Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range

Chemical-looping hydrogen generation can produce hydrogen from fossils fuels with inherent separation of CO2. In this article, a novel compact fluidized bed is used for CLHG to solve the problem of low fuel gas conversion causing by thermodynamic limit. Based on the compact fluidized bed, a modellin...

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Main Authors: Xue Zhipeng, Xu Junfeng, Zhao Minmin
Format: Article
Language:English
Published: EDP Sciences 2019-01-01
Series:E3S Web of Conferences
Online Access:https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/44/e3sconf_icaeer18_02035.pdf
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spelling doaj-49dc521836b24f0daf0087ecb72347102021-03-02T11:00:58ZengEDP SciencesE3S Web of Conferences2267-12422019-01-011180203510.1051/e3sconf/201911802035e3sconf_icaeer18_02035Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating rangeXue Zhipeng0Xu Junfeng1Zhao Minmin2PH.D, Huadian Electric Power Research InstituteENGINEER, Huadian Electric Power Research InstituteENGINEER, Huadian Electric Power Research InstituteChemical-looping hydrogen generation can produce hydrogen from fossils fuels with inherent separation of CO2. In this article, a novel compact fluidized bed is used for CLHG to solve the problem of low fuel gas conversion causing by thermodynamic limit. Based on the compact fluidized bed, a modelling of three-reactor system for CLHG process is built to study the operating range of this system. The results show that the low limit of the system temperature is 650°C, or else unexpected reaction will occur in reactors. The system can achieve heat-integrated by mixing a certain amount of inert support into oxygen carrier and adjusting a suitable temperature different among reactors. Moreover, an operational range of the oxygen carrier recycle rate between 6 and 8 mol Fe/mol CH4 is recommended for more extensive operating region and relative higher CH4/H2 ratio can be obtain. Finally, a fitting formula described the operating range of this system is proposed to provide a reference for the experiment and simulation in further work.https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/44/e3sconf_icaeer18_02035.pdf
collection DOAJ
language English
format Article
sources DOAJ
author Xue Zhipeng
Xu Junfeng
Zhao Minmin
spellingShingle Xue Zhipeng
Xu Junfeng
Zhao Minmin
Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
E3S Web of Conferences
author_facet Xue Zhipeng
Xu Junfeng
Zhao Minmin
author_sort Xue Zhipeng
title Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
title_short Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
title_full Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
title_fullStr Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
title_full_unstemmed Modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
title_sort modelling of three-reactor system for chemical looping hydrogen generation: identifying a suitable operating range
publisher EDP Sciences
series E3S Web of Conferences
issn 2267-1242
publishDate 2019-01-01
description Chemical-looping hydrogen generation can produce hydrogen from fossils fuels with inherent separation of CO2. In this article, a novel compact fluidized bed is used for CLHG to solve the problem of low fuel gas conversion causing by thermodynamic limit. Based on the compact fluidized bed, a modelling of three-reactor system for CLHG process is built to study the operating range of this system. The results show that the low limit of the system temperature is 650°C, or else unexpected reaction will occur in reactors. The system can achieve heat-integrated by mixing a certain amount of inert support into oxygen carrier and adjusting a suitable temperature different among reactors. Moreover, an operational range of the oxygen carrier recycle rate between 6 and 8 mol Fe/mol CH4 is recommended for more extensive operating region and relative higher CH4/H2 ratio can be obtain. Finally, a fitting formula described the operating range of this system is proposed to provide a reference for the experiment and simulation in further work.
url https://www.e3s-conferences.org/articles/e3sconf/pdf/2019/44/e3sconf_icaeer18_02035.pdf
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AT xujunfeng modellingofthreereactorsystemforchemicalloopinghydrogengenerationidentifyingasuitableoperatingrange
AT zhaominmin modellingofthreereactorsystemforchemicalloopinghydrogengenerationidentifyingasuitableoperatingrange
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