{"title":"根霉内作用果胶酶水解果胶的动力学模型","authors":"S. Todisco, V. Calabrò, G. Iorio","doi":"10.1016/0304-5102(94)00076-X","DOIUrl":null,"url":null,"abstract":"<div><p>Enzyme kinetics of pectin hydrolysis reaction catalysed by an <em>endo</em>-polygalacturonase from <em>Rhizopus</em> have been analysed experimentally in a stirred batch reactor at pH=4.5 and <em>T</em>=34°C using a sodium salt of polygalacturonic acid as substrate. The reaction products, consisting of oligomers of galacturonic acid, were classified in four classes of oligomeric fractions employing three hollow fibre ultrafiltration units characterised by different molecular weight cut-off (<em>MW</em><sub>co</sub>). On the basis of the time-concentration data, a kinetic model of the reacting system has been proposed in terms of a series-side reaction pattern. Identification of kinetic parameters was carried out by a non-linear regression optimization procedure based on the Powell's algorithm of conjugated directions. Finally, the kinetic model was used to predict the best reactor configuration able to control the product distribution for a given enzyme/substrate concentration ratio.</p></div>","PeriodicalId":16567,"journal":{"name":"分子催化","volume":"92 3","pages":"Pages 333-346"},"PeriodicalIF":0.0000,"publicationDate":"1994-09-13","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"https://sci-hub-pdf.com/10.1016/0304-5102(94)00076-X","citationCount":"6","resultStr":"{\"title\":\"A kinetic model for the pectin hydrolysis using an endo-acting pectinase from Rhizopus\",\"authors\":\"S. Todisco, V. Calabrò, G. Iorio\",\"doi\":\"10.1016/0304-5102(94)00076-X\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"<div><p>Enzyme kinetics of pectin hydrolysis reaction catalysed by an <em>endo</em>-polygalacturonase from <em>Rhizopus</em> have been analysed experimentally in a stirred batch reactor at pH=4.5 and <em>T</em>=34°C using a sodium salt of polygalacturonic acid as substrate. The reaction products, consisting of oligomers of galacturonic acid, were classified in four classes of oligomeric fractions employing three hollow fibre ultrafiltration units characterised by different molecular weight cut-off (<em>MW</em><sub>co</sub>). On the basis of the time-concentration data, a kinetic model of the reacting system has been proposed in terms of a series-side reaction pattern. Identification of kinetic parameters was carried out by a non-linear regression optimization procedure based on the Powell's algorithm of conjugated directions. Finally, the kinetic model was used to predict the best reactor configuration able to control the product distribution for a given enzyme/substrate concentration ratio.</p></div>\",\"PeriodicalId\":16567,\"journal\":{\"name\":\"分子催化\",\"volume\":\"92 3\",\"pages\":\"Pages 333-346\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"1994-09-13\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"https://sci-hub-pdf.com/10.1016/0304-5102(94)00076-X\",\"citationCount\":\"6\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"分子催化\",\"FirstCategoryId\":\"1089\",\"ListUrlMain\":\"https://www.sciencedirect.com/science/article/pii/030451029400076X\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q4\",\"JCRName\":\"Chemical Engineering\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"分子催化","FirstCategoryId":"1089","ListUrlMain":"https://www.sciencedirect.com/science/article/pii/030451029400076X","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q4","JCRName":"Chemical Engineering","Score":null,"Total":0}
A kinetic model for the pectin hydrolysis using an endo-acting pectinase from Rhizopus
Enzyme kinetics of pectin hydrolysis reaction catalysed by an endo-polygalacturonase from Rhizopus have been analysed experimentally in a stirred batch reactor at pH=4.5 and T=34°C using a sodium salt of polygalacturonic acid as substrate. The reaction products, consisting of oligomers of galacturonic acid, were classified in four classes of oligomeric fractions employing three hollow fibre ultrafiltration units characterised by different molecular weight cut-off (MWco). On the basis of the time-concentration data, a kinetic model of the reacting system has been proposed in terms of a series-side reaction pattern. Identification of kinetic parameters was carried out by a non-linear regression optimization procedure based on the Powell's algorithm of conjugated directions. Finally, the kinetic model was used to predict the best reactor configuration able to control the product distribution for a given enzyme/substrate concentration ratio.
期刊介绍:
Journal of Molecular Catalysis (China) is a bimonthly journal, founded in 1987. It is a bimonthly journal, founded in 1987, sponsored by Lanzhou Institute of Chemical Physics, Chinese Academy of Sciences, under the supervision of Chinese Academy of Sciences, and published by Science Publishing House, which is a scholarly journal openly circulated both at home and abroad. The journal mainly reports the latest progress and research results on molecular catalysis. It contains academic papers, research briefs, research reports and progress reviews. The content focuses on coordination catalysis, enzyme catalysis, light-ribbed catalysis, stereochemistry in catalysis, catalytic reaction mechanism and kinetics, the study of catalyst surface states and the application of quantum chemistry in catalysis. We also provide contributions on the activation, deactivation and regeneration of homogeneous catalysts, solidified homogeneous catalysts and solidified enzyme catalysts in industrial catalytic processes, as well as on the optimisation and characterisation of catalysts for new catalytic processes.
The main target readers are scientists and postgraduates working in catalysis in research institutes, industrial and mining enterprises, as well as teachers and students of chemistry and chemical engineering departments in colleges and universities. Contributions from related professionals are welcome.