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Production of human serum albumin by immobilized yeast.

机译:通过固定酵母生产人血清白蛋白。

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Production of human serum albumin (HSA) in fermentations using the yeast P. pastoris, immobilized in a calcium alginate matrix was explored. HSA, produced by the P. pastoris GS115 Muts strain, was able to diffuse through the calcium alginate gel into the supernatant. The immobilized cell fermentations were conducted in both shake flask and bioreactor scales. The effects of several parameters (bead size, initial cell loading and ratio of immobilized cell beads to liquid medium) were investigated. An automatic data acquisition system and methanol control scheme were developed using a low-cost, automobile exhaust gas analyzer. Mathematical models were also constructed to describe cell growth using glycerol and HSA production during the methanol induction phase.; Glutamate medium was more effective than several other media (BMMY, MMY and MM medium) in stabilizing the calcium alginate immobilized cells. Production of HSA using the glutamate medium during suspended cell fermentation, however, suggested the presence of nutrient limitation. The production of HSA in calcium alginate immobilized cell fermentation was affected by the pH of the liquid medium, and it is hypothesized that electrostatic interactions between HSA and the uronic acids comprising the alginate could inhibit diffusion of HSA out of the immobilized cell beads. Immobilized cells beads were metabolically active in producing HSA, and remained intact for at least 38 days in shake flask fermentation and 17 days in the bioreactor.; Although HSA concentrations in immobilized cell fermentation were less than that in suspended cell fermentation, the maximum specific total protein production rates of immobilized cell and suspended cell fermentations in glutamate medium were comparable, 0.00109 and 0.00148 mg total protein/(mg cell dry weight day), respectively. The maximum specific total protein production rates in both suspended and immobilized cells were not sustained throughout glutamate fermentation presumably due to nutrient limitation. This immobilized fermentation using calcium alginate entrapment seems promising as an alternative means to produce recombinant protein. Further studies to optimize glutamate medium, investigate the pH effect, explore an extended period of fermentation, and examine alternative immobilized reactor types merit consideration.
机译:探索了使用固定在藻酸钙基质中的酵母

P。pastoris 在发酵中生产人血清白蛋白(HSA)的方法。 HSA,由 P产生。巴斯德毕赤酵母GS115 Mut s 菌株能够通过藻酸钙凝胶扩散到上清液中。固定化细胞发酵在摇瓶和生物反应器规模上进行。研究了几个参数的影响(珠大小,初始细胞载量和固定的细胞珠与液体培养基的比例)。使用低成本的汽车尾气分析仪开发了自动数据采集系统和甲醇控制方案。还建立了数学模型来描述在甲醇诱导阶段使用甘油和HSA产生的细胞生长。谷氨酸培养基在稳定藻酸钙固定化细胞方面比其他几种培养基(BMMY,MMY和MM培养基)更有效。然而,在悬浮细胞发酵过程中使用谷氨酸培养基生产HSA,表明存在营养限制。固定于藻酸钙的细胞发酵中HSA的产生受液体培养基的pH值影响,并且假设HSA与包含藻酸盐的糖醛酸之间的静电相互作用可以抑制HSA从固定化的细胞珠中扩散出来。固定的细胞珠在产生HSA中具有代谢活性,在摇瓶发酵中至少保持38天完整,在生物反应器中保持至少17天完整。尽管固定化细胞发酵中的HSA浓度低于悬浮细胞发酵中的HSA浓度,但是固定化细胞和悬浮细胞发酵在谷氨酸培养基中的最大比总蛋白生产率是可比的,分别为0.00109和0.00148 mg总蛋白/(mg细胞干重日) , 分别。在整个谷氨酸发酵过程中,悬浮液和固定化细胞的最大特定总蛋白生产速率均无法维持,这可能是由于营养限制所致。这种利用藻酸钙包埋的固定化发酵有望作为生产重组蛋白的替代手段。进一步研究可优化谷氨酸盐培养基,研究pH值的影响,探索延长的发酵时间,并检查值得考虑的其他固定反应器类型。

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