Ni Hui, Hong Qinglin, Xiao Anfeng, Li Lijun, Cai Huinong, Su Wenjin
College of Bioengineering, Jimei University, Xiamen 361021, China
Sheng Wu Gong Cheng Xue Bao. 2011 Jul;27(7):1065-75.
We evaluated an astaxanthin overproducing Phaffia rhodozyma JMU-MVP14, and developed astaxanthin high-yielding fermentation process. We analyzed several fermentation parameters, i.e., biomass, astaxanthin and total carotenoids content to compare the characteristics of P rhodozyma JMU-MVP14 and the original strain through flask fermentation experiments. We conducted batch and fed-batch fermentation experiments in 7 L fermentor to investigate the effects of pH controlling models and feeding medium compositions on the production of astaxanthin. We further evaluated the capability and practical value of P rhodozyma JMU-MVP14 by fed-batch cultivation in the 1 m3 fermentor. Flask fermentation experiments revealed that P. rhodozyma JMU-MVP14 produced high yield of astaxanthin and carotenoids with specific productivity of astaxanthin and specific productivity of total carotenoids of 6.01 mg/g and 10.38 mg/g. Results of batch culture experiments in the 7 L fermentor showed that controlling the pH by ammonia auto-feeding was better than discontinuously adjusting pH value at 6.0 with regard to the high productivities of biomasses and astaxanthin. This P. rhodozyma strain synthesized astaxanthin partially linked to the growth with the Ks and pmax of 0.20 h ' and 21.73 g/L, respectively. Results of batch-fed fermentations in 7 L fermentor indicated that the complex feeding medium consisted of 50% glucose, 0.5% yeast extract and 0.3% corn steep syrup had lower astaxanthin productivity than the simple feeding medium containing only 50% glucose, which produced biomass, volumetric productivity of astaxanthin, volumetric productivity of total carotenoids, specific productivity of astaxanthin and total carotenoids at 32.81 g/L, 155.99 mg/L, 4.94 mg/g, 399.99 mg/L and 12.19 mg/g, respectively. As fed-batch cultured in 1 m3 fermentor, P rhodozyma JMU-MVP14 yielded 85.11 g/L of biomass, 279.96 mg/L of volumetric productivity of astaxanthin, 618.01 mg/L of volumetric productivity of total carotenoids, 3.29 mg/g of specific productivity of astaxanthin and 7.26 mg/g of specific productivity of total carotenoids. Additionally, P rhodozyma JMU-MVP14 cell contained 21.54% of protein, 41.34% of carbohydrate and 34.31% of lipid. These comprehensive results suggest that P. rhodozyma JMU-MVPl14 has great practical prosperity related to its strong ability to produce astaxanthin and good value byproducts.
我们评估了虾青素高产的红发夫酵母JMU-MVP14,并开发了虾青素高产发酵工艺。我们分析了几个发酵参数,即生物量、虾青素和总类胡萝卜素含量,通过摇瓶发酵实验比较红发夫酵母JMU-MVP14与原始菌株的特性。我们在7 L发酵罐中进行了分批和补料分批发酵实验,以研究pH控制模式和补料培养基组成对虾青素生产的影响。我们通过在1 m³发酵罐中进行补料分批培养,进一步评估了红发夫酵母JMU-MVP14的能力和实用价值。摇瓶发酵实验表明,红发夫酵母JMU-MVP14虾青素和类胡萝卜素产量高,虾青素比生产速率和总类胡萝卜素比生产速率分别为6.01 mg/g和10.38 mg/g。7 L发酵罐中的分批培养实验结果表明,就生物量和虾青素的高生产率而言,通过氨自动补料控制pH比在6.0间断调节pH值更好。该红发夫酵母菌株合成的虾青素部分与生长相关,Ks和pmax分别为0.20 h⁻¹和21.73 g/L。7 L发酵罐中的分批补料发酵结果表明,由50%葡萄糖、0.5%酵母提取物和0.3%玉米浆组成的复合补料培养基的虾青素生产率低于仅含50%葡萄糖的简单补料培养基,后者产生的生物量、虾青素体积生产率、总类胡萝卜素体积生产率、虾青素比生产速率和总类胡萝卜素比生产速率分别为32.81 g/L、155.99 mg/L、4.94 mg/g、399.99 mg/L和12.19 mg/g。在1 m³发酵罐中进行补料分批培养时,红发夫酵母JMU-MVP14的生物量产量为85.11 g/L,虾青素体积生产率为279.96 mg/L,总类胡萝卜素体积生产率为618.01 mg/L,虾青素比生产速率为3.29 mg/g,总类胡萝卜素比生产速率为7.26 mg/g。此外,红发夫酵母JMU-MVP14细胞含有21.54%的蛋白质、41.34%的碳水化合物和34.31%的脂质。这些综合结果表明,红发夫酵母JMU-MVP14因其强大的虾青素生产能力和良好的副产物价值而具有巨大实用前景。