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不同醇类对磷钨酸催化超临界醇解液化木屑的影响

曾常伟 吕建华 郑怀玉 陈学榕 黄彪

曾常伟, 吕建华, 郑怀玉, 陈学榕, 黄彪. 不同醇类对磷钨酸催化超临界醇解液化木屑的影响[J]. 燃料化学学报(中英文), 2016, 44(3): 342-348.
引用本文: 曾常伟, 吕建华, 郑怀玉, 陈学榕, 黄彪. 不同醇类对磷钨酸催化超临界醇解液化木屑的影响[J]. 燃料化学学报(中英文), 2016, 44(3): 342-348.
ZENG Chang-wei, LÜ Jian-hua, ZHENG Huai-yu, CHEN Xue-rong, HUANG Biao. Effect of solvent on the solvolysis liquefaction of sawdust with phosphotungstic acid under supercritical condition[J]. Journal of Fuel Chemistry and Technology, 2016, 44(3): 342-348.
Citation: ZENG Chang-wei, LÜ Jian-hua, ZHENG Huai-yu, CHEN Xue-rong, HUANG Biao. Effect of solvent on the solvolysis liquefaction of sawdust with phosphotungstic acid under supercritical condition[J]. Journal of Fuel Chemistry and Technology, 2016, 44(3): 342-348.

不同醇类对磷钨酸催化超临界醇解液化木屑的影响

基金项目: 

教育部高等学校博士学科点专项科研基金 20123515110015

福建省科技重大专项 2014NZ003

详细信息
    通讯作者:

    黄彪, E-mail: fjhuangbiao@hotmail.com

  • 中图分类号: TQ037

Effect of solvent on the solvolysis liquefaction of sawdust with phosphotungstic acid under supercritical condition

Funds: 

Specialized Research Fund for the Doctoral Program of Higher Education of China 20123515110015

and Fujian Provincial Science and Technology Major Project 2014NZ003

  • 摘要: 以可溶解于醇类的磷钨酸为催化剂, 在超临界醇体系下液化木屑, 探讨甲醇、乙醇、正丙醇、异丙醇等不同醇类溶剂对木屑醇解液化的影响, 同时采用FT-IR和GC-MS等对液化产物进行了表征分析.结果表明, 反应压力和溶剂的极性大小对木屑的液化效率以及液化产物影响显著.甲醇、乙醇、正丙醇、异丙醇反应体系的液化率和主要液化产物酯类化合物的含量比率, 分别为54.75%和43.759%、90.29%和23.531%、85.90%和41.761%、89.15%和28.619%, 特别在甲醇体系中, 乙酰丙酸甲酯的含量高达33.374%;在异丙醇体系中酚类化合物可达到24.342%;醛类化合物只出现在甲醇体系中.在正丙醇体系中没有酚类产物, 表明极性最小的正丙醇, 提供很少的H*, 更不容易将木质素降解.
  • 图  1  高压液化实验设备示意图及液化产物分离流程示意图

    Figure  1  Sketch of liquefaction and separation experiment

    图  2  不同溶剂在同一条件下的液化率

    Figure  2  Yield contrast chart of liquefaction with different solvents under the same condition

    图  3  不同溶剂在同一条件下液化产物轻油和重油质量

    Figure  3  Mass comparison of light bio-oil and heavy bio-oil obtained by liquefaction with different solvents

    : bio-oil; : light oil; : heavy oil

    图  4  杉木屑(a)、甲醇的液化残渣(b)、乙醇的液化残渣(c)、正丙醇的液化残渣(d) 和异丙醇的液化残渣(e) 以及甲醇的产物重油(f)、乙醇的产物重油(g)、正丙醇的产物重油(h) 和异丙醇的产物重油(i) 的红外光谱谱图

    Figure  4  Figure 4 FT-IR spectra of fir sawdust (a), the residue obtained from liquefaction with methanol (b), ethanol (c), n-propanol (d) and iso-isopropanol (e) the heavy oil obtained from liquefaction with methanol (f), ethanol (g), n-propanol (h) and isopropanol (i)

    图  5  碳水化合物转化为乙酰丙酸酯的反应路线

    Figure  5  Reaction pathway of carbohydrate to levulinate ester

    表  1  不同溶剂的实际反应温度、压力和液化率

    Table  1  Comparison of liquefaction yield with different solvents

    SolventMethanolEthanoln-propanolIsopropanol
    t /℃258-260260-268258-262258-262
    p / MPa11.2-11.911.2-11.95.8-8.617.0-17.6
    ηa/%54.7590.2985.9089.15
    a: liquefaction yield determined by the average value of repeated experiments
    下载: 导出CSV

    表  2  不同溶剂条件下液化产物的组分种类及其GC总含量

    Table  2  Major compositions and total relative content in the liquefaction products obtained by different solvents

    Reaction
    solvents
    GC content w/%
    alcoholsaldehydesketonesacidsphenolsethersestersothers
    Methanol1.0412.6051.5390.96115.7800.57143.75925.93
    Ethanol0023.398019.873023.53113.708
    n-propanol13.177014.1056.44504.03141.76111.340
    Isopropanol10.09308.333024.342028.61913.817
    下载: 导出CSV
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出版历程
  • 收稿日期:  2015-08-28
  • 修回日期:  2015-11-18
  • 网络出版日期:  2021-01-23
  • 刊出日期:  2016-03-30

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