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Ca-enhanced hematite oxygen carriers for chemical looping reforming of biomass pyrolyzed gas coupled with CO_2 splitting

机译:CA-增强的赤铁矿氧载体,用于化学环状重整生物质热解气体与CO_2分裂相结合

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摘要

Chemical looping reforming (CLR) of biomass pyrolyzed gases coupled with CO2 splitting was proposed to improve the H-2/CO ratio of gaseous product by using Ca-enhanced hematite oxygen carriers. The oxygen carriers mainly consist of Fe2O3, Ca2Fe2O5, CaO and SiO2. The impurity gas in biomass pyrolyzed gases is consumed in CLR stage, attributing to the dry reforming reaction over a catalytic effect of oxygen carriers. The highest CH4 conversion 98.26% and CO2 conversion 71.92% are realized in the CLR process with the crystal transformation of Fe2O3 and Ca2Fe2O5 to Fe and CaO. The improved reactivity of hematite oxygen carriers by CaO is mainly ascribed to the intermetallic synergistic effect in Ca2Fe2O5, which influences the lattice oxygen release and selectivity of gaseous products. The maximum H-2/CO ratio of gaseous product in CLR process is nearly 3 times as high as the initial H-2/CO ratio of biomass pyrolyzed gas. Moreover, up to 80.95% CO2 conversion efficiency and 2.32 mmol/min/g CO yield are achieved in CO2 splitting step with the generation of Fe3O4 and CaFe3O5 in oxygen carriers. The CO2 conversion shows positive correlation with reaction temperature but negative correlation with weight hourly space velocity. The metallic synergistic effect between Ca/Fe are conductive to improve CO2 conversion though shifting the reaction equilibrium and enhancing ion diffusion. Modest reactivity and stability of Ca-modified oxygen carriers are confirmed in 15 cycles reaction, which indicates that potentially application prospect in CLR of biomass pyrolyzed gases coupled with CO2 splitting process.
机译:提出了与CO2分裂偶联的生物质热解气体的化学环状重整(CLR),通过使用Ca-Enhoppated赤铁矿氧载体来改善气态产物的H-2 / Co比。氧载体主要由Fe 2 O 3,Ca2Fe 2 O 5,CaO和SiO 2组成。生物质热解气体中的杂质气体在CLR阶段消耗,归因于氧载体的催化效应上的干燥重整反应。最高CH4转化98.26%和CO 2转化71.92%在CLR过程中实现了Fe2O3和Ca2Fe2O5至Fe和CaO的晶体转化。 CaO的赤铁矿氧载体的改善反应性主要归因于CA2FE2O5中的金属间协同作用,这影响了格子氧释放和气态产物的选择性。 CLR过程中气态产物的最大H-2 /共比几乎与生物质热解气体的初始H-2 / Co比的高度高3倍。此外,CO 2分裂步骤在氧载体中产生Fe3O4和CaFe3O5的CO 2分裂步骤中实现了高达80.95%的CO 2转化效率和2.32mmol / min / g族产量。 CO2转化显示与反应温度的正相关,但与重量小时间速度的负相关性。 Ca / Fe之间的金属协同效应是导致改善CO 2转化,但虽然换反应平衡和增强离子扩散。在15个循环反应中确认了Ca-修饰的氧载体的适度反应性和稳定性,这表明潜在的应用前景在与CO 2分裂过程中加上的生物质热解气体的CLR。

著录项

  • 来源
    《Fuel》 |2021年第1期|119125.1-119125.10|共10页
  • 作者单位

    Taiyuan Univ Technol Training Base State Key Lab Coal Sci & Technol Jo Taiyuan 030024 Peoples R China|Chinese Acad Sci Guangzhou Inst Energy Convers Guangzhou 510640 Peoples R China|CAS Key Lab Renewable Energy Guangzhou 510640 Peoples R China|Guangdong Prov Key Lab New & Renewable Energy Res Guangzhou 510640 Peoples R China;

    Taiyuan Univ Technol Training Base State Key Lab Coal Sci & Technol Jo Taiyuan 030024 Peoples R China;

    Guangdong Commun Polytech Guangzhou 510800 Peoples R China;

    Taiyuan Univ Technol Training Base State Key Lab Coal Sci & Technol Jo Taiyuan 030024 Peoples R China;

    Taiyuan Univ Technol Training Base State Key Lab Coal Sci & Technol Jo Taiyuan 030024 Peoples R China;

    Chinese Acad Sci Guangzhou Inst Energy Convers Guangzhou 510640 Peoples R China;

    Chinese Acad Sci Guangzhou Inst Energy Convers Guangzhou 510640 Peoples R China;

    Chinese Acad Sci Guangzhou Inst Energy Convers Guangzhou 510640 Peoples R China;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    Biomass pyrolyzed gases; Chemical looping reforming; Ca-modified hematite oxygen carriers; Ca2Fe2O5; CO2 splitting;

    机译:生物质热解气体;化学环循环重整;Ca-改性赤铁矿氧载体;CA2FE2O5;CO2分裂;

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