Yield of poly-D(-)-3-hydroxybutyrate from various carbon sources: a theoretical study

The theoretical yield of poly-D(-)-3-hydroxybutyrate (PHB) has been estimated from the biochemical pathway leading to PHB when a carbohydrate (glucose), a C(1) compound (methanol), a C(2) compound (acetic acid), or a C(4) compound (butyric acid) is used as a carbon source. In estimating the yield, recycling (or regeneration) of NADP(+)/ (NADPH + H(+)) and NAD(+) /(NADH + H(+)) have been taken into account. A special emphasis is made on te regeneration of NADPH, which is the coenzyme of acetoacetyl-CoA reductase, one of three key enzymes involved in the biosynthesis of PHB. As a NADPH-regenerating enzyme, glucose-6-phosphate dehydrogenase or isocitrate dehydrogenase is conceived. An equation which predicts the overall yield of PHB when non-PHB residual biomass is actually formed has been derived as a function of both the theoretical yield and PHB content of the dry cell mass. The ratio of the overall yield to the theoretical yield is roughly proportional to the PHB content. (c) 1993 John Wiley & Sons, Inc.     

Zur Kinetik des Wachstums und der Speicherung von Poly-D(−)-3-hydroxybuttersäure bei Alcaligenes latus

Alcaligenes latus strain DSM 1123 has been tested for the production of Poly-D(?3)-3-hydroxybutyric acid using sucrose as the only carton source. The strain is capable of accumulating the polymer associated to the growth very fast and lup to high concentrations in the biomass. Alcaligenes lotus seems to be very interesting for the production of Poly-D(?)-3-hydroxybutyrate in a cheaper and easier way as with other organisms discussed for the biotechnological process in the past.     

Biosynthesis of poly(3-hydroxybutyrate) copolymers by Azotobacter chroococcum 7B: A precursor feeding strategy

A precursor feeding strategy for effective biopolymer producer strain Azotobacter chroococcum 7B was used to synthesize various poly(3-hydroxybutyrate) (PHB) copolymers. We performed experiments on biosynthesis of PHB copolymers by A. chroococcum 7B using various precursors: sucrose as the primary carbon source, various carboxylic acids and ethylene glycol (EG) derivatives [diethylene glycol (DEG), triethylene glycol (TEG), poly(ethylene glycol) (PEG) 300, PEG 400, PEG 1000] as additional carbon sources. We analyzed strain growth parameters including biomass and polymer yields as well as molecular weight and monomer composition of produced copolymers. We demonstrated that A. chroococcum 7B was able to synthesize copolymers using carboxylic acids with the length less than linear 6C, including poly(3-hydroxybutyrate-co-3-hydroxy-4-methylvalerate) (PHB-4MHV) using Y-shaped 6C 3-methylvaleric acid as precursor as well as EG-containing copolymers: PHB–DEG, PHB–TEG, PHB–PEG, and PHB–HV–PEG copolymers using short-chain PEGs (with n?≤?9) as precursors. It was shown that use of the additional carbon sources caused inhibition of cell growth, decrease in polymer yields, fall in polymer molecular weight, decrease in 3-hydroxyvalerate content in produced PHB–HV–PEG copolymer, and change in bacterial cells morphology that were depended on the nature of the precursors (carboxylic acids or EG derivatives) and the timing of its addition to the growth medium.     

High level production of supra molecular weight poly (3-hydroxybutyrate) by metabolically engineered<Emphasis Type="Italic">Escherichia coli</Emphasis>

The supra molecular weight poly ([R]-3-hydroxybutyrate) (PHB), having a molecular weight greater than 2 million Da, has recently been found to possess improved mechanical properties compared with the normal molecular weight PHB, which has a molecular weight of less than 1 million Da. However, applications for this PHB have been hampered due to the difficulty of its production. Reported here, is the development of a new metabolically engineeredEscherichia coli strain and its fermentation for high level production of supra molecular weight PHB. RecombinantE. coli strains, harboring plasmids of different copy numbers containing theAlcaligenes latus PHB biosynthesis genes, were cultured and the molecular weights of the accumulated PHB were compared. When the recombinantE. coli XL 1-Blue, harboring a medium-copy-number pJC2 containing theA. latus PHB biosynthesis genes, was cultivated by fed-batch culture at pH 6.0, supra molecular weight PHB could be produced at up to 89.8 g/L with a productivity of 2.07 g PHB/L-h. The molecular weight of PHB obtained under these conditions was as high as 22 MDa, exceeding by an order of magnitude the molecular weight of PHB typically produced inRalstonia eutropha or recombinantE. coli     

Occurrence of poly-d(−)-3-hydroxyalkanoates in the genus Bacillus

A range of Bacillus strains were examined for their ability to accumulate poly-D(-)-3-hydroxyalkanoates (poly-HAKs) which are naturally occurring materials that are optically active, biodegradable thermoplastics. The organisms could produce poly-D(-)-3-hydroxybutyrate (poly-HB) up to 50% of cell dry weight. The content of poly-HB in the cells varied with the growth conditions. The addition of propionate or valerate in the culture resulted in a synthesis of poly-D(-)-3-hydroxyvalerate (poly-HV). All the strains tested had the ability to synthesize the co-polyester poly-HB-co-HV.     

Utilization of agricultural residues for poly(3-hydroxybutyrate) production by Halomonas boliviensis LC1

Aims: Utilization of cheap and readily available agricultural residues as cheap carbon sources for poly(3‐hydroxybutyrate) (PHB) production by Halomonas boliviensis. Methods and Results: Wheat bran was hydrolysed by a crude enzyme preparation from Aspergillus oryzae NM1 to provide a mixture of reducing sugars composed mainly of glucose, mannose, xylose and arabinose. Growth of H. boliviensis using a mixture of glucose (0·75% w/v) and xylose (0·25% w/v) in the medium led to a PHB content and concentration of 45 wt% and 1 g l^?1, respectively, after 30 h. A similar PHB concentration was attained when H. boliviensis was grown on wheat bran hydrolysate but with a lower PHB content, 34 wt%. In a batch cultivation mode in a fermentor, using 1·8% (w/v) reducing sugars, the maximum PHB accumulation by H. boliviensis was attained in 20 h, but was reduced to about 30 wt%. By adding butyric acid (0·8% v/v), sodium acetate (0·8% w/v) and decreasing the reducing sugars concentration to 1·0% w/v in the medium, PHB accumulation and concentration were increased to 50 wt% and 4 g l^?1, respectively, after 20 h. Butyric acid and sodium acetate for PHB production could also be provided by anaerobic digestion of solid potato waste. Conclusions: Cheap and readily available agricultural residues can be used as substrates to produce PHB. The production of PHB by H. boliviensis using wheat bran hydrolysate as source of carbon is expected to reduce the production cost and motivates further studies. Significance and Impact of the Study: Large‐scale commercial utilization of PHB is mainly hampered by its high production cost. Carbon source for PHB production accounts up to 50% of the total production costs. Thus, the use of waste agricultural residues can substantially reduce the substrate cost (and in turn even provide value to the waste), and can downsize the production costs. This improves the market competitiveness. Studies on PHB production by moderate halophiles were recently initiated with H. boliviensis and findings show that it has potential for commercial exploitation. PHB production by H. boliviensis using wheat bran and potato waste is hence interesting.     

Production of poly(3-hydroxybutyrate) from whey by cell recycle fed-batch culture of recombinant Escherichia coli

A new fermentation strategy using cell recycle membrane system was developed for the efficient production of poly(3-hydroxybutyrate) (PHB) from whey by recombinant Escherichia coli strain CGSC 4401 harboring the Alcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes. By cell recycle, fed-batch cultivation employing an external membrane module, the working volume of fermentation could be constantly maintained at 2.3 l. The final cell concentration, PHB concentration and PHB content of 194 g l^–1, 168 g l^–1 and 87%, respectively, were obtained in 36.5 h by the pH-stat cell recycle fed-batch culture using whey solution concentrated to contain 280 g lactose l^–1 as a feeding solution, resulting in a high productivity of 4.6 g PHB l^–1 h^–1.     

Effect of amino acid supplementation on the synthesis of poly(3-hydroxybutyrate) by recombinant pha Sa + Escherichia coli

The effect of different amino acid supplements to the basal medium on poly(3-hydroxybutyrate) (PHB) accumulation by recombinant pha _Sa ⁺ Escherichia coli (ATCC: PTA-1579) harbouring the poly(3-hydroxybutyrate)-synthesizing genes from Streptomyces aureofaciens NRRL 2209 was studied. With the exception of glycine and valine, all other amino acid supplements brought about enhancement of PHB accumulation. In particular, cysteine, isoleucine or methionine supplementation increased PHB accumulation by 60, 45 and 61% respectively by the recombinant E. coli as compared with PHB accumulation by this organism in the basal medium. The effect of co-ordinated addition of assorted combinations of these three amino acids on PHB accumulation was studied using a 2³ factorial design. The three-factor interaction analyses revealed that the effect of the three amino acids on PHB accumulation by the recombinant E. coli was in the order of cysteine > methionine > isoleucine. The defined medium supplemented with cysteine, methionine and isoleucine at the concentration of 150 mgl^–1 each and glycerol as the carbon source was the optimum medium that resulted in the accumulation of about 52% PHB of cell dry weight.     

Production of poly(3-hydroxybutyrate) from inexpensive substrates

Two inexpensive substrates, starch and whey were used to produce poly(3-hydroxybutyrate) (PHB) in fed-batch cultures of Azotobacter chroococcum and recombinant Escherichia coli, respectively. Oxygen limitation increased PHB contents in both fermentations. In fed-batch culture of A. chroococcum, cell concentration of 54 g l⁻¹ with 46% PHB was obtained with oxygen limitation, whereas 71 g l⁻¹ of cell with 20% PHB was obtained without oxygen limitation. The timing of PHB biosynthesis in recombinant E. coli was controlled using the agitation speed of a stirred tank fermentor. A PHB content of 80% could be obtained with oxygen limitation by increasing the agitation speed up to only 500 rpm.     

Effect of simple and complex carbon sources,low temperature culture and complex carbon feeding policies on poly-3-hydroxybutyric acid (PHB) content and molecular weight (Mw) from Azotobacter chroococcum 6B

The molecular weight (M _w) of poly-3-hydroxybutyrate (PHB), produced by shake-flask culture of Azotobacter chroococcum showed little variation with increasing glucose concentration as carbon source (being in the range of 400–500 kDa), while M _w increased from 300–400 to 640 kDa when grown with increasing concentration of sugar cane molasses. Molecular weight increased nearly 30% from 48 to 72 h culture time when 5% molasses as carbon source was used, while with glucose the highest M _w was reached at 48 h. Under fermentor cultivation A. chroococcum produced PHB with a relatively high M _w of 1590 kDa at 53 h culture time when grown in modified Burk's medium with glucose as carbon source at an initial C/N ratio (molar basis) of 69 under fermentor cultivation. A batch glucose-grown ammonium-limited fermentor culture was repeatedly fed with sugar cane molasses (initial C/N ratio 69) and it was observed that PHB content curve decreased at a slower rate than in the fed-batch culture in which glucose and sucrose were not consumed in the culture medium after the feed.     

Pilot scale production of poly(3-hydroxybutyrate-co-3-hydroxy-valerate) by fed-batch culture of recombinantEscherichia coli

Production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB/V)], by fed-batch culture of recombinantEscherichia coli harboring a plasmid containing theAlcaligenes latus polyhydroxyalkanoate (PHA) biosynthesis genes, was examined in two pilot-scale fermentors with air supply only. In a 30 L fermentor having aK _La value of 0.11 s⁻¹, the final P(3HB/V) concentration and the P(3HB/V) content obtained were 29.6 g/L and 70.1 wt%, respectively, giving a productivity of 1.37 g P(3HB/V)/L-h. In a 300 L fermentor having aK _La of 0.03 s⁻¹, the P(3HB/V) concentration and the P(3HB/V) content were 20.4 g/L and 69 wt%, respectively, giving a productivity of 1.06 g P(3HB/V)/L-h. These results suggest that economical production of P(3HB/V) is possible by fed-batch culture of recombinantE. coli in a large-scale fermentor having lowK _La value.     

Comparison of recombinant Escherichia coli strains for synthesis and accumulation of poly-(3-hydroxybutyric acid) and morphological changes

A stable high-copy-number plasmid pSYL105 containing the Alcaligenes eutrophus polyhydroxyalkanoic acid (PHA) biosynthesis genes was constructed. This plasmid was transferred to seven Escherichia coli strains (K12, B, W, XL1-Blue, JM109, DH5alpha, and HB101), which were subsequently compared for their ability to synthesize and accumulate ploy- (3-hydroxybutyric acid) (PHB). Growth of recombinant cells and PHB synthesis were investigated in detail in Luria-Bertani (LB) medium containing 20 g/L glucose. Cell growth, the rate of PHB synthesis, the extent of PHB accumulation, the amount of glucose utilized, and the amount of acetate formed varied from one strain to another. XL1-Blue (pSYL105) and B (pSYL105) synthesized PHB at the fastest rate, which was ca. 0.2 g PHB/g true cell mass-h, and produced PHB up to 6-7 g/L. The yields of cell mass, true cell mass, and PHB varied considerably among the strains. The PHB yield of XL1-Blue (pSYL105) in LB plus 20 g/L glucose was as high as 0.369 g PHB/g glucose. Strains W (pSYL105) and K12 (pSYL105) accumulated the least amount of PHB with the lowest PHB yield at the lowest synthesis rate. JM109 (pSYL105) accumulated PHB to the highest extent (85.6%) with relatively low true cell mass (0.77 g/L). Considerable filamentation of cells accumulating PHB was observed for all strains except for K12 and W, which seemed to be due either to the overexpression of the foreign PHA biosynthesis enzymes or to the accumulation of PHB. (c) 1994 John Wiley & Sons, Inc.     

3-(Trifluoromethyl)-3-(m-isothiocyanophenyl)diazirine: Synthesis and chemical characterization of a heterobifunctional carbene-generating crosslinking reagent

A new hydrophobic heterobifunctional photocrosslinking reagent 3-(trifluoromethyl)-3-(m-isothiocyanophenyl)diazirine (TRIMID), a carbene precursor, and its radioiodinated analogue [¹²⁵I]TRIMID, have been synthesized and chemically characterized. The reagents were applied for membrane protein modification in human erythrocyte membranes and purple membranes fromHalobacterium halobium. Covalent labeling of the anion transport protein (band 3) via the isothiocyanate function was confirmed. Radiolabeled TRIMID was detected in at least two thermolysin-generated transmembrane fragments of the anion transport protein, and half-maximal inhibition of the erythrocyte anion transport activity was attained with 2.2 mM reagent. In bacteriorhodopsin (BR), a common binding site for the monofunctional phenylisothiocyanate and the bifunctional crosslinking reagent was identified: preincubation of purple membranes with TRIMID suppressed phenylisothio-[¹⁴C]-cyanate binding to BR. [¹²⁵I]TRIMID was recovered in V-1, the N-terminal segment of BR, which includes the phenylisothiocyanate binding site Lys-41. Light-induced intramolecular crosslinking of band 3-derived thermolytic fragments was not observed, although the carbene was generatedin situ and photocrosslinking of the protease V8 fragments of BR was not detected. Chemical and physicochemical characteristics of the new reagent are discussed with regard to limitations imposed for photoinduced site-directed crosslink formation.     

Optimizing conditions for poly(β-hydroxybutyrate) production by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis> LC1 in batch culture with sucrose as carbon source

Halomonas boliviensis LC1 is able to accumulate poly(β-hydroxybutyrate) (PHB) under conditions of excess carbon source and depletion of essential nutrients. This study was aimed at an efficient production of PHB by growing H. boliviensis to high cell concentrations in batch cultures. The effect of ammonium, phosphate, and yeast extract concentrations on cell concentration [cell dry weight (CDW)] and PHB content of H. boliviensis cultured in shake flasks was assayed using a factorial design. High concentrations of these nutrients led to increments in cell growth but reduced the PHB content to some extent. Cultivations of H. boliviensis under controlled conditions in a fermentor using 1.5% (w/v) yeast extract as N source, and intermittent addition of sucrose to provide excess C source, resulted in a polymer accumulation of 44 wt.% and 12 g l⁻¹ CDW after 24 h of cultivation. Batch cultures in a fermentor with initial concentrations of 2.5% (w/v) sucrose and 1.5% (w/v) yeast extract, and with induced oxygen limitation, resulted in an optimum PHB accumulation, PHB concentration and CDW of 54 wt.%, 7.7 g l⁻¹ and 14 g l⁻¹, respectively, after 19 h of cultivation. The addition of casaminoacids in the medium increased the CDW to 14.4 g l⁻¹ in 17 h but reduced the PHB content in the cells to 52 wt.%.     

Mutations induced by 4-(methylnitrosamino)-1-(3-pyridyl)-1-butanone (NNK) in the lacZ and cII genes of Muta™ Mouse

4-(Methylnitrosamino)-1-(3-pyridyl)-1-butanone (NNK) found in chewing tobacco, snuff, cigarettes, and cigars is a tobacco-specific nitrosamine and classified as a possible human carcinogen (Class 2B) by the International Agency for Research on Cancer (IARC). NNK given intraperitoneally was seen to induce lung and liver adenomas.To evaluate the genotoxicity of NNK in vivo, NNK was intraperitoneally administered to Muta™ Mouse at two concentrations (125 and 250 mg/kg, once a week for 4 weeks) followed by the measurement of mutant frequencies in the lacZ and cII genes from lung and liver in the same mice. Characterization of the types of the mutation was determined by sequencing the cII genes from mutant plaques. The mutant frequencies in both target genes from both organs dose-dependently increased up to 10 times compared to those of the control group. For the types of mutations, the ratio of the G:C to A:T mutation in the total number of mutants was less than the ratio of A:T to T:A and A:T to C:G transversion, contrary to a previous report [Cancer Res, 49 (1989) 5305]. The A:T to T:A transversion was the most highly induced mutation both in the lung and liver cII genes. The increasing rate of mutant frequencies in lung and liver over the vehicle control was 55 and 56 times, respectively, while the increasing rate of G:C to A:T transition was only 1.9 and 2.8 times, respectively.These observations show that NNK predominantly induces DNA adducts leading to A:T to T:A and/or A:T to C:G mutations in the transgene.     

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant Escherichia coli arcA mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the ‘one-factor-at-a-time’ technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett–Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box–Wilson design. Under such optimized conditions (22.02 g l⁻¹ glycerol, 1.78 g l⁻¹ CAS, and 1.83 g l⁻¹ inoculum) microaerobic batch cultures gave rise to 8.37 g l⁻¹ CDW and 3.52 g l⁻¹ PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l⁻¹. After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l⁻¹, respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users. An erratum to this article can be found at     

Optimization of cell growth and poly(3-hydroxybutyrate) accumulation on date syrup by a Bacillus megaterium strain

Optimal growth and PHB accumulation in Bacillus megaterium occurred with 5% (w/v) date syrup or beet molasses supplemented with NH₄Cl. When date syrup and beet molasses were used alone without an additional nitrogen source, a cell density of about 3gl^–1 with a PHB content of the cells of 50% (w/w) was achieved. NH₄NO₃ followed by ammonium acetate and then NH₄Cl supported cell growth up to 4.8gl^–1, whereas PHB accumulation was increased with NH₄Cl followed by ammonium acetate, NH₄NO₃ and then (NH₄)₂SO₄ to a PHB content of nearly 42% (w/w). Cultivation of B.megaterium at 30l scale gave a PHB content of 25% (w/w) of the cells and a cell density of 3.4gl^–1 after 14h growth.     

Poly(3-hydroxybutyrate) (PHB) synthesis by recombinant Escherichia coli harbouring Streptomyces aureofaciens PHB biosynthesis genes: effect of various carbon and nitrogen sources

Recombinant Escherichia coli (ATCC:PTA-1579) harbouring poly(3-hydroxybutyrate) (PHB) synthesising genes from Streptomyces aureofaciens NRRL 2209 accumulates PHB. Effects of different carbon and nitrogen sources on PHB accumulation by recombinant E. coli were studied. Among the carbon sources used glycerol, glucose, palm oil and ethanol supported PHB accumulation. No PHB accumulated in recombinant cells when sucrose or molasses were used as carbon source. Yeast extract, peptone, a combination of yeast extract and peptone, and corn steep liquor were used as nitrogen sources. The maximum PHB accumulation (60% of cell dry weight) was measured after 48 h of cell growth at 37 degrees C in a medium with glycerol as the sole carbon source, and yeast extract and peptone as nitrogen sources. Scanning electron microscopy of the PHB granules isolated from recombinant E. coli revealed these to be spherical in shape with a diameter ranging from 0.11 to 0.35 pm with the mean value of 0.23 +/- 0.06 pm.     

Degradation of poly (3-hydroxybutyrate) and its copolymer poly (3-hydroxybutyrate-co-3-hydroxyvalerate) by a marine Streptomyces sp. SNG9

A marine Streptomyces sp. SNG9 was characterized by its ability to utilize poly(3-hydroxybutyrate) (PHB) and its copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate P (3HB-co-HV). The bacterium grew efficiently in a simple mineral liquid medium enriched with 0.1% poly(3-hydroxybutyrate) powder as the sole carbon source. Cells excreted PHB depolymerase and degraded the polymer particles to complete clarity in 4 days. The degradation activity was detectable by the formation of a clear zone around the colony (petri plates) or a clear depth under the colony (test tubes). The expression of PHB depolymerase was repressed by the presence of simple soluble carbon sources. Bacterial degradation of the naturally occurring sheets of poly(3-hydroxybutyrate) and its copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate) was observed by scanning electron microscopy (SEM). Morphological alterations of the polymers sheets were evidence for bacterial hydrolysis.     

Poly(3-hydroxybutyrate) production by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis> in fed-batch culture

High poly(3-hydroxybutyrate) (PHB) content and volumetric productivity were achieved by fed-batch culture of Halomonas boliviensis using a defined medium. Initial shake flask cultivations in a minimal medium revealed that the growth of H. boliviensis was supported only when the medium was supplemented with aspartic acid, glycine, or glutamine. Addition of 0.1% (w/v) glutamine in the medium resulted in the highest cell dry weight (CDW; 3.9 g l⁻¹). Glutamine was replaced by the less expensive monosodium glutamate (MSG) in the medium without any notable change in the final cell density. Effect of initial concentrations of NH₄Cl and K₂HPO₄ on cell growth and PHB accumulation by H. boliviensis was then analyzed using a fed-batch fermentation system. The best conditions for PHB production by H. boliviensis were attained using 0.4% (w/v) NH₄Cl and 0.22% (w/v) K₂HPO₄ and adding MSG intermittently to the fermentor. Poly(3-hydroxybutyrate) content and CDW reached 90 wt.% and 23 g l⁻¹, respectively, after 18 h of cultivation. In order to increase CDW and PHB content, MSG, NH₄Cl, and K₂HPO₄ were initially fed to the fermentor to maintain their concentrations at 2%, 0.4%, and 0.22% (w/v), respectively, and subsequently their feed was suppressed. This resulted in a CDW of 44 g l⁻¹, PHB content of 81 wt.%, and PHB volumetric productivity of 1.1 g l⁻¹ h⁻¹.