Design and performance of asymmetric supported membranes for oxygen and hydrogen separation

被引：14
|
作者：
Sadykov, Vladislav A. [1 ,2 ]
Eremeev, Nikita F. [1 ]
Fedorova, Yulia E. [1 ]
Krasnov, Alexey V. [1 ,2 ]
Bobrova, Ludmilla N. [1 ]
Bespalko, Yulia N. [1 ,2 ]
Lukashevich, Anton I. [1 ]
Skriabin, Pavel I. [1 ]
Smorygo, Oleg L. [3 ]
Veen, Andre C. Van [4 ]
机构：
[1] Boreskov Inst Catalysis, Fed Res Ctr, Pr Akad Lavrentieva 5, Novosibirsk, Russia
[2] Novosibirsk State Univ, Pirogova Str 2, Novosibirsk 630090, Russia
[3] Powder Met Inst, Platonova Str 41, Minsk 220005, BELARUS
[4] Univ Warwick, Sch Engn, Coventry CV4 7AL, W Midlands, England
来源：
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY | 2021年 / 46卷 / 38期
关键词：
Asymmetric supported membranes; Oxygen and hydrogen separation; Nanocomposites; Methane and ethanol reforming; Process parameters; PROTON CONDUCTING MEMBRANES; HIGH-PURITY HYDROGEN; OXIDE FUEL-CELLS; PARTIAL OXIDATION; NANOCOMPOSITE MATERIALS; TRANSPORT-PROPERTIES; NICKELATE-COBALTITE; LANTHANUM TUNGSTATE; PERMEABLE MEMBRANE; CATALYTIC MEMBRANE;
D O I：
10.1016/j.ijhydene.2020.01.106
中图分类号：
O64 [物理化学（理论化学）、化学物理学];
学科分类号：
070304 ; 081704 ;
摘要：
Producing syngas and hydrogen from biofuels is a promising technology in the modern energy. In this work results of authors' research aimed at design of supported membranes for oxygen and hydrogen separation are reviewed. Nanocomposites were deposited as thin layers on Ni-Al foam substrates. Oxygen separation membranes were tested in CH4 selective oxidation/oxi-dry reforming. The hydrogen separation membranes were tested in C2H5OH steam reforming. High oxygen/hydrogen fluxes were demonstrated. For oxygen separation membranes syngas yield and methane conversion increase with
引用
收藏
页码：20222 / 20239
页数：18
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