Integrated adsorption and absorption process for post-combustion CO2 capture

被引:17
|
作者
Xiao, Gongkui [1 ]
Xiao, Penny [2 ]
Hoadley, Andrew [3 ]
Webley, Paul [2 ]
机构
[1] Univ Western Australia, Dept Chem Engn, Perth, WA 6009, Australia
[2] Univ Melbourne, Dept Chem Engn, Melbourne, Vic 3010, Australia
[3] Monash Univ, Dept Chem Engn, Clayton, Vic 3800, Australia
关键词
vacuum swing adsorption; monoethanolamine; post-combustion; CO2; capture; integrated process; PRESSURE SWING ADSORPTION; CARBON CAPTURE; FLUE-GAS; MEA; MONOETHANOLAMINE; DEGRADATION; CORROSION; TECHNOLOGIES; SEPARATION; MEMBRANE;
D O I
10.1007/s11705-020-1964-3
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
This study explored the feasibility of integrating an adsorption and solvent scrubbing process for post-combustion CO2 capture from a coal-fired power plant. This integrated process has two stages: the first is a vacuum swing adsorption (VSA) process using activated carbon as the adsorbent, and the second stage is a solvent scrubber/stripper system using monoethanolamine (30 wt-%) as the solvent. The results showed that the adsorption process could enrich CO2 in the flue gas from 12 to 50 mol-% with aCO(2) recovery of > 90%, and the concentrated CO2 stream fed to the solvent scrubber had a significantly lower volumetric flowrate. The increased CO2 concentration and reduced feed flow to the absorption section resulted in significant reduction in the diameter of the solvent absorber, bringing the size of the absorber from uneconomically large to readily achievable domain. In addition, the VSA process could also remove most of the oxygen initially existed in the feed gas, alleviating the downstream corrosion and degradation problems in the absorption section. The findings in this work will reduce the technical risks associated with the state-of-the art solvent absorption technology for CO2 capture and thus accelerate the deployment of such technologies to reduce carbon emissions.
引用
收藏
页码:483 / 492
页数:10
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