Continuous synthesis of lauroyl or oleoyl erythritol by a packed-bed reactor with an immobilized lipase

被引:17
|
作者
Piao, J
Takashi, KA
Adachi, S [1 ]
Nakanishi, K
Matsuno, R
机构
[1] Kyoto Univ, Grad Sch Agr, Div Food Sci & Biotechnol, Sakyo Ku, Kyoto 6068502, Japan
[2] Okayama Univ, Fac Engn, Dept Biosci & Biotechnol, Okayama 7008530, Japan
关键词
lipase; erythritol; condensation; lauric acid; oleic acid; packed-bed reactor;
D O I
10.1016/S0032-9592(03)00151-1
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
A system is proposed for the continuous synthesis of an acyl erythritol through the immobilised-lipase-catalysed condensation of the corresponding fatty acid and erythritol in acetone. A fatty acid dissolved in acetone was fed to a column packed with erythritol powders, and erythritol was dissolved in the column at a saturated concentration. The effluent from the column was introduced to a packed-bed reactor of immobilised lipase from Candida antarctica to produce the acyl erythritol. Some saturated acyl erythritols and oleoryl erithritol could be continuously synthesised using this system. A selectivity higher than 0.8 was obtained for the monolauroyl erythritol synthesis at 50 mmol/l of lauric acid, with residence times longer than 4.5 min and 60 degreesC. The system could be stably operated at 60 degreesC for at least 2 weeks without any loss of enzyme activity. Productivities of 1.25 and 1.36 kg/l-reactor day were achieved for the synthesis of the lauroyl and oleoyl erythritols, respectively. (C) 2003 Elsevier Ltd. All rights reserved.
引用
收藏
页码:681 / 686
页数:6
相关论文
共 50 条
  • [41] Evaluation of oil transesterification in a packed-bed reactor containing lipase immobilized in starch-alginate jet cutting beads
    Almeida, Francisco Lucas Chaves
    Sampaio, Klicia Araujo
    Prata, Ana Silvia
    Forte, Marcus Bruno Soares
    BIOFUELS BIOPRODUCTS & BIOREFINING-BIOFPR, 2024, 18 (06): : 2005 - 2014
  • [42] Transesterification of Palm Oil Catalyzed by Pseudomonas fluorescens Lipase in a Packed-Bed Reactor
    Dors, Gisanara
    Freitas, Larissa
    Mendes, Adriano A.
    Furigo, Agenor, Jr.
    de Castro, Heizir F.
    ENERGY & FUELS, 2012, 26 (09) : 5977 - 5982
  • [43] A kinetic study on lipase-catalyzed interesterification of soybean oil with oleic acid in a continuous packed-bed reactor
    Masamichi Akimoto
    Yoshiko Nagashima
    Daiki Sato
    Applied Biochemistry and Biotechnology, 1999, 81 : 131 - 142
  • [44] Continuous lipase-catalyzed synthesis of hexyl laurate in a packed-bed reactor: optimization of the reaction conditions in a solvent-free system
    Ju, Hen-Yi
    Yang, Cheng-Kang
    Yen, Yue-Horng
    Shieh, Chwen-Jen
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 2009, 84 (01) : 29 - 33
  • [45] A kinetic study on lipase-catalyzed interesterification of soybean oil with oleic acid in a continuous packed-bed reactor
    Akimoto, M
    Nagashima, Y
    Sato, D
    APPLIED BIOCHEMISTRY AND BIOTECHNOLOGY, 1999, 81 (02) : 131 - 142
  • [46] Electrostatic effect on apparent kinetic parameters in a packed-bed immobilized enzyme reactor
    Miyakawa, H
    Shiraishi, F
    KAGAKU KOGAKU RONBUNSHU, 1997, 23 (04) : 587 - 590
  • [47] MATHEMATICAL MODELIZATION OF A PACKED-BED REACTOR PERFORMANCE WITH IMMOBILIZED YEAST FOR ETHANOL FERMENTATION
    GODIA, F
    CASAS, C
    SOLA, C
    BIOTECHNOLOGY AND BIOENGINEERING, 1987, 30 (07) : 836 - 843
  • [48] Optimization of lipase-catalyzed biodiesel by isopropanolysis in a continuous packed-bed reactor using response surface methodology
    Chang, Cheng
    Chen, Jiann-Hwa
    Chang, Chieh-ming J.
    Wu, Tsung-Ta
    Shieh, Chwen-Jen
    NEW BIOTECHNOLOGY, 2009, 26 (3-4) : 187 - 192
  • [49] ANALYSIS OF IMMOBILIZED ENZYMATIC-REACTION IN A PACKED-BED REACTOR WITH ENZYME DENATURATION
    LIN, SH
    CHEMICAL ENGINEERING JOURNAL AND THE BIOCHEMICAL ENGINEERING JOURNAL, 1977, 14 (02): : 129 - 136
  • [50] ANALYSIS OF A PACKED-BED REACTOR FOR HYDROLYSIS OF PICROCROCIN BY IMMOBILIZED BETA-GLUCOSIDASE
    IBORRA, JL
    CASTELLAR, MR
    CANOVAS, M
    MANJON, A
    ENZYME AND MICROBIAL TECHNOLOGY, 1993, 15 (09) : 780 - 784