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通过中和剂、有机酸和渗透压抑制代谢工程改造的大肠杆菌中琥珀酸的产生。

Inhibition of succinic acid production in metabolically engineered Escherichia coli by neutralizing agent, organic acids, and osmolarity.

作者信息

Andersson Christian, Helmerius Jonas, Hodge David, Berglund Kris A, Rova Ulrika

机构信息

Div. of Biochemical and Chemical Process Engineering, Luleå University of Technology, SE-97187, Luleå, Sweden.

出版信息

Biotechnol Prog. 2009 Jan-Feb;25(1):116-23. doi: 10.1002/btpr.127.

Abstract

The economical viability of biochemical succinic acid production is a result of many processing parameters including final succinic acid concentration, recovery of succinate, and the volumetric productivity. Maintaining volumetric productivities >2.5 g L(-1) h(-1) is important if production of succinic acid from renewable resources should be competitive. In this work, the effects of organic acids, osmolarity, and neutralizing agent (NH4OH, KOH, NaOH, K2CO3, and Na2CO3), and Na2CO3) on the fermentative succinic acid production by Escherichia coli AFP184 were investigated. The highest concentration of succinic acid, 77 g L(-1), was obtained with Na2CO3. In general, irrespective of the base used, succinic acid productivity per viable cell was significantly reduced as the concentration of the produced acid increased. Increased osmolarity resulting from base addition during succinate production only marginally affected the productivity per viable cell. Addition of the osmoprotectant glycine betaine to cultures resulted in an increased aerobic growth rate and anaerobic glucose consumption rate, but decreased succinic acid yield. When using NH4OH productivity completely ceased at a succinic acid concentration of approximately 40 g L(-1). Volumetric productivities remained at 2.5 g L(-1) h(-1) for up to 10 h longer when K- or Na-bases where used instead of NH4OH. The decrease in cellular succinic acid productivity observed during the anaerobic phase was found to be due to increased organic acid concentrations rather than medium osmolarity.

摘要

生化法生产琥珀酸的经济可行性取决于许多工艺参数,包括最终琥珀酸浓度、琥珀酸盐的回收率和体积产率。如果利用可再生资源生产琥珀酸要具有竞争力,保持体积产率>2.5 g L(-1) h(-1)很重要。在本研究中,考察了有机酸、渗透压以及中和剂(NH4OH、KOH、NaOH、K2CO3和Na2CO3)对大肠杆菌AFP184发酵生产琥珀酸的影响。使用Na2CO3时获得了最高的琥珀酸浓度,为77 g L(-1)。一般来说,无论使用何种碱,随着所产酸浓度的增加,每个活细胞的琥珀酸生产率都会显著降低。琥珀酸生产过程中因添加碱导致的渗透压升高仅对每个活细胞的生产率产生轻微影响。向培养物中添加渗透保护剂甘氨酸甜菜碱会使需氧生长速率和厌氧葡萄糖消耗速率增加,但琥珀酸产量降低。使用NH4OH时,在琥珀酸浓度约为40 g L(-1)时生产率完全停止。使用K碱或Na碱代替NH4OH时,体积产率可在2.5 g L(-1) h(-1)保持长达10小时以上。厌氧阶段观察到的细胞琥珀酸生产率下降是由于有机酸浓度增加而非培养基渗透压所致。

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