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利用微滤生物反应器在大肠杆菌中有效生产来自嗜热栖热菌的耐热α-葡萄糖苷酶。

Effective production of a thermostable alpha-glucosidase from Sulfolobus solfataricus in Escherichia coli exploiting a microfiltration bioreactor.

作者信息

Schiraldi C, Martino A, Acone M, Di Lernia I, Di Lazzaro A, Marulli F, Generoso M, Cartenì M, De Rosa M

机构信息

CRIB-Istituto di Farmacologia e Tossicologia, II Università degli Studi di Napoli, Facoltà di Medicina e Chirurgia, Via Costantinopoli 16-80138 Napoli, Italy.

出版信息

Biotechnol Bioeng. 2000 Dec 20;70(6):670-6. doi: 10.1002/1097-0290(20001220)70:6<670::aid-bit9>3.0.co;2-7.

Abstract

A microfiltration (MF) membrane bioreactor was developed for an efficient production of a recombinant thermostable alpha-glucosidase (rSsGA) from Sulfolobus solfataricus MT-4. The aim of the membrane bioreactor was to improve the control of the concentration of key components in the growth of genetic engineered microorganisms, such as Escherichia coli. The influence of medium composition was studied in relation to cell growth and alpha-glucosidase production. The addition of components such as yeast extract and tryptone resulted in a higher enzyme production. High cell density cultivation of E. coli BL21(DE3) on semidefined medium, exploiting a microfiltration bioreactor, was studied in order to optimize rSsGA production. In addition to medium composition, the inducer employed (either isopropyl beta-D-thiogalactopyranoside or lactose), the induction duration, and the cultivation mode influenced both the final biomass and the enzyme yield. The MF bioreactor allowed a cell concentration of 50 g/L dry weight and a corresponding alpha-glucosidase production of 11,500 U/L. The improvement obtained in the enzyme production combining genetic engineering and the microfiltration strategy was estimated to be 2,000-fold the wild-type strain.

摘要

开发了一种微滤(MF)膜生物反应器,用于高效生产来自嗜热栖热菌MT-4的重组热稳定α-葡萄糖苷酶(rSsGA)。该膜生物反应器的目的是改善对基因工程微生物(如大肠杆菌)生长过程中关键成分浓度的控制。研究了培养基组成对细胞生长和α-葡萄糖苷酶生产的影响。添加酵母提取物和胰蛋白胨等成分可提高酶的产量。利用微滤生物反应器,在半限定培养基上对大肠杆菌BL21(DE3)进行高细胞密度培养,以优化rSsGA的生产。除了培养基组成外,所使用的诱导剂(异丙基β-D-硫代半乳糖苷或乳糖)、诱导持续时间和培养模式都会影响最终生物量和酶产量。该MF生物反应器的细胞浓度可达50 g/L干重,相应的α-葡萄糖苷酶产量为11500 U/L。结合基因工程和微滤策略,酶产量的提高估计是野生型菌株的2000倍。

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