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大肠杆菌中利用乙酸作为主要碳源合成聚羟基烷酸酯的代谢工程。

Metabolic engineering of Escherichia coli for the synthesis of polyhydroxyalkanoates using acetate as a main carbon source.

机构信息

Beijing Advanced Innovation Center for Soft Matter Science and Engineering, Beijing University of Chemical Technology, Mailbox 53, No. 15 Beisanhuan Donglu, Chaoyang District, Beijing, 100029, China.

Beijing Key Laboratory of Bioprocess, College of Life Science and Technology, Beijing University of Chemical Technology, Beijing, 100029, China.

出版信息

Microb Cell Fact. 2018 Jul 3;17(1):102. doi: 10.1186/s12934-018-0949-0.

DOI:10.1186/s12934-018-0949-0
PMID:29970091
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC6029019/
Abstract

BACKGROUND

High production cost of bioplastics polyhydroxyalkanoates (PHA) is a major obstacle to replace traditional petro-based plastics. To address the challenges, strategies towards upstream metabolic engineering and downstream fermentation optimizations have been continuously pursued. Given that the feedstocks especially carbon sources account up to a large portion of the production cost, it is of great importance to explore low cost substrates to manufacture PHA economically.

RESULTS

Escherichia coli was metabolically engineered to synthesize poly-3-hydroxybutyrate (P3HB), poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (P3HB4HB), and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (PHBV) using acetate as a main carbon source. Overexpression of phosphotransacetylase/acetate kinase pathway was shown to be an effective strategy for improving acetate assimilation and biopolymer production. The recombinant strain overexpressing phosphotransacetylase/acetate kinase and P3HB synthesis operon produced 1.27 g/L P3HB when grown on minimal medium supplemented with 10 g/L yeast extract and 5 g/L acetate in shake flask cultures. Further introduction succinate semialdehyde dehydrogenase, 4-hydroxybutyrate dehydrogenase, and CoA transferase lead to the accumulation of P3HB4HB, reaching a titer of 1.71 g/L with a 4-hydroxybutyrate monomer content of 5.79 mol%. When 1 g/L of α-ketoglutarate or citrate was added to the medium, P3HB4HB titer increased to 1.99 and 2.15 g/L, respectively. To achieve PHBV synthesis, acetate and propionate were simultaneously supplied and propionyl-CoA transferase was overexpressed to provide 3-hydroxyvalerate precursor. The resulting strain produced 0.33 g/L PHBV with a 3-hydroxyvalerate monomer content of 6.58 mol%. Further overexpression of propionate permease improved PHBV titer and 3-hydroxyvalerate monomer content to 1.09 g/L and 10.37 mol%, respectively.

CONCLUSIONS

The application of acetate as carbon source for microbial fermentation could reduce the consumption of food and agro-based renewable bioresources for biorefineries. Our proposed metabolic engineering strategies illustrate the feasibility for producing polyhydroxyalkanoates using acetate as a main carbon source. Overall, as an abundant and renewable resource, acetate would be developed into a cost-effective feedstock to achieve low cost production of chemicals, materials, and biofuels.

摘要

背景

生物塑料聚羟基烷酸酯(PHA)的高生产成本是替代传统石油基塑料的主要障碍。为了解决这些挑战,人们一直在不断寻求上游代谢工程和下游发酵优化策略。鉴于原料,尤其是碳源,占生产成本的很大一部分,因此探索经济实惠的低成本底物来制造 PHA 非常重要。

结果

大肠杆菌被代谢工程改造,以乙酸盐作为主要碳源合成聚-3-羟基丁酸酯(P3HB)、聚(3-羟基丁酸酯-共-4-羟基丁酸酯)(P3HB4HB)和聚(3-羟基丁酸酯-共-3-羟基戊酸酯)(PHBV)。过表达磷酸转乙酰酶/乙酸激酶途径被证明是提高乙酸盐同化和生物聚合物生产的有效策略。在摇瓶培养中,在补充有 10g/L 酵母提取物和 5g/L 乙酸盐的最小培养基上生长时,过表达磷酸转乙酰酶/乙酸激酶和 P3HB 合成操纵子的重组菌株可生产 1.27g/L 的 P3HB。进一步引入琥珀酸半醛脱氢酶、4-羟基丁酸脱氢酶和 CoA 转移酶可导致 P3HB4HB 的积累,其 4-羟基丁酸单体含量达到 5.79mol%,达到 1.71g/L。当向培养基中添加 1g/L 的α-酮戊二酸或柠檬酸盐时,P3HB4HB 的产量分别增加到 1.99 和 2.15g/L。为了实现 PHBV 的合成,同时供应乙酸盐和丙酸盐,并过表达丙酰 CoA 转移酶以提供 3-羟基戊酸前体。所得菌株生产 0.33g/L 的 PHBV,其 3-羟基戊酸单体含量为 6.58mol%。进一步过表达丙酸盐透性酶可提高 PHBV 的产量和 3-羟基戊酸单体含量,分别达到 1.09g/L 和 10.37mol%。

结论

将乙酸盐用作微生物发酵的碳源可以减少生物炼制厂对粮食和农业可再生生物资源的消耗。我们提出的代谢工程策略说明了使用乙酸盐作为主要碳源生产聚羟基烷酸酯的可行性。总的来说,作为一种丰富且可再生的资源,乙酸盐将被开发为一种具有成本效益的原料,以实现化学品、材料和生物燃料的低成本生产。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/fcaf/6029019/8345ef849556/12934_2018_949_Fig7_HTML.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/fcaf/6029019/4775d4007c67/12934_2018_949_Fig3_HTML.jpg
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