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准东煤水热提质过程中煤质特性变化对CO2气化影响

张小培 张成 余圣辉 李鑫 冯小飞 马亚飞 陈刚

张小培, 张成, 余圣辉, 李鑫, 冯小飞, 马亚飞, 陈刚. 准东煤水热提质过程中煤质特性变化对CO2气化影响[J]. 燃料化学学报(中英文), 2017, 45(10): 1185-1190.
引用本文: 张小培, 张成, 余圣辉, 李鑫, 冯小飞, 马亚飞, 陈刚. 准东煤水热提质过程中煤质特性变化对CO2气化影响[J]. 燃料化学学报(中英文), 2017, 45(10): 1185-1190.
ZHANG Xiao-pei, ZHANG Cheng, YU Sheng-hui, LI Xin, FENG Xiao-fei, MA Ya-fei, CHEN Gang. Changes of Zhundong coal properties by hydrothermal upgrading and its impacts on CO2 gasification[J]. Journal of Fuel Chemistry and Technology, 2017, 45(10): 1185-1190.
Citation: ZHANG Xiao-pei, ZHANG Cheng, YU Sheng-hui, LI Xin, FENG Xiao-fei, MA Ya-fei, CHEN Gang. Changes of Zhundong coal properties by hydrothermal upgrading and its impacts on CO2 gasification[J]. Journal of Fuel Chemistry and Technology, 2017, 45(10): 1185-1190.

准东煤水热提质过程中煤质特性变化对CO2气化影响

基金项目: 

国家自然科学基金 51676076

国家国际科技合作专项 2015DFA60410

华中科技大学自主创新研究基金 5003120003

详细信息
    通讯作者:

    张成, Tel:027-87542417-8321;Fax:027-87545526;E-mail:chengzhang@mail.hust.edu.cn

  • 中图分类号: TQ536.1

Changes of Zhundong coal properties by hydrothermal upgrading and its impacts on CO2 gasification

Funds: 

National Natural Science Foundation of China 51676076

National Program of International Science and Technology Cooperation 2015DFA60410

Graduates' Innovation Fund of HUST 5003120003

  • 摘要: 选取准东高钠煤为研究对象,在高压反应釜中进行了不同温度(150-350℃)下的水热提质处理实验,依托电感耦合等离子体质谱(ICP-MS)、氮气等温吸附模型(BET)和X射线衍射(XRD)等技术,分析了煤样的煤质特性变化以及对CO2气化的综合影响规律。结果表明,水热提质处理后煤样成熟度增加,煤阶上升,钠的脱除效果显著,在300-350℃时脱除率均大于95%。煤焦化学结构致密、有序、稳定;煤样CO2气化曲线向高温区偏移,气化活性指数呈下降趋势且300-350℃时下降明显。水热提质过程中煤样气化反应活性受到煤阶、碱金属钠含量、物理孔隙结构、化学微晶结构等多个因素的综合影响。
  • 图  1  水热改性提质实验装置示意图

    Figure  1  Schematic diagram of hydrothermal upgrading experimental apparatus

    图  2  不同水热温度下钠的脱除率

    Figure  2  Removal of sodium under different hydrothermal temperatures

    图  3  原煤及提质煤焦的孔隙结构

    Figure  3  Pore structure parameters of the raw and upgraded chars

    图  4  原煤及提质煤焦的XRD谱图

    Figure  4  XRD spectra of the raw and upgraded chars

    图  5  原煤焦XRD的分峰谱图

    Figure  5  Gauss fitting-curves of WCW-raw char

    图  6  煤焦气化反应曲线

    Figure  6  Gasification curves during 600-950℃

    图  7  煤焦CO2气化活性指数(R0.5)

    Figure  7  CO2 gasification reactivity index (R0.5) of coal chars

    图  8  CO2气化活性影响机制分析示意图

    Figure  8  Analysis on the mechanism of CO2 gasification reactivity

    表  1  煤样的工业分析、元素分析

    Table  1  Proximate and ultimate analysis of samples

    Sample Proximate analysis w/% Ultimate analysis wdaf/% Qnet, d
    / (MJ·kg-1)
    Atomic ratio (daf)
    Mad Ad Vd FCd C H O* N S H/C O/C
    Raw 10.95 5.61 31.90 62.49 73.95 3.97 20.90 0.54 0.64 25.52 0.644 0.212
    H150 9.02 5.15 31.86 62.99 74.42 3.92 20.77 0.56 0.40 25.59 0.632 0.209
    H200 5.56 5.43 31.15 63.42 74.52 3.90 20.62 0.58 0.38 25.60 0.628 0.208
    H250 4.82 5.03 29.86 65.11 74.92 3.80 20.38 0.58 0.32 25.76 0.608 0.204
    H300 4.24 5.22 28.48 66.31 76.31 3.79 19.02 0.60 0.29 26.28 0.595 0.187
    H350 2.41 5.38 25.36 69.26 78.47 3.73 16.98 0.59 0.23 27.08 0.570 0.162
    *:by difference
    下载: 导出CSV

    表  2  焦样的XRD参数

    Table  2  XRD parameters of coal chars

    Sample 2 θ002/(°) 2 θ100/(°) d002/nm Lc/nm La/nm
    Raw 24.93 43.89 0.357 1.556 1.897
    H150 25.04 43.79 0.355 1.557 2.299
    H200 25.17 43.95 0.354 1.705 2.376
    H250 25.26 43.84 0.352 1.850 2.382
    H300 25.34 44.06 0.351 1.905 2.389
    H350 25.58 43.44 0.348 2.243 2.411
    下载: 导出CSV
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出版历程
  • 收稿日期:  2017-06-09
  • 修回日期:  2017-07-25
  • 网络出版日期:  2021-01-23
  • 刊出日期:  2017-10-10

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