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[求助] 求助两篇文章的检索证明信息 已有1人参与

求助下面两篇文章的检索证明,截个图就行,先谢谢了
(1)A novel integrated process for hydrogen production from biomass

(2)Hydrogen Production from Bio-Char via Steam Gasification in a Fluidized-Bed Reactor
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Accession number:       
20133516667484
        Title:        Hydrogen Production from Bio-Char via Steam Gasification in a Fluidized-Bed Reactor
        Authors:        Ma, Z.1; Zhang, S.1, 2 Email author zsp@ecust.edu.cn; Xie, D.1; Yan, Y.1, 2; Ren, Z.1
        Author affiliation:        1 East China University of Science and Technology, Research Center for Biomass Energy, Shanghai, China
                2 East China University of Science and Technology, Key Laboratory of Coal Gasification and Energy Chemical Engineering, Ministry of Education, Shanghai, China
        Corresponding author:        Zhang, S. (zsp@ecust.edu.cn)
        Source title:        Chemical Engineering and Technology
        Abbreviated source title:        Chem. Eng. Technol.
        Volume:        36
        Issue:        9
        Issue date:        September, 2013
        Publication year:        2013
        Pages:        1599-1602
        Language:        English
        ISSN:        09307516
        E-ISSN:        15214125
        CODEN:        CETEER
        Document type:        Journal article (JA)
        Publisher:        Wiley-VCH Verlag, P.O. Box 101161, Weinheim, D-69451, Germany
        Abstract:        Bio-char was used as feedstock to investigate hydrogen production via steam gasification in a fluidized-bed reactor. The effects of reaction conditions such as reaction temperature and steam-to-char ratio on hydrogen yield, potential hydrogen yield, and carbon conversion were studied. Finally, 83.3mol hydrogen was generated per kilogram of bio-char through steam gasification of bio-char in a fluidized-bed reactor. © 2013 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim.
        Number of references:        17
        Main heading:        Hydrogen production
        Controlled terms:        Chemical reactors  -  Gasification  -  Steam  -  Supersaturation
        Uncontrolled terms:        Bio chars  -  Carbon conversions  -  Fluidized bed reactors  -  Hydrogen yields  -  Potential hydrogens  -  Reaction conditions  -  Reaction temperature  -  Steam gasification
        Classification code:        522 Gas Fuels -  614 Steam Power Plants -  801.4 Physical Chemistry -  802.1 Chemical Plants and Equipment -  802.3 Chemical Operations
        DOI:        10.1002/ceat.201300057
        Database:        Compendex
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2楼2015-09-29 16:42:21
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Accession number:       
20135217143544
        Title:        A novel integrated process for hydrogen production from biomass
        Authors:        Ma, Zhong1; Zhang, Su-Ping1 Email author zsp@ecust.edu.cn; Xie, Deng-Yin1; Yan, Yong-Jie1
        Author affiliation:        1 Research Center for Biomass Energy, Ministry of Education, East China University of Science and Technology, 130 Meilong Road, Shanghai 200237, China
        Corresponding author:        Zhang, S.-P. (zsp@ecust.edu.cn)
        Source title:        International Journal of Hydrogen Energy
        Abbreviated source title:        Int J Hydrogen Energy
        Volume:        39
        Issue:        3
        Issue date:        Janaury 16, 2014
        Publication year:        2014
        Pages:        1274-1279
        Language:        English
        ISSN:        03603199
        CODEN:        IJHEDX
        Document type:        Journal article (JA)
        Publisher:        Elsevier Ltd, Langford Lane, Kidlington, Oxford, OX5 1GB, United Kingdom
        Abstract:        A novel process, which integrated with biomass pyrolysis, gas-solid simultaneous gasification and catalytic reforming processes, was utilized to produce hydrogen. The effects of gasification temperature and reforming temperature on hydrogen yield and carbon conversion efficiency were investigated. The results showed that both higher gasification temperature and reforming temperature led to higher hydrogen yield and carbon conversion efficiency. Compared with the two-stage pyrolysis-catalytic reforming process, hydrogen yield and carbon conversion efficiency were greatly increased from 43.58 to 75.96 g H2/kg biomass and 66.18%-82.20% in the integrated process. Copyright © 2013, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
        Number of references:        30
        Main heading:        Hydrogen production
        Controlled terms:        Biomass  -  Carbon  -  Catalytic reforming  -  Conversion efficiency  -  Gasification  -  Pyrolysis
        Uncontrolled terms:        Biomass pyrolysis  -  Carbon conversions  -  Gas-solid  -  Gasification temperatures  -  Hydrogen yields  -  Reforming process  -  Reforming temperatures
        Classification code:        522 Gas Fuels -  525.1 Energy Resources and Renewable Energy Issues -  525.5 Energy Conversion Issues -  802.2 Chemical Reactions -  802.3 Chemical Operations -  804 Chemical Products Generally
        DOI:        10.1016/j.ijhydene.2013.10.146
        Database:        Compendex
QQ:250321723
3楼2015-09-29 16:42:35
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