a javooni - Oil Design and Constraction Co. (ODCC), Tehran ۱۵۹۴۹-۷۶۱۱۱, Iran,
h ale ebrahim - Chemical Engineering Department, Petrochemical Center Excellency, Amirkabir University of Technology (Tehran Polytechnic), Tehran ۱۵۸۷۵-۴۴۱۳, Iran
b dabir - Chemical Engineering Department, Petrochemical Center Excellency, Amirkabir University of Technology (Tehran Polytechnic), Tehran ۱۵۸۷۵-۴۴۱۳, Iran

Alkylation is a usual method for producing high octane number and environmental friendly gasoline from reaction between isobutane and butenes. From many years ago, researches have begun for invention a solid acid catalyst to replace the corrosive and toxic liquid acid catalysts. In this work, we will have simulated a moving bed reactor for alkylation process which operates with solid catalyst. Kinetics of solid catalyst extracted from a literatures. At first, a suitable model will have created to analyze the conversion in reactor. Then, we will consider a base case according to best industrial schemes. Afterward, effect of change in some main reaction parameters on conversion will have been analyzed by results of solving differential equations simultaneously

Alkylation, Moving bed, Isobutane, Butene, Solid acid catalyst, Green gasoline