Enzymatic synthesis of butyl acetate in a packed bed reactor under liquid and supercritical conditions

被引:13
|
作者
Escandell, J. [1 ]
Wurm, D. J. [1 ]
Belleville, M. P. [1 ]
Sanchez, J. [1 ]
Harasek, M. [2 ]
Paolucci-Jeanjean, D. [1 ]
机构
[1] Univ Montpellier 2, CNRS ENSCM UM2, IEM, UMR 5635, F-34095 Montpellier, France
[2] Vienna Univ Technol, Inst Chem Engn E166, A-1060 Vienna, Austria
关键词
Biocatalytic ester synthesis; Enzymatic packed bed reactor; Continuous process; Supercritical CO2; Candida antarctica lipase B; LIPASE-CATALYZED ESTERIFICATION; DENSE CARBON-DIOXIDE; ACID; ENZYMES; ESTER; TRANSESTERIFICATION; SELECTIVITY; EQUATION; SOLVENTS; SILICA;
D O I
10.1016/j.cattod.2015.01.048
中图分类号
O69 [应用化学];
学科分类号
081704 ;
摘要
In this work we studied the synthesis of butyl acetate in an enzymatic packed bed reactor using lipaseB, from Candida antarctica, immobilized by simple physical adsorption on porous pellets. The enzymatic reaction was carried out in two different solvents: a conventional organic solvent (n-hexane) and a green solvent (supercritical carbon dioxide). The highest ester productivity in hexane (119 mu mol min(-1) g(pellets)(-1)) was reached at 323 K, whereas in supercritical CO2, a maximum productivity of 501 mu mol min(-1) g(pellets)(-1) was achieved at 333 K and under 12 MPa. The environmental impacts of each process were estimated by means of the E-factor (mass ratio of amount of waste produced divided by amount of desired product) and the values obtained under the previous conditions were 28.7 and 12.0 respectively. Results show that replacing hexane by supercritical CO2 in a continuous process increases ester productivity and reduces environmental impact, thus allowing making a more environmentally friendly process. (C) 2015 Elsevier B.V. All rights reserved.
引用
收藏
页码:3 / 9
页数:7
相关论文
共 50 条
  • [21] A micro packed-bed reactor for chemical synthesis
    Losey, MW
    Schmidt, MA
    Jensen, KF
    [J]. MICROREACTION TECHNOLOGY: INDUSTRIAL PROSPECTS, 2000, : 277 - 286
  • [22] Synthesis of Silver Sulfide Quantum Dots Via the Liquid–Liquid Interface Reaction in a Rotating Packed Bed Reactor
    Qing Liu
    Yuan Pu
    Zhijian Zhao
    Jiexin Wang
    Dan Wang
    [J]. Transactions of Tianjin University, 2020, 26 : 273 - 282
  • [23] DETERMINATION OF THE INTERFACIAL AREA OF A LIQUID-LIQUID PACKED-BED REACTOR
    GARCIA, FC
    [J]. AFINIDAD, 1994, 51 (454) : 455 - 460
  • [24] LIQUID PHASE AUTOXIDATION OF DIPHENYLMETHANE IN GAS LIQUID COCURRENT PACKED BED REACTOR
    OKADA, J
    KITAMURA, K
    HAYAKAWA, K
    [J]. YAKUGAKU ZASSHI, 1971, 91 (11): : 1233 - &
  • [25] Liquid-liquid heterogeneous mixing efficiency in a rotating packed bed reactor
    Zhang, Yi-Dong
    Zhang, Liang-Liang
    Wang, Ze-Xin
    Sun, Bao-Chang
    Chu, Guang-Wen
    Chen, Jian-Feng
    [J]. AICHE JOURNAL, 2023, 69 (06)
  • [26] The enhancement of waste PET particles enzymatic degradation with a rotating packed bed reactor
    Lu, Dong
    Wu, Jinglong
    Jin, Shuming
    Wu, Qiuyang
    Deng, Li
    Wang, Fang
    Nie, Kaili
    [J]. JOURNAL OF CLEANER PRODUCTION, 2024, 434
  • [27] Synthesis of Nano-Ni by Liquid Reduction Method in a Combined Reactor of Rotating Packed Bed and Stirred Tank Reactor
    Dong, Kun
    Yang, Yong
    Luo, Yong
    Zhang, Liangliang
    Chu, Guangwen
    Zou, Haikui
    Sun, Baochang
    Chen, Jian-Feng
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (11) : 3908 - 3913
  • [28] Strategies to remove water formed as by-product on the monoolein synthesis by enzymatic esterification performed on packed bed reactor
    L. Freitas
    G. S. Silva
    J. C. Santos
    P. C. Oliveira
    H. F. de Castro
    [J]. European Food Research and Technology, 2011, 233 : 743 - 750
  • [29] Strategies to remove water formed as by-product on the monoolein synthesis by enzymatic esterification performed on packed bed reactor
    Freitas, L.
    Silva, G. S.
    Santos, J. C.
    Oliveira, P. C.
    de Castro, H. F.
    [J]. EUROPEAN FOOD RESEARCH AND TECHNOLOGY, 2011, 233 (05) : 743 - 750
  • [30] Simultaneous sulfide and acetate oxidation under denitrifying conditions using an inverse fluidized bed reactor
    Beristain-Cardoso, Ricardo
    Texier, Anne-Claire
    Sierra-Alvarez, Reyes
    Field, Jim A.
    Razo-Flores, Elias
    Gomez, Jorge
    [J]. JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2008, 83 (09) : 1197 - 1203