scholarly journals Dynamic simulation of pure hydrogen production via ethanol steam reforming in a catalytic membrane reactor

Energy ◽  
2016 ◽  
Vol 117 ◽  
pp. 316-324 ◽  
Author(s):  
Ali Hedayati ◽  
Olivier Le Corre ◽  
Bruno Lacarrière ◽  
Jordi Llorca
Keyword(s):  
Hydrogen Production ◽  
Dynamic Simulation ◽  
Steam Reforming ◽  
Membrane Reactor ◽  
Ethanol Steam Reforming ◽  
Pure Hydrogen ◽  
Catalytic Membrane ◽  
Catalytic Membrane Reactor ◽  
Ethanol Steam

Reaction and hydrogen production phenomena of ethanol steam reforming in a catalytic membrane reactor

Energy ◽  
2021 ◽  
Vol 220 ◽  
pp. 119737
Author(s):  
Wei-Hsin Chen ◽  
Shu-Cheng Li ◽  
Steven Lim ◽  
Zih-Yu Chen ◽  
Joon Ching Juan
Keyword(s):  
Hydrogen Production ◽  
Steam Reforming ◽  
Membrane Reactor ◽  
Ethanol Steam Reforming ◽  
Catalytic Membrane ◽  
Catalytic Membrane Reactor ◽  
Ethanol Steam

scholarly journals An Experimental Performance Study of a Catalytic Membrane Reactor for Ethanol Steam Reforming over a Metal Honeycomb Catalyst

Membranes ◽  
2021 ◽  
Vol 11 (10) ◽  
pp. 790
Author(s):  
Nikita Eremeev ◽  
Alexey Krasnov ◽  
Yuliya Bespalko ◽  
Ludmilla Bobrova ◽  
Oleg Smorygo ◽  
...  
Keyword(s):  
Steam Reforming ◽  
Membrane Reactor ◽  
Hydrogen Permeation ◽  
Molar Ratio ◽  
Ethanol Steam Reforming ◽  
Catalytic Membrane ◽  
Catalytic Membrane Reactor ◽  
Monolithic Catalyst ◽  
Supported Membrane ◽  
Ethanol Steam

The present study deals with the combination of ethanol steam reforming over a monolithic catalyst and hydrogen separation by membrane in a lab-scale catalytic membrane reactor (CMR). The catalyst was comprised of honeycomb thin-walled Fechralloy substrate loaded with Ni + Ru/Pr0.35Ce0.35Zr0.35O2 active component. The asymmetric supported membrane consisted of a thin Ni-Cu alloy–Nd tungstate nanocomposite dense permselective layer deposited on a hierarchically structured asymmetric support. It has been shown that the monolithic catalyst-assisted CMR is capable of increasing the driving potential for hydrogen permeation through the same membrane as compared with that of the packed bed catalyst by increasing the retentate hydrogen concentration. Important operating parameters responsible for the low carbon deposition rate as well as the amount of hydrogen produced from 1 mol of ethanol, such as the temperature range of 700–900 °C, the water/ethanol molar ratio of 4 in the feed, have been determined. Regarding the choice of the reagent concentration (ethanol and steam in Ar), its magnitude may directly interfere with the effectiveness of the reaction-separation process in the CMR.

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