Biodiesel production in packed-bed reactors using lipase-nanoparticle biocomposite

被引:90
|
作者
Wang, Xia [2 ]
Liu, Xueying [2 ]
Zhao, Chuanming [2 ]
Ding, Yi [1 ]
Xu, Ping [2 ,3 ,4 ]
机构
[1] Shandong Univ, Sch Chem & Chem Engn, Jinan 250100, Peoples R China
[2] Shandong Univ, State Key Lab Microbial Technol, Jinan 250100, Peoples R China
[3] Shanghai Jiao Tong Univ, MOE Key Lab Microbial Metab, Shanghai 200240, Peoples R China
[4] Shanghai Jiao Tong Univ, Sch Life Sci & Biotechnol, Shanghai 200240, Peoples R China
基金
中国国家自然科学基金;
关键词
Biodiesel; Fe3O4; Lipase; Nanoparticle; Packed-bed reactor; FUEL PRODUCTION; PALM OIL; HYDROLYSIS; KINETICS;
D O I
10.1016/j.biortech.2011.03.003
中图分类号
S2 [农业工程];
学科分类号
0828 ;
摘要
The development of appropriate reactors is crucial for the production of biodiesel. In this study, a packed-bed reactor system using lipase-Fe3O4 nanoparticle biocomposite catalyst was successfully developed for biodiesel production based on soybean oil methanolysis. Emulsification before methanolysis improved the reaction rate. The lipase-nanoparticle biocomposite showed high activity and stability in the single-packed-bed reactor at an optimal flow rate (0.25 mL min(-1)). After 240 h of reaction, the conversion rate was sustained as high as 45%. The conversion rate and stability achieved using the four-packed-bed reactor were much higher than those achieved using the single-packed-bed reactor. The conversion of biodiesel was maintained at a high rate of over 88% for 192 h, and it only slightly declined to approximately 75% after 240 h of reaction. The packed-bed reactor system, therefore, has a great potential for achieving the design and operation of enzymatic biodiesel production on the industrial scale. (C) 2011 Elsevier Ltd. All rights reserved.
引用
收藏
页码:6352 / 6355
页数:4
相关论文
共 50 条
  • [1] OPTIMIZATION OF BIODIESEL PRODUCTION USING A STIRRED PACKED-BED REACTOR
    Ani, Farid Nasir
    Said, Nur Hamzah
    Said, Mohd Farid Muhamad
    [J]. INTERNATIONAL JOURNAL OF TECHNOLOGY, 2018, 9 (02) : 219 - 228
  • [2] Cost analysis of enzymatic biodiesel production in small-scaled packed-bed reactors
    Budzaki, Sandra
    Miljic, Goran
    Sundaram, Smitha
    Tisma, Marina
    Hessel, Volker
    [J]. APPLIED ENERGY, 2018, 210 : 268 - 278
  • [3] Synthesis of Biodiesel in Batch and Packed-Bed Reactors Using Powdered and Granular Sugar Catalyst
    Janaun, J.
    Lim, P. M.
    Balan, W. S.
    Yaser, A. Z.
    Chong, K. P.
    [J]. 29TH SYMPOSIUM OF MALAYSIAN CHEMICAL ENGINEERS (SOMCHE) 2016, 2017, 206
  • [4] PACKED-BED REACTORS - A REVIEW
    VARMA, A
    [J]. ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1980, 180 (AUG): : 51 - INDE
  • [5] RUNAWAY OF PACKED-BED REACTORS
    ELSAWI, M
    EMIG, G
    HOFFMANN, U
    [J]. INTERNATIONAL CHEMICAL ENGINEERING, 1978, 18 (02): : 221 - 223
  • [6] Continuous Production of Lipase-Catalyzed Biodiesel in a Packed-Bed Reactor: Optimization and Enzyme Reuse Study
    Chen, Hsiao-Ching
    Ju, Hen-Yi
    Wu, Tsung-Ta
    Liu, Yung-Chuan
    Lee, Chih-Chen
    Chang, Cheng
    Chung, Yi-Lin
    Shieh, Chwen-Jen
    [J]. JOURNAL OF BIOMEDICINE AND BIOTECHNOLOGY, 2011,
  • [7] PACKED-BED CATALYTIC MEMBRANE REACTORS
    TSOTSIS, TT
    CHAMPAGNIE, AM
    VASILEIADIS, SP
    ZIAKA, ZD
    MINET, RG
    [J]. CHEMICAL ENGINEERING SCIENCE, 1992, 47 (9-11) : 2903 - 2908
  • [8] MULTIPHASE CATALYTIC PACKED-BED REACTORS
    HOFMANN, HP
    [J]. CATALYSIS REVIEWS-SCIENCE AND ENGINEERING, 1978, 17 (01): : 71 - 117
  • [9] PACKED-BED ELECTROCHEMICAL FLOW REACTORS
    ALKIRE, RC
    NG, PK
    [J]. JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1973, 120 (03) : C109 - +
  • [10] PACKED-BED BIOFILM REACTORS - DESIGN
    MEUNIER, AD
    WILLIAMSON, KJ
    [J]. JOURNAL OF THE ENVIRONMENTAL ENGINEERING DIVISION-ASCE, 1981, 107 (02): : 319 - 337