Effect of La2O3 and CeO2 loadings on formation of nickel-phyllosilicate precursor during preparation of Ni/SBA-15 for hydrogen-rich gas production from ethanol steam reforming

2019 ◽  
Vol 44 (56) ◽  
pp. 29537-29546 ◽  
Author(s):  
Surendar Moogi ◽  
In-Gu Lee ◽  
Ji-Yeon Park
Keyword(s):  
Steam Reforming ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Ethanol Steam

A novel BEA-type zeolite core–shell multiple catalyst for hydrogen-rich gas production from ethanol steam reforming

2016 ◽  
Vol 6 (14) ◽  
pp. 5427-5439 ◽  
Author(s):  
Ziliang Zheng ◽  
Donghua Yang ◽  
Tingting Li ◽  
Xuemei Yin ◽  
Shiyao Wang ◽  
...  
Keyword(s):  
Steam Reforming ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Core Shell ◽  
Type Zeolite ◽  
Ethanol Steam

BEA-type core–shell catalysts consisting of a core supporting Cu and Fe and a Ni-based shell were investigated for their ethanol steam reforming (ESR) activity.

scholarly journals Preparation of 27Ni6Zr4O143M(M=Mg, Ca, Sr, or Ba)O/70 Zeolite Y Catalysts and Hydrogen-rich Gas Production by Ethanol Steam Reforming

2013 ◽  
Vol 34 (7) ◽  
pp. 2073-2080
Author(s):  
Dongjin Kim ◽  
Jun Su Lee ◽  
Gayoung Lee ◽  
Byung-Hyun Choi ◽  
Mi-Jung Ji ◽  
...  
Keyword(s):  
Steam Reforming ◽  
Zeolite Y ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Ethanol Steam

Synthesis gas production from bio-oil: steam reforming of ethanol as a model compound

RSC Advances ◽  
2014 ◽  
Vol 4 (72) ◽  
pp. 37964-37972 ◽  
Author(s):  
S. Pavlova ◽  
P. Yaseneva ◽  
V. Sadykov ◽  
V. Rogov ◽  
S. Tikhov ◽  
...  
Keyword(s):  
Synthesis Gas ◽  
Steam Reforming ◽  
Model Compound ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Syngas Production ◽  
Monolithic Catalysts ◽  
Steam Reforming Of Ethanol ◽  
Bio Oil ◽  
Ethanol Steam

Syngas production via ethanol steam reforming has been studied over solid Ru/Ce0.5Zr0.5O2 and alumina supported Ru/Ce0.4Zr0.4Sm0.2O2 as granulated and monolithic catalysts.

Synergy effect of MgO and ZnO in a Ni/Mg–Zn–Al catalyst during ethanol steam reforming for H2-rich gas production

2011 ◽  
Vol 178 (1) ◽  
pp. 206-213 ◽  
Author(s):  
Guangming Zeng ◽  
Qinghua Liu ◽  
Ruixue Gu ◽  
Lihong Zhang ◽  
Yongdan Li
Keyword(s):  
Steam Reforming ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Synergy Effect ◽  
Ethanol Steam

Hydrogen-rich gas production from ethanol steam reforming over Ni/Ga/Mg/Zeolite Y catalysts at mild temperature

2011 ◽  
Vol 88 (12) ◽  
pp. 4366-4375 ◽  
Author(s):  
Byeong Sub Kwak ◽  
Jun Su Lee ◽  
Jun Sung Lee ◽  
Byung-Hyun Choi ◽  
Mi Jung Ji ◽  
...  
Keyword(s):  
Steam Reforming ◽  
Zeolite Y ◽  
Gas Production ◽  
Ethanol Steam Reforming ◽  
Mild Temperature ◽  
Ethanol Steam

scholarly journals Effect of Asymmetric Membrane Structure on Hydrogen Transport Resistance and Performance of a Catalytic Membrane Reactor for Ethanol Steam Reforming

Membranes ◽  
2021 ◽  
Vol 11 (5) ◽  
pp. 332
Author(s):  
Ludmilla Bobrova ◽  
Nikita Eremeev ◽  
Nadezhda Vernikovskaya ◽  
Vladislav Sadykov ◽  
Oleg Smorygo
Keyword(s):  
Steam Reforming ◽  
Transport Model ◽  
Hydrogen Permeation ◽  
Ethanol Steam Reforming ◽  
Clear Understanding ◽  
Catalytic Membrane ◽  
Structure Property ◽  
Asymmetric Membrane ◽  
Supported Membrane ◽  
Ethanol Steam

The performance of catalytic membrane reactors (CMRs) depends on the specific details of interactions at different levels between catalytic and separation parts. A clear understanding of decisive factors affecting their operational parameters can be provided via mathematical simulations. In the present paper, main results of numerical studies of ethanol steam reforming, followed by downstream hydrogen permeation through an asymmetric supported membrane, are reported. The membrane module consists of a thin selective layer supported on a substrate with graded porous structure. One-dimensional isothermal reaction–transport model for the CMR has been developed, and its validation has been carried out by using performance data from a lab-scale reactor with a disk-shaped membrane. Simulations demonstrate the model’s capabilities to analyze local concentrations gradients, as required to provide accurate estimates of the relationship between structure–property–performance. It was shown that transport properties of multilayer asymmetric membranes are highly related to the structural properties of each single layer.

scholarly journals Effects of LHSV and Reaction Temperature upon Ethanol-Steam-Reforming Performance

2012 ◽  
Vol 78 (787) ◽  
pp. 415-419 ◽  
Author(s):  
Toshio SHINOKI ◽  
Tsuyoshi MAEDA ◽  
Jiro FUNAKI ◽  
Katsuya HIRATA
Keyword(s):  
Reaction Temperature ◽  
Steam Reforming ◽  
Ethanol Steam Reforming ◽  
Ethanol Steam
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