Lipase-Catalyzed Interesterification in Packed Bed Reactor Using 2 Different Temperatures

被引:6
|
作者
Chae, Mi-Hwa [1 ]
Park, Hye-Kyung [2 ]
Kwon, Kwang-Il [2 ]
Kim, Jong-Wook [2 ]
Hong, Seung In [1 ]
Kim, Yangha [3 ]
Kim, Byung Hee [4 ]
Kim, In-Hwan [1 ]
机构
[1] Korea Univ, Dept Food & Nutr, Seoul 136703, South Korea
[2] Korea Food & Drug Adm, Nutr Policy Div, Seoul 122704, South Korea
[3] Ewha Womans Univ, Dept Nutr Sci & Food Management, Seoul 120749, South Korea
[4] Chung Ang Univ, Dept Food Sci & Technol, Anseong 456756, South Korea
关键词
fully hydrogenated soybean oil; high oleic sunflower oil; interesterification; lipase; packed-bed reactor; FULLY HYDROGENATED FAT; THERMOMYCES-LANUGINOSA LIPASE; PALM KERNEL OLEIN; ENZYMATIC INTERESTERIFICATION; IMMOBILIZED LIPASE; OIL BLENDS; CHEMICAL INTERESTERIFICATION; STRUCTURED LIPIDS; MARGARINE FATS; SESAME OIL;
D O I
10.1111/j.1750-3841.2011.02115.x
中图分类号
TS2 [食品工业];
学科分类号
0832 ;
摘要
Lipase-catalyzed interesterification of high oleic sunflower oil and fully hydrogenated soybean oil (70 : 30, wt/ wt) was carried out in a packed bed reactor using an immobilized lipase from Thermomyces lanuginosus (Lipozyme TL IM) and the effect of a stepwise temperature protocol involving the 2 different temperatures, 60 and 70 degrees C, was investigated. The melting point of a fat that was incubated at 70 degrees C for 9 min was 57 degrees C, which suggested that it should be to employ a lower reaction temperature of 60 degrees C, after the first 9 min of the reaction. There were no significant differences (P < 0.05) in the conversion degree, triacylglycerol profile, and solid fat content between a constant temperature protocol (70 degrees C) and a stepwise temperature protocol (a combination of 70 and 60 degrees C). After 50 cycles, the overall residual activities of enzymes employed in stepwise temperature protocol were significantly (P < 0.05) higher than those of enzymes employed in constant temperature protocol.
引用
收藏
页码:C555 / C559
页数:5
相关论文
共 50 条
  • [1] 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
  • [2] 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
  • [3] AGFD 175-Production of trans-free fat by lipase-catalyzed interesterification in a batch reactor and a packed bed reactor
    Kim, Sang Woo
    Park, Young Woo
    Lee, J. H.
    Chang, P. S.
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 2008, 236
  • [4] Production of structured lipids by lipase-catalyzed interesterification in a packed bed reactor: effect of reaction parameters on the level of diacylglycerols in the products
    Mu, HL
    Xu, XB
    Adler-Nissen, J
    Hoy, CE
    FETT-LIPID, 1999, 101 (05): : 158 - 164
  • [5] Interesterification of Lard and Soybean Oil Blends Catalyzed by Immobilized Lipase in a Continuous Packed Bed Reactor
    da Silva, Roberta Claro
    Schaffer De Martini Soares, Fabiana Andreia
    Fernandes, Thais Gonzaga
    Donadi Castells, Anna Laura
    Guimaraes da Silva, Kelly Caroline
    Almeida Goncalves, Maria Ines
    Ming, Chiu Chih
    Guaraldo Goncalves, Lireny Aparecida
    Gioielli, Luiz Antonio
    JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2011, 88 (12) : 1925 - 1933
  • [6] Modeling and Optimization of Lipase-Catalyzed Partial Hydrolysis for Diacylglycerol Production in Packed Bed Reactor
    Phuah, Eng-Tong
    Lee, Yee-Ying
    Tang, Teck-Kim
    Lai, Oi-Ming
    Choong, Thomas Shean-Yaw
    Tan, Chin-Ping
    Ng, Wee-Nak
    Lo, Seong-Koon
    INTERNATIONAL JOURNAL OF FOOD ENGINEERING, 2016, 12 (07) : 681 - 689
  • [7] Modeling of lipase-catalyzed oil hydrolysis in supercritical CO2 in a packed-bed reactor
    Sovova, Helena
    Pleskac, Ondrej
    Sajfrtova, Marie
    JOURNAL OF SUPERCRITICAL FLUIDS, 2022, 187
  • [8] Production of structured lipids by lipase-catalyzed interesterification in a flat membrane reactor
    Xu, X
    Balchen, S
    Jonsson, G
    Adler-Nissen, J
    JOURNAL OF THE AMERICAN OIL CHEMISTS SOCIETY, 2000, 77 (10) : 1035 - 1041
  • [10] 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