Fatma Zia, Hartman Hassan, Poolman Mark G, Fell David A, Srivastava Shireesh, Shakeel Tabinda, Yazdani Syed Shams
Microbial Engineering Group, International Centre for Genetic Engineering and Biotechnology, New Delhi, India; DBT-ICGEB Centre for Advanced Bioenergy Research, International Centre for Genetic Engineering and Biotechnology, New Delhi, India.
Department of Biological and Medical Sciences, Oxford Brookes University, Oxford, UK.
Metab Eng. 2018 Mar;46:1-12. doi: 10.1016/j.ymben.2018.01.002. Epub 2018 Feb 3.
Biologically-derived hydrocarbons are considered to have great potential as next-generation biofuels owing to the similarity of their chemical properties to contemporary diesel and jet fuels. However, the low yield of these hydrocarbons in biotechnological production is a major obstacle for commercialization. Several genetic and process engineering approaches have been adopted to increase the yield of hydrocarbon, but a model driven approach has not been implemented so far. Here, we applied a constraint-based metabolic modeling approach in which a variable demand for alkane biosynthesis was imposed, and co-varying reactions were considered as potential targets for further engineering of an E. coli strain already expressing cyanobacterial enzymes towards higher chain alkane production. The reactions that co-varied with the imposed alkane production were found to be mainly associated with the pentose phosphate pathway (PPP) and the lower half of glycolysis. An optimal modeling solution was achieved by imposing increased flux through the reaction catalyzed by glucose-6-phosphate dehydrogenase (zwf) and iteratively removing 7 reactions from the network, leading to an alkane yield of 94.2% of the theoretical maximum conversion determined by in silico analysis at a given biomass rate. To validate the in silico findings, we first performed pathway optimization of the cyanobacterial enzymes in E. coli via different dosages of genes, promoting substrate channelling through protein fusion and inducing substantial equivalent protein expression, which led to a 36-fold increase in alka(e)ne production from 2.8 mg/L to 102 mg/L. Further, engineering of E. coli based on in silico findings, including biomass constraint, led to an increase in the alka(e)ne titer to 425 mg/L (major components being 249 mg/L pentadecane and 160 mg/L heptadecene), a 148.6-fold improvement over the initial strain, respectively; with a yield of 34.2% of the theoretical maximum. The impact of model-assisted engineering was also tested for the production of long chain fatty alcohol, another commercially important molecule sharing the same pathway while differing only at the terminal reaction, and a titer of 1506 mg/L was achieved with a yield of 86.4% of the theoretical maximum. Moreover, the model assisted engineered strains had produced 2.54 g/L and 12.5 g/L of long chain alkane and fatty alcohol, respectively, in the bioreactor under fed-batch cultivation condition. Our study demonstrated successful implementation of a combined in silico modeling approach along with the pathway and process optimization in achieving the highest reported titers of long chain hydrocarbons in E. coli.
由于生物衍生的碳氢化合物的化学性质与当代柴油和喷气燃料相似,它们被认为具有作为下一代生物燃料的巨大潜力。然而,这些碳氢化合物在生物技术生产中的低产量是商业化的主要障碍。已经采用了几种基因和过程工程方法来提高碳氢化合物的产量,但到目前为止尚未实施基于模型驱动的方法。在这里,我们应用了一种基于约束的代谢建模方法,其中对烷烃生物合成施加了可变需求,并将共变反应视为进一步工程改造已经表达蓝细菌酶以提高高链烷烃产量的大肠杆菌菌株的潜在目标。发现与施加的烷烃生产共变的反应主要与磷酸戊糖途径(PPP)和糖酵解的下半部分相关。通过增加由葡萄糖-6-磷酸脱氢酶(zwf)催化的反应通量并从网络中迭代去除7个反应,实现了最佳建模解决方案,在给定生物量速率下,烷烃产量达到了计算机模拟分析确定的理论最大转化率的94.2%。为了验证计算机模拟结果,我们首先通过不同剂量的基因对大肠杆菌中的蓝细菌酶进行途径优化,通过蛋白质融合促进底物通道化并诱导大量等效蛋白质表达,这导致烷烃产量从2.8 mg/L增加到102 mg/L,增加了36倍。此外,基于计算机模拟结果对大肠杆菌进行工程改造,包括生物量约束,导致烷烃滴度增加到425 mg/L(主要成分是249 mg/L十五烷和160 mg/L十七烯),分别比初始菌株提高了148.6倍;产率为理论最大值的34.2%。还测试了模型辅助工程对长链脂肪醇生产的影响,长链脂肪醇是另一种商业上重要的分子,共享相同的途径但仅在末端反应上有所不同,实现了1506 mg/L的滴度,产率为理论最大值的86.4%。此外,在补料分批培养条件下,模型辅助工程改造的菌株在生物反应器中分别产生了2.54 g/L和12.5 g/L的长链烷烃和脂肪醇。我们的研究表明,成功实施了计算机模拟建模方法与途径和过程优化相结合的方法,以实现大肠杆菌中报道的最高长链碳氢化合物滴度。