Journal of Energy and Natural Resources

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Adsorption Removal of Inhibiting Compounds by Modified Activated Carbon

Received: 10 May 2017    Accepted:     Published: 10 May 2017
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Abstract

The effects of modification on the surface properties and inhibiting compounds (formic acid, acetic acid, 5-hydroxymethylfurfural and furfural) removal performance of activate carbon (AC) were investigated. The raw and modified ACs were characterized, the result showed that the surface chemistries of the modified ACs were significant changed, but only the porous structure of modified by HNO3 were slightly damaged, and the others no obvious change. The formic acid and acetic acid removal performance of modified AC had a certain amount of improvement compared to the raw AC, but it is still relatively low (15% and 14%), so AC adsorption is not suitable for removal formic acid and acetic acid. And the 5-hydroxymethylfurfural (5-HMF) and furfural removal performance of modified AC by ZNCl2 is good (89% and 81%). the process of adsorption of 5-HMF and furfural by activated carbon belongs to the process of exothermic physical adsorption and is the entropy reduction process. The adsorption is best carried out at low temperature.

DOI 10.11648/j.jenr.20170602.12
Published in Journal of Energy and Natural Resources (Volume 6, Issue 2, April 2017)
Page(s) 24-30
Creative Commons

This is an Open Access article, distributed under the terms of the Creative Commons Attribution 4.0 International License (http://creativecommons.org/licenses/by/4.0/), which permits unrestricted use, distribution and reproduction in any medium or format, provided the original work is properly cited.

Copyright

Copyright © The Author(s), 2024. Published by Science Publishing Group

Keywords

Inhibiting Compounds, Modified Active Carbon, Adsorption, Kinetics, Isotherms

References
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[8] Liu H, Hu H, Jahan M. S, et al. Purification of Hemicelluloses in Pre-Hydrolysis Liquor of Kraft-Based Dissolving Pulp Production Process Using Activated Carbon and Ion-Exchange Resin Adsorption Followed by Nanofiltration [J]. Journal of Biobased Materials & Bioenergy, 2014, 8(3): 325-330(6).
[9] Mahaninia M. H, Rahimian P, Kaghazchi T. Modified activated carbons with amino groups and their copper adsorption properties in aqueous solution [J]. Chinese Journal of Chemical Engineering, 2015, 23(1): 50-56.
[10] Yao S, Zhang J, Shen D, et al. Removal of Pb(II) from water by the activated carbon modified by nitric acid under microwave heating [J]. J Colloid Interface Sci, 2016, 463: 118-27.
[11] Shen J, Kaur I, Baktash M. M, et al. A. combined process of activated carbon adsorption, ion exchange resin treatment and membrane concentration for recovery of dissolved organics in pre-hydrolysis liquor of the kraft-based dissolving pulp production process [J]. Bioresource Technology, 2013, 127(1): 59-65.
[12] Wang Z, Zhuang J, Wang X, et al. Limited adsorption selectivity of active carbon toward non-saccharide compounds in lignocellulose hydrolysate [J]. Bioresour Technol, 2016, 208: 195-9.
[13] Montané D, Nabarlatz D, Martorell A, et al. Removal of Lignin and Associated Impurities from Xylo-oligosaccharides by Activated Carbon Adsorption [J]. Industrial & Engineering Chemistry Research, 2006, 45(45): págs. 2294-2302.
[14] Liu H, Gao Q, Dai P, et al. Preparation and characterization of activated carbon from lotus stalk with guanidine phosphate activation: Sorption of Cd(II) [J]. Journal of Analytical & Applied Pyrolysis, 2013, 102(102): 7-15.
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Author Information
  • Key Lab of Pulp and Paper Science & Technology, Ministry of Education, Qilu University of Technology, Ji’nan, China

  • Key Lab of Pulp and Paper Science & Technology, Ministry of Education, Qilu University of Technology, Ji’nan, China; Institute of Chemical Industry of Forestry Products, Nanjing, China

  • Key Lab of Pulp and Paper Science & Technology, Ministry of Education, Qilu University of Technology, Ji’nan, China

  • Institute of Chemical Industry of Forestry Products, Nanjing, China

  • Key Lab of Pulp and Paper Science & Technology, Ministry of Education, Qilu University of Technology, Ji’nan, China

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  • APA Style

    Hao Ma, Xingxiang Ji, Zhongjian Tian, Guigan Fang, Guihua Yang. (2017). Adsorption Removal of Inhibiting Compounds by Modified Activated Carbon. Journal of Energy and Natural Resources, 6(2), 24-30. https://doi.org/10.11648/j.jenr.20170602.12

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    ACS Style

    Hao Ma; Xingxiang Ji; Zhongjian Tian; Guigan Fang; Guihua Yang. Adsorption Removal of Inhibiting Compounds by Modified Activated Carbon. J. Energy Nat. Resour. 2017, 6(2), 24-30. doi: 10.11648/j.jenr.20170602.12

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    AMA Style

    Hao Ma, Xingxiang Ji, Zhongjian Tian, Guigan Fang, Guihua Yang. Adsorption Removal of Inhibiting Compounds by Modified Activated Carbon. J Energy Nat Resour. 2017;6(2):24-30. doi: 10.11648/j.jenr.20170602.12

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  • @article{10.11648/j.jenr.20170602.12,
      author = {Hao Ma and Xingxiang Ji and Zhongjian Tian and Guigan Fang and Guihua Yang},
      title = {Adsorption Removal of Inhibiting Compounds by Modified Activated Carbon},
      journal = {Journal of Energy and Natural Resources},
      volume = {6},
      number = {2},
      pages = {24-30},
      doi = {10.11648/j.jenr.20170602.12},
      url = {https://doi.org/10.11648/j.jenr.20170602.12},
      eprint = {https://download.sciencepg.com/pdf/10.11648.j.jenr.20170602.12},
      abstract = {The effects of modification on the surface properties and inhibiting compounds (formic acid, acetic acid, 5-hydroxymethylfurfural and furfural) removal performance of activate carbon (AC) were investigated. The raw and modified ACs were characterized, the result showed that the surface chemistries of the modified ACs were significant changed, but only the porous structure of modified by HNO3 were slightly damaged, and the others no obvious change. The formic acid and acetic acid removal performance of modified AC had a certain amount of improvement compared to the raw AC, but it is still relatively low (15% and 14%), so AC adsorption is not suitable for removal formic acid and acetic acid. And the 5-hydroxymethylfurfural (5-HMF) and furfural removal performance of modified AC by ZNCl2 is good (89% and 81%). the process of adsorption of 5-HMF and furfural by activated carbon belongs to the process of exothermic physical adsorption and is the entropy reduction process. The adsorption is best carried out at low temperature.},
     year = {2017}
    }
    

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  • TY  - JOUR
    T1  - Adsorption Removal of Inhibiting Compounds by Modified Activated Carbon
    AU  - Hao Ma
    AU  - Xingxiang Ji
    AU  - Zhongjian Tian
    AU  - Guigan Fang
    AU  - Guihua Yang
    Y1  - 2017/05/10
    PY  - 2017
    N1  - https://doi.org/10.11648/j.jenr.20170602.12
    DO  - 10.11648/j.jenr.20170602.12
    T2  - Journal of Energy and Natural Resources
    JF  - Journal of Energy and Natural Resources
    JO  - Journal of Energy and Natural Resources
    SP  - 24
    EP  - 30
    PB  - Science Publishing Group
    SN  - 2330-7404
    UR  - https://doi.org/10.11648/j.jenr.20170602.12
    AB  - The effects of modification on the surface properties and inhibiting compounds (formic acid, acetic acid, 5-hydroxymethylfurfural and furfural) removal performance of activate carbon (AC) were investigated. The raw and modified ACs were characterized, the result showed that the surface chemistries of the modified ACs were significant changed, but only the porous structure of modified by HNO3 were slightly damaged, and the others no obvious change. The formic acid and acetic acid removal performance of modified AC had a certain amount of improvement compared to the raw AC, but it is still relatively low (15% and 14%), so AC adsorption is not suitable for removal formic acid and acetic acid. And the 5-hydroxymethylfurfural (5-HMF) and furfural removal performance of modified AC by ZNCl2 is good (89% and 81%). the process of adsorption of 5-HMF and furfural by activated carbon belongs to the process of exothermic physical adsorption and is the entropy reduction process. The adsorption is best carried out at low temperature.
    VL  - 6
    IS  - 2
    ER  - 

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