Enzyme-catalyzed production of 1-glyceryl benzoate in compressed n-butane

被引:8
作者
Ceni, Giovana [1 ,2 ]
da Silva, Patricia Costa [1 ]
Lerin, Lindomar [2 ]
Charin, Rafael Mengotti [1 ,3 ]
Oliveira, J. Vladimir [1 ]
Toniazzo, Geciane [1 ]
Treichel, Helen [1 ]
Oestreicher, Enrique Guillermo [2 ]
de Oliveira, Debora [1 ]
机构
[1] Univ Reg Integrada Alto Uruguai & Missoes URI, Dept Engn Alimentos, BR-99700000 Erechim, RS, Brazil
[2] Univ Fed Rio de Janeiro, Inst Quim, BR-21941909 Rio De Janeiro, Brazil
[3] Univ Fed Parana, Dept Engn Quim, BR-80060000 Curitiba, Parana, Brazil
基金
加拿大自然科学与工程研究理事会; 美国国家科学基金会;
关键词
Lipase; Transesterification; Compressed solvent; n-Butane; 1-Glyceryl benzoate; Phase equilibrium data; PHASE-EQUILIBRIUM MEASUREMENTS; ACID ETHYL-ESTERS; PALM KERNEL OIL; CARBON-DIOXIDE; SOYBEAN OIL; BIODIESEL FUEL; CASTOR-OIL; LIPASE; BEHAVIOR; PROPANE;
D O I
10.1016/j.enzmictec.2010.01.007
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The aim of this work is to report the enzymatic transesterification production of 1-glyceryl benzoate in compressed n-butane, using a commercial immobilized lipase, Novozym 435. For this purpose, reaction experiments were performed on the basis of phase equilibrium data of the system methyl benzoate/n-butane, measured using the static synthetic method with a variable-volume view cell in the temperature range of 313.15-343.15 K and pressures up to 12 MPa, in the entire compositional range of n-butane. Results indicate the existence of a relatively complex phase behavior for all temperatures investigated with the occurrence of vapor-liquid and liquid-liquid phase transitions. Reaction results showed that the strategy adopted for the experimental design proved to be useful in optimizing the reaction conversion in pressurized n-butane and Novozym 435. The optimum conditions were found to be 5.5 wt% of enzyme, methyl benzoate to glycerol molar ratio of 3:1, 50 degrees C and 6 h of reaction, affording about 6% of 1-glyceryl benzoate yield. (C) 2010 Elsevier Inc. All rights reserved.
引用
收藏
页码:513 / 519
页数:7
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