Design and thermodynamic analysis of a pathway enabling anaerobic production of poly-3-hydroxybutyrate in Escherichia coli

• Published in: Synthetic and systems biotechnology Vol. 8; no. 4; pp. 629 - 639
• Main Authors: Olavarria, Karel, Becker, Marco V., Sousa, Diana Z., van Loosdrecht, Mark C.M., Wahl, S. Aljoscha
• Format: Journal Article
• Language: English
• Published: Elsevier B.V 01.12.2023; KeAi Publishing; KeAi Communications Co., Ltd
• Subjects: Anaerobic metabolism; Engineered pathways; Metabolite concentrations; Original; Pathway feasibility analysis; Protein cost; Anaerobic metabolism; Engineered pathways; Protein cost; Metabolite concentrations; Pathway feasibility analysis
• ISSN: 2405-805X; 2405-805X
• DOI: 10.1016/j.synbio.2023.09.005

Utilizing anaerobic metabolisms for the production of biotechnologically relevant products presents potential advantages, such as increased yields and reduced energy dissipation. However, lower energy dissipation may indicate that certain reactions are operating closer to their thermodynamic equilibrium. While stoichiometric analyses and genetic modifications are frequently employed in metabolic engineering, the use of thermodynamic tools to evaluate the feasibility of planned interventions is less documented. In this study, we propose a novel metabolic engineering strategy to achieve an efficient anaerobic production of poly-(R)-3-hydroxybutyrate (PHB) in the model organism Escherichia coli. Our approach involves re-routing of two-thirds of the glycolytic flux through non-oxidative glycolysis and coupling PHB synthesis with NADH re-oxidation. We complemented our stoichiometric analysis with various thermodynamic approaches to assess the feasibility and the bottlenecks in the proposed engineered pathway. According to our calculations, the main thermodynamic bottleneck are the reactions catalyzed by the acetoacetyl-CoA β-ketothiolase (EC 2.3.1.9) and the acetoacetyl-CoA reductase (EC 1.1.1.36). Furthermore, we calculated thermodynamically consistent sets of kinetic parameters to determine the enzyme amounts required for sustaining the conversion fluxes. In the case of the engineered conversion route, the protein pool necessary to sustain the desired fluxes could account for 20% of the whole cell dry weight.