbonization power plant
Author/Authors :
Xu، نويسنده , , Gang and Hu، نويسنده , , Yue and Tang، نويسنده , , Baoqiang and Yang، نويسنده , , Yongping and Zhang، نويسنده , , Kai and Liu، نويسنده , , Wenyi، نويسنده ,
Issue Information :
روزنامه با شماره پیاپی سال 2014
Pages :
10
From page :
277
To page :
286
Abstract :
A new integrated system with power generation and CO2 capture to achieve higher techno-economic performance is proposed in this study. In the new system, three measures are adopted to recover the surplus energy from the CO2 capture process. The three measures are as follows: (1) using a portion of low-pressure steam instead of high-pressure extracted steam by installing the steam ejector, (2) mixing a portion of flash-off water with the extracted steam to utilize the superheat degree of the extracted steam, and (3) recycling the low-temperature waste heat from the CO2 capture process to heat the condensed water. As a result, the power output of the new integrated system is 107.61 MW higher than that of a decarbonization power plant without integration. The efficiency penalty of CO2 capture is expected to decrease by 4.91%-points. The increase in investment produced by the new system is 3.25 M$, which is only 0.88% more than the total investment of a decarbonization power plant without integration. Lastly, the cost of electricity and CO2 avoided is 15.14% and 33.1% lower than that of a decarbonization power generation without integration, respectively. The promising results obtained in this study provide a new approach for large-scale CO2 removal with low energy penalty and economic cost.
Keywords :
Coal-fired power plant , steam ejector , CO2 capture , Surplus energy utilization , Techno-economic analysis
Journal title :
Applied Thermal Engineering
Serial Year :
2014
Journal title :
Applied Thermal Engineering
Record number :
1908344
Link To Document :
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