Jiangfeng Zhu

Replacing Escherichia coli NAD-dependent glyceraldehyde 3-phosphate dehydrogenase (GAPDH) with a NADP-dependent enzyme from Clostridium acetobutylicum facilitates NADPH dependent pathways

Reactions requiring reducing equivalents, NAD(P)H, are of enormous importance for the synthesis of industrially valuable compounds such as carotenoids, polymers, antibiotics and chiral alcohols among others. The use of whole-cell biocatalysis can reduce process cost by acting as catalyst and cofactor regenerator at the same time; however, product yields might be limited by cofactor availability within the cell. Thus, our study focussed on the genetic manipulation of a whole-cell system by modifying metabolic pathways and enzymes to improve the overall production process. In the present work, we genetically engineered an Escherichia coli strain to increase NADPH availability to improve the productivity of products that require NADPH in its biosynthesis. The approach involved an alteration of the glycolysis step where glyceraldehyde-3-phosphate (GAP) is oxidized to 1,3 bisphophoglycerate (1,3-BPG). This reaction is catalyzed by NAD-dependent endogenous glyceraldehyde-3-phosphate dehydrogenase (GAPDH) encoded by the gapA gene. We constructed a recombinant E. coli strain by replacing the native NAD-dependent gapA gene with a NADP-dependent GAPDH from Clostridium acetobutylicum, encoded by the gene gapC. The beauty of this approach is that the recombinant E. coli strain produces 2 mol of NADPH, instead of NADH, per mole of glucose consumed. Metabolic flux analysis showed that the flux through the pentose phosphate (PP) pathway, one of the main pathways that produce NADPH, was reduced significantly in the recombinant strain when compared to that of the parent strain. The effectiveness of the NADPH enhancing system was tested using the production of lycopene and epsilon-caprolactone as model systems using two different background strains. The recombinant strains, with increased NADPH availability, consistently showed significant higher productivity than the parent strains.

Succinate production from different carbon sources under anaerobic conditions by metabolic engineered Escherichia coli strains

Succinic acid has drawn much interest as a precursor of many industrially important chemicals. Using a variety of feedstocks for the bio-production of succinic acid would be economically beneficial to future industrial processes. Escherichia coli SBS550MG is able to grow on both glucose and fructose, but not on sucrose. Therefore, we derived a SBS550MG strain bearing both the pHL413 plasmid, which contains Lactococcus lactis pycA gene, and the pUR400 plasmid, which contains the scrK, Y, A, B, and R genes for sucrose uptake and catalyzation. Succinic acid production by this modified strain and the SBS550pHL413 strain was tested on fructose, sucrose, a mixture of glucose and fructose, a mixture of glucose, fructose and sucrose, and sucrose hydrolysis solution. The modified strain can produce succinic acid efficiently from all combinations of different carbon sources tested with minimal byproduct formation and with high molar succinate yields close to that of the maximum theoretic values. The molar succinic acid yield from fructose was the highest among the carbon sources tested. Using the mixture of glucose and fructose as the carbon source resulted in slightly lower yields and much higher productivity than using fructose alone. Fermenting sucrose mixed with fructose and glucose gave a 1.76-fold higher productivity than that when sucrose was used as the sole carbon source. Using sucrose pretreated with sulfuric acid as carbon source resulted in a similar succinic acid yield and productivity as that when using the mixture of sucrose, fructose, and glucose. The results of the effect of agitation rate in aerobic phase on succinate production showed that supplying large amount of oxygen in aerobic phase resulted in higher productions of formate and acetate, and therefore lower succinate yield. This study suggests that fructose, sucrose, mixture of glucose and fructose, mixture of glucose, fructose and sucrose, or sucrose hydrolysis solution could be used for the economical and efficient production of succinic acid by our metabolic engineered E. coli strain.

Metabolic Flux Analysis of Escherichia coli creB and arcA Mutants Reveals Shared Control of Carbon Catabolism under Microaerobic Growth Conditions

Escherichia coli has several elaborate sensing mechanisms for response to availability of oxygen and other electron acceptors, as well as the carbon source in the surrounding environment. Among them, the CreBC and ArcAB two-component signal transduction systems are responsible for regulation of carbon source utilization and redox control in response to oxygen availability, respectively. We assessed the role of CreBC and ArcAB in regulating the central carbon metabolism of E. coli under microaerobic conditions by means of (13)C-labeling experiments in chemostat cultures of a wild-type strain, DeltacreB and DeltaarcA single mutants, and a DeltacreB DeltaarcA double mutant. Continuous cultures were conducted at D = 0.1 h(-1) under carbon-limited conditions with restricted oxygen supply. Although all experimental strains metabolized glucose mainly through the Embden-Meyerhof-Parnas pathway, mutant strains had significantly lower fluxes in both the oxidative and the nonoxidative pentose phosphate pathways. Significant differences were also found at the pyruvate branching point. Both pyruvate-formate lyase and the pyruvate dehydrogenase complex contributed to acetyl-coenzyme A synthesis from pyruvate, and their activity seemed to be modulated by both ArcAB and CreBC. Strains carrying the creB deletion showed a higher biomass yield on glucose compared to the wild-type strain and its DeltaarcA derivative, which also correlated with higher fluxes from building blocks to biomass. Glyoxylate shunt and lactate dehydrogenase were active mainly in the DeltaarcA strain. Finally, it was observed that the tricarboxylic acid cycle reactions operated in a rather cyclic fashion under our experimental conditions, with reduced activity in the mutant strains.

Heterologous pyc gene expression under various natural and engineered promoters in Escherichia coli for improved succinate production.

In this study, the expression level of the pyc gene from Lactococcus lactis was fine tuned to improve succinate production in Escherichia coli SBS550MG. IPTG induction in the cultures of SBS550MG with pHL413, a positive control plasmid previously constructed (Sanchez et al., 2005), gave drastically decreased PYC activity and succinate yield. We constructed several plasmids for the expression of pyc to change copy number and variant promoters. Among the constructs, as compared to pHL413, the PYC activity dropped significantly with the Plac, Ptac, Ptrc or native Ppyc promoters in medium or high copy vectors, which resulted in a decrease in succinate yield. Three constructs pThio12, pHL413-Km, and pHL413-Km(lacIq-)N showed considerable PYC activity and improved succinate production in E. coli SBS550MG. The native Ppyc promoter was also modified in order to vary pyc expression levels by site-directed mutagenesis of the -10, -35, -44 regions, and the spacer regions between -10 to -35 and -35 to -44 regions. Out of 9 native promoter variants, the MIII variant resulted in a 20% increase in PYC activity, and improved succinate yield in SBS550MG. We also determined the copy number and stability of pHL413 and pHL413-Km. The two plasmids showed roughly the same copy number, but the pHL413-Km plasmid was relatively more stable. This study provides more understanding of the plasmid characteristics and fine tuning of the expression level of pyc for optimization of the succinate production processes.

Manipulating respiratory levels in Escherichia coli for aerobic formation of reduced chemical products

Optimizing the productivity of bioengineered strains requires balancing ATP generation and carbon atom conservation through fine-tuning cell respiration and metabolism. Traditional approaches manipulate cell respiration by altering air feeding, which are technically difficult especially in large bioreactors. An approach based on genetic regulation may better serve this purpose. With excess oxygen supply to the culture, we efficiently manipulated Escherichia coli cell respiration by adding different amount of coenzyme Q1 to strains lacking the ubiCA genes, which encode two critical enzymes for ubiquinone synthesis. As a proof-of-concept, the metabolic effect of the ubiCA gene knockout and coenzyme Q1 supplementation were characterized, and the metabolic profiles of the experimental strains showed clear correlations with coenzyme Q1 concentrations. Further proof-of-principle experiments were performed to illustrate that the approach can be used to optimize cell respiration for the production of chemicals of interest such as ethanol. This study showed that controlled respiration through genetic manipulation can be exploited to allow much larger operating windows for reduced product formation even under fully aerobic conditions.

Succinate Production from Sucrose by Metabolic Engineered Escherichia coli Strains Under Aerobic Conditions

Two metabolically engineered E. coli strains HL2765k and HL27659k, while capable of producing succinate from glucose with high yields, are not able to grow and produce succinate on sucrose. Consequently, the pUR400 plasmid containing scrK, Y, A, B, and R genes was introduced into HL2765k and HL27659k, respectively. Shake flask culture studies showed that the resulting strains can utilize sucrose; the strain HL2765k pUR400 and HL27659k pUR400 can produce succinate aerobically with a molar yield of 0.78 ± 0.02 mol/mol and 1.35 ± 0.13 mol/mol, respectively. On introduction of the plasmid pHL413, which encodes the heterologous pyruvate carboxylase (PYC) from Lactococcus lactis, the molar succinate yield increased to 1.60 ± 0.01 mol of succinate per mole of sucrose by the HL2765k pUR400 pHL413 strain and to 1.84 ± 0.10 by the HL27659k pUR400 pHL413 strain. In aerobic batch bioreactor studies, the succinate production rate was faster, and succinate production reached 101.83 mM with a yield of 1.90 when dissolved oxygen (DO) was controlled at 40 ± 7%. In addition, the results showed that DO had an important effect on succinate production by influencing PYC activity. This work demonstrates the possibility of producing succinate aerobically using sucrose as the carbon source.