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耦合TiO2直接苛化的黑液半焦与石油焦水蒸气共气化特性研究

王贵金 袁洪友 靳立军 李扬 杨赫 胡浩权

王贵金, 袁洪友, 靳立军, 李扬, 杨赫, 胡浩权. 耦合TiO2直接苛化的黑液半焦与石油焦水蒸气共气化特性研究[J]. 燃料化学学报(中英文), 2023, 51(3): 348-357. doi: 10.1016/S1872-5813(22)60046-X
引用本文: 王贵金, 袁洪友, 靳立军, 李扬, 杨赫, 胡浩权. 耦合TiO2直接苛化的黑液半焦与石油焦水蒸气共气化特性研究[J]. 燃料化学学报(中英文), 2023, 51(3): 348-357. doi: 10.1016/S1872-5813(22)60046-X
WANG Gui-jin, YUAN Hong-you, JIN Li-jun, LI Yang, YANG He, HU Hao-quan. Steam co-gasification characteristics of black liquor char and petroleum coke coupled with TiO2 direct causticization[J]. Journal of Fuel Chemistry and Technology, 2023, 51(3): 348-357. doi: 10.1016/S1872-5813(22)60046-X
Citation: WANG Gui-jin, YUAN Hong-you, JIN Li-jun, LI Yang, YANG He, HU Hao-quan. Steam co-gasification characteristics of black liquor char and petroleum coke coupled with TiO2 direct causticization[J]. Journal of Fuel Chemistry and Technology, 2023, 51(3): 348-357. doi: 10.1016/S1872-5813(22)60046-X

耦合TiO2直接苛化的黑液半焦与石油焦水蒸气共气化特性研究

doi: 10.1016/S1872-5813(22)60046-X
基金项目: 中央高校基本科研业务费(DUT21TD103),辽宁省“兴辽英才计划”(XLYC1908033)和大连市支持高层次人才创新创业项目计划(重点领域创新团队支持计划项目)(2019RT10)资助
详细信息
    通讯作者:

    Tel: 0411-84986157, E-mail: hhu@dlut.edu.cn

  • 中图分类号: TK6

Steam co-gasification characteristics of black liquor char and petroleum coke coupled with TiO2 direct causticization

Funds: The project was supported by the Fundamental Research Funds for the Central Universities (DUT21TD103), Liaoning Revitalization Talent Program (XLYC1908033) and Dalian Innovation Team Support Plan in Key Areas (2019RT10)
  • 摘要: 以黑液半焦(BLC)-苛化剂(TiO2)-石油焦(PC)三元混合物(BTP)为研究对象,借助热重分析仪和固定床反应器在850 ℃进行了恒温水蒸气气化实验,从反应速率、产气特性和残余固体特性等方面探究了耦合TiO2直接苛化的BLC和PC共气化过程。结果表明,源于mNa2nTiO2对有机碳气化反应的促进作用,与单独的TiO2直接苛化BLC气化和PC气化加权平均(BTPtheo)相比,耦合共气化过程表现出显著的协同效应。BTP最大反应速率达到7.0%/min,为BTPtheo的2.9倍;BTP产气中有效气组分(H2+CO)的含量及其产率分别为81.1%和2059 mL/g,气体热值为9343 kJ/m3,相对于BTPtheo分别提高6.8%、137.3%和5.5%;BTP的碳转化率和能源输出比分别为95.0%和1.13,相比BTPtheo,分别提高61.6%和135.4%。此外,BTP在气化过程中的无机盐损失得到有效控制,相对损失率约9.4%;BTP残余固体中的Na盐以高热稳定性的mNa2nTiO2为主,并保持颗粒状,有利于后续的碱回收。
  • FIG. 2160.  FIG. 2160.

    FIG. 2160.  FIG. 2160.

    图  1  水蒸气气化实验装置流程图

    Figure  1  Flow diagram of experimental apparatus for steam gasification

    图  2  TiO2直接苛化的BLC与PC的850 ℃恒温水蒸气共气化(a)及升温共热解(b)的TG-DTG曲线

    Figure  2  Experimental and calculative TG-DTG curves of isothermal steam co-gasification at 850 ℃ (a) and non-isothermal co-pyrolysis (b) of BTP

    图  3  850 ℃热处理前后BTP的XRD谱图

    Figure  3  XRD patterns of BTP before and after heat-treatment at 850 ℃

    图  4  850 ℃热处理前(a)后(b)的BTP的SEM照片

    Figure  4  SEM images of BTP before (a) and after (b) heat-treatment at 850 ℃

    图  5  不同添加物对BLC热化学转化过程无机盐损失的影响

    Figure  5  Effect of various additives on inorganic salts loss during the thermochemical conversion process of BLC

    图  6  BLC在850 ℃热处理前后的XRD谱图

    Figure  6  XRD patterns of BLC before and after heat-treatment at 850 ℃

    图  7  BLC在850 ℃热处理前(a)后(b)的SEM照片

    Figure  7  SEM images of BLC before (a) and after (b) heat-treatment at 850 ℃

    图  8  不同固体反应物水蒸气气化的产气特性

    Figure  8  Characteristics of gaseous products from steam gasification of different solid reactants (a): yield of each gas component; (b): H2/CO and CO/CO2; (c): content and yield of the effective gas components (H2+CO); (d): lower heating value of gas (LHVgas)

    图  9  不同固体反应物水蒸气气化的碳转化率(xC)和能源输出比(EOR)

    Figure  9  Carbon conversion (xC) and energy output ratio (EOR) for the steam gasification of different solid reactants

    图  10  850 ℃水蒸气气化残余固体的SEM照片

    Figure  10  SEM images of the steam gasification residues at 850 ℃

    (a): GRBLC; (b): GRBT; (c): GRBTP(images inside the circles are magnified by 50 times for those outside the circles)

    图  11  850 ℃水蒸气气化残余固体的XRD谱图

    Figure  11  XRD patterns of the steam gasification residues at 850 ℃

    表  1  黑液半焦与石油焦的基本分析

    Table  1  Fundamental analyses of the black liquor char (BLC) and petroleum coke (PC)

    SampleUltimate analysis wdaf/%H/CO/CProximate analysis wd/%QLHV/(MJ·kg−1, d)
    CHNSO*AVFC*
    BLC74.222.650.911.9420.280.430.2064.911.024.17.13
    PC91.043.082.230.702.950.410.020.49.090.635.01
    * by difference; d: dry basis; daf: dry ash-free basis; A: ash; V: volatile matter; FC: fixed carbon; LHV: lower heating value
    下载: 导出CSV
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  • 收稿日期:  2022-05-22
  • 修回日期:  2022-06-23
  • 录用日期:  2022-06-23
  • 网络出版日期:  2022-10-25
  • 刊出日期:  2023-03-15

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