A Heterogeneous Modeling and Simulation for Catalytic WGS Reactor
سال انتشار: 1395
نوع سند: مقاله کنفرانسی
زبان: انگلیسی
مشاهده: 898
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شناسه ملی سند علمی:
CHCONF02_029
تاریخ نمایه سازی: 9 مرداد 1395
چکیده مقاله:
In this work, a simulation of a fixed bed reactor for water gas shift reaction, which forms part of a hydrogen production, was carried out. A commercial CuO/ZnO/Al2O3 catalyst was employed and a one-dimensional heterogeneous model was applied for the simulation. The kinetic information has been taken from literature for the above reaction. The distribution of concentration in fluid bulk as well as porous catalyst, rate of reaction, pressure profile and superficial velocity distribution were represented as results of study. gPROMS, a general purpose modeling package, was used for modeling and simulation of the water–gas shift reaction.
کلیدواژه ها:
نویسندگان
D Mohammady
Department of Chemical Engineering, Petroleum University of Technology, Abadan, Iran
A Shariati
Department of Gas Engineering, Petroleum University of Technology, Ahwaz, Iran
B Roozbehani
Department of Chemical Engineering, Petroleum University of Technology, Abadan, Iran
M.R Khosravi Nikou
Department of Gas Engineering, Petroleum University of Technology, Ahwaz, Iran