烟气
膜
燃烧
气体分离
膜技术
分离过程
工艺工程
参数统计
化学
化石燃料
化学工程
材料科学
环境科学
废物管理
色谱法
工程类
有机化学
生物化学
统计
数学
作者
Li Zhao,E. Riensche,R. Menzer,L. Blum,Detlef Stolten
标识
DOI:10.1016/j.memsci.2008.07.058
摘要
Capture of CO 2 from flue gases produced by the combustion of fossil fuels and biomass in air is referred to as post-combustion capture. Chemisorbent processes are considered to be the most feasible method and are already at an advanced stage of development, but gas separation membranes are attracting more and more attention as a possible alternative. This paper describes a detailed parametric study of mass and energy balances for a simulated single membrane process. Typical operating conditions (CO 2 concentration in the flue gas, pressure and temperature, etc.) together with the influence of the membrane quality (permeability, selectivity) and membrane area on membrane performance (CO 2 separation degree and CO 2 purity) are simulated over a wide range of parameters.
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