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Modeling and simulation of sour gas membrane-absorption system: Influence of operational parameters on species removal

机译:酸性气体膜吸收系统的建模与仿真:操作参数对物质去除的影响

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摘要

Membrane-based gas separation process is an effective method for separation of species from gas mixtures. Combination of membrane process with other separation methods such as absorption is an appropriate method for gas separation. One of applications of hybrid systems of membrane-absorption is sour gas sweetening. In this paper, the hollow fiber membrane contactor and amine solution are used for separation of CO2 and H2S from CO2/H2S/CH4 gas mixture. Sour gas and amine solution enter the shell and fiber respectively. CO2 and H2S react with the amine solution. Reaction mechanism and equations for three phases of gas, liquid, and membrane are needed for modeling of this system. MATLAB software is used for simulation. The results show that concentrations of CO2 and H2S decrease in the beginning of the fiber. Liquid phase is controlling phase. Furthermore, pressure increase has a positive effect on separation.
机译:基于膜的气体分离过程是从气体混合物中分离物质的有效方法。膜工艺与其他分离方法(例如吸收法)的结合是气体分离的合适方法。混合膜吸收系统的应用之一是酸性气体脱硫。在本文中,中空纤维膜接触器和胺溶液用于从CO2 / H2S / CH4气体混合物中分离出CO2和H2S。酸性气体和胺溶液分别进入外壳和纤维。 CO2和H2S与胺溶液反应。对该系统进行建模需要气体,液体和膜的三相反应机理和方程式。 MATLAB软件用于仿真。结果表明,在纤维开始时,CO2和H2S的浓度降低。液相为控制相。此外,压力增加对分离具有积极作用。

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