Production of poly-β-hydroxybutyrate by fed-batch culture of recombinantEscherichia coli

Summary A recombinantEscherichia coli strain harboring the PHB biosynthesis genes fromAlcaligenes eutrophus was used to produce poly--hydroxybutyrate (PHB) by pH-stat fedbatch culture. Initial glucose concentration for optimal growth was found to be 20g/L from a series of flask cultures. A final PHB concentration of 88.8 g/L could be obtained after 42 hrs of cultivation.     

Production of poly-β-hydroxybutyrate by Alcaligenes eutrophus on different carbon sources

Poly--hydroxybutyrate was produced in shake cultures by Alcaligenes eutrophus H16 on fructose, xylose, and fumaric, itaconic, lactic and propionic acids in a three-stage process. The maximum polymer concentration of 6.9 g l^–1 (69% of cell dry matter) was obtained with 20g l^–1 of fructose with a volumetric productivity of about 0.22 g l^–1 h^–1 at 24h. Up to about 3 g l^–1 (about 50% of cell dry matter) of polymer was also produced on lactic and propionic acids as the sole carbon source during the production phase. In multivatiate optimization employing an orthogonal 2³-factorial central composite experimental design with fructose as the substrate in a single-stage process, the optimal initial fructose concentration decreased from 35 g l^–1 to 24 g l^–1 when the incubation time was increased from about 35 h to 96 h. The optimal shaking speed range was 90–113 rpm. Correspondence to: S. Linko     

Production of poly-β-hydroxybutyrate by Azotobacter vinelandii strain UWD during growth on molasses and other complex carbon sources

Summary Azotobacter vinelandii strain UWD formed >2 mg/ml poly--hydroxybutyrate (pHB) during exponential growth in media containing ammonium acetate and 1% w/v glucose, fructose, sucrose, or maltose, and >1.5 mg/ml with 1% w/v sodium gluconate or glycerol. After acetate exhaustion, pHB formation accompanied carbohydrate utilization and pHB rapidly accounted for 53%–70% of the cell mass. Strain UWD also formed >2 mg/ml pHB when it was grown with 2% w/v corn syrup, cane molasses, beet molasses, or malt extract. Beet molasses had a growth stimulatory effect which promoted higher yields of pHB/ml and a high ratio of pHB/protein. Malt extract also promoted higher yields of pHB/ml. In this case, pHB formation was no longer subject to acetate repression and the cells contained a higher ratio of pHB/protein. This study shows that unrefined carbon sources support pHB formation in strain UWD and that the yields of pHB were comparable to or better than those obtained with refined carbon sources.     

Increased poly-β-hydroxybutyrate (PHB) chain length by the modulation of PHA synthase activity in recombinant Escherichia coli

A second promoter (P1) was inserted to the PHA (poly--hydroxyalkanoate) operon (pSP2) of Esherichia coli DH5 with an optimal E. coli ribosome binding site and a trc strong promoter (pSJS1) to obtain poly--hydroxybutyrate (PHB) with long chain length. When the inducer, IPTG was added to the culture at 0.4 mM, the average molecular weight was 1.1 × 10⁶ Da. However, an even greater increase of the PHB average molecular weight to 2.5 × 10⁷ Da was observed without IPTG being added.     

Production of poly-β-hydroxybutyrate by Alcaligenes eutrophus transformants harbouring cloned phbCAB genes

Summary Three transformants of Alcaligenes eutrophus harbouring the recombinant plasmids containing phbCAB, phbAB, and phbC genes, were cultivated to investigate the effect of cloned genes on cell growth and poly--hydroxybutyrate accumulation. Both in the nutrient-rich and minimal media, the increased PHB accumulation in the transformants was observed compared to the parent strain, and this was the result of the increased enzyme activities in the transformants. Low carbon concentration and high C/N molar ratio favored higher PHB accumulations in the transformants. The transformant harbouring the phbC gene showed the highest PHB accumulation, which indicated that PHB synthase was the most critical enzyme for PHB biosynthesis in the transformant.     

Production of poly-(β-hydroxybutyrate) from saponified Vernonia galamensis oil by Alcaligenes eutrophus

Saponified vernonia oil was converted exclusively to poly(β-hydroxybutyrate) (PHB) by Alcaligenes eutrophus in a single-stage batch culture. After harvesting, centrifugation followed by lyophilization, the resulting dried cells contained up to 42.8 wt% PHB having a peak molecular mass of 381 863 Da, weight-average molecular mass of 308 390 Da, and a polydispersity of 1.1. The PHB had a melting point (T_m) range of 163–174°C with a maximum at 172°C (lit. T_m, 175°C), and heat of fusion of 18.43 cal g⁻¹. Fermentation performed under varying conditions of nitrogen limitation indicated that there was no significant effect of nitrogen concentration on the molecular mass of PHB produced from vernonia oil by A. eutrophus. Received 27 March 1998/ Accepted in revised form 17 July 1998     

Over-production of human interferon-γ by HCDC of recombinant Escherichia coli

A simple fed-batch process was developed using a modified variable specific growth rate feeding strategy for high cell density cultivation of Escherichia coli BL21 (DE3) expressing human interferon-gamma (hIFN-γ). The feeding rate was adjusted to achieve the maximum attainable specific growth rate during fed-batch cultivation. In this method, specific growth rate was changed from a maximum value of 0.55 h⁻¹ at the beginning of feeding and then it was reduced to 0.4 h⁻¹ at induction time.The final concentration of biomass and IFN-γ was reached to ∼115 g l⁻¹ (DCW) and 42.5 g(hIFN-γ) l⁻¹ after 16.5 h, also the final specific yield and overall productivity of recombinant hIFN-γ (rhIFN-γ) were obtained 0.37 g(hIFN-γ) g⁻¹ DCW and 2.57 g(hIFN-γ) l⁻¹ h⁻¹, respectively. According to available data this is the highest specific yield and productivity that has been reported for recombinant proteins production yet.     

Effect of Inducers on the Production of 5‐Aminolevulinic Acid by Recombinant Escherichia coli

Abstract

Aminolevulinic acid (ALA) was produced by recombinant Escherichia coli BL21(DE3) (pET28‐A.R‐hemA) harboring the ALA synthase gene (hemA) from Agrobacterium radiobacter zju‐0121. The effects of inducers on the ALA synthase activity and ALA productivity were evaluated. The results indicated that a low isopropyl‐β‐D‐thiogalactoside (IPTG) concentration (0.05 mmol/L) was favorable for high expression of ALA synthase, which resulted in higher ALA productivity. For metabolic engineering applications, lactose was a better substitute of IPTG for active enzyme expression. When lactose concentration was 5 mmol/L, the specific ALA synthase activity and ALA productivity reached 16.7 nmol/(min · mg of protein) and 1.15 g/L, respectively, which were about 15% and 43% higher than those induced by IPTG.     

Production of poly-β-hydroxybutyrate by Azotobacter vinelandii UWD in media containing sugars and complex nitrogen sources

Summary Vigorously aerated batch cultures of Azotobacter vinelandii UWD formed < 1 g poly--hydroxybutyrate (PHB)/l in media containing pure sugars and 3 g PHB/l in media containing cane molasses, corn syrup or malt extract. However, > 7 g PHB/l was formed when the medium contained 5% beet molasses. Increased yields of PHB were promoted in the media containing pure or unrefined sugars by the addition of complex nitrogen sources. The greatest effect was obtained with 0.05–0.2% fish peptone (FP), proteose peptone no. 3 or yeast extract. Peptones caused a 1.6-fold increase in residual non-PHB biomass and up to a 25-fold increase in PHB content. Hence the increased PHB formation was not simply due to stimulation of culture growth. The amount of PHB per cell protein formed by UWD in media containing FP was greatest in glucose = corn syrup > malt extract > sucrose = fructose = cane molasses > maltose, as carbon sources. The addition of FP to medium containing beet molasses did not stimulate PHB yield. The peptone effect was most significant in well-aerated cultures, which were fixed nitrogen and consuming glucose at a high rate. An explanation for the peptone effect on PHB yield stimulation is proposed.     

Rapid and simple analysis of poly-β-hydroxybutyrate content by capillary isotachophoresis

Summary We present a rapid method for the direct analysis of poly--hydroxybutyrate (PHB) content in the soil bacteria Alcaligenes eutrophus. PHB from the fresh cells was converted by sulfuric acid to the crotonic acid and measured by capillary isotachophoresis after the neutralization by CaCO₃. The method can be used for rapid and routine monitoring of the fermentation processes in samples containing 0.001 to 20 mg of PHB.     

Production and characterization of poly-β-hydroxybutyrate (PHB) polymer from Aulosira fertilissima

Biopolymers such as polyhydroxyalkanoates (PHAs) are a class of secondary metabolites with promising importance in the field of environmental, agricultural, and biomedical sciences. To date, high-cost commercial production of PHAs is being carried out with heterotrophic bacterial species. In this study, a photoautotrophic N₂-fixing cyanobacterium, Aulosira fertilissima, has been identified as a potential source for the production of poly-β-hydroxybutyrate (PHB). An accumulation up to 66% dry cell weight (dcw) was recorded when the cyanobacterium was cultured in acetate (0.3%) + citrate (0.3%)-supplemented medium against 6% control. Aulosira culture supplemented with 0.5% citrate under P deficiency followed by 5?days of dark incubation also depicted a PHB accumulation of 51% (dcw). PHB content of A. fertilissima reached up to 77% (dcw) under P deficiency with 0.5% acetate supplementation. Optimization of process parameters by response surface methodology resulted into polymer accumulation up to 85% (dcw) at 0.26% citrate, 0.28% acetate, and 5.58?mg?L^?1 K₂HPO₄ for an incubation period of 5?days. In the A. fertilissima cultures pre-grown in fructose (1.0%)-supplemented BG 11 medium, when subjected to the optimized condition, the PHB pool boosted up to 1.59?g?L^?1, a value ～50-fold higher than the control. A. fertilissima is the first cyanobacterium where PHB accumulation reached up to 85% (dcw) by manipulating the nutrient status of the culture medium. The polymer extracted from A. fertilissima exhibited comparable material properties with the commercial polymer. As compared with heterotrophic bacteria, carbon requirement in A. fertilissima for PHB production is lower by one order magnitude; thus, low-cost PHB production can be envisaged.     

Production of poly(β-hydroxybutyrate) by Comamonas testosteroni during growth on naphthalene

Comamonas testosteroni has been found to produce poly(-hydroxybutyrate) (PHB) during its growth on naphthalene. Fourier transform infrared spectroscopy (FTIR) and ¹³C nuclear magnetic resonance (NMR) analysis confirmed it as a homopolymer of 3-hydroxybutyrate. Oxygen and essential nutrient limitation other than carbon source play a major role in maximum PHB production. Nitrogen limitation was found to have a profound effect, with 0.2 g ammonium nitrate/l optimum for PHB production. Both aeration and iron were found to be essential for growth and PHB accumulation. Ferric chloride at 0.04 g/l concentration was found to be optimum for PHB accumulation. Phosphate source variation showed no significant effect. Using naphthalene as a sole carbon source in optimized Bushnell Haas medium, 85% of the dry cell mass was extracted as chloroform-soluble PHB.     

Enzymatic synthesis of poly-β-hydroxybutyrate inZoogloea ramigera

The enzyme activity synthesizing poly--hydroxybutyrate (PHB) was mainly localized in the PHB-containing particulate fraction ofZoogloea ramigera I-16-M, when it grew flocculatedly in a medium supplemented with glucose. On the other hand, the enzyme activity remained in the soluble fraction, when the bacterium grew dispersedly in a glucose-starved medium.The soluble PHB synthase activity became associated with the particulate fraction as PHB synthesis was initiated on the addition of glucose to the dispersed culture. Conversely, the enzyme activity was released from the PHB-containing granules to the soluble fraction when the flocculated culture was kept incubated without supplementing the medium with glucose.PHB synthase was also incorporated into the newly formed PHB fraction when partially purified soluble PHB synthase was incubated withd(-)--hydroxybutyryl CoA in vitro.Although attempts to solubilize the particulate enzyme were unsuccessful, and the soluble enzyme became extremely unstable in advanced stages of purification, both PHB synthases had the same strict substrate specificity ford(-)--hydroxybutyryl CoA, and showed the same pH optimum at 7.0.Non-Standard Abbreviations PHB poly--hydroxybutyrate     

Production of β-carotene by recombinant Escherichia coli with engineered whole mevalonate pathway in batch and fed-batch cultures

Recombinant Escherichia coli engineered to contain the whole mevalonate pathway and foreign genes for β-carotene biosynthesis, was utilized for production of β-carotene in bioreactor cultures. Optimum culture conditions were established in batch and pH-stat fed-batch cultures to determine the optimal feeding strategy thereby improving production yield. The specific growth rate and volumetric productivity in batch cultures at 37°C were 1.7-fold and 2-fold higher, respectively, than those at 28°C. Glycerol was superior to glucose as a carbon source. Maximum β-carotene production (titer of 663 mg/L and overall volumetric productivity of 24.6 mg/L × h) resulted from the simultaneous addition of 500 g/L glycerol and 50 g/L yeast extract in pH-stat fed-batch culture.     

Transport of poly-β-hydroxybutyrate in human plasma

Poly-β-hydroxybutyrate (PHB) is an amphiphilic lipid that has been found to be a ubiquitous component of the cellular membranes of bacteria, plants and animals. The distribution of PHB in human plasma was investigated using chemical and immunological methods. PHB concentrations proved highly variable; in a random group of 24 blood donors, total plasma PHB ranged from 0.60 to 18.2 mg/l, with a mean of 3.5 mg/l. In plasma separated by density gradient ultracentrifugation, lipoproteins carried 20–30% of total plasma PHB; 6–14% in the very low density lipoproteins (VLDL), 8–16% in the low density lipoproteins (LDL), and < 3% in the high density lipoproteins (HDL). The majority of plasma PHB (70–80%) was found in protein fractions of density > 1.22 g/ml. Western blot analysis of the high density fractions with anti-PHB F(ab')₂ identified albumin as the major PHB-binding protein. The affinity of albumin for PHB was confirmed by in vitro studies which demonstrated transfer of ¹⁴C-PHB from chloroform into aqueous solutions of human and bovine serum albumins. PHB was less tightly bound to LDL than to other plasma components; the polymer could be isolated from LDL by extraction with chloroform, or by digestion with alkaline hypochlorite, but it could not similarly be recovered from VLDL or albumin. PHB in the LDL correlated positively with total plasma cholesterol and LDL cholesterol, and negatively with HDL cholesterol. The wide concentration range of PHB in plasma, its presence in VLDL and LDL and absence in HDL, coupled with its physical properties, suggest it may have important physiological effects.     

Production of poly-β-hydroxybutyrate from methanol: characterization of a new isolate of Methylobacterium extorquens

Summary Poly--hydroxybutyric acid (PHB) and similar bacterial polyesters are promising candidates for the development of environment-friendly, totally biodegradable plastics. The use of methanol, one of the cheapest noble substrates available, may help to reduce the cost of producing such bioplastics. As a first step, a culture collection of 118 putative methylotrophic microorganisms was obtained from various soil samples without any laboratory enrichment step to favour culture diversity. The most promising culture was selected based on rapidity of growth and PHB accumulation and later identified as Methylobacterium extorquens. This isolate was obtained from soml contaminated regularly with used oil products for some 40 years. Concentrations of methanol greater than 8 g/l affected growth significantly and the methanol concentration was optimal at 1.7 g/l. PHB concentrations averaged 25–30% (w/v) of dry weight under non-optimized conditions. Controlling methanol concentration, using an open-loop configuration, led to biomass levels of 9–10 g/l containing 30–33% PHB while preventing methanol accumulation. The new isolate was also able to produce the co-polymer PHB/poly--hydroxyvalerate (PHV) using the mixture methanol + valerate. The PHV-to-PHB ratio was about 0.2 at the end of the fermentation. An average molecular mass varying between 2 and 3 × 10⁵ Da was obtained for three PHB samples using two different measurement methods.Publication number NRCC No. 33672 Offprint requests to: D. Groleau     

Production of poly-β-hydroxybutyrate by thermophilic cyanobacterium, Synechococcus sp. MA19, under phosphate-limited conditions

Synechococcus sp. MA19, grown autotrophically under phosphate-limited conditions at 50 °C, produced poly--hydroxybutyrate (PHB) when intracellular phosphate content was 0.043–0.076mmol per g of cellular components. In the culture for 260h using Ca₃(PO₄)₂ as a phosphate source, strain MA19 accumulated PHB at 55% (w/w) of the dry cells and the amount of PHB produced was 2.4gl^–1 which was almost twice that without Ca₃(PO₄)₂ addition.     

Production of γ-aminobutyric acid in Escherichia coli by engineering MSG pathway

Abstract

The compound γ-aminobutyric acid (GABA) has many important physiological functions. The effect of glutamate decarboxylases and the glutamate/GABA antiporter on GABA production was investigated in Escherichia coli. Three genes, gadA, gadB, and gadC were cloned and ligated alone or in combination into the plasmid pET32a. The constructed plasmids were transformed into Escherichia coli BL21(DE3). Three strains, E. coli BL21(DE3)/pET32a-gadA, E. coli BL21(DE3)/pET32a-gadAB and E. coli BL21(DE3)/pET32a-gadABC were selected and identified. The respective titers of GABA from the three strains grown in shake flasks were 1.25, 2.31, and 3.98?g/L. The optimal titer of the substrate and the optimal pH for GABA production were 40?g/L and 4.2, respectively. The highest titer of GABA was 23.6?g/L at 36?h in batch fermentation and was 31.3?g/L at 57?h in fed-batch fermentation. This study lays a foundation for the development and use of GABA.     

Optimal Production of Poly-γ-glutamic Acid by Metabolically Engineered Escherichia coli

Metabolically-engineered Escherichia coli strains were developed by cloning poly-γ-glutamic acid (γ-PGA) biosynthesis genes, consisting of pgsB, pgsC and pgsA, from Bacillus subtilis The metabolic and regulatory pathways of γ-PGA biosynthesis in E. coli were analyzed by DNA microarray. The inducible trc promoter and a constitutive promoter (P_HCE) derived from the d-amino acid aminotransferase (D-AAT) gene of Geobacillus toebii were employed. The constitutive HCE promoter was more efficient than inducible trc promoter for the expression of γ-PGA biosynthesis genes. DNA microarray analysis showed that the expression levels of several NtrC family genes, glnA, glnK, glnG, yhdX, yhdY, yhdZ, amtB, nac, argT and cbl were up-regulated and sucA, B, C, D genes were down-regulated. When (NH₄)₂SO₄ was added at 40 g/l into the feeding solution, the final γ-PGA concentration reached 3.7 g/l in the fed-batch culture of recombinant E. coli/pCOpgs.