The native ability of Clostridium thermocellum to efficiently solubilize cellulose makes it an interesting platform for sustainable biofuel production through consolidated bioprocessing. Together with other improvements, industrial implementation of C. thermocellum, as well as fundamental studies into its metabolism, would benefit from improved and reproducible consumption of hexose sugars. To investigate growth of C. thermocellum on glucose or fructose, as well as the underlying molecular mechanisms, laboratory evolution was performed in carbon-limited chemostats with increasing concentrations of glucose or fructose and decreasing cellobiose concentrations. Growth on both glucose and fructose was achieved with biomass yields of 0.09 ± 0.00 and 0.18 ± 0.00 gbiomass gsubstrate−1, respectively, compared to 0.15 ± 0.01 gbiomass gsubstrate−1 for wild type on cellobiose. Single-colony isolates had no or short lag times on the monosaccharides, whilst wild type showed 42 ± 4 hours on glucose and >80 hours on fructose. With good growth on glucose, fructose, and cellobiose, the fructose isolates were chosen for genome sequence-based reverse metabolic engineering. Deletion of a putative transcriptional regulator (Clo1313_1831), which upregulated fructokinase activity, reduced lag time on fructose to 12 hours with a growth rate of 0.11 ± 0.01 h−1 and resulted in immediate growth on glucose at 0.24 ± 0.01 h−1. Additional introduction of a cbpAG148V mutation resulted in immediate growth on fructose at 0.32 ± 0.03 h−1. These insights can guide engineering of strains for fundamental studies into transport and the upper glycolysis, as well as maximizing product yields in industrial settings. Importance. C. thermocellum is an important candidate for sustainable and cost-effective production of bioethanol through consolidated bioprocessing. In addition to unsurpassed cellulose deconstruction, industrial application and fundamental studies would benefit from improvement of glucose and fructose consumption. This study demonstrated that C. thermocellum can be evolved for reproducible constitutive growth on glucose or fructose. Subsequent genome sequencing, gene editing and physiological characterization identified two underlying mutations with a role in (regulation of) transport or metabolism of the hexose sugars. In light of these findings, such mutations have likely (and unknowingly) also occurred in previous studies with C. thermocellum using hexose-based media with possible broad regulatory consequences. By targeted modification of these genes, industrial and research strains of C. thermocellum can be engineered to i) reduce glucose accumulation, ii) study cellodextrin transport systems in vivo, iii) allow experiments at >120 g L−1 soluble substrate concentration, or iv) reduce costs for labelling studies.
The atypical glycolysis of Clostridium thermocellum is characterized by the use of pyrophosphate (PP i ) as phosphoryl donor for phosphofructokinase (Pfk) and pyruvate phosphate dikinase (Ppdk) reactions. Previously, biosynthetic PP i was calculated to be stoichiometrically insufficient to drive glycolysis. This study investigates the role of a H + -pumping membrane-bound pyrophosphatase, glycogen cycling, a predicted Ppdk–malate shunt cycle and acetate cycling in generating PP i . Knockout studies and enzyme assays confirmed that clo1313_0823 encodes a membrane-bound pyrophosphatase. Additionally, clo1313_0717-0718 was confirmed to encode ADP-glucose synthase by knockouts, glycogen measurements in C. thermocellum and heterologous expression in E. coli . Unexpectedly, individually-targeted gene deletions of the four putative PP i sources did not have a significant phenotypic effect. Although combinatorial deletion of all four putative PP i sources reduced the growth rate by 22% (0.30±0.01 h −1 ) and the biomass yield by 38% (0.18±0.00 g biomass g substrate −1 ), this change was much smaller than what would be expected for stoichiometrically essential PP i -supplying mechanisms. Growth-arrested cells of the quadruple knockout readily fermented cellobiose indicating that the unknown PP i -supplying mechanisms are independent of biosynthesis. An alternative hypothesis that ATP-dependent Pfk activity circumvents a need for PP i altogether, was falsified by enzyme assays, heterologous expression of candidate genes and whole-genome sequencing. As a secondary outcome, enzymatic assays confirmed functional annotation of clo1313_1832 as ATP- and GTP-dependent fructokinase. These results indicate that the four investigated PP i sources individually and combined play no significant PP i -supplying role and the true source(s) of PP i , or alternative phosphorylating mechanisms, that drive glycolysis in C. thermocellum remain(s) elusive. IMPORTANCE Increased understanding of the central metabolism of C. thermocellum is important from a fundamental as well as from a sustainability and industrial perspective. In addition to showing that H + -pumping membrane-bound PPase, glycogen cycling, a Ppdk–malate shunt cycle, and acetate cycling are not significant sources of PP i supply, this study adds functional annotation of four genes and availability of an updated PP i stoichiometry from biosynthesis to the scientific domain. Together, this aids future metabolic engineering attempts aimed to improve C. thermocellum as a cell factory for sustainable and efficient production of ethanol from lignocellulosic material through consolidated bioprocessing with minimal pretreatment. Getting closer to elucidating the elusive source of PP i , or alternative phosphorylating mechanisms, for the atypical glycolysis is itself of fundamental importance. Additionally, the findings of this study directly contribute to investigations into trade-offs between thermodynamic driving force versus energy yield of PP i - and ATP-dependent glycolysis.
Background Clostridium thermocellum is a promising candidate for consolidated bioprocessing of lignocellulosic biomass to ethanol. The low ethanol tolerance of this microorganism is one of the remaining obstacles to industrial implementation. Ethanol inhibition can be caused by end-product inhibition and/or chaotropic-induced stress resulting in increased membrane fluidization and disruption of macromolecules. The highly reversible glycolysis of C. thermocellum might be especially sensitive to end-product inhibition. The chaotropic effect of ethanol is known to increase with temperature. This study explores the relative contributions of these two aspects to investigate and possibly mitigate ethanol-induced stress in growing and non-growing C. thermocellum cultures. Results To separate chaotropic from thermodynamic effects of ethanol toxicity, a non-ethanol producing strain AVM062 (Pclo1313_2638::ldh* ∆adhE) was constructed by deleting the bifunctional acetaldehyde/alcohol dehydrogenase gene, adhE, in a lactate-overproducing strain. Exogenously added ethanol lowered the growth rate of both wild-type and the non-ethanol producing mutant. The mutant strain grew quicker than the wild-type at 50 and 55 °C for ethanol concentrations ≥ 10 g L−1 and was able to reach higher maximum OD600 at all ethanol concentrations and temperatures. For the wild-type, the maximum OD600 and relative growth rates were higher at 45 and 50 °C, compared to 55 °C, for ethanol concentrations ≥ 15 g L−1. For the mutant strain, no positive effect on growth was observed at lower temperatures. Growth-arrested cells of the wild-type demonstrated improved fermentative capacity over time in the presence of ethanol concentrations up to 40 g L−1 at 45 and 50 °C compared to 55 °C. Conclusion Positive effects of temperature on ethanol tolerance were limited to wild-type C. thermocellum and are likely related to mechanisms involved in the ethanol-formation pathway and redox cofactor balancing. Lowering the cultivation temperature provides an attractive strategy to improve growth and fermentative capacity at high ethanol titres in high-cellulose loading batch cultivations. Finally, non-ethanol producing strains are useful platform strains to study the effects of chaotropicity and thermodynamics related to ethanol toxicity and allow for deeper understanding of growth and/or fermentation cessation under industrially relevant conditions.
Clostridium thermocellumis a cellulolytic thermophile considered for consolidated bioprocessing of lignocellulose to ethanol. Improvements in ethanol yield are required for industrial implementation, but incompletely understood causes of amino acid secretion impede progress. In this study, amino acid secretion was investigated by gene deletions in ammonium-regulated NADPH-supplying and -consuming pathways and physiological characterization in cellobiose- or ammonium-limited chemostats. First, the contribution of the NADPH-supplying malate shunt was studied with strains using either the NADPH-yielding malate shunt (Δppdk) or redox-independent conversion of PEP to pyruvate (ΔppdkΔmalE::Peno-pyk). In the latter, branched-chain amino acids, especially valine, were significantly reduced, whereas the ethanol yield increased 46-60%, suggesting that secretion of these amino acids balances NADPH surplus from the malate shunt. Unchanged amino acid secretion in Δppdkfalsified a previous hypothesis on ammonium-regulated PEP-to-pyruvate flux redistribution. Possible involvement of another NADPH-supplier, namely NADH-dependent reduced ferredoxin:NADP+oxidoreductase (nfnAB), was also excluded. Finally, deletion of glutamate synthase (gogat) in ammonium assimilation resulted in upregulation of NADPH-linked glutamate dehydrogenase activity and decreased amino acid yields. SincegogatinC. thermocellumis putatively annotated as ferredoxin-linked, which is supported by product redistribution observed in this study, this deletion likely replaced ferredoxin with NADPH in ammonium assimilation. Overall, these findings indicate that a need to reoxidize NADPH is driving the observed amino acid secretion, likely at the expense of NADH needed for ethanol formation. This suggests that metabolic engineering strategies on simplifying redox metabolism and ammonium assimilation can contribute to increased ethanol yields.
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