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指数补料分批培养作为恒化器的替代方法:重组大肠杆菌生产青霉素酰化酶的案例

Exponentially fed-batch cultures as an alternative to chemostats: the case of penicillin acylase production by recombinant E. coli.

作者信息

Ramírez O T, Zamora R, Quintero R, López-Munguía A

机构信息

Departamento de Bioingeniería, Universidad Nacional Autónoma de México, Cuernavaca, Morelos.

出版信息

Enzyme Microb Technol. 1994 Oct;16(10):895-903. doi: 10.1016/0141-0229(94)90065-5.

Abstract

Exponentially fed-batch cultures (EFBCs), fed with medium containing a highly concentrated carbon source, are commonly employed for attainment of high cell densities. However, large variations in environmental conditions occur, and quasi-steady-state is usually achieved only for the limiting substrate concentration, restricting the use of such cultures in kinetic characterization studies. In this work we report the production of recombinant penicillin acylase (PA) in EFBC of an E. coli JM101 transformed with the pPA102 plasmid, which includes the PA gene under regulation of the lacZ gene promoter and using isopropyl-beta-thio-galactopyranoside (IPTG) as inducer. The culture was fed with nonconcentrated complete medium, resulting in the attainment of quasi-steady-state conditions not only in substrate concentration, but also in cell concentration, and in the specific rates of growth, product production, and substrate consumption. Similar transient behavior was observed between EFBC and chemostat results. At quasi-steady-state, the dilution rate in the EFBC equaled the growth rate. Specific PA production rate during the fed-batch phase remained relatively constant at each dilution rate and followed typical Luedeking-Piret kinetics, with growth-associated and non-growth-associated constants of 142 U gDCW-1 and 7.2 U gDCW-1 h-1, respectively. Specific glucose consumption rate linearly increased from 0.025 to 0.6 g gDCW-1 h-1 as the dilution rate increased from 0.01 to 0.35 h-1. The maximum specific PA activity increased with decreasing dilution rate, reaching its highest value of 2.0 U mg-1 at a dilution rate of 0.01 h-1, the lowest dilution tested.(ABSTRACT TRUNCATED AT 250 WORDS)

摘要

指数流加培养(EFBCs)通过添加含有高浓度碳源的培养基来进行,常用于获得高细胞密度。然而,环境条件会出现很大变化,通常仅在限制性底物浓度方面能达到准稳态,这限制了此类培养在动力学表征研究中的应用。在本研究中,我们报道了用pPA102质粒转化的大肠杆菌JM101在EFBC中生产重组青霉素酰化酶(PA)的情况,该质粒包含在lacZ基因启动子调控下的PA基因,并使用异丙基-β-硫代半乳糖苷(IPTG)作为诱导剂。培养过程中添加的是非浓缩完全培养基,结果不仅在底物浓度方面,而且在细胞浓度以及生长、产物合成和底物消耗的比速率方面都达到了准稳态条件。在EFBC和恒化器结果之间观察到了相似的瞬态行为。在准稳态时,EFBC中的稀释率等于生长速率。在每个稀释率下,补料分批阶段的PA比生产速率保持相对恒定,并遵循典型的Luedeking-Piret动力学,生长相关和非生长相关常数分别为142 U gDCW-1和7.2 U gDCW-1 h-1。随着稀释率从0.01 h-1增加到0.35 h-1,葡萄糖比消耗速率从0.025线性增加到0.6 g gDCW-1 h-1。最大比PA活性随着稀释率的降低而增加,在0.01 h-1(测试的最低稀释率)时达到最高值2.0 U mg-1。(摘要截短于250字)

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