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Coenzyme Q production in a 150-l reactor by a mutant strain of Rhodobacter sphaeroides

机译:球形球形假单胞菌突变菌株在150升反应器中生产辅酶Q

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For the commercial production of CoQ, batch-type fermentations were attempted in a 150-l fermenter using a mutant strain of R. sphaeroides. Optimum temperature and initial aeration rate were found to be 30pC and 2 vvm, respectively. Under optimum fermentation conditions, the maximum value of specific CoQ content was achieved reproducibly as 6.34 mg/g DCW after 24 h, with 3.02 g/l of DCW. During the fermentation, aeration shift (from the adequate aeration at the early growth phase to the limited aeration in active cellular metabolism) was a key factor in CoQ production for scale-up. A higher value of the specific CoQ content (8.12 mg/g DCW) was achieved in fed-batch fermentation and comparable to those produced by the pilot-scale fed-batch fermentations of A. tumefaciens, which indicated that the mutant strain of R. sphaeroides used in this study was a potential high CoQ producer. This is the first detailed study to demonstrate a pilot-scale production of CoQ using a mutant strain of R. sphaeroides.
机译:为了商业生产辅酶Q,尝试使用球形芽孢杆菌的突变株在150升发酵罐中进行分批发酵。最佳温度和初始曝气速率分别为30pC和2 vvm。在最佳发酵条件下,24小时后可再生的特定辅酶QQ最大值达到6.34 mg / g DCW,其中DCW为3.02 g / l。在发酵过程中,通气量的变化(从早期生长阶段的通气量到活跃的细胞代谢中有限的通气量)是扩大辅酶Q产量的关键因素。分批补料发酵获得的特定辅酶Q含量较高(8.12 mg / g DCW),与根癌农杆菌的中试分批补料发酵产生的值相当,这表明R.本研究中所用的六溴化物是潜在的高辅酶Q生产者。这是第一个详细的研究,以证明使用球形红球菌的突变菌株进行辅酶Q的中试规模生产。

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