Membrane CO2 Separation System Improvement for Coal-Fired Power Plant Integration

被引:1
作者
Alabid, Maytham [1 ]
Dinca, Cristian [1 ,2 ]
机构
[1] Natl Univ Sci & Technol Politehn Bucharest, Fac Power Engn, Energy Generat & Use Dept, 313 Splaiul Independentei, Bucharest 060042, Romania
[2] Acad Romanian Scientists, Ilfov 3, Bucharest 050044, Romania
关键词
coal-fired power plant; CO2; capture; expander; polymeric membrane; CARBON-DIOXIDE SEPARATION; GAS SEPARATION; FLUE-GAS; CAPTURE; OPTIMIZATION; PERFORMANCE; ADSORPTION;
D O I
10.3390/en17020464
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
Even though there are numerous CO2 capture technologies (such as chemical and physical absorption), investigators are still trying to come up with novel methods that can minimize the energy requirements for their integration into thermal power plants, as well as the CAPEX and OPEX expenses. In this work, the technical and financial aspects of integrating two-stage polymeric membranes into a coal-fired power plant with a capacity of 330 MW were examined. The study researched the membrane post-combustion CO2 capture process utilizing CHEMCAD version 8.1 software with several parameters and an expander to decrease the total cost. The simulation showed promising results regarding reducing power consumption after using an expander for both a high capture rate (>90%) and a CO2 concentration of more than 95%. Thus, the CO2 captured cost decreased from 58.4 EUR/t (no expander) to 48.7 EUR/t (with expander).
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页数:23
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