Center for Process Biotechnology, Department of Biotechnology, Block 223, Technical University of Denmark, DK-2800 Lyngby, Denmark.
Biotechnol Bioeng. 1997 Jul 20;55(2):447-54. doi: 10.1002/(SICI)1097-0290(19970720)55:2<447::AID-BIT22>3.0.CO;2-C.
Overexpression of the homologous protein proteinase A (PrA) in Saccharomyces cerevisiae has been achieved by inserting the PrA gene (PEP4) with its own promoter on a 2mu multicopy plasmid. With this system the specific PrA production rate was found to be described well by a linear function of the oxidative glucose metabolism, the reductive glucose metabolism, and the oxidative ethanol metabolism, with a significant lower yield resulting from the reductive glucose metabolism compared with the oxidative glucose metabolism. To describe the experimental data, a simple mathematical model has been set up. The model is based on an assumption of a limited respiratory capacity as suggested by Sonnleitner and Käppeli but extended to describe production of an extracellular protein. The model predicts correctly the critical dilution rate to be between 0.15 and 0.16 h(-1), the decrease in the biomass yield above the critical dilution rate, and the production of proteinase A at different dilution rates. Both the experimental data and model simulations suggest that the optimum operating conditions for protein production is just at the critical dilution rate. (c) 1997 John Wiley & Sons, Inc. Biotechnol Bioeng 55: 447-454, 1997.
在酿酒酵母中通过将带有自身启动子的蛋白水解酶 A(PrA)基因(PEP4)插入 2μ多拷贝质粒来实现同源蛋白的过表达。使用该系统,发现 PrA 的特定生产速率很好地由氧化葡萄糖代谢、还原葡萄糖代谢和氧化乙醇代谢的线性函数来描述,与氧化葡萄糖代谢相比,还原葡萄糖代谢导致的产率显著降低。为了描述实验数据,建立了一个简单的数学模型。该模型基于 Sonnleitner 和 Käppeli 提出的呼吸能力有限的假设,但扩展到描述胞外蛋白的生产。该模型正确预测了临界稀释率在 0.15 到 0.16 h(-1)之间,高于临界稀释率时生物量产率下降,以及在不同稀释率下生产蛋白水解酶 A。实验数据和模型模拟均表明,蛋白质生产的最佳操作条件刚好在临界稀释率。(c)1997 年 John Wiley & Sons,Inc.《生物工程学报》55:447-454,1997 年。