globalchange  > 气候变化与战略
CSCD记录号: CSCD:5036821
论文题名:
CO_2化学吸收技术的模拟及环境影响评价
其他题名: Simulation of CO_2 Chemical Absorption Process and Environmental Assessment
作者: 尤健; 何雅玲; 姚森; 李明佳
刊名: 工程热物理学报
ISSN: 0253-231X
出版年: 2014
卷: 35, 期:1, 页码:1013-1020
语种: 中文
中文关键词: CO_2捕集 ; 二乙醇胺 ; 环境影响
英文关键词: Aspen plus ; CO_2 capture ; Aspen plus ; DEA ; environmental impact
WOS学科分类: ENERGY FUELS
WOS研究方向: Energy & Fuels
中文摘要: 本文采用二乙醇胺(DEA)作为化学吸收剂,通过流程模拟工具Aspen plus对电厂烟道气的CO_2捕集过程进行模拟,分析各个关键参数对系统性能的影响。最后利用MATLAB软件构建了三种模型,对CO_2捕集技术的环境影响进行评价。结论表明:升高吸收溶液温度会减少DEA溶剂损失,降低再沸器热负荷,不过提高溶液温度会消耗额外的能量;当吸收溶液质量分数为0.25时,再沸器消耗的等效功最少;在轮船运输场景下,当泄漏因子取0.05时,其有效排放因子大于参考电厂的排放因子,CCS技术在减缓气候变暖中不会起到作用。
英文摘要: A CO_2-capture process for the flue gas from electric power plants is modeled by the simulation tool Aspen plus in this paper. The DEA is used as chemical absorption for CO_2-capture. And then the effects of the critical parameters to the system performance are analyzed. At last, three models are built by MATLAB to evaluate the environmental impact of CCS (carbon capture sequestration) technology. The results show that the higher temperature of the solution could reduce the DEA loss and the reboiler heat duty. However, raising the temperature of the solution will lead to additional energy consumption. The reboiler heat duty becomes the lowest when the mass fraction of DEA (diethanolamine) of the solution is 0.25. When the leakage factor of the ship transport scenario is 0.05, the effective emission factor of the plant is higher than that of the reference plant, and then the CCS technology will not play a role in the mitigation of the climate warming.
资源类型: 期刊论文
标识符: http://119.78.100.158/handle/2HF3EXSE/147833
Appears in Collections:气候变化与战略

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作者单位: 西安交通大学能源与动力工程学院, 热流科学与工程教育部重点实验室, 西安, 陕西 710049, 中国

Recommended Citation:
尤健,何雅玲,姚森,等. CO_2化学吸收技术的模拟及环境影响评价[J]. 工程热物理学报,2014-01-01,35(1):1013-1020
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