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沉淀法回收生物油高温馏分中的酚类物质

赵欣 李凯 李明 马善为 朱锡锋

赵欣, 李凯, 李明, 马善为, 朱锡锋. 沉淀法回收生物油高温馏分中的酚类物质[J]. 机械工程学报, 2016, 44(2): 201-208.
引用本文: 赵欣, 李凯, 李明, 马善为, 朱锡锋. 沉淀法回收生物油高温馏分中的酚类物质[J]. 机械工程学报, 2016, 44(2): 201-208.
ZHAO Xin, LI Kai, LI Ming, MA Shan-wei, ZHU Xi-feng. Separating phenols from high-temperature fraction of bio-oil by precipitation[J]. JOURNAL OF MECHANICAL ENGINEERING, 2016, 44(2): 201-208.
Citation: ZHAO Xin, LI Kai, LI Ming, MA Shan-wei, ZHU Xi-feng. Separating phenols from high-temperature fraction of bio-oil by precipitation[J]. JOURNAL OF MECHANICAL ENGINEERING, 2016, 44(2): 201-208.

沉淀法回收生物油高温馏分中的酚类物质

基金项目: 

国家重点基础研究发展规划 973计划, 2013CB228103

中国科学院重点部署项目 KGZD-EW-304-3

详细信息
  • 中图分类号: TK6

Separating phenols from high-temperature fraction of bio-oil by precipitation

More Information
  • 摘要: 为了研究金属离子沉淀法对生物油高温馏分中酚类物质的回收, 提高生物油中化学物质的利用率, 利用气相色谱-质谱联用仪 (GC-MS) 从NaOH试剂浓度、反应温度和反应时间三个方面研究了镁离子对生物油中酚类物质的回收效果。结果表明, 镁离子与酚类物质形成了不溶物, 而且不同浓度的氢氧化钠溶液 (1.0-4.0 mol/L)、不同的反应温度 (25-85℃) 以及不同的反应时间 (5-35 min) 对实验结果有着不同程度的影响。结果表明, 在反应温度为25℃、氢氧化钠浓度为2.5 mol/L, 反应时间在20 min时为最佳反应条件。在此条件下, 对生物油高温馏分中对乙基苯酚的回收率可达34.97%。

     

  • 图  沉淀法回收生物油中酚类物质的工艺路线示意图

    Figure  1.  Extraction procedure of phenolic compounds from bio-oil

    图  不溶物的红外光谱谱图

    Figure  2.  FT-IR spectrum of the complex

    图  乙酸乙酯层的总离子色谱图

    Figure  3.  Total ion chromatogram of ethyl acetate layer

    图  在不同NaOH浓度下对乙基苯酚的萃取率和pH值

    Figure  4.  4-ethylphenol extraction rate and pH value at various concentrations of sodium hydroxide solution

    图  在不同温度下对乙基苯酚的萃取率和pH值

    Figure  5.  4-ethylphenol extraction rate and pH value at various temperatures

    图  在不同时间下对乙基苯酚的萃取率和pH值

    Figure  6.  4-ethylphenol extraction rate and pH value at various reaction times

    表  1  生物油高温馏分中酚类物质的化学成分

    Table  1.   Chemical compositions of phenolic compounds from high temperature fractions of bio-oil

    No.Chemical compoundMolecular formulaMolecular weight /(g·mol-1)StructurePeak area /%
    1phenolC6H6O944.47
    2phenol, 2-methyl-C7H8O1085.67
    3phenol, 3-methyl-C7H8O1086.56
    4phenol, 2-methoxy-C7H8O21243.35
    52, 5-xylenolC8H10O1221.88
    6phenol, 4-ethyl-C8H10O12221.5
    7phenol, 2-methoxy-4-methyl-C8H10O21382.86
    81, 2-benzenediolC6H6O21103.41
    9phenol, 3-(1-methylethyl)-C9H10O1343.05
    10phenol, 3-methyl-4-ethyl-C9H10O1341.58
    11phenol, 4-isopropyl-C9H12O1363.89
    12guaiacol, 4-ethyl-C9H10O21503.75
    131, 2-benzenediol, 4-methyl-C7H8O21242.1
    14phenol, 4-sec-butyl-C10H14O1502.37
    15phenol, 2, 6-dimethoxy-C8H10O31543.15
    16guaiacol, 5-allyl-C10H12O21642.51
    17phenol, 2-methoxy-4-propyl-C10H14O21662.94
    18catechol, 4-ethyl-C8H10O21382.2
    19guaiacol, 4-propenyl-C10H12O21642.04
    下载: 导出CSV

    表  2  乙酸乙酯层中的酚类化合物

    Table  2.   Phenolic compounds identified in the ethyl acetate layer

    No.Chemical compoundMolecular formulaMolecular weight /(g·mol-1)StructurePeak area /%
    1phenolC6H6O945.48
    2phenol, 3-methyl-C7H8O1086.47
    3guaiacolC7H8O21244.03
    4phenol, 4-ethyl-C8H10O12221.75
    5guaiacol, 4-methylC8H10O21383.74
    6catecholC6H6O21103.19
    7phenol, 3-(1-methylethyl)-C9H10O1343.95
    8phenol, 2-ethyl-5-methyl-C9H12O1362.09
    9phenol, 4-propyl-C9H12O1364.01
    10guaiacol, 4-ethyl-C9H10O21505.6
    11catechol, 4-methyl-C8H10O21381.77
    12phenol, 4-sec-butyl-C10H14O1501.48
    13phenol, 2, 6-dimethoxy-C8H10O31542.78
    14guaiacol, 5-allyl-C10H12O21561.85
    15phenol, 2-methoxy-4-propyl-C10H14O21663.96
    16catechol, 4-ethyl-C8H10O21381.56
    17guaiacol, 4-propenyl-C9H12O1362.1
    下载: 导出CSV
  • [1] 朱锡锋.生物油制备技术[M].北京:化学工业出版社, 2013.

    ZHU Xi-feng.Preparation and application of bio-oil[M].Beijing:Chemical Industry Presss, 2013.
    [2] OASMAA A, CZERNIK S.Fuel oil quality of biomass pyrolysis oils-state of the art for the end user[J].Energy Fuels, 1999, 13:914-921. doi: 10.1021/ef980272b
    [3] BRIDGWATER A V, PEACOCKE G V C.Fast pyrolysis processes for biomass[J].Renew Sust Energy Rev, 2000, 4:1-73. doi: 10.1016/S1364-0321(99)00007-6
    [4] AMEN-CHEN C, PAKDEL H, ROY C.Separation of phenols from Eucalyptus wood tar[J].Biomass Bioenergy, 1997, 13(1/2):25-37.
    [5] MAHFUD F H, VAN GEEL F P, VENDERBOSCH R H, HEERES H J.Acetic acid recovery from fast pyrolysis oil:An exploratory study on liquid-liquid reactive extraction using aliphatic tertiary amines[J].Sep Sci Technol, 2008, 43(11/12):3056-3074.
    [6] GANDER M, RAPP K M, SCHIWECK H.Process for preparing 1, 6-β-anhydroglucopyranose (levoglucosan) in high purity:US, 5023330[P].1991-06-11.
    [7] STRADAL J A, UNDERWOOD G L.Process for producing hydroxyacetaldehyde:US, 5252188[P].1993-10-12.
    [8] STRADAL J A, UNDERWOOD G L.Process for producing hydroxyacetaldehyde:US, 5393542[P].1995-02-28.
    [9] DINESH M, CHARLES U P, PHILIP H S.Pyrolysis of wood/biomass for bio-oil:A critical review[J].Energy Fuels, 2006, 20:848-889. doi: 10.1021/ef0502397
    [10] EFFENDI A, GERHAUSER H, BRIDGWATER A V.Production of renewable phenolic resins by thermochemical conversion of biomass:A review[J].Renew Sust Energy Rev, 2008, 12:2092-2116. doi: 10.1016/j.rser.2007.04.008
    [11] LI J, WANG C, YANG Z.Production and separation of phenols from biomass-derived bio-petroleum[J].J Anal Appl Pyrolysis, 2010, 89(2):218-224. doi: 10.1016/j.jaap.2010.08.004
    [12] GE Y Z, JIN H.Recovery process for phenolic compounds from coal-derived oils by ions of solublemetal salts[J].Fuel, 1996, 75:1681-1683. doi: 10.1016/0016-2361(95)00276-6
    [13] WANG D, LI D B, LIU Y Q, LV D C, YE Y Y, ZHU S J, ZHANG B B.Study of a new complex method for extraction of phenolic compounds from bio-oils[J].Sep Purif Technol, 2014, 134:132-138. doi: 10.1016/j.seppur.2014.07.033
    [14] 葛宜掌, 金红, 李斌.Ba2+离子沉淀法回收酚类化学过程的研究[J].燃料化学学报, 1996, 24(3):266-270. http://www.cnki.com.cn/Article/CJFDTOTAL-RLHX603.014.htm

    GE Yi-zhang, JIN Hong, LI Bin.Study on recovery of phenolic compounds using Ba2+ as precipitant[J].J Fuel Chem Technol, 1996, 24(3):266-270. http://www.cnki.com.cn/Article/CJFDTOTAL-RLHX603.014.htm
    [15] JEWEL A.CAPUNITAN, SERGIO C.CAPAREDA.Characterization and separation of corn stover bio-oil by fractional distillation[J].Fuel, 2013, 112:60-73. doi: 10.1016/j.fuel.2013.04.079
    [16] 明珠, 吴云海, 阿依妮尕尔·艾尔肯.茶汤与金属离子络合反应的研究[J].环境科技, 2015, 28(4):5-11. http://youxian.cnki.com.cn/yxdetail.aspx?filename=JSHJ2015072100F&dbname=CAPJ2015

    MING Zhu, WU Yun-hai, ARKEN·AYINIGAR.Study on complexation reaction of tea infusion with metal ions[J].Environ Sci Technol, 2015, 28(4):5-11. http://youxian.cnki.com.cn/yxdetail.aspx?filename=JSHJ2015072100F&dbname=CAPJ2015
    [17] GE Y, JIN H.Recovery of phenols from coal tar and waste water by precipitation[J].J China Coal Soc, 1995, 20:545-548.
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出版历程
  • 收稿日期:  2015-09-18
  • 修回日期:  2015-11-19

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