Simulation of Water Gas Shift Zeolite Membrane Reactor

被引:0
|
作者
Makertiharta, I. G. B. N. [1 ]
Rizki, Z. [1 ]
Zunita, Megawati [1 ]
Dharmawijaya, P. T. [1 ]
机构
[1] Inst Teknol Bandung, Chem Engn Dept, Jl Ganesha 10, Bandung 40132, West Java, Indonesia
关键词
MFI-TYPE ZEOLITE; HYDROGEN-PRODUCTION; CATALYTIC CRACKING; PERMEATION; SEPARATION;
D O I
10.1088/1757-899X/214/1/012013
中图分类号
T [工业技术];
学科分类号
08 ;
摘要
The search of alternative energy sources keeps growing from time to time. Various alternatives have been introduced to reduce the use of fossil fuel, including hydrogen. Many pathways can be used to produce hydrogen. Among all of those, the Water Gas Shift (WGS) reaction is the most common pathway to produce high purity hydrogen. The WGS technique faces a downstream processing challenge due to the removal hydrogen from the product stream itself since it contains a mixture of hydrogen, carbon dioxide and also the excess reactants. An integrated process using zeolite membrane reactor has been introduced to improve the performance of the process by selectively separate the hydrogen whilst boosting the conversion. Furthermore, the zeolite membrane reactor can be further improved via optimizing the process condition. This paper discusses the simulation of Zeolite Membrane Water Gas Shift Reactor (ZMWGSR) with variation of process condition to achieve an optimum performance. The simulation can be simulated into two consecutive mechanisms, the reaction prior to the permeation of gases through the zeolite membrane. This paper is focused on the optimization of the process parameters (e.g. temperature, initial concentration) and also membrane properties (e.g. pore size) to achieve an optimum product specification (concentration, purity).
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页数:9
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