Catalytic and sorbent materials based on mayenite for sorption enhanced steam methane reforming with different packed-bed configurations

被引:29
|
作者
Di Giuliano, Andrea [1 ,2 ]
Giancaterino, Fabrizio [2 ]
Gallucci, Katia [2 ]
Foscolo, Pier Ugo [2 ]
Courson, Claire [1 ]
机构
[1] Univ Strasbourg, Inst Chim & Procedes Energie Environm & La Sante, 25 Rue Becquerel, F-67087 Strasbourg 2, France
[2] Univ Aquila, Dipartimento Ingn Ind & Dell Informaz & Econ, Nucleo Ind Pile, 18Via G Gronchi, I-67100 Laquila, Italy
关键词
Sorption enhanced steam methane reforming; CO2-capture; CaO-based sorbent; Ni-based catalyst; Packed-bed configurations; NI-CAO-MAYENITE; HYDROGEN-PRODUCTION; CO2; SORBENTS; TECHNOLOGY; STABILITY; CAPTURE; ETHANOL;
D O I
10.1016/j.ijhydene.2018.10.003
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
An experimental study was performed on sorption enhanced steam methane reforming (SESMR) by Ni-mayenite reforming catalyst and CaO-mayenite CO2-sorbents with several CaO contents. Materials were synthesized, characterized (by XRD, BET and BJH methods, TPR) and tested in a micro-reactor, comparing two configurations: two separated, consequential packed-beds and the more usual raw mixing. Ni-mayenite always allowed a high, stable CH4 conversion (>93%). A generalized direct effect from CO2 capture emerged on water gas shift reaction extent, while enhancement of methane conversion took place only in raw mixing. In practical applications, investigated materials are bound to face alternatively reforming and sorbent regeneration conditions: an automated bench-scale system was used to perform 205 SESMR/regeneration cycles, with separate beds of Ni-mayenite and CaO-mayenite (30 wt% free-CaO), proving good activity and stability throughout cycles (stable CH4 conversion > 95%, pre-breakthrough CO2 concentration < 3 vol% dry, dilution free). (C) 2018 Hydrogen Energy Publications LLC. Published by Elsevier Ltd. All rights reserved.
引用
收藏
页码:21279 / 21289
页数:11
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