Hydrogen production from oxidative steam reforming of ethanol in a palladium–silver alloy composite membrane reactor

In this investigation, we studied the oxidative steam reforming reaction of ethanol in a Pd–Ag/PSS membrane reactor for the production of high purity hydrogen. Palladium and silver were deposited on porous stainless steel (PSS) tube via the sequential electroless plating procedure with an overall film thickness of 20 μm and Pd/Ag weight ratio of 78/22. An ethanol–water mixture (nwater/nethanol = 1 or 3) and oxygen (noxygen/nethanol = 0.2, 0.7 or 1.0) were fed concurrently into the membrane reactor packed with Zn–Cu commercial catalyst (MDC-3). The reaction temperatures were set at 593–723 K and the pressures at 3–10 atm. The hydrogen flux in the permeation side increased proportionately with increasing pressure; however, it reduced slightly when increasing oxygen input. This is probably due to the fast oxidation reaction that consumes hydrogen before the onset of the steam reforming reaction. The effect of oxygen plays a vital role on the ethanol oxidation steam reforming reaction, especially for a Pd–Ag membrane reactor in which a higher flux of hydrogen is required. The selectivity of CO2 increased with increasing flow rate of oxygen, while the selectivity of CO remained almost the same.