US EPA

1226537 

Journal Article 

Hydrogen production by reforming of liquid hydrocarbons in a membrane reactor for portable power generation - Experimental studies 

Damle, AS 

2009 

Yes 

Journal of Power Sources
ISSN: 0378-7753 

Elesevier Science B.V., P.O. Box 211 Amsterdam 1000 AE Netherlands 

186 

1 (Jan 1 

167-177 

10.1016/j.jpowsour.2008.09.059 

WOS:000262796000021 

https://linkinghub.elsevier.com/retrieve/pii/S0378775308018600
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One of the most promising technologies for lightweight, compact, portable power generation is proton exchange membrane (PEM) fuel cells. PEM fuel cells, however, require a source of pure hydrogen. Steam reforming of hydrocarbons in an integrated membrane reactor has potential to provide pure hydrogen in a compact system. Continuous separation of product hydrogen from the reforming gas mixture is expected to increase the yield of hydrogen significantly as predicted by model simulations. In the laboratory-scale experimental studies reported here steam reforming of liquid hydrocarbon fuels, butane, methanol and Clearlite[super][registered] was conducted to produce pure hydrogen in a single step membrane reformer using commercially available Pd-Ag foil membranes and reforming/WGS catalysts. All of the experimental results demonstrated increase in hydrocarbon conversion due to hydrogen separation when compared with the hydrocarbon conversion without any hydrogen separation. Increase in hydrogen recovery was also shown to result in corresponding increase in hydrocarbon conversion in these studies demonstrating the basic concept. The experiments also provided insight into the effect of individual variables such as pressure, temperature, gas space velocity, and steam to carbon ratio. Steam reforming of butane was found to be limited by reaction kinetics for the experimental conditions used: catalysts used, average gas space velocity, and the reactor characteristics of surface area to volume ratio. Steam reforming of methanol in the presence of only WGS catalyst on the other hand indicated that the membrane reactor performance was limited by membrane permeation, especially at lower temperatures and lower feed pressures due to slower reconstitution of CO and H sub(2 into methane thus maintaining high hydrogen partial pressures in the reacting gas mixture. The limited amount of data collected with steam reforming of Clearlite[super][registered] indicated very good match between theoretical predictions and experimental results indicating that the underlying assumption of the simple model of conversion of hydrocarbons to CO and H) sub(2) followed by equilibrium reconstitution to methane appears to be reasonable one. 

Temperature; Membranes; Catalysts; Kinetics; Electric power generation; Fuel technology; Simulation; Hydrogen; Methane; 2009)