Development of Halomonas TD01 as a host for open production of chemicals

Genetic engineering of Halomonas spp. was seldom reported due to the difficulty of genetic manipulation and lack of molecular biology tools. Halomonas TD01 can grow in a continuous and unsterile process without other microbial contaminations. It can be therefore exploited for economic production of chemicals. Here, Halomonas TD01 was metabolically engineered using the gene knockout procedure based on markerless gene replacement stimulated by double-strand breaks in the chromosome. When gene encoding 2-methylcitrate synthase in Halomonas TD01 was deleted, the conversion efficiency of propionic acid to 3-hydroxyvalerate (3HV) monomer fraction in random PHBV copolymers of 3-hydroxybutyrate (3HB) and 3HV was increased from around 10% to almost 100%, as a result, cells were grown to accumulate 70% PHBV in dry weight (CDW) consisting of 12 mol% 3HV from 0.5 g/L propionic acid in glucose mineral medium. Furthermore, successful deletions on three PHA depolymerases eliminate the possible influence of PHA depolymerases on PHA degradation in the complicated industrial fermentation process even though significant enhanced PHA content was not observed. In two 500 L pilot-scale fermentor studies lasting 70 h, the above engineered Halomonas TD01 grew to 112 g/L CDW containing 70 wt% P3HB, and to 80 g/L CDW with 70 wt% P(3HB-co-8 mol% 3HV) in the presence of propionic acid. The cells grown in shake flasks even accumulated close to 92% PHB in CDW with a significant increase of glucose to PHB conversion efficiency from around 30% to 42% after 48 h cultivation when pyridine nucleotide transhydrogenase was overexpressed. Halomonas TD01 was also engineered for producing a PHA regulatory protein PhaR which is a robust biosurfactant.     

Production of polyhydroxyalkanoates from whey by Thermus thermophilus HB8

The thermophilic bacterium Thermus thermophilus HB8 is able to utilize lactose from whey-based media for the biosynthesis of polyhydroxyalkanoates (PHAs) under nitrogen limitation. T. thermophilus can utilize both, glucose and galactose, the products of lactose hydrolysis. When T. thermophilus HB8 was grown in culture media containing 24% (v/v) whey, PHA was accumulated up to 35% (w/w) of its biomass after 24 h of cultivation. The effect of initial phosphate concentration on the PHA production was also investigated. Using an initial phosphate concentration of 50 mM the PHA accumulation was enhanced. Analysis of the produced PHA from T. thermophilous HB8 grown in whey-based media revealed a novel heteropolymer consisting of the short chain length 3-hydroxyvalerate (3HV; 38 mol%) and the medium chain length, 3-hydroxyheptanoate (3HHp; 9.89 mol%), 3-hydroxynanoate (3HN; 16.59 mol%) and 3-hydroxyundecanoate (3HU; 35.42 mol%). Despite the low molecular weight of the produced PHA by T. thermophilus, whey could be an excellent substrate for the production of heteropolymers with unique properties.     

Poly(3-hydroxybutyrate) production by Cupriavidus necator using waste glycerol

Polyhydroxyalkanoates (PHAs) have been recognized as good substitutes for the non-biodegradable petrochemically produced polymers. However, their high (real or estimated) current production cost limits their industrial applications. This work exploits two strategies to enhance PHAs substitution potential: the increase in PHA volumetric productivity in high density cultures and the use of waste glycerol (GRP), a by-product from the biodiesel industry, as primary carbon source for cell growth and polymer synthesis. Cupriavidus necator DSM 545 was used to accumulate poly(3-hydroxybutyrate) (P(3HB)) from GRP and from commercial glycerol (PG) as control substrate. On PG, productivities between 0.6 g_PHB L^?1 h^?1 and 1.5 g_PHB L^?1 h^?1 were attained. The maximum cell DW was 82.5 g_DW L^?1, the P(3HB) content being 62%. When GRP was used, 68.8 g_DW L^?1 with a P(3HB) accumulation of 38% resulting in a final productivity of 0.84 g_PHB L^?1 h^?1 was obtained. By decreasing the biomass concentration at which accumulation was triggered, a productivity of 1.1 g_PHB L^?1 h^?1 (50% P(3HB), w/w) was attained using GRP. P(3HB) molecular weights (M_w) ranged from 7.9 × 10⁵ to 9.6 × 10⁵ Da.     

Production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) from unrelated carbon sources by metabolically engineered Escherichia coli

A metabolically engineered Escherichia coli has been constructed for the production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] from unrelated carbon sources. Genes involved in succinate degradation in Clostridium kluyveri and P(3HB) accumulation pathway of Ralstonia eutropha were co-expressed for the synthesis of the above copolyester. E. coli native succinate semialdehyde dehydrogenase genes sad and gabD were both deleted for eliminating succinate formation from succinate semialdehyde, which functioned to enhance the carbon flux to 4HB biosynthesis. The metabolically engineered E. coli produced 9.4 g l^?1 cell dry weight containing 65.5% P(3HB-co-11.1 mol% 4HB) using glucose as carbon source in a 48 h shake flask growth. The presence of 1.5–2 g l^?1 α-ketoglutarate or 1.0 g l^?1 citrate enhanced the 4HB monomer content from 11.1% to more than 20%. In a 6 l fermentor study, a 23.5 g l^?1 cell dry weight containing 62.7% P(3HB-co-12.5 mol% 4HB) was obtained after 29 h of cultivation. To the best of our knowledge, this study reports the highest 4HB monomer content in P(3HB-co-4HB) produced from unrelated carbon sources.     

Thermophilic bacterium Caldimonas taiwanensis produces poly(3-hydroxybutyrate-co-3-hydroxyvalerate) from starch and valerate as carbon sources

Caldimonas taiwanensis accumulated polyhydroxybutyrate (PHB) at 55 °C from gluconate, fructose, maltose, and glycerol under nitrogen-limited condition. The PHB content peaked at 14 h after inoculation from gluconate. C. taiwanensis did not grow or accumulate PHA from fatty acids as the sole carbon source; however, it incorporated 3-hydroxyvalerate (3-HV) into PHB polymer from gluconate and valerate as a mixed carbon source. By adjusting the valerate concentration, the molar fraction of 3-HV could be modulated from 10 mol% to 95 mol%. Fatty acid valerate substantially inhibited cell growth and PHA accumulation with the addition of as little as 5 mM to the medium. Supplementing the medium with yeast extract overcame the inhibition, which enhanced not only the yield of biomass but also PHA productivity. The in vivo substrate specificity of PHA synthase ranged from C₄ to C₆. In addition, C. taiwanensis also incorporated a wide range of 3-HV into PHA from soluble starch and valerate as a mixed carbon source. Food-grade starches made from cassava, corn, potato, sweet potato and wheat respectively mixed with valerate were studied for poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] production. In this study, C. taiwanensis exhibited high promise for reducing the production cost of P(3HB-co-3HV).     

Xylose-based hydrolysate from eucalyptus extract as feedstock for poly(lactate-co-3-hydroxybutyrate) production in engineered Escherichia coli

Woody extract-derived hemicellulosic hydrolysate, which was obtained from dissolving pulp manufacturing, was utilized as feedstock for the production of poly(lactate-co-3-hydroxybutyrate) [P(LA-co-3HB)] in engineered Escherichia coli. The hydrolysate was composed of mainly xylose and galactose, and contained impurities mainly acetate, which was found to inhibit the polymer synthesis rather than the cell growth. Thus, acetate and other impurities were removed through active charcoal and ion-exchange columns. Using the purified hydrolysate, P(LA-co-3HB) was successfully produced (cell dry weight 8.6 g/L, polymer concentration 5.4 g/L, LA fraction 5.5 mol%, polymer content 62.4%), the amount of which was comparable to that obtained using reagent grade xylose and galactose. Therefore, the hydrolysate from woody extract is considered as an abundant, inexpensive and efficient feedstock applicable to consolidated process for P(LA-co-3HB) production, when the removal of acetic acid was satisfactorily accomplished.     

Production and characterization of terpolyester poly(3-hydroxybutyrate-co-3-hydroxyvalerate-co-3-hydroxyhexanoate) by recombinant Aeromonas hydrophila 4AK4 harboring genes phaAB

Recombinant Aeromonas hydrophila 4AK4 harboring phbA and phbB (phaAB) genes encoding β-ketothiolase and acetoacetyl-CoA reductase of Ralstonia eutropha produced a terpolyester of 3-hydroxybutyrate (3HB), 3-hydroxyvalerate (3HV), and 3-hydroxyhexanoate (3HHx) [P(3HB-co-3HV-co-3HHx)] from mixtures of dodecanoic acid and propionic acid. Depending on the concentration of propionic acid in bacterial cultures, cell growth represented by cellular dry weight (CDW), P(3HB-co-3HV-co-3HHx) contents in dry cells and 3HV molar percentage in the terpolyester ranged from 0.43 g l⁻¹ to 3.29 g l⁻¹, 20.7% to 35.6%, 2.3 mol% to 7.1 mol%, respectively. Number average molecular (M_n) weights of the terpolyesters were 303,000–800,000, independent from monomer fraction content. This terpolyester was characterized by nuclear magnetic resonance (NMR), gel-permeation chromatography (GPC), differential scanning calorimetry (DSC), thermogravimetric analysis (TGA) and stress–strain measurement studies. Results showed that the terpolyester had higher thermal stability and elongation at break compared with that of homopolymer poly(3-hydroxybutyrate) (PHB) and its copolymers P(3HB-co-5 mol%3HV) or P(3HB-co-12 mol%3HHx). In addition, the terpolyester had lower melting (T_m) temperatures and enthalpy of fusions (ΔH_m) than PHB did.     

Synthesis of polyhydroxyalkanoates from glucose that contain medium-chain-length monomers via the reversed fatty acid β-oxidation cycle in Escherichia coli

Polyhydroxyalkanoates that contain the medium-chain-length monomers (mcl-PHAs) have a wide range of applications owing to their superior physical and mechanical properties. A challenge to synthesize such mcl-PHAs from unrelated and renewable sources is exploiting the efficient metabolic pathways that lead to the formation of precursor (R)-3-hydroxyacyl-CoA. Here, by engineering the reversed fatty acid β-oxidation cycle, we were able to synthesize mcl-PHAs in Escherichia coli directly from glucose. After deletion of the major thioesterases, the engineered E. coli produced 6.62 wt% of cell dry weight mcl-PHA heteropolymers. Furthermore, when a low-substrate-specificity PHA synthase from Pseudomonas stutzeri 1317 was employed, recombinant E. coli synthesized 12.10 wt% of cell dry weight scl–mcl PHA copolymers, of which 21.18 mol% was 3-hydroxybutyrate and 78.82 mol% was medium-chain-length monomers. The reversed fatty acid β-oxidation cycle offered an efficient metabolic pathway for mcl-PHA biosynthesis in E. coli and can be further optimized.     

Aerobic degradation of 2-picolinic acid by a nitrobenzene-assimilating strain: Streptomyces sp. Z2

Streptomyces sp. Z2 was isolated from nitrobenzene contaminated activated sludge, which utilized nitrobenzene as a sole source of carbon, nitrogen, and energy under aerobic condition. It was found that besides nitrobenzene strain Z2 can degrade 2-picolinic acid. Strain Z2 completely degraded 2-picolinic acid with initial concentration of 500 mg/L, 1000 mg/L, 1500 mg/L, 2000 mg/L, 2500 mg/L, and 3000 mg/L within 36 h, 50 h, 72 h, 100 h, 136 h, and 180 h, respectively. Kinetics of 2-picolinic acid degradation was described using the Andrews equation. The kinetic parameters were as follows: q_max = 3.81 h^?1, K_s = 83.10 mg/L, and K_i = 252.11 mg/L. During the biodegradation process, Z2 transformed 2-picolinic acid into a product which was identified as 6-hydroxy picolinic acid by UV–vis spectrometry, ¹H nuclear magnetic resonance spectroscopy, and mass spectrometry. 6-Hydroxy picolinic acid was then cleaved and mineralized with release of ammonia.     

Production and characterization of homopolymer polyhydroxyheptanoate (P3HHp) by a fadBA knockout mutant Pseudomonas putida KTOY06 derived from P. putida KT2442

Pseudomonas putida KT2442 commonly produces medium-chain-length polyhydroxyalkanoates (PHA) consisting of 3-hydroxyhexanoate (C6) to 3-hydroxydodecanoate (C12) when grown in glucose or even number fatty acid. When two of the beta-oxidation genes fadBA were deleted, the P. pudida KT2442 mutant named KTOY06 accumulated a homopolymer of poly-3-hydroxyheptanoate (P3HHp) up to 71 wt% of its cell dry weight in the presence of heptanoate as a single carbon source. P3HHp contents in the cell dry weight were in direct proportional to Na-heptanoate concentration up to 10 g/L. In contrast, under the same cultivation conditions, the wild type P. putida KT2442 produced a copolymer consisting of 3-hydroxyheptanoate (3HHp) and 5.3–8.4 mol% 3-hydroxynonanoate (3HN). Gas chromatography (GC), nuclear magnetic resonance (NMR), differential scanning calorimetry (DSC), thermogravimetric analysis (TGA) and gel permeation chromatography (GPC) were used to characterize the homopolymer P3HHp, respectively. It was found that the P3HHp with an average molecular weight of 455 kDa was a completely amorphous homopolymer without crystallinity. P3HHp is thermo-degradable at around 250 °C.     

Bioprocess strategies for mass multiplication of and metabolite synthesis by plant growth promoting pseudomonads for agronomical applications

The exponential substrate feeding (open-loop) and automated feedback substrate feeding (closed loop) strategies were developed to obtain high cell densities of fluorescent pseudomonad strains R62 and R81 and enhanced production of antifungal compound 2,4-diacetylphloroglucinol (DAPG) from glycerol as a sole carbon source. The exponential feeding strategy resulted in increased glycerol accumulation during the fed-batch cultivation when the predetermined specific growth rate (μ) was set at 0.10 or 0.20 h^?1 (<μ_m = 0.29 h^?1). Automated feeding strategies using dissolved oxygen (DO) or pH as feedback signals resulted in minimal to zero accumulation of glycerol for both the strains. In case of DO-based feeding strategy, biomass productivity of 0.24 g/(L h) and 0.29 g/(L h) was obtained for R62 and R81, respectively. Using pH-based feeding strategy, biomass productivity could be increased to a maximum of 0.51 and 0.54 g/(L h), for the strains R62 and R81, respectively, whereas the DAPG concentration was enhanced to 298 mg/L for R62 and 342 mg/L for R81 strains. These yields of DAPG are thus far the highest reported from GRAS organisms.     

Solution for promoting egl3 gene of Trichoderma reesei high-efficiency secretory expression in Escherichia coli and Lactococcus lactis

The objective of this study was to develop a solution for promoting egl3 gene of Trichoderma reesei (coding β-1,4-endoglucanase, EGIII) high-efficiency secretory expression in Escherichia coli and Lactococcus lactis and to investigate the effect of the best recombinant on degrading paper and wheat straw. The coding sequence of the egl3 gene fused with a gene fragment of Usp45 (usp45) of L. lactis was cloned to pMG36e and was expressed in E. coli DH 5α (DH 5α) and L. lactis subsp. lactis MG1363 (MG1363). The maximal productivity in recombinant DH 5α was 226 mU mL⁻¹ for extracellular EGIII and 535 mU mL⁻¹ for intracellular EGIII. The maximal productivity in recombinant MG1363 was 1118 mU mL⁻¹ for extracellular EGIII and 761 mU mL⁻¹ for intracellular EGIII. The plasmid stability in recombinant MG1363 was higher than 85% at 60 generations. Recombinant MG1363 vigorously degraded paper and wheat straw and produced sufficient acids. This study provided EGIII transgenic lactic acid bacteria for processing agricultural byproducts.     

Modelling and simulation of continuous L (+) lactic acid production from sugarcane juice in membrane integrated hybrid-reactor system

Modelling and simulation was done for a two-stage membrane-integrated hybrid reactor system for continuous production of L (+) lactic acid under non-neutralizing conditions. The model captures microbial conversion of sugar cane juice to lactic acid under substrate–product inhibitions with downstream purification by nanofiltration. All the major phenomena and the governing parameters like fluid flow, feed dilution, substrate–product inhibitions, Donnan and steric effects during micro and nanofiltration for cell recycle, product separation and purification have been reflected in the modelling. The model describes a green, integrated continuous process of direct lactic acid production starting with a cheap, renewable carbon source. The highest lactic acid concentration achieved after the final stage of nanofiltration was 66.97 g/L at 13 kg/cm² operating pressure when the overall productivity reached 12.40 g/(L h). The developed model could successfully predict production, purification and transport of lactic acid through two stage membrane modules. Performance of the model was very good as indicated in the high overall correlation coefficient (R² > 0.980) and the low relative error (RE < 0.1).     

Effects of redox potential control on succinic acid production by engineered Escherichia coli under anaerobic conditions

The effects of oxido-reduction potential (ORP) control on succinic acid production have been investigated in Escherichia coli LL016. In LL016, two CO₂ fixation pathways were achieved and NAD⁺ supply was enhanced by co-expression of heterologous pyruvate carboxylase (PYC) and nicotinic acid phosphoribosyltransferase (NAPRTase). During anaerobic fermentation, cell growth and metabolite distribution were changed with redox potential levels in the range of −200 to −400 mV. From the results, the ORP level of −400 mV was preferable, which resulted in the high succinic acid concentration (28.6 g/L) and high succinic acid productivity (0.33 g/L/h). Meanwhile, the yield of succinic acid at the ORP level of −400 mV was 39% higher than that at the ORP level of −200 mV. In addition, a higher NADH/NAD⁺ ratio and increased enzyme activities were also achieved by regulating the culture to a more reductive environment, which further enhanced the succinic acid production.     

Rapid ethanol production at elevated temperatures by engineered thermotolerant Kluyveromyces marxianus via the NADP(H)-preferring xylose reductase-xylitol dehydrogenase pathway

Conversion of xylose to ethanol by yeasts is a challenge because of the redox imbalances under oxygen-limited conditions. The thermotolerant yeast Kluyveromyces marxianus grows well with xylose as a carbon source at elevated temperatures, but its xylose fermentation ability is weak. In this study, a combination of the NADPH-preferring xylose reductase (XR) from Neurospora crassa and the NADP⁺-preferring xylitol dehydrogenase (XDH) mutant from Scheffersomyces stipitis (Pichia stipitis) was constructed. The xylose fermentation ability and redox balance of the recombinant strains were improved significantly by over-expression of several downstream genes. The intracellular concentrations of coenzymes and the reduced coenzyme/oxidized coenzyme ratio increased significantly in these metabolic strains. The byproducts, such as glycerol and acetic acid, were significantly reduced by the disruption of glycerol-3-phosphate dehydrogenase (GPD1). The resulting engineered K. marxianus YZJ088 strain produced 44.95 g/L ethanol from 118.39 g/L xylose with a productivity of 2.49 g/L/h at 42 °C. Additionally, YZJ088 realized glucose and xylose co-fermentation and produced 51.43 g/L ethanol from a mixture of 103.97 g/L xylose and 40.96 g/L glucose with a productivity of 2.14 g/L/h at 42 °C. These promising results validate the YZJ088 strain as an excellent producer of ethanol from xylose through the synthetic xylose assimilation pathway.     

Improvement on the yield of polyhydroxyalkanotes production from cheese whey by a recombinant Escherichia coli strain using the proton suicide methodology

In this work Escherichia coli strain CML3-1 was engineered through the insertion of Cupriavidus necator P(3HB)-synthesis genes, fused to a lactose-inducible promoter, into the chromosome, via transposition-mediated mechanism. It was shown that polyhydroxyalkanotes (PHAs) production by this strain, using cheese whey, was low due to a significant organic acids (OA) synthesis. The proton suicide method was used as a strategy to obtain an E. coli mutant strain with a reduced OA-producing capacity, aiming at driving bacterial metabolism toward PHAs synthesis.Thirteen E. coli mutant strains were obtained and tested in shake flask assays, using either rich or defined media supplemented with lactose. P8-X8 was selected as the best candidate strain for bioreactor fed-batch tests using cheese whey as the sole carbon source. Although cell growth was considerably slower for this mutant strain, a lower yield of OA on substrate (0.04 Cmol_OA/Cmol_lac) and a higher P(3HB) production (18.88 g_P(3HB)/L) were achieved, comparing to the original recombinant strain (0.11 Cmol_OA/Cmol_lac and 7.8 g_P(3HB)/L, respectively). This methodology showed to be effective on the reduction of OA yield by consequently improving the P(3HB) yield on lactose (0.28 Cmol_P(3HB)/Cmol_lac vs 0.10 Cmol_P(3HB)/Cmol_lac of the original strain).     

Mycophenolic acid production in solid-state fermentation using a packed-bed bioreactor

Mycophenolic acid (MPA) was produced from Penicillium brevicompactum by solid-state fermentation (SSF) using pearl barley, and submerged fermentation (SmF) using mannitol. It was found that SSF was superior to SmF in terms of MPA concentration (1219 mg/L vs. 60 mg/L after 144 h fermentation), and the product yields were 6.1 mg/g pearl barley for SSF and 1.2 mg/g mannitol for SmF. The volumetric productivities were 8.5 and 0.42 mg/L h for SSF and SmF, respectively.The optimum solid substrate of SSF for MPA production was pearl barley, producing 5470 mg/kg compared with wheat bran (1601 mg/kg), oat (3717 mg/kg) and rice (2597 mg/kg). The optimum moisture content, incubation time and inoculum concentrations were 70%, 144 h and 6%, respectively. Neither the addition of mannitol or (NH4)₂HPO₄ nor adjustment of media pH within the range of 3–7 significantly enhanced MPA production.MPA production by SSF using a packed-bed bioreactor was performed and an increased maximum production of MPA 6.9 mg/g was achieved at 168 h incubation time. The higher volumetric productivity and concentrations makes SSF an attractive alternative to SmF for MPA production.     

Use of different carbon sources in cultivation of recombinant Pichia pastoris for angiostatin production

To improve the growth of recombinant Pichia pastoris with a phenotype of Mut^S and expression of angiostatin, the effects of glycerol, sorbitol, acetate and lactic acid which were, respectively, added together with methanol in the expression phase, were studied in a 5-l fermentor. Methanol concentration was automatically controlled at 5 g/l by a methanol monitor and control system, while the feeding of the other carbon source was manually adjusted. The angiostatin production level was 108 mg/l when glycerol was added at an initial rate of 2.3 g/h and gradually increased to 9.9 g/h within an induction period of 96 h. The angiostatin concentration was 141 mg/l as sorbitol was used, while only 52 mg/l were obtained on acetate. The highest angiostatin production of 191 mg/l was achieved as lactic acid was used; whose feeding rate was gradually increased from 2.6 to 11.3 g/h. Lactic acid accumulated during the induction phase and reached 6.3 g/l at the end of fermentation. However, the accumulation of lactic acid did not interfere with angiostatin production, indicating that lactic acid to be a non-repressive carbon source. The average productivity and specific productivity of angiostatin obtained on lactic acid and methanol were, respectively, 2.96 and 0.044 mg/(g h), 1.7- and 2.5-fold of those obtained in the fermentation fed with glycerol and methanol.     

Heterologous production of caffeic acid from tyrosine in Escherichia coli

Caffeic acid is a plant secondary metabolite and its biological synthesis has attracted increased attention due to its beneficial effects on human health. In this study, Escherichia coli was engineered for the production of caffeic acid using tyrosine as the initial precursor of the pathway. The pathway design included tyrosine ammonia lyase (TAL) from Rhodotorula glutinis to convert tyrosine to p-coumaric acid and 4-coumarate 3-hydroxylase (C3H) from Saccharothrix espanaensis or cytochrome P450 CYP199A2 from Rhodopseudomonas palustris to convert p-coumaric acid to caffeic acid. The genes were codon-optimized and different combinations of plasmids were used to improve the titer of caffeic acid. TAL was able to efficiently convert 3 mM of tyrosine to p-coumaric acid with the highest production obtained being 2.62 mM (472 mg/L). CYP199A2 exhibited higher catalytic activity towards p-coumaric acid than C3H. The highest caffeic acid production obtained using TAL and CYP199A2 and TAL and C3H was 1.56 mM (280 mg/L) and 1 mM (180 mg/L), respectively. This is the first study that shows caffeic acid production using CYP199A2 and tyrosine as the initial precursor. This study suggests the possibility of further producing more complex plant secondary metabolites like flavonoids and curcuminoids.