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采用两段式溶解氧控制策略提高米根霉产富马酸。

Enhancement of fumaric acid production by Rhizopus oryzae using a two-stage dissolved oxygen control strategy.

机构信息

College of Biotechnology and Pharmaceutical Engineering, State Key Laboratory of Materials-Oriented Chemical Engineering, Nanjing University of Technology, Nanjing 210009, People's Republic of China.

出版信息

Appl Biochem Biotechnol. 2010 Oct;162(4):1031-8. doi: 10.1007/s12010-009-8831-5. Epub 2009 Nov 21.

Abstract

Batch fermentative production of fumaric acid by Rhizopus oryzae ME-F12 was investigated in a 7-l stirred tank fermentor under different dissolved oxygen (DO) concentrations. High fumaric acid yield on glucose (0.56 g/g) was achieved under high DO concentration (80%), but the glucose consumption rate and fumaric acid productivity were rather low (0.91 and 0.51 g/l/h). Fumaric acid productivity was enhanced under low DO concentration (30%), but the fuamric acid yield on glucose decreased to 0.52 g/g. In order to achieve the high fumaric acid yield and productivity simultaneously, a two-stage dissolved oxygen control strategy was proposed, in which the DO concentration was controlled at 80% in the first 18 h and then switched to 30%. This was experimentally proven to be successful. Relatively high fumaric acid production (56.2 g/l), high fumaric acid yield on glucose (0.54 g/g), and high glucose consumption rate (1.3 g/l/h) were achieved by applying this strategy. The productivity (0.7 g/l/h) was improved by 37%, 21%, and 9%, respectively, compared with fermentations in which DO concentrations were kept constant at 80%, 60%, and 30%.

摘要

摇瓶发酵生产富马酸的研究在不同的溶解氧(DO)浓度下进行了米根霉 ME-F12。在高 DO 浓度(80%)下,葡萄糖的富马酸产量很高(0.56 g/g),但葡萄糖消耗率和富马酸得率都相当低(0.91 和 0.51 g/l/h)。在低 DO 浓度(30%)下,富马酸的得率有所提高,但葡萄糖的富马酸得率下降到 0.52 g/g。为了同时获得高的富马酸得率和得率,提出了一种两阶段溶氧控制策略,即在最初的 18 h 内将 DO 浓度控制在 80%,然后切换到 30%。实验证明这是成功的。通过应用这种策略,实现了相对较高的富马酸产量(56.2 g/l)、较高的葡萄糖富马酸得率(0.54 g/g)和较高的葡萄糖消耗率(1.3 g/l/h)。与 DO 浓度分别保持在 80%、60%和 30%的发酵相比,生产力(0.7 g/l/h)分别提高了 37%、21%和 9%。

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