Preparation of Pt-loaded hydrogen selective membranes for methanol reforming

• DOI: 10.1016/j.cattod.2005.12.005
• Publication Date: 2006-07-26T06:25:07Z
• Authors: Dong-Wook Lee; Seung-Eun Nam; Bongkuk Sea; Son-Ki Ihm; Kew-Ho Lee
• Keywords: Membrane reactor; Methanol reformer; Knudsen diffusion

Abstract We prepared Pt-included microporous silica membranes (SiO 2 /γ-Al 2 O 3 /Pt–SiO 2 /porous stainless steel (SUS)) to improve CO removal efficiency in a methanol reforming membrane reactor. The permeation test of an H 2 (99%)/CO (1%) mixture between 25 and 200 °C was conducted to observe the effect of the Pt intermediate layer included in the membrane on CO removal efficiency. A mesoporous membrane with the Pt intermediate layer (γ-Al 2 O 3 /Pt–SiO 2 /SUS) showed a remarkable H 2 /CO separation factor of 5.22–7.03, exceeding the Knudsen-dominated transport characteristics expected from a mesoporous γ-Al 2 O 3 layer. After coating a microporous silica skin layer on the Pt-included γ-Al 2 O 3 membrane, CO was not detected in the permeate side of the membrane by the corona ionization detector (CID). When the Pt-included microporous silica membrane was used in the methanol reforming membrane reactor, methanol conversion at 200 °C (methanol/water feed flow rate = 0.004 ml/min) was improved from 73.2% to 93.2% in comparison with the case of a conventional reactor, and CO in the produced gas mixture was efficiently rejected through the Pt-included silica composite membrane. The introduction of the Pt catalyst into the intermediate layer of the composite membrane contributed to the improvement in CO removal efficiency. The dilution of CH 3 OH/H 2 O feed led to an increase in the extent of methanol conversion improvement (a difference of methanol conversion between a membrane reactor and a conventional reactor) due to an increase in the hydrogen recovery.