Cu/ZnO/Al2O3/Cr2O3/CeO2 Catalyst for Hydrogen Production by Oxidative Methanol Reforming via Washcoat Catalyst Preparation in Microchannel Reactor

DOI: https://doi.org/10.9767/bcrec.12.3.966.384-392
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Submitted: 28-02-2017
Published: 28-10-2017
Section: Original Research Articles
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The oxidative methanol reforming reaction was carried out using Cu/ZnO/Al2O3/Cr2O3/CeO2 (15/15/2.5/1.25/1.25 mol%), with washcoat by EC sol on microchannel reactor. The experimental conditions were used various sol for washcoat of catalyst, various method for calcinations of catalyst, steam to methanol mole ratio, the mole ratio of oxygen to methanol, weight hourly space velocity, reaction temperature. The experiment result shows that methanol conversion achieved 98.8 % and carbon    monoxide concentration equal to 1204 ppm when using Cu/ZnO/Al2O3/Cr2O3/CeO2 (15/15/2.5/1.25/1.25 mol%) catalyst mixed with EC sol at the reaction temperature of 200 oC. Copyright © 2017 BCREC Group. All rights reserved

Received: 28th February 2017; Revised: 2nd May 2017; Accepted: 3rd May 2017; Available online: 27th October 2017; Published regularly: December 2017

How to Cite: Lesmana, D., Wu, H.S. (2017). Cu/ZnO/Al2O3/Cr2O3/CeO2 Catalyst for Hydrogen Production by Oxidative Methanol Reforming via Washcoat Catalyst Preparation in Microchannel Reactor. Bulletin of Chemical Reaction Engineering & Catalysis, 12 (3): 384-392 (doi:10.9767/bcrec.12.3.966.384-392)

 

Keywords

Oxidative Methanol Reforming; Hydrogen; Microchannel Reactor; Washcoat; Cu/ZnO/Al2O3/Cr2O3/CeO2

  1. Donny Lesmana 
    Department of Chemical Engineering, Faculty of Engineering, Universitas Lampung, 1 Soemantri Brojonegoro, Rajabasa, Bandar Lampung, 35145, Indonesia
  2. Ho Shing Wu 
    Department of Chemical Engineering and Material Science, Yuan-Ze University, 135 Yuan Tung Road, Chung Li, Taoyuan, 32003, Taiwan, Province of China
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