Zhengxiang Wang

Glycerol production by microbial fermentation: A review

Microbial production of glycerol has been known for 150 years, and glycerol was produced commercially during World War I. Glycerol production by microbial synthesis subsequently declined since it was unable to compete with chemical synthesis from petrochemical feedstocks due to the low glycerol yields and the difficulty with extraction and purification of glycerol from broth. As the cost of propylene has increased and its availability has decreased especially in developing countries and as glycerol has become an attractive feedstock for production of various chemicals, glycerol production by fermentation has become more attractive as an alternative route. Substantial overproduction of glycerol by yeast from monosaccharides can be obtained by: (1) forming a complex between acetaldehyde and bisulfite ions thereby retarding ethanol production and restoring the redox balance through glycerol synthesis; (2) growing yeast cultures at pH values near 7 or above; or (3) using osmotolerant yeasts. In recent years, significant improvements have been made in the glycerol production using osmotolerant yeasts on a commercial scale in China. The most outstanding achievements include: (1) isolation of novel osmotolerant yeast strains producing up to 130 g/L glycerol with yields up to 63% and the productivities up to 32 g/(L day); (2) glycerol yields, productivities and concentrations in broth up to 58%, 30 g/(L day) and 110-120 g/L, respectively, in an optimized aerobic fermentation process have been attained on a commercial scale; and (3) a carrier distillation technique with a glycerol distillation efficiency greater than 90% has been developed. As glycerol metabolism has become better understood in yeasts, opportunities will arise to construct novel glycerol overproducing microorganisms by metabolic engineering.

Metabolic engineering of Escherichia coli : A sustainable industrial platform for bio-based chemical production

In order to decrease carbon emissions and negative environmental impacts of various pollutants, more bulk and/or fine chemicals are produced by bioprocesses, replacing the traditional energy and fossil based intensive route. The Gram-negative rod-shaped bacterium, Escherichia coli has been studied extensively on a fundamental and applied level and has become a predominant host microorganism for industrial applications. Furthermore, metabolic engineering of E. coli for the enhanced biochemical production has been significantly promoted by the integrated use of recent developments in systems biology, synthetic biology and evolutionary engineering. In this review, we focus on recent efforts devoted to the use of genetically engineered E. coli as a sustainable platform for the production of industrially important biochemicals such as biofuels, organic acids, amino acids, sugar alcohols and biopolymers. In addition, representative secondary metabolites produced by E. coli will be systematically discussed and the successful strategies for strain improvements will be highlighted. Moreover, this review presents guidelines for future developments in the bio-based chemical production using E. coli as an industrial platform.

Genetically switched D-lactate production in Escherichia coli.

During a fermentation process, the formation of the desired product during the cell growth phase competes with the biomass for substrates or inhibits cell growth directly, which results in a decrease in production efficiency. A genetic switch is required to precisely separate growth from production and to simplify the fermentation process. The ldhA promoter, which encodes the fermentative D-lactate dehydrogenase (LDH) in the lactate producer Escherichia coli CICIM B0013-070 (ack-pta pps pflB dld poxB adhE frdA), was replaced with the λ p(R) and p(L) promoters (as a genetic switch) using genomic recombination and the thermo-controllable strain B0013-070B (B0013-070, ldhAp::kan-cI(ts)857-p(R)-p(L)), which could produce two-fold higher LDH activity at 42°C than the B0013-070 strain, was created. When the genetic switch was turned off at 33°C, strain B0013-070B produced 10% more biomass aerobically than strain B0013-070 and produced only trace levels of lactate which could reduce the growth inhibition caused by oxygen insufficiency in large scale fermentation. However, 42°C is the most efficient temperature for switching on lactate production. The volumetric productivity of B0013-070B improved by 9% compared to that of strain B0013-070 when it was grown aerobically at 33°C with a short thermo-induction at 42°C and then switched to the production phase at 42°C. In a bioreactor experiment using scaled-up conditions that were optimized in a shake flask experiment, strain B0013-070B produced 122.8 g/l D-lactate with an increased oxygen-limited productivity of 0.89 g/g·h. The results revealed the effectiveness of using a genetic switch to regulate cell growth and the production of a metabolic compound.

Evaluation of Genetic Manipulation Strategies on d-Lactate Production by Escherichia coli

In order to rationally manipulate the cellular metabolism of Escherichia coli for d-lactate production, single-gene and multiple-gene deletions with mutations in acetate kinase (ackA), phosphotransacetylase (pta), phosphoenolpyruvate synthase (pps), pyruvate formate lyase (pflB), FAD-binding d-lactate dehydrogenase (dld), pyruvate oxidase (poxB), alcohol dehydrogenase (adhE), and fumarate reductase (frdA) were tested for their effects in two-phase fermentations (aerobic growth and oxygen-limited production). Lactate yield and productivity could be improved by single-gene deletions of ackA, pta, pflB, dld, poxB, and frdA in the wild type E. coli strain but were unfavorably affected by deletions of pps and adhE. However, fermentation experiments with multiple-gene mutant strains showed that deletion of pps in addition to ackA-pta deletions had no effect on lactate production, whereas the additional deletion of adhE in E. coli B0013-050 (ackA-pta pps pflB dld poxB) increased lactate yield. Deletion of all eight genes in E. coli B0013 to produce B0013-070 (ackA-pta pps pflB dld poxB adhE frdA) increased lactate yield and productivity by twofold and reduced yields of acetate, succinate, formate, and ethanol by 95, 89, 100, and 93%, respectively. When tested in a bioreactor, E. coli B0013-070 produced 125xa0g/l d-lactate with an increased oxygen-limited lactate productivity of 0.61xa0g/gxa0h (2.1-fold greater than E. coli B0013). These kinetic properties of d-lactate production are among the highest reported and the results have revealed which genetic manipulations improved d-lactate production by E. coli.

Improving ethanol productivity by modification of glycolytic redox factor generation in glycerol-3-phosphate dehydrogenase mutants of an industrial ethanol yeast

The GPD2 gene, encoding NAD+-dependent glycerol-3-phosphate dehydrogenase in an industrial ethanol-producing strain of Saccharomyces cerevisiae, was deleted. And then, either the non-phosphorylating NADP+-dependent glyceraldehyde-3-phosphate dehydrogenase (GAPN) from Bacillus cereus, or the NADP+-dependent glyceraldehyde-3-phosphate dehydrogenase (GAPDH) from Kluyveromyces lactis, was expressed in the obtained mutant AG2 deletion of GPD2, respectively. The resultant recombinant strain AG2A (gpd2Δ PPGK-gapN) exhibited a 48.70xa0±xa00.34% (relative to the amount of substrate consumed) decrease in glycerol production and a 7.60xa0±xa00.12% (relative to the amount of substrate consumed) increase in ethanol yield, while recombinant AG2B (gpd2Δ PPGK-GAPDH) exhibited a 52.90xa0±xa00.45% (relative to the amount of substrate consumed) decrease in glycerol production and a 7.34xa0±xa00.15% (relative to the amount of substrate consumed) increase in ethanol yield compared with the wild-type strain. More importantly, the maximum specific growth rates (μmax) of the recombinant AG2A and AG2B were higher than that of the mutant gpd2Δ and were indistinguishable compared with the wild-type strain in anaerobic batch fermentations. The results indicated that the redox imbalance of the mutant could be partially solved by expressing the heterologous genes.

Gene cloning, heterologous expression, and characterization of a high maltose-producing α-amylase of Rhizopus oryzae.

A putative α-amylase gene, designated as RoAmy, was cloned from Rhizopus oryzae. The deduced amino acid sequence showed the highest (42.8%) similarity to the α-amylase from Trichoderma viride. The RoAmy gene was successfully expressed in Pichia pastoris GS115 under the induction of methanol. The molecular weight of the purified RoAmy determined by sodium dodecyl sulfate polyacrylamide gel electrophoresis was approximately 48xa0kDa. The optimal pH and temperature were 4–6 and 60xa0°C, respectively. The enzyme was stable at pH ranges of 4.5–6.5 and temperatures below 50xa0°C. Purified RoAmy had a Km and Vmax of 0.27xa0mg/ml and 0.068xa0mg/min, respectively, with a specific activity of 1,123xa0U/mg on soluble starch. Amylase activity was strongly inhibited by 5xa0mM Cu2+ and 5xa0mM Fe2+, whereas 5xa0mM Ca2+ showed no significant effect. The RoAmy hydrolytic activity was the highest on wheat starch but showed only 55% activity on amylopectin relative to soluble corn starch, while the pullulanase activity was negligible. The main end products of the polysaccharides tested were glucose and maltose. Maltose reached a concentration of 74% (w/w) with potato starch as the substrate. The enzyme had an extremely high affinity (Kmu2009=u20090.22xa0mM) to maltotriose. A high ratio of glucose/maltose of 1:4 was obtained when maltotriose was used at an initial concentration of 40xa0mM.

Cloning, expression, characterization, and biocatalytic investigation of a novel bacilli thermostable type I pullulanase from Bacillus sp. CICIM 263.

The pulA1 gene, encoding a novel thermostable type I pullulanase PulA1 from Bacillus sp. CICIM 263, was identified from genomic DNA. The open reading frame of the pulA1 gene was 2655 base pairs long and encoded a polypeptide (PulA1) of 885 amino acids with a calculated molecular mass of 100,887 Da. The pulA1 gene was expressed in Escherichia coli and Bacillus subtilis. Recombinant PuLA1 showed optimal activity at pH 6.5 and 70 °C. The enzyme demonstrated moderate thermostability as PuLA1 maintained more than 88% of its acitivity when incubated at 70 °C for 1 h. The enzyme could completely hydrolyze pullulan to maltotriose, and hydrolytic activity was also detected with glycogen, starch and amylopection, but not with amylose, which is consistent with the property of type I pullulanase. PulA1 may be suitable for industrial applications to improve the yields of fermentable sugars for bioethanol production.

Cloning and characterization of a NAD+‐dependent glycerol‐3‐phosphate dehydrogenase gene from Candida glycerinogenes, an industrial glycerol producer

The osmotolerant yeast Candida glycerinogenes produces glycerol as a major metabolite on an industrial scale, but the underlying molecular mechanisms are poorly understood. We cloned and characterized a 4900-bp genomic fragment containing the CgGPD gene encoding a glycerol-3-phosphate dehydrogenase homologous to GPD genes in other yeasts using degenerate primers in conjunction with inverse PCR. Sequence analysis revealed a 1167-bp open reading frame encoding a putative peptide of 388 deduced amino acids with a molecular mass of 42 695 Da. The CgGPD gene consisted of an N-terminal NAD(+)-binding domain and a central catalytic domain, whereas seven stress response elements were found in the upstream region. Functional analysis revealed that Saccharomyces cerevisiae gpd1Delta and gpd1Delta/gpd2Delta osmosensitive mutants transformed with CgGPD were restored to the wild-type phenotype when cultured in high osmolarity media, suggesting that it is a functional GPD protein. Transformants also accumulated glycerol intracellularly and GPD-specific activity increased significantly when stressed with NaCl, whereas the S. cerevisiae mutants transformed with the empty plasmid showed only slight increases. The full-length CgGPD gene sequence including upstream and downstream regions has been deposited in GenBank under accession no. EU186536.

Efficient bioconversion of crude glycerol from biodiesel to optically pure D-lactate by metabolically engineered Escherichia coli

Biodiesel has attracted considerable attention as one of the best choices among alternative and renewable fuels. Large quantities of crude glycerol are produced as a main co-product with increasing biodiesel production. Currently, the problem of waste glycerol utilization needs to be crucially addressed, not only for environmental protection but also for the economy of the biodiesel industry. In this paper, the use of crude glycerol for the production of D-lactate by engineered Escherichia coli was investigated. Engineered E. coli B0013-070 with a homolactic pathway for D-lactate synthesis by elimination of byproduct pathways (ethanol, succinate, formate and acetate) could convert 20 g L−1 of crude glycerol to 13.6 g L−1 of D-lactate with a yield of 0.67 g g−1 glycerol. Overexpression of D-lactate dehydrogenase by a low-copy vector in E. coli B0013-070 resulted in the increased production and yield of D-lactate, in which 14.5 g L−1 of D-lactate was produced with a yield of 0.72 g g−1 glycerol from crude glycerol. The effect of temperature on D-lactate fermentation by the engineered strain E. coli B0013-070-pTHldhA was also investigated, and 34 °C and 40 °C were found to be the optimal temperatures for cell growth and lactate production, respectively. The engineered strain B0013-070-pTHldhA produced 100.3 g L−1 of D-lactate with 99.97% optical purity from 531.5 g of crude glycerol with an overall productivity of 2.78 g L−1 h−1 and a yield of 75.4 g per 100 g glycerol (0.77 mol mol−1) using two phase fermentation combined with a temperature shifting strategy in a 7 L bioreactor. In summary, this paper shows that crude glycerol could be directly converted to D-lactate without any prior purification.

Highly efficient L-lactate production using engineered Escherichia coli with dissimilar temperature optima for L-lactate formation and cell growth

L-Lactic acid, one of the most important chiral molecules and organic acids, is produced via pyruvate from carbohydrates in diverse microorganisms catalyzed by an NAD+-dependent L-lactate dehydrogenase. Naturally, Escherichia coli does not produce L-lactate in noticeable amounts, but can catabolize it via a dehydrogenation reaction mediated by an FMN-dependent L-lactate dehydrogenase. In aims to make the E. coli strain to produce L-lactate, three L-lactate dehydrogenase genes from different bacteria were cloned and expressed. The L-lactate producing strains, 090B1 (B0013-070, ΔldhA::diflldD::Pldh-ldhLca), 090B2 (B0013-070, ΔldhA::diflldD::Pldh-ldhStrb) and 090B3 (B0013-070, ΔldhA::diflldD::Pldh-ldhBcoa) were developed from a previously developed D-lactate over-producing strain, E. coli strain B0013-070 (ack-ptappspflBdldpoxBadhEfrdA) by: (1) deleting ldhA to block D-lactate formation, (2) deleting lldD to block the conversion of L-lactate to pyruvate, and (3) expressing an L-lactate dehydrogenase (L-LDH) to convert pyruvate to L-lactate under the control of the ldhA promoter. Fermentation tests were carried out in a shaking flask and in a 25-l bioreactor. Strains 090B1, 090B2 or 090B3 were shown to metabolize glucose to L-lactate instead of D-lactate. However, L-lactate yield and cell growth rates were significantly different among the metabolically engineered strains which can be attributed to a variation between temperature optimum for cell growth and temperature optimum for enzymatic activity of individual L-LDH. In a temperature-shifting fermentation process (cells grown at 37°C and L-lactate formed at 42°C), E. coli 090B3 was able to produce 142.2 g/l of L-lactate with no more than 1.2 g/l of by-products (mainly acetate, pyruvate and succinate) accumulated. In conclusion, the production of lactate by E. coli is limited by the competition relationship between cell growth and lactate synthesis. Enzymatic properties, especially the thermodynamics of an L-LDH can be effectively used as a factor to regulate a metabolic pathway and its metabolic flux for efficient L-lactate production.HighlightsThe enzymatic thermodynamics was used as a tool for metabolic regulation. ► minimizing the activity of L-lactate dehydrogenase in growth phase improved biomass accumulation. ► maximizing the activity of L-lactate dehydrogenase improved lactate productivity in production phase.