Production of acrylic acid and propionic acid by constructing a portion of the 3-hydroxypropionate/4-hydroxybutyrate cycle from <Emphasis Type="Italic">Metallosphaera sedula</Emphasis> in <Emphasis Type="Italic">Escherichia coli</Emphasis>

Acrylic acid and propionic acid are important chemicals requiring affordable, renewable production solutions. Here, we metabolically engineered Escherichia coli with genes encoding components of the 3-hydroxypropionate/4-hydroxybutyrate cycle from Metallosphaera sedula for conversion of glucose to acrylic and propionic acids. To construct an acrylic acid-producing pathway in E. coli, heterologous expression of malonyl-CoA reductase (MCR), malonate semialdehyde reductase (MSR), 3-hydroxypropionyl-CoA synthetase (3HPCS), and 3-hydroxypropionyl-CoA dehydratase (3HPCD) from M. sedula was accompanied by overexpression of succinyl-CoA synthetase (SCS) from E. coli. The engineered strain produced 13.28 ± 0.12 mg/L of acrylic acid. To construct a propionic acid-producing pathway, the same five genes were expressed, with the addition of M. sedula acryloyl-CoA reductase (ACR). The engineered strain produced 1430 ± 30 mg/L of propionic acid. This approach can be expanded to synthesize many important organic chemicals, creating new opportunities for the production of chemicals by carbon dioxide fixation.     

Improved 1, 2, 4-butanetriol production from an engineered <Emphasis Type="Italic">Escherichia coli</Emphasis> by co-expression of different chaperone proteins

1, 2, 4-Butanetriol (BT) is a high-value non-natural chemical and has important applications in polymers, medical production and military industry. In the constructed BT biosynthesis pathway from xylose in Escherichia coli, the xylose dehydrogenase (Xdh) and the benzoylformate decarboxylase (MdlC) are heterologous enzymes and the activity of MdlC is the key limiting factor for BT production. In this study, six chaperone protein systems were introduced into the engineered E. coli harboring the recombinant BT pathway. The chaperone GroES–GroEL was beneficial to Xdh activity but had a negative effect on MdlC activity and BT titer. The plasmid pTf16 containing the tig gene (trigger factor) was beneficial to Xdh and MdlC activities and improved the BT titer from 0.42 to 0.56 g/l from 20 g/l xylose. However, co-expression of trigger factor and GroES–GroEL simultaneously reduced the activity of MdlC and had no effect on the BT production. The plasmid pKJE7 harboring dnaK–dnaJ–grpE showed significant negative effects on these enzyme activities and cell growth, leading to completely restrained the BT production. Similarly, co-expression of DnaKJ–GrpPE and GroES–GroEL simultaneously reduced Xdh and MdlC activities and decreased the BT titer by 45.2 %. The BT production of the engineered E. coli harboring pTf16 was further improved to the highest level at 1.01 g/l under pH control (pH 7). This work showed the potential application of chaperone proteins in microorganism engineering to get high production of target compounds as an effective and valuable tool.     

Engineered short branched-chain acyl-CoA synthesis in E. coli and acylation of chloramphenicol to branched-chain derivatives

Short branched-chain acyl-CoAs are important building blocks for a wide variety of pharmaceutically valuable natural products. Escherichia coli has been used as a heterologous host for the production of a variety of natural compounds for many years. In the current study, we engineered synthesis of isobutyryl-CoA and isovaleryl-CoA from glucose in E. coli by integration of the branched-chain α-keto acid dehydrogenase complex from Streptomyces avermitilis. In the presence of the chloramphenicol acetyltransferase (cat) gene, chloramphenicol was converted to both chloramphenicol-3-isobutyrate and chloramphenicol-3-isovalerate by the recombinant E. coli strains, which suggested successful synthesis of isobutyryl-CoA and isovaleryl-CoA. Furthermore, we improved the α-keto acid precursor supply by overexpressing the alsS gene from Bacillus subtilis and the ilvC and ilvD genes from E. coli and thus enhanced the synthesis of short branched-chain acyl-CoAs. By feeding 25 mg/L chloramphenicol, 2.96?±?0.06 mg/L chloramphenicol-3-isobutyrate and 3.94?±?0.06 mg/L chloramphenicol-3-isovalerate were generated by the engineered E. coli strain, which indicated efficient biosynthesis of short branched-chain acyl-CoAs. HPLC analysis showed that the most efficient E. coli strain produced 80.77?±?3.83 nmol/g wet weight isovaleryl-CoA. To our knowledge, this is the first report of production of short branched-chain acyl-CoAs in E. coli and opens a way to biosynthesize various valuable natural compounds based on these special building blocks from renewable carbon sources.     

Pyruvate decarboxylase and alcohol dehydrogenase overexpression in Escherichia coli resulted in high ethanol production and rewired metabolic enzyme networks

Pyruvate decarboxylase and alcohol dehydrogenase are efficient enzymes for ethanol production in Zymomonas mobilis. These two enzymes were over-expressed in Escherichia coli, a promising candidate for industrial ethanol production, resulting in high ethanol production in the engineered E. coli. To investigate the intracellular changes to the enzyme overexpression for homoethanol production, 2-DE and LC–MS/MS were performed. More than 1,000 protein spots were reproducibly detected in the gel by image analysis. Compared to the wild-type, 99 protein spots showed significant changes in abundance in the recombinant E. coli, in which 46 were down-regulated and 53 were up-regulated. Most proteins related to tricarboxylic acid cycle, glycerol metabolism and other energy metabolism were up-regulated, whereas proteins involved in glycolysis and glyoxylate pathway were down-regulated, indicating the rewired metabolism in the engineered E. coli. As glycolysis is the main pathway for ethanol production, and it was inhibited significantly in engineered E. coli, further efforts should be directed at minimizing the repression of glycolysis to optimize metabolism network for higher yields of ethanol production.     

Engineering E. coli for caffeic acid biosynthesis from renewable sugars

Caffeic acid is a valuable aromatic compound that possesses many important pharmacological activities. In structure, caffeic acid belongs to the hydroxycinnamic acid family and can be biosynthesized from the aromatic amino acid tyrosine. In the present paper, the caffeic acid biosynthesis pathway was reconstituted in engineered Escherichia coli to produce caffeic acid from simple biomass sugar glucose and xylose. Different engineering approaches were utilized to optimize the production. Specifically, two parallel biosynthesis routes leading from tyrosine to caffeic acid were studied. The copy number of the intermediate biosynthesis genes was varied to find appropriate gene doses for caffeic acid biosynthesis. Three different media, including a MOPS medium, a synthetic medium, and a rich medium, were also examined to improve the production. The highest specific caffeic acid production achieved was 38 mg/L/OD. Lastly, cultivation of engineered E. coli in a bioreactor resulted in a production of 106 mg/L caffeic acid after 4 days.     

Fermentation characterization of an L-tryptophan producing Escherichia coli strain with inactivated phosphotransacetylase

Acetate is a primary inhibitory metabolite in Escherichia coli cultivation which is detrimental to bacterial growth and the formation of desired products. It can be derived from acetyl coenzyme A by the phosphotransacetylase (Pta)–acetate kinase (AckA) pathway. In this study, the fermentation characteristics of Pta mutant strain E. coli TRTHΔpta were compared with those of the control strain E. coli TRTH in a 30-L fermentor. The effects of glucose concentration and dissolved oxygen (DO) level were investigated, and the results suggest that DO and glucose concentration are vital influencing parameters for the production of L-tryptophan. Based on our experimental results, we then tested a DO-stat fed-batch fermentation strategy. When DO was controlled at about 20 % during L-tryptophan fermentation in the DO-stat fed-batch system, the pta mutant was able to maintain a higher growth rate at the exponential phase, and the final biomass and L-tryptophan production were increased to 55.3 g/L and 35.2 g/L, respectively. Concomitantly, as the concentration of acetate decreased to 0.7 g/L, the accumulation of pyruvate and lactate increased in the mutant strain as compared with the control strain. This characterization of the recombinant mutant strain provides useful information for the rational modification of metabolic fluxes to improve tryptophan production.     

High yield production of four-carbon dicarboxylic acids by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

Several metabolic engineered Escherichia coli strains were constructed and evaluated for four-carbon dicarboxylic acid production. Fumarase A, fumarase B and fumarase C single, double and triple mutants were constructed in a ldhA adhE mutant background overexpressing the pyruvate carboxylase from Lactococcus lactis. All the mutants produced succinate as the main four-carbon (C4) dicarboxylic acid product when glucose was used as carbon source with the exception of the fumAC and the triple fumB fumAC deletion strains, where malate was the main C4-product with a yield of 0.61–0.67 mol (mole glucose)^?1. Additionally, a mdh mutant strain and a previously engineered high-succinate-producing strain (SBS550MG-Cms pHL413-Km) were investigated for aerobic malate production from succinate. These strains produced 40.38 mM (5.41 g/L) and 50.34 mM (6.75 g/L) malate with a molar yield of 0.53 and 0.55 mol (mole succinate)^?1, respectively. Finally, by exploiting the high-succinate production capability, the strain SBS550MG-Cms243 pHL413-Km showed significant malate production in a two-stage process from glucose. This strain produced 133 mM (17.83 g/L) malate in 47 h, with a high yield of 1.3 mol (mole glucose)^?1 and productivity of 0.38 g L^?1 h^?1.     

Metabolic engineering of Candida utilis for isopropanol production

A genetically-engineered strain of the yeast Candida utilis harboring genes encoding (1) an acetoacetyl-CoA transferase from Clostridium acetobutylicum ATCC 824, (2) an acetoacetate decarboxylase, and (3) a primary–secondary alcohol dehydrogenase derived from Clostridium beijerinckii NRRL B593 produced up to 0.21 g/L of isopropanol. Because the engineered strain accumulated acetate, isopropanol titer was improved to 1.2 g/L under neutralized fermentation conditions. Optimization of isopropanol production was attempted by the overexpression and disruption of several endogenous genes. Simultaneous overexpression of two genes encoding acetyl-CoA synthetase and acetyl-CoA acetyltransferase increased isopropanol titer to 9.5 g/L. Moreover, in fed-batch cultivation, the resultant recombinant strain produced 27.2 g/L of isopropanol from glucose with a yield of 41.5 % (mol/mol). This is the first demonstration of the production of isopropanol by genetically engineered yeast.     

Microbial production of fatty alcohols

Fatty alcohols have numerous commercial applications, including their use as lubricants, surfactants, solvents, emulsifiers, plasticizers, emollients, thickeners, and even fuels. Fatty alcohols are currently produced by catalytic hydrogenation of fatty acids from plant oils or animal fats. Microbial production of fatty alcohols may be a more direct and environmentally-friendly strategy since production is carried out by heterologous enzymes, called fatty acyl-CoA reductases, able to reduce different acyl-CoA molecules to their corresponding primary alcohols. Successful examples of metabolic engineering have been reported in Saccharomyces cerevisiae and Escherichia coli in which the production of fatty alcohols ranged from 1.2 to 1.9 g/L, respectively. Due to their metabolic advantages, oleaginous yeasts are considered the best hosts for production of fatty acid-derived chemicals. Some of these species can naturally produce, under specific growth conditions, lipids at high titers (>50 g/L) and therefore provide large amounts of fatty acyl-CoAs or fatty acids as precursors. Very recently, taking advantage of such features, over 8 g/L of C₁₆–C₁₈ fatty alcohols have been produced in Rhodosporidium toruloides. In this review we summarize the different metabolic engineering strategies, hosts and cultivation conditions used to date. We also point out some future trends and challenges for the microbial production of fatty alcohols.     

Heavy oils,principally long-chain n-alkanes secreted by Aureobasidium pullulans var. melanogenum strain P5 isolated from mangrove system

In this study, the yeast strain P5 isolated from a mangrove system was identified to be a strain of Aureobasidium pullulans var. melanogenum and was found to be able to secrete a large amount of heavy oil into medium. After optimization of the medium for heavy oil production and cell growth by the yeast strain P5, it was found that 120.0 g/l of glucose and 0.1 % corn steep liquor were the most suitable for heavy oil production. During 10-l fermentation, the yeast strain P5 produced 32.5 g/l of heavy oil and cell mass was 23.0 g/l within 168 h. The secreted heavy oils contained 66.15 % of the long-chain n-alkanes and 26.4 % of the fatty acids, whereas the compositions of the fatty acids in the yeast cells were only C_16:0 (21.2 %), C_16:1(2.8 %), C_18:0 (2.9 %), C_18:1 (39.8 %), and C_18:2 (33.3 %). We think that the secreted heavy oils may be used as a new source of petroleum in marine environments. This is the first report of yeast cells which can secrete the long-chain n-alkanes.     

Enhanced production of the nonribosomal peptide antibiotic valinomycin in Escherichia coli through small-scale high cell density fed-batch cultivation

Nonribosomal peptides (NRPs), a large family of natural products, possess numerous pharmaceutically significant bioactivities. However, many native microbial producers of NRPs are not cultivable or have low production yields making mass production infeasible. The recombinant production of natural products in a surrogate host has emerged as a strategy to overcome these limitations. De novo recombinant production of the NRP antibiotic valinomycin in an engineered Escherichia coli host strain was established with the necessary biosynthetic pathway constituents from Streptomyces tsusimaensis. In the present study, the initially modest valinomycin yields could be significantly increased from 0.3 up to 2.4 mg L^?1 by switching from a batch to an enzyme-based fed-batch mode in shake flasks. A subsequent design of experiment-driven optimization of parallel fed-batch cultivations in 24-well plates with online monitoring of dissolved oxygen and pH led to valinomycin yields up to 6.4 mg L^?1. Finally, repeated glucose polymer feeding to enzyme-based high cell density cultivations in shake flasks resulted in cell densities of OD₆₀₀ >50 and a valinomycin titer of appr. 10 mg L^?1. This represents a 33-fold improvement compared to the initial batch cultivations and is the highest concentration of a nonribosomal peptide which has been produced in E. coli without feeding of specific precursors so far to our knowledge. Also, such a small-scale optimization under fed-batch conditions may be generally applicable for the development and scale-up of natural product production processes in E. coli.     

Fatty alcohol production in engineered E. coli expressing Marinobacter fatty acyl-CoA reductases

Although successful production of fatty alcohols in metabolically engineered Escherichia coli with heterologous expression of fatty acyl-CoA reductase has been reported, low biosynthetic efficiency is still a hurdle to be overcome. In this study, we examined the characteristics of two fatty acyl-CoA reductases encoded by Maqu_2220 and Maqu_2507 genes from Marinobacter aquaeolei VT8 on fatty alcohol production in E. coli. Fatty alcohols with diversified carbon chain length were obtained by co-expressing Maqu_2220 with different carbon chain length-specific acyl-ACP thioesterases. Both fatty acyl-CoA reductases displayed broad substrate specificities for C12–C18 fatty acyl chains in vivo. The optimized mutant strain of E. coli carrying the modified tesA gene and fadD gene from E. coli and Maqu_2220 gene from Marinobacter aquaeolei VT8 produced fatty alcohols at a remarkable level of 1.725 g/L under the fermentation condition.     

Optimization of Cultivating Conditions for Triterpenoids Production from Antrodia cinnmomea

The submerged cultivating conditions for triterpenoids production from Antrodia cinnamomea were optimized using uniform design method and the one-factor-at-a-time method was adopted to investigate the effect of plants oils and glucose supply on triterpenoids production and mycelia growth. Corn starch and culturing time were identified as more significant variables for triterpenoids production. The optimal conditions for triterpenoids production was 20.0 g/L corn starch, 20.0 g/L wheat bran, 1.85 g/L MgSO4, initial pH 3 and 16 days of cultivation. In addition, investigation of plant oils and glucose supply showed that 0.3 % (v/v) olive oil supply at the beginning of fermentation stimulated mycelia growth and significantly increased triterpenoids production; 0.2 % (w/v) glucose supplement at 10th day enhanced production of triterpenoids with slight effect on biomass, which is reported for the first time. The triterpenoids production experimentally obtained under the optimal conditions was 7.23 % (w/w). The uniform design method may be used to optimize many environmental and genetic factors such as temperature and agitation that can also affect the triterpenoids production from A. cinnamomea.     

Novel SNPs and INDEL polymorphisms in the 3′UTR of DGAT1 gene: in silico analyses and a possible association

Diacylglycerol–O–acyltransferase (DGAT1) gene encodes the rate-limiting enzyme of triglyceride synthesis. A polymorphism in this gene, DGAT1 K232A, has been associated with milk production and composition in taurine breeds. However, this polymorphism is not a good tool for ascertaining the effects of this QTL in Bos indicus (Zebu), since the frequency of the DGAT1 232A allele is too low in these breeds. We sequenced the 3′-untranslated region of DGAT1 gene in a sample of bulls of the breeds Guzerá (Bos indicus) and Holstein (Bos taurus) and, using in silico analysis, we searched for genetic variation, evolutionary conservation, regulatory elements, and possible substitution effects. Six single nucleotide (SNPs) and one insertion-deletion (INDEL) polymorphisms were found in the Guzerá bulls. Additionally, we developed a preliminary association study, using this INDEL polymorphism as a genetic marker. A significant association was detected (P ≤ 0.05) between the INDEL (DGAT1 3′UTR INDEL) and the breeding values (BV) for protein, fat, and milk yields over a 305-day lactation period. The DGAT1 3′ UTR INDEL genotype I/I (I, for insertion) was associated with lower BVs (?38.77 kg for milk, ?1.86 kg for fat, and ?1.48 kg for protein yields), when compared to the genotype I/D (D, for deletion). I/D genotype was lower D/D genotype (?34.98 kg milk, ?1.73 kg fat, and ?1.09 kg protein yields). This study reports the first polymorphism of DGAT1 3′UTR in the Guzerá breed, as well as its association with BV for milk protein, fat, and milk yields.     

Engineering Escherichia coli for odd straight medium chain free fatty acid production

Microbial biosynthesis of free fatty acids (FFAs) can be achieved by introducing an acyl–acyl carrier protein thioesterase gene into Escherichia coli. The engineered E. coli usually produced even chain FFAs. In this study, propionyl-CoA synthetase (prpE) from Salmonella enterica was overexpressed in two efficient even chain FFAs producers, ML103 (pXZM12) carrying the acyl-ACP thioesterase gene from Umbellularia californica and ML103 (pXZ18) carrying the acyl-ACP thioesterase gene from Ricinus communis combined with supplement of extracellular propionate. With these metabolically engineered E. coli, the odd straight chain FFAs, undecanoic acid (C11:0), tridecanoic acid (C13:0), and pentadecanoic acid (C15:0) were produced from glucose and propionate. The highest total odd straight chain FFAs produced by ML103 (pXZM12, pBAD-prpE) reached 276 mg/l with a ratio of 23.43 % of the total FFAs. In ML103 (pXZ18, pBAD-prpE), the highest total odd straight chain FFAs accumulated to 297 mg/l, and the ratio reached 17.68 % of the total FFAs. Due to the different substrate specificity of the acyl-ACP thioesterases, the major odd straight chain FFA components of ML103 (pXZM12, pBAD-prpE) were undecanoic acid and tridecanoic acid, while the ML103 (pXZ18, pBAD-prpE) preferred pentadecanoic acid.     

Production of 3-hydroxypropionic acid from glycerol by acid tolerant Escherichia coli

The biological production of 3-hydroxypropionic acid (3-HP) has attracted significant attention because of its industrial importance. The low titer, yield and productivity, all of which are related directly or indirectly to the toxicity of 3-HP, have limited the commercial production of 3-HP. The aim of this study was to identify and select a 3-HP tolerant Escherichia coli strain among nine strains reported to produce various organic acids efficiently at high titer. When transformed with heterologous glycerol dehydratase, reactivase and aldehyde dehydrogenase, all nine E. coli strains produced 3-HP from glycerol but the level of 3-HP production, protein expression and activities of the important enzymes differed significantly according to the strain. Two E. coli strains, W3110 and W, showed higher levels of growth than the others in the presence of 25 g/L 3-HP. In the glycerol fed-batch bioreactor experiments, the recombinant E. coli W produced a high level of 3-HP at 460 ± 10 mM (41.5 ± 1.1 g/L) in 48 h with a yield of 31 % and a productivity of 0.86 ± 0.05 g/L h. In contrast, the recombinant E. coli W3110 produced only 180 ± 8.5 mM 3-HP (15.3 ± 0.8 g/L) in 48 h with a yield and productivity of 26 % and 0.36 ± 0.02 g/L h, respectively. This shows that the tolerance to and the production of 3-HP differ significantly among the well-known, similar strains of E. coli. The titer and productivity obtained with E. coli W were the highest reported thus far for the biological production of 3-HP from glycerol by E. coli.     

Enhanced production of N-acetyl-d-neuraminic acid by multi-approach whole-cell biocatalyst

N-Acetyl-d-neuraminic acid (Neu5Ac) has attracted considerable interest due to its promising potential applications in medicine. Significant efforts have been made in whole-cell biocatalyst for Neu5Ac production, but the processes often result in suboptimal performance due to poor expression of enzymes, imbalances of pathway components, disturbance of competing pathways, and barriers of mass transport. In this study, we engineered Escherichia coli strains capable of producing Neu5Ac by assembling a two-step heterologous pathway consisting of N-acetyl-d-glucosamine 2-epimerase (AGE) and Neu5Ac aldolase (NanA). Multiple approaches were used to improve the efficiency of the engineered pathway and process for enhanced Neu5Ac production. Firstly, we identified that NanA was the rate-controlling enzyme in this pathway. With increased expression of NanA, a ninefold increase in Neu5Ac production (65 mM) was observed. Secondly, knocking out nanTEK genes blocked Neu5Ac uptake and the competing pathway, which kept the reactions to the synthetic direction as the final product went outside of the cells and enhanced the Neu5Ac production by threefold, resulting in 173.8 mM of Neu5Ac. Thirdly, we improved the performance of the system by promoting substrate transport and optimizing concentrations of substrates. An overall whole-cell biocatalytic process was developed and a maximum titer of 240 mM Neu5Ac (74.2 g/L) was achieved, with productivity of 6.2 g Neu5Ac/L/h and conversion yield of 40 % from GlcNAc. The engineered strain could be reused for at least five cycles with a productivity of >6 g/L/h. It is a cost-effective process for Neu5Ac production with potential applications in large-scale industrial production.     

Production of isoprene,one of the high-density fuel precursors,from peanut hull using the high-efficient lignin-removal pretreatment method

Background

Isoprene as the feedstock can be used to produce renewable energy fuels, providing an alternative to replace the rapidly depleting fossil fuels. However, traditional method for isoprene production could not meet the demands for low-energy consumption and environment-friendliness. Moreover, most of the previous studies focused on biofuel production out of lignocellulosic materials such as wood, rice straw, corn cob, while few studies concentrated on biofuel production using peanut hull (PH). As is known, China is the largest peanut producer in the globe with an extremely considerable amount of PH to be produced each year. Therefore, a novel, renewable, and environment-friendly pretreatment strategy to increase the enzymatic hydrolysis efficiency of cellulose and reduce the inhibitors generation was developed to convert PH into isoprene.

Results

The optimal pretreatment conditions were 100 °C, 60 min, 10% (w/v) solid loading with a 2:8 volume ratio of phosphoric acid and of hydrogen peroxide. In comparison with the raw PH, the hemicellulose and lignin were reduced to 85.0 and 98.0%, respectively. The cellulose–glucose conversion of pretreated PH reached up to 95.0% in contrast to that of the raw PH (19.1%). Only three kinds of inhibitors including formic acid, levulinic acid, and a little furfural were formed during the pretreatment process, whose concentrations were too low to inhibit the isoprene yield for Escherichia coli fermentation. Moreover, compared with the isoprene yield of pure glucose fermentation (298 ± 9 mg/L), 249 ± 6.7 and 294 ± 8.3 mg/L of isoprene were produced using the pretreated PH as the carbon source by the engineered strain via separate hydrolysis and fermentation and simultaneous saccharification and fermentation (SSF) methods, respectively. The isoprene production via SSF had a 9.8% glucose–isoprene conversion which was equivalent to 98.8% of isoprene production via the pure glucose fermentation.

Conclusions

The optimized phosphoric acid/hydrogen peroxide combination pretreatment approach was proved effective to remove lignin and hemicellulose from lignocellulosic materials. Meanwhile, the pretreated PH could be converted into isoprene efficiently in the engineered Escherichia coli. It is concluded that this novel strategy of isoprene production using lignocellulosic materials pretreated by phosphoric acid/hydrogen peroxide is a promising alternative to isoprene production using traditional way which can fully utilize non-renewable fossil sources.

     

A general inhibition kinetics model for ethanol production using a novel carbon source: sodium gluconate

In this study, sodium gluconate was applied as a novel carbon source for the fuel ethanol production using an engineered Escherichia coli strain KO11 in batch fermentations. Ethanol and acetic acid were produced as two major products as well as small amount of lactic acid during the fermentation. Compared to the conventional carbon source glucose, the bioconversion of sodium gluconate possessed two distinct advantages: faster utilization rate of sodium gluconate (1.66 g/L per h) compared to glucose (0.996 g/L per h) and no requirement for pH control during fermentation. A general inhibition model including both substrate and products inhibitory effects was proposed, which adequately simulated batch fermentation kinetics at various concentrations of sodium gluconate. All of the products showed inhibitory effects on cell growth. The order of the inhibitory strength of all products and substrate was for the first time clarified in this study. Acetic acid was the most inhibitory product mitigating the cell growth, followed by ethanol and lactic acid. Sodium gluconate stimulated cell growth when its concentration was below 16 g/L, while it inhibited the cell growth when the concentration was above this concentration. It completely inhibited the cell growth when the concentration was 325 g/L. The high value of both the coefficient of determination (R ²) and the adjusted R ² verified the good fit of the model. This paper provides key insights into further engineering these strains to improve ethanol production.     

Synthesis of nylon 4 from gamma-aminobutyrate (GABA) produced by recombinant Escherichia coli

In this study, we developed recombinant Escherichia coli strains expressing Lactococcus lactis subsp. lactis Il1403 glutamate decarboxylase (GadB) for the production of GABA from glutamate monosodium salt (MSG). Syntheses of GABA from MSG were examined by employing recombinant E. coli XL1-Blue as a whole cell biocatalyst in buffer solution. By increasing the concentration of E. coli XL1-Blue expressing GadB from the OD₆₀₀ of 2–10, the concentration and conversion yield of GABA produced from 10 g/L of MSG could be increased from 4.3 to 4.8 g/L and from 70 to 78 %, respectively. Furthermore, E. coli XL1-Blue expressing GadB highly concentrated to the OD₆₀₀ of 100 produced 76.2 g/L of GABA from 200 g/L of MSG with 62.4 % of GABA yield. Finally, nylon 4 could be synthesized by the bulk polymerization using 2-pyrrolidone that was prepared from microbially synthesized GABA by the reaction with Al₂O₃ as catalyst in toluene with the yield of 96 %.