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Wei C, Zhou Y, Zhuang W, Li G, Jiang M, Zhang H. Improving the performance of immobilized β-glucosidase using a microreactor. J Biosci Bioeng 2018; 125:377-384. [DOI: 10.1016/j.jbiosc.2017.09.011] [Citation(s) in RCA: 10] [Impact Index Per Article: 1.4] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 05/02/2017] [Revised: 08/10/2017] [Accepted: 09/28/2017] [Indexed: 10/18/2022]
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Xu Y, Zhang DY, Meng XY, Liu X, Sheng S, Wu GH, Wang J, Wu FA. Generic DART-MS platform for monitoring the on-demand continuous-flow production of pharmaceuticals: Advancing the quantitative protocol for caffeates in microfluidic biocatalysis. J Pharm Biomed Anal 2017; 137:243-251. [DOI: 10.1016/j.jpba.2017.01.050] [Citation(s) in RCA: 1] [Impact Index Per Article: 0.1] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 11/23/2016] [Revised: 01/21/2017] [Accepted: 01/25/2017] [Indexed: 01/11/2023]
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Wang J, Gu SS, Cui HS, Yang LQ, Wu XY. Rapid synthesis of propyl caffeate in ionic liquid using a packed bed enzyme microreactor under continuous-flow conditions. BIORESOURCE TECHNOLOGY 2013; 149:367-374. [PMID: 24128399 DOI: 10.1016/j.biortech.2013.09.098] [Citation(s) in RCA: 27] [Impact Index Per Article: 2.3] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Subscribe] [Scholar Register] [Received: 07/18/2013] [Revised: 09/19/2013] [Accepted: 09/21/2013] [Indexed: 06/02/2023]
Abstract
Propyl caffeate has the highest antioxidant activity among caffeic acid alkyl esters, but its industrial production via enzymatic transesterification in batch reactors is hindered by a long reaction time (24h). To develop a rapid process for the production of propyl caffeate in high yield, a continuous-flow microreactor composed of a two-piece PDMS in a sandwich-like microchannel structure was designed for the transesterification of methyl caffeate and 1-propanol catalyzed by Novozym 435 in [B mim][CF3SO3]. The maximum yield (99.5%) in the microreactor was achieved in a short period of time (2.5h) with a flow rate of 2 μL/min, which kinetic constant Km was 16 times lower than that of a batch reactor. The results indicated that the use of a continuous-flow packed bed enzyme microreactor is an efficient method of producing propyl caffeate with an overall yield of 84.0%.
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Affiliation(s)
- Jun Wang
- School of the Environment, Jiangsu University, Zhenjiang 212013, PR China; School of Biology and Chemical Engineering, Jiangsu University of Science and Technology, Zhenjiang 212018, PR China.
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Lee DE, Park KM, Choi SJ, Shim JH, Chang PS. Enhancing operational stability and exhibition of enzyme activity by removing water in the immobilized lipase-catalyzed production of erythorbyl laurate. Biotechnol Prog 2013; 29:882-9. [DOI: 10.1002/btpr.1745] [Citation(s) in RCA: 6] [Impact Index Per Article: 0.5] [Reference Citation Analysis] [Track Full Text] [Journal Information] [Subscribe] [Scholar Register] [Received: 12/14/2012] [Revised: 02/18/2013] [Indexed: 11/09/2022]
Affiliation(s)
- Da Eun Lee
- Dept. of Agricultural Biotechnology; Seoul National University; Seoul 151-742 Republic of Korea
| | - Kyung Min Park
- Dept. of Agricultural Biotechnology; Seoul National University; Seoul 151-742 Republic of Korea
| | - Seung Jun Choi
- Dept. of Food Science and Technology; Seoul National University of Science and Technology; Seoul 139-743 Republic of Korea
| | - Jae-Hoon Shim
- Dept. of Food Science and Nutrition; Hallym University; Chuncheon 200-702 Republic of Korea
| | - Pahn-Shick Chang
- Dept. of Agricultural Biotechnology; Seoul National University; Seoul 151-742 Republic of Korea
- Center for Food Safety and Toxicology; Center for Food and Bioconvergence, and Research Institute for Agriculture and Life Sciences; Seoul National University; Seoul 151-742 Republic of Korea
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Contesini FJ, de Alencar Figueira J, Kawaguti HY, de Barros Fernandes PC, de Oliveira Carvalho P, Nascimento MDG, Sato HH. Potential applications of carbohydrases immobilization in the food industry. Int J Mol Sci 2013; 14:1335-69. [PMID: 23344046 PMCID: PMC3565324 DOI: 10.3390/ijms14011335] [Citation(s) in RCA: 33] [Impact Index Per Article: 2.8] [Reference Citation Analysis] [Abstract] [Key Words] [MESH Headings] [Track Full Text] [Download PDF] [Figures] [Journal Information] [Subscribe] [Scholar Register] [Received: 10/30/2012] [Revised: 12/17/2012] [Accepted: 12/18/2012] [Indexed: 11/16/2022] Open
Abstract
Carbohydrases find a wide application in industrial processes and products, mainly in the food industry. With these enzymes, it is possible to obtain different types of sugar syrups (viz. glucose, fructose and inverted sugar syrups), prebiotics (viz. galactooligossacharides and fructooligossacharides) and isomaltulose, which is an interesting sweetener substitute for sucrose to improve the sensory properties of juices and wines and to reduce lactose in milk. The most important carbohydrases to accomplish these goals are of microbial origin and include amylases (α-amylases and glucoamylases), invertases, inulinases, galactosidases, glucosidases, fructosyltransferases, pectinases and glucosyltransferases. Yet, for all these processes to be cost-effective for industrial application, a very efficient, simple and cheap immobilization technique is required. Immobilization techniques can involve adsorption, entrapment or covalent bonding of the enzyme into an insoluble support, or carrier-free methods, usually based on the formation of cross-linked enzyme aggregates (CLEAs). They include a broad variety of supports, such as magnetic materials, gums, gels, synthetic polymers and ionic resins. All these techniques present advantages and disadvantages and several parameters must be considered. In this work, the most recent and important studies on the immobilization of carbohydrases with potential application in the food industry are reviewed.
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Affiliation(s)
- Fabiano Jares Contesini
- Laboratory of Food Biochemistry, Department of Food Science, College of Food Engineering, State University of Campinas (UNICAMP), Monteiro Lobato Street, 80, 13083-862, P.O. Box 6121, Campinas, SP, Brazil; E-Mails: (J.A.F.); (H.Y.K.); (H.H.S.)
| | - Joelise de Alencar Figueira
- Laboratory of Food Biochemistry, Department of Food Science, College of Food Engineering, State University of Campinas (UNICAMP), Monteiro Lobato Street, 80, 13083-862, P.O. Box 6121, Campinas, SP, Brazil; E-Mails: (J.A.F.); (H.Y.K.); (H.H.S.)
| | - Haroldo Yukio Kawaguti
- Laboratory of Food Biochemistry, Department of Food Science, College of Food Engineering, State University of Campinas (UNICAMP), Monteiro Lobato Street, 80, 13083-862, P.O. Box 6121, Campinas, SP, Brazil; E-Mails: (J.A.F.); (H.Y.K.); (H.H.S.)
| | | | - Patrícia de Oliveira Carvalho
- Laboratory of Multidisciplinary Research, University São Francisco, São Francisco de Assis Av, 218, 12916-900, Bragança Paulista, SP, Brazil; E-Mail:
| | - Maria da Graça Nascimento
- Chemistry Department, Federal University of Santa Catarina, Florianópolis, Santa Catarina, 88040-900, Brazil; E-Mail:
| | - Hélia Harumi Sato
- Laboratory of Food Biochemistry, Department of Food Science, College of Food Engineering, State University of Campinas (UNICAMP), Monteiro Lobato Street, 80, 13083-862, P.O. Box 6121, Campinas, SP, Brazil; E-Mails: (J.A.F.); (H.Y.K.); (H.H.S.)
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