Friday, October 14, 2016

Enhanced hydrogen production by sorption-enhanced steam reforming from glycerol with in-situ CO2 removal in a fixed-bed reactor



Enhanced hydrogen production by sorption-enhanced steam reforming from glycerol with in-situ CO2 removal in a fixed-bed reactor
Type
Journal Article
Author
Binlin Dou
Author
Bo Jiang
URL
Volume
166
Pages
340-346
Publication
Fuel
Date
February 15, 2016
Abstract
For the fixed-bed reactor configuration in the sorption-enhanced steam reforming process (SERP), solid mixture of catalyst and sorbent is stationary and alternatively exposed to reaction and regeneration conditions for multi-cycles by periodically switching the feed gases for enhanced hydrogen production with in-situ CO2 removal. Researchers prepared A NiO/NiAl2O4 catalyst using the co-precipitation method with rising pH technique. The crystalline spinel phase of NiAl2O4 was formed under the calcination temperature of 900 °C.
Results revealed that hydrogen production by SERP can be clearly divided into three periods. The experimental gaseous products were compared with non-stoichiometric thermodynamic calculations. H2 purity was greatly increased, and CO2, CO and CH4 concentrations were reduced by in-situ CO2 removal during the pre-breakthrough period.
Enhanced hydrogen production depended on in-situ CO2 removal. The operation durations for producing high-purity hydrogen of more than 90% were decreased with the increase of the cycles.

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