STABILITY OF IMMOBILIZED Rhizomucor miehei LIPASE FOR THE SYNTHESIS OF PENTYL OCTANOATE IN A CONTINUOUS PACKED BED BIOREACTOR

被引:10
|
作者
Skoronski, E. [1 ]
Padoin, N. [2 ]
Soares, C. [2 ]
Furigo, A., Jr. [3 ]
机构
[1] Univ Estado Santa Catarina UDESC, Dept Engn Ambiental, BR-88520000 Lages, SC, Brazil
[2] Univ Fed Santa Catarina, Dept Engn Quim & Engn Alimentos EQA, LEMA, BR-88040900 Florianopolis, SC, Brazil
[3] Univ Fed Santa Catarina, Dept Engn Quim & Engn Alimentos EQA, Lab Engn Bioquim ENGEBIO, BR-88040900 Florianopolis, SC, Brazil
关键词
Continuous bioreactor; Biosynthesis of ester; Biocatalysis; Deactivation; KINETICALLY CONTROLLED SYNTHESIS; CONTINUOUS BIOSYNTHESIS; THERMAL INACTIVATION; BETA-GALACTOSIDASE; HIGH-PRESSURE; ESTERIFICATION; OPTIMIZATION; EQUILIBRIUM; LAURATE; FLAVOR;
D O I
10.1590/0104-6632.20140313s00002978
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The enzymatic synthesis of organic compounds in continuous bioreactors is an efficient way to obtain industrially important chemicals. However, few works have focused on the study of the operational conditions and the bioprocess performance. In this work, the aliphatic ester pentyl octanoate was obtained by direct esterification using a continuous packed bed bioreactor containing the immobilized enzyme Lipozyme (R) RM IM as catalyst. Enzymatic deactivation was evaluated under different conditions for the operational parameters substrate/enzyme ratio (5.00, 1.67, 0.83 and 0.55 mmol(substrate).min(-1).g(-1) enzyme) and temperature (30, 40, 50 and 60 degrees C). The optimal condition was observed at 30 degrees C, which gave the minimum enzymatic deactivation rate and the maximum conversion to the desired product, yielding approximately 60 mmols of ester for an enzyme loading of 0.5 g into the bioreactor. A first-order deactivation model showed good agreement with the experimental data.
引用
收藏
页码:633 / 641
页数:9
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