Tailor-made type II <Emphasis Type="Italic">Pseudomonas</Emphasis> PHA synthases and their use for the biosynthesis of polylactic acid and its copolymer in recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Previously, we have developed metabolically engineered Escherichia coli strains capable of producing polylactic acid (PLA) and poly(3-hydroxybutyrate-co-lactate) [P(3HB-co-LA)] by employing evolved Clostridium propionicum propionate CoA transferase (Pct _Cp ) and Pseudomonas sp. MBEL 6-19 polyhydroxyalkanoate (PHA) synthase 1 (PhaC1 _Ps6-19). Introduction of mutations four sites (E130, S325, S477, and Q481) of PhaC1 _Ps6-19 have been found to affect the polymer content, lactate mole fraction, and molecular weight of P(3HB-co-LA). In this study, we have further engineered type II Pseudomonas PHA synthases 1 (PhaC1s) from Pseudomonas chlororaphis, Pseudomonas sp. 61-3, Pseudomonas putida KT2440, Pseudomonas resinovorans, and Pseudomonas aeruginosa PAO1 to accept short-chain-length hydroxyacyl-CoAs including lactyl-CoA and 3-hydroxybutyryl-CoA as substrates by site-directed mutagenesis of four sites (E130, S325, S477, and Q481). All PhaC1s having mutations in these four sites were able to accept lactyl-CoA as a substrate and supported the synthesis of P(3HB-co-LA) in recombinant E. coli, whereas the wild-type PhaC1s could not accumulate polymers in detectable levels. The contents, lactate mole fractions, and the molecular weights of P(3HB-co-LA) synthesized by recombinant E. coli varied depending upon the source of the PHA synthase and the mutants used. PLA homopolymer could also be produced at ca. 7 wt.% by employing the several PhaC1 variants containing E130D/S325T/S477G/Q481K quadruple mutations in wild-type E. coli XL1-Blue.     

Biosynthesis of poly(3-hydroxybutyrate-co-3-hydroxyalkanoates) by recombinant bacteria expressing the PHA synthase gene phaC1 from Pseudomonas sp. 61-3

Pseudomonas sp. 61-3 accumulated a blend of poly(3-hydroxybutyrate) [P(3HB)] homopolymer and a random copolymer consisting of 3-hydroxyalkanoate (3HA) units of 4–12 carbon atoms. The genes encoding β-ketothiolase (PhbA_Re) and NADPH-dependent acetoacetyl-CoA reductase (PhbB_Re) from Ralstoniaeutropha were expressed under the control of promoters for Pseudomonas sp. 61-3 pha locus or R. eutropha phb operon together with phaC1 _Ps gene (PHA synthase 1 gene) from Pseudomonas sp. 61-3 in PHA-negative mutants P. putida GPp104 and R. eutropha PHB⁻4 to produce copolyesters [P(3HB-co-3HA)] consisting of 3HB and medium-chain-length 3HA units of 6–12 carbon atoms. The introduction of the three genes into GPp104 strain conferred the ability to synthesize P(3HB-co-3HA) with relatively high 3HB compositions (up to 49 mol%) from gluconate and alkanoates, although 3HB units were not incorporated at all or at a very low fraction (3 mol%) into copolyesters by the strain carrying phaC1 _Ps gene only. In addition, recombinant strains of R. eutropha PHB⁻4 produced P(3HB-co-3HA) with higher 3HB fractions from alkanoates and plant oils than those from recombinant GPp104 strains. One of the recombinant strains, R. eutropha PHB⁻4/pJKSc46-pha, in which all the genes introduced were expressed under the control of the native promoter for Pseudomonas sp. 61-3 pha locus, accumulated P(3HB-co-3HA) copolyester with a very high 3HB fraction (85 mol%) from palm oil. The nuclear magnetic resonance analyses showed that the copolyesters obtained here were random copolymers of 3HB and 3HA units. Received: 12 July 1999 / Received revision: 1 October 1999 / Accepted: 2 October 1999     

Enhanced production of poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-4-hydroxybutyrate) copolymer with manipulated variables and its properties

Cupriavidus sp. USMAA1020, a local isolate was able to biosynthesis poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] copolymer with various 4HB precursors as the sole carbon source. Manipulation of the culture conditions such as cell concentration, phosphate ratio and culture aeration significantly affected the synthesis of P(3HB-co-4HB) copolymer and 4HB composition. P(3HB-co-4HB) copolymer with 4HB compositions ranging from 23 to 75 mol% 4HB with various mechanical and thermal properties were successfully produced by varying the medium aeration. The physical and mechanical properties of P(3HB-co-4HB) copolymers were characterized by NMR spectroscopy, gel-permeation chromatography, tensile test, and differential scanning calorimetry. The number-average molecular weights (M _n) of copolymers ranged from 260 × 10³ to 590 × 10³Da, and the polydispersities (M _w/M _n) were between 1.8 and 3.0. Increases in the 4HB composition lowered the molecular weight of these copolymers. In addition, the increase in 4HB composition affected the randomness of copolymer, melting temperature (T _m), glass transition temperature (T _g), tensile strength, and elongation to break. Enzymatic degradation of P(3HB-co-4HB) films with an extracellular depolymerase from Ochrobactrum sp. DP5 showed that the degradation rate increased proportionally with time as the 4HB fraction increased from 17 to 50 mol% but were much lower with higher 4HB fraction. Degradation of P(3HB-co-4HB) films with lipase from Chromobacterium viscosum exhibited highest degradation rate at 75 mol% 4HB. The biocompatibility of P(3HB-co-4HB) copolymers were evaluated and these copolymers have been shown to support the growth and proliferation of fibroblast cells.     

A lower specificity PhaC2 synthase from Pseudomonas stutzeri catalyses the production of copolyesters consisting of short-chain-length and medium-chain-length 3-hydroxyalkanoates

A polyhydroxyalkanoate (PHA) synthase gene phaC2 _Ps from Pseudomonas stutzeri strain 1317 was introduced into a PHA synthase gene phbC _Re negative mutant, Ralstonia eutropha PHB⁻4. It conferred on the host strain the ability to synthesize PHA, the monomer compositions of which varied widely when grown on different carbon sources. During cultivation on gluconate, the presence of phaC2 _Ps in R. eutropha PHB⁻4 led to the accumulation of polyhydroxybutyrate (PHB) homopolymer in an amount of 40.9 wt% in dry cells. With fatty acids, the recombinant successfully produced PHA copolyesters containing both short-chain-length and medium-chain-length 3-hydroxyalkanoate (3HA) of 4–12 carbon atoms in length. When cultivated on a mixture of gluconate and fatty acid, the monomer composition of accumulated PHA was greatly affected and the monomer content was easily regulated by the addition of fatty acids in the cultivation medium. After the (R)-3-hydroxydecanol-ACP:CoA transacylase gene phaG _Pp from Pseudomonas putida was introduced into phaC2 _Ps-containing R. eutropha PHB⁻4, poly(3HB-co-3HA) copolyester with a very high 3-hydroxybutyrate (3HB) fraction (97.3 mol%) was produced from gluconate and the monomer compositions of PHA synthesized from fatty acids were also altered. This study clearly demonstrated that PhaC2_Ps cloned from P. stutzeri 1317 has extraordinarily low substrate specificity in vivo, though it has only 54% identity in comparison to a previously described low-substrate-specificity PHA synthase PhaC1_Ps from Pseudomonas sp. 61–3. This study also indicated that the monomer composition and content of the synthesized PHA can be effectively modulated by controlling the addition of carbon sources or by modifying metabolic pathways in the hosts.     

Production of copolymer poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-4-hydroxybutyrate) through a one-step cultivation process

A one-step cultivation process for the production of biodegradable polymer poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] by Cupriavidus sp. USMAA2-4 was carried out using various carbon sources. It was found that Cupriavidus sp. USMAA2-4 could produce approximately 44 wt.% copolymer of P(3HB-co-4HB) with 27 mol% 4HB composition when the combination of oleic acid and 1,4-butanediol are used as carbon sources in 60 h cultivation. The manipulation of carbon-to-nitrogen ratio (C/N) resulted in the increase of dry cell weight, PHA content as well as 4HB composition. A new strategy of introducing oleic acid and 1,4-butanediol together and separately at different concentration demonstrated different yield in PHA content ranging from 47 to 58 wt.%. The molecular weight obtained was 234 kDa (by adding 1,4-butanediol and oleic acid together) and 212 kDa (by adding 1,4-butanediol separately). The copolymer of P(3HB-co-4HB) produced by Cupriavidus sp. USMAA2-4 was detected statistically as a random copolymer when analysed by nuclear magnetic resonance (NMR) spectroscopy.     

Biosynthesis of polylactic acid and its copolymers using evolved propionate CoA transferase and PHA synthase

For the synthesis of polylactic acid (PLA) and its copolymers by one‐step fermentation process, heterologous pathways involving Clostridium propionicum propionate CoA transferase (Pct_Cp) and Pseudomonas sp. MBEL 6‐19 polyhydroxyalkanoate (PHA) synthase 1 (PhaC1_Ps6‐19) were introduced into Escherichia coli for the generation of lactyl‐CoA endogenously and incorporation of lactyl‐CoA into the polymer, respectively. Since the wild‐type PhaC1_Ps6‐19 did not efficiently accept lactyl‐CoA as a substrate, site directed mutagenesis as well as saturation mutagenesis were performed to improve the enzyme. The wild‐type Pct_Cp was not able to efficiently convert lactate to lactyl‐CoA and was found to exert inhibitory effect on cell growth, random mutagenesis by error‐prone PCR was carried out. By employing engineered PhaC1_Ps6‐19 and Pct_Cp, poly(3‐hydroxybutyrate‐co‐lactate), P(3HB‐co‐LA), containing 20–49 mol% lactate could be produced up to 62 wt% from glucose and 3HB. By controlling the 3HB concentration in the medium, PLA homopolymer and P(3HB‐co‐LA) containing lactate as a major monomer unit could be synthesized. Also, P(3HB‐co‐LA) copolymers containing various lactate fractions could be produced from glucose alone by introducing the Cupriavidus necator β‐ketothiolase and acetoacetyl‐CoA reductase genes. Fed‐batch cultures were performed to produce P(3HB‐co‐LA) copolymers having 9–64 mol% of lactate, and their molecular weights, thermal properties, and melt flow properties were determined. Biotechnol. Bioeng. 2010; 105: 150–160. © 2009 Wiley Periodicals, Inc.     

Engineering of polyhydroxyalkanoate (PHA) synthase PhaC2<Subscript>Ps</Subscript> of <Emphasis Type="Italic">Pseudomonas stutzeri</Emphasis> via site-specific mutation for efficient production of PHA copolymers

The site-specific mutagenesis for PHA synthase PhaC2_Ps1317 from Pseudomonas stutzeri 1317 was conducted for optimizing production of short-chain-length and medium-chain-length polyhydroxyalkanoates (scl-mcl PHA). Recombinant Ralstonia eutropha PHB-4 harboring double mutated phaC2 _Ps1317 gene (phaC2 _Ps QKST) produced 42 wt.% PHA content in the cell dry weight (CDW) with 93 mol% 3-hydroxybutyrate (HB) as monomer in the PHA copolymer. Compared to that of wild-type phaC2 _Ps1317 , the higher PHA content indicated the effectiveness of the specific point mutations for improvement on PhaC2_Ps1317 activity and PHA production. The physical characterization revealed that the PHA produced by the recombinant strain was scl-mcl PHA copolymers with molecular weights and polydispersity reasonable for practical applications. Recombinant R. eutropha PHB-4 containing mutated phaC2 _Ps1317 termed phaC2 _Ps QKST was demonstrated to be able to produce scl-mcl PHA copolymers consisting of even-numbered, odd-numbered, or a combination of even- and odd-numbered monomers covering the carbon chain lengths from C4 to C12 when related substrates were provided. Recombinant R. eutropha PHB-4 containing phaC2PsQKST could be used as a strain for production of copolymers consisting of dominated HB and medium-chain-length 3-hydroxyalkanoates (HA) with better application properties.     

Production of a novel copolyester of 3-hydroxybutyric acid and medium-chain-length 3-hydroxyalkanoic acids by Pseudomonas sp. 61-3 from sugars

 Pseudomonas sp. 61-3 (isolated from soil) produced a polyester consisting of 3-hydroxybutyric acid (3HB) and of medium-chain-length 3-hydroxyalkanoic acids (3HA) of C₆, C₈, C₁₀ and C₁₂, when sugars of glucose, fructose and mannose were fed as the sole carbon source. The polyester produced was a blend of homopolymer and copolymer, which could be fractionated with boiling acetone. The acetone-insoluble fraction of the polyester was a homopolymer of 3-hydroxybutyrate units [poly (3HB)], while the acetone-soluble fraction was a copolymer [poly(3HB-co-3HA)] containing both short- and medium-chain-length 3-hydroxyalkanoate units ranging from C₄ to C₁₂:44 mol% 3-hydroxybutyrate, 5 mol% 3-hydroxyhexanoate, 21 mol% 3-hydroxyoctanoate, 25 mol% 3-hydroxydecanoate, 2 mol% 3-hydroxydodecanoate and 3 mol% 3-hydroxy-5-cis-dodecenoate. The copolyester was shown to be a random copolymer of 3-hydroxybutyrate and medium-chain-length 3-hydroxyalkanoate units by analysis of the ¹³C-NMR spectrum. The poly(3HB) homopolymer and poly (3HB-co-3HA) copolymer were produced simultaneously within cells from glucose in the absence of any nitrogen source, which suggests that Pseudomonas sp. 61-3 has two types of polyhydroxy-alkanoate syntheses with different substrate specificities. Received: 9 June 1995/Received last revision: 30 October 1995/Accepted: 6 November 1995     

Location of functional region at N-terminus of polyhydroxyalkanoate (PHA) synthase by N-terminal mutation and its effects on PHA synthesis

Polyhydroxyalkanoate (PHA) synthase PhaC plays a very important role in biosynthesis of microbial polyesters PHA. Compared to the extensively analyzed C-terminus of PhaC, N-terminus of PhaC was less studied. In this paper, the N-terminus of two class I PHA synthases PhaC_Re and PhaC_Ah from Ralstonia eutropha and Aeromonas hydrophila, respectively, and one class II synthase PhaC2_Ps of Pseudomonas stutzeri strain 1317, were investigated for their effect on PHA synthesis. For PhaC_Re, deletion of 2–65 amino acid residues on the N-terminus led to enhanced PHB production with high PHB molecular weight of 2.50 × 10⁶ Da. For PhaC_Ah, the deletion of the N-terminal residues resulted in increasing molecular weights and widening polydispersity accompanied by a decreased PHA production. It was found that 3-hydroxybutyrate (3HB) monomer content in copolyesters of 3-hydroxybutyrate and 3-hydroxyhexanoate (3HHx) increased when the first 2–9 and 2–13 amino acid residues in the N-terminus of PhaC2_Ps were deleted. However, deletion up to the 40th amino acid disrupted the PHA synthesis. This study confirmed that N-terminus in different types of PHA synthases showed significant roles in the PHA productivity and elongation activity. It was also indicated that N-terminal mutation was very effective for the location of functional regions at N-terminus.     

Regulating the molar fraction of 4-hydroxybutyrate in Poly(3-hydroxybutyrate-co-4-hydroxybutyrate) by biological fermentation and enzymatic degradation

The regulation of 4-hydroxybutyrate (4HB) molar fraction in the poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] of a local isolate Cupriavidus sp. USMAA1020 was attempted by employing a feeding strategy through fed-batch fermentation in 100-L fermenter. The growth of Cupriavidus sp. USMAA1020 was enhanced by frequently feeding carbon and nitrogen at a ratio of 5 (C/N 5) using a DO-stat with cascade mode at 20% (v/v) dissolved oxygen (DO). The feeding of C/N 5 and the use of the DO-stat mode were able to regulate the 4HB composition from 0–67 mol% by sequential feeding of γ-butyrolactone and supplementing oleic acid. A high 4HB molar fraction of 67 mol% with a PHA concentration of 5.2 g/L was successfully obtained by employing this feeding strategy. Notably, enzymatic degradation carried out enhanced the 4HB composition of the copolymer synthesized. PHB depolymerase enzyme from Acidovorax sp. was used to degrade this P(3HB-co-70-mol%4HB) copolymer and the 4HB composition could be increased up to 83 mol%. The degradation process was observed by monitoring the time-dependent change in the weight loss of copolymer films. The percentage of weight loss of solvent-cast film increased proportionally up to 19% within 3 h, whereas salt-leached films showed 90% of weight loss within 3 h of incubation and were completely degraded by 4 h. The molecular weight (M _n ) of the films treated with enzyme demonstrated a slight decrease. SEM observation exhibited a rough surface morphology of the copolymer degraded with depolymerase enzyme.     

Biosynthesis of polyhydroxyalkanoates containing 2-hydroxybutyrate from unrelated carbon source by metabolically engineered <Emphasis Type="Italic">Escherichia coli</Emphasis>

We have previously reported in vivo biosynthesis of polylactic acid (PLA) and poly(3-hydroxybutyrate-co-lactate) [P(3HB-co-LA)] employing metabolically engineered Escherichia coli strains by the introduction of evolved Clostridium propionicum propionyl-CoA transferase (Pct _Cp ) and Pseudomonas sp. MBEL 6-19 polyhydroxyalkanoate (PHA) synthase 1 (PhaC1 _Ps6-19). Using this in vivo PLA biosynthesis system, we presently report the biosynthesis of PHAs containing 2-hydroxybutyrate (2HB) monomer by direct fermentation of a metabolically engineered E. coli strain. The recombinant E. coli ldhA mutant XLdh strain expressing PhaC1 _Ps6-19 and Pct _Cp was developed and cultured in a chemically defined medium containing 20 g/L of glucose and varying concentrations of 2HB and 3HB. PHAs consisting of 2HB, 3HB, and a small fraction of lactate were synthesized. Their monomer compositions were dependent on the concentrations of 2HB and 3HB added to the culture medium. Even though the ldhA gene was completely deleted in the chromosome of E. coli, up to 6 mol% of lactate was found to be incorporated into the polymer depending on the culture condition. In order to synthesize PHAs containing 2HB monomer without feeding 2HB into the culture medium, a heterologous metabolic pathway for the generation of 2HB from glucose was constructed via the citramalate pathway, in which 2-ketobutyrate is synthesized directly from pyruvate and acetyl-CoA. Introduction of the Lactococcus lactis subsp. lactis Il1403 2HB dehydrogenase gene (panE) into E. coli allowed in vivo conversion of 2-ketobutyrate to 2HB. The metabolically engineered E. coli XLdh strain expressing the phaC1437, pct540, cimA3.7, and leuBCD genes together with the L. lactis Il1403 panE gene successfully produced PHAs consisting of 2HB, 3HB, and a small fraction of lactate by varying the 3HB concentration in the culture medium. As the 3HB concentration in the medium increased the 3HB monomer fraction in the polymer, the polymer content increased. When Ralstonia eutropha phaAB genes were additionally expressed in this recombinant E. coli XLdh strain, P(2HB-co-3HB-co-LA) having small amounts of 2HB and LA monomers could also be produced from glucose as a sole carbon source. The metabolic engineering strategy reported here should be useful for the production of PHAs containing 2HB monomer.     

Hyperproduction of PHA copolymers containing high fractions of 4-hydroxybutyrate (4HB) by outer membrane-defected Halomonas bluephagenesis grown in bioreactors

Bacterial outer membrane (OM) is a self-protective and permeable barrier, while having many non-negligible negative effects in industrial biotechnology. Our previous studies revealed enhanced properties of Halomonas bluephagenesis based on positive cellular properties by OM defects. This study further expands the OM defect on membrane compactness by completely deleting two secondary acyltransferases for lipid A modification in H. bluephagenesis, LpxL and LpxM, and found more significant advantages than that of the previous lpxL mutant. Deletions on LpxL and LpxM accelerated poly(3-hydroxybutyrate) (PHB) production by H. bluephagenesis WZY229, leading to a 37% increase in PHB accumulation and 84-folds reduced endotoxin production. Enhanced membrane permeability accelerates the diffusion of γ-butyrolactone, allowing H. bluephagenesis WZY254 derived from H. bluephagenesis WZY229 to produce 82wt% poly(3-hydroxybutyrate-co-23mol%4-hydroxybutyrate) (P(3HB-co-23mol%4HB)) in shake flasks, showing increases of 102% and 307% in P(3HB-co-4HB) production and 4HB accumulation, respectively. The 4HB molar fraction in copolymer can be elevated to 32 mol% in the presence of more γ-butyrolactone. In a 7-l bioreactor fed-batch fermentation, H. bluephagenesis WZY254 supported a 84 g l⁻¹ dry cell mass with 81wt% P(3HB-co-26mol%4HB), increasing 136% in 4HB molar fraction. This study further demonstrated that OM defects generate a hyperproduction strain for high 4HB containing copolymers.     

Biosynthesis of Poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-3-hydroxyvalerate-<Emphasis Type="Italic">co</Emphasis>-4-hydroxybutyrate) terpolymer by <Emphasis Type="Italic">Cupriavidus</Emphasis> sp. USMAA2-4 through two-step cultivation process

A locally isolated Gram-negative bacterium, Cupriavidus sp. USMAA2-4 was found capable of producing terpolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate-co-4-hydroxybutyrate) [P(3HB-co-3HV-co-4HB)] using γ-butyrolactone or 1,4-butanediol with either valeric acid or 1-pentanol as the carbon source. The present of 3HB, 3HV and 4HB monomers were confirmed by gas chromatography (GC) and nuclear magnetic resonance (NMR) analysis. PHA concentration of 1.9 g/l was the highest value obtained using the combination of 1,4-butanediol and 1-pentanol through one-step cultivation process. PHA concentration obtained through two-step cultivation process was higher for all the combinations and the highest value achieved was 2.5 g/l using γ-butyrolactone and 1-pentanol as carbon source. Various molar fractions of 4HB and 3HV ranging from 6 to 14 mol% and 39 to 87 mol%, respectively were produced through two-step cultivation process by manipulating the concentration of γ-butyrolactone. As the culture aeration was reduced, the molar fraction of 3HV and 4HB increased from 40 to 67 mol% and 10 to 24 mol%, respectively while the dry cell weight and PHA content decreased. The terpolymer produced was characterized using gel permeation chromatography (GPC) and differential scanning calorimetry (DSC). The number-average molecular weight (M _n) and the melting temperature (T _m)) of the terpolymer were in the range of 177–484 kDa and 160–164°C, respectively.     

Heterologous expression of <Emphasis Type="Italic">Cupriavidus</Emphasis> sp. USMAA2-4 PHA synthase gene in PHB<Superscript>−</Superscript>4 mutant for the production of poly(3-hydroxybutyrate) and its copolymers

Ecological deterioration and human health concerns arising from the usage of non-biodegradable plastics have prompted mankind to search for greener alternatives which are biodegradable, biocompatible and easily produced from renewable sources. Polyhydroxyalkanoates (PHA), among other biopolymers, are emerging as a viable replacement for fossil fuel-based synthetic plastics. A PHA-producing strain, identified as Cupriavidus sp. (designated Cupriavidus sp. USMAA2-4) was isolated from a soil sample from western peninsular Malaysia. Heterologous expression of the PHA synthase gene (phaC _USMAA2-4) in mutant C. necator PHB⁻4 complemented its PHA-producing ability. More than 60 wt% of P(3HB) was synthesized from various plant oils. The highest P(3HB) production of 2.38 g/l at 68 wt% was attained when crude palm kernel oil was fed as the sole carbon source. The 3HV molar fraction in poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] was significantly affected by the type of the precursor used and their respective feeding time. The 3HV molar fraction ranged from 4 to 31 mol% when sodium propionate/valerate was fed at different cultivation times. In addition, with the supplementation of 4HB-monomer precursors, approximately 67 wt% P(3HB-co-4HB) with 4–5 mol% of 4-hydroxybutyrate monomer was synthesized, regardless of the precursor feeding time used. Variation in the molar fraction of the second monomer along with its biodegradability and biocompatibility characteristics promotes the potential of these copolymers as replacements for traditional commodity plastics.     

Characteristics of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) production byRalstonia eutropha NCIMB 11599 and ATCC 17699

Ralstonia eutropha NCIMB 11599 and ATCC 17699 were grown, and their productions of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] compared. In flask cultures ofR. eutropha NCIMB 11599, cell concentration, P(3HB-co-4HB) concentration and polymer content decreased considerably with increases in the γ-butyrolactone concentration, and the 4HB fraction was also very low (maximum 1.74 mol%). In fed-batch cultures ofR. eutropha NCIMB 11599, glucose and γ-butyrolactone were fed as the carbon sources, under a phosphate limitation strategy. When glucose was fed as the sole carbon source, with its concentration controlled using an on-line glucose analyzer, 86% of the P(3HB) homopolymer was obtained from 201 g/L of cells. In a two-stage fed-batch culture, where the cell concentration was increased to 104 g/L, with glucose fed in the first step and constant feeding of γ-butyrolactone, at 6 g/h, in the second, final cell concentration at 67 h was 106 g/L, with a polymer content of 82%, while the 4HB fraction was only 0.7 mol%. When the same feeding strategy was applied to the fedbatch culture ofR. eutropha ATCC 17699, where the cell concentration was increased to 42 g/L, by feeding fructose in the first step and γ-butyrolactone (1.5 g/h) in the second, the final cell concentration, polymer content and 4HB fraction at 74 h were 51 g/L, 35% and 32 mol%, respectively. In summary,R. eutropha ATCC 17699 was better thanR. eutropha NCIMB 11599 in terms of P(3HB-co-4HB) production with various 4HB fractions.     

Identification and characterization of two polyhydroxyalkanoate biosynthesis loci in Pseudomonas sp. strain 3Y2

A Pseudomonas strain, 3Y2, that produced polyhydroxyalkanoate (PHA) polymers consisting of 3-hydroxybutyric acid (3HB) and medium-chain-length 3-hydroxyalkanoate (mcl-HA) units, with up to 30% 3HB, was isolated. Two PHA biosynthesis loci (pha _Ps-1 and pha _Ps-2) from 3Y2 were cloned by polymerase chain reaction amplification techniques. The pha _Ps-2 locus was similar to the PHA biosynthesis loci of other PHA-producing Pseudomonas strains, with five tandem open reading frames (ORFs) located in the order ORF1 _Ps-2-phaC1 _Ps-2-phaZ _Ps-2-phaC2 _Ps-2-phaD _Ps-2. The pha _Ps-1 locus that contains phaC1 _Ps-1-phaZ _Ps-1 appears to have arisen by a duplication event that placed it downstream of a gene (ORF1 _Ps-1), encoding a putative glucose-methanol-choline flavoprotein oxidoreductase. The PHA synthases 1 encoded by phaC1 _Ps-1 and phaC1 _Ps-2 were investigated by heterologous expression in Wautersia eutropha PHB⁻4. Both synthases displayed similar substrate specificities for incorporating 3HB and mcl-HA units into PHA. The ability of PhaC1 _Ps-1 to confer PHA synthesis, however, appeared reduced compared to that of PhaC1 _Ps-2, since cells harboring PhaC1 _Ps-1 accumulated 2.5 to 4.6 times less PHA than cells expressing PhaC1 _Ps-2. Primary sequence analysis revealed that PhaC1 _Ps-1 had markedly diverged from the other PHA synthases with a relatively high substitution rate (14.9 vs 2% within PhaC1 _Ps-2). The mutations affected a highly conserved C-terminal region and the surroundings of the essential active site cysteine (Cys296) with a loss of hydrophobicity. This led us to predict that if phaC1 _Ps-1 produces a protein product in the native strain, it is likely that PhaC1 _Ps-1 may be destined for elimination by the accumulation of inactivating mutations, although its specialization to accommodate different substrates cannot be eliminated.     

Improved production of poly(3-hydroxybutyrate-co-4-hydroxbutyrate) copolymer using a combination of 1,4-butanediol and γ-butyrolactone

A locally isolated Gram-negative bacterium, Cupriavidus sp. USMAA2-4 was able to synthesize poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] when fed with the precursor carbon 1,4-butanediol using a two-stage cultivation process. When 1% (w/v) of 1,4-butanediol was used, 31 wt.% of P(3HB-co-4HB) copolymer with 41 mol.% of 4HB molar fraction was produced. Both the PHA content and 4HB composition of the copolymer increased as the concentration of 1,4-butanediol increased but the cell biomass did not show any significant changes. However, the 4HB fraction could be further increased using a combination of γ-butyrolactone and 1,4-butanediol. As high as 84 mol.% of 4HB composition was achieved with a combination of 0.35% (w/v) 1,4-butanediol and 1.4% (w/v) γ-butyrolactone. Nevertheless, it was found that Cupriavidus sp. USMAA2-4 cells were inhibited by high concentration of γ-butyrolactone. P(3HB-co-4HB) copolymer was also successfully synthesized using a simplified aerated tank.     

Synthesis of biodegradable polyesters by Gram negative bacterium isolated from Malaysian environment

A locally isolated Gram negative bacterium, Cupriavidus sp. USMAA9-39 was able to produce various types of biodegradable polyesters through a two-step cultivation process. These are copolymer poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)], copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] and terpolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate-co-4-hydroxybutyrate) [P(3HB-co-3HV-co-4HB)]. These polymers were synthesized by this bacterium when grown with a combination of some carbon sources. The biosynthesis of P(3HB-co-4HB) was achieved by using carbon sources such as γ-butyrolactone or 1,4-butanediol or by a combination of oleic acid with either γ-butyrolactone or 1,4-butanediol. Meanwhile, poly(3-hydroxybutyrate-co-3-hydroxyvalerate) was produced using 1-pentanol or valeric acid or by a combination of oleic acid with either 1-pentanol or valeric acid. When γ-butyrolactone or 1,4-butanediol with either valeric acid or 1-pentanol were used as mixed carbon sources, P(3HB-co-3HV-co-4HB) terpolymer were produced. The presence of 3HB, 3HV or/and 4HB monomers were confirmed by gas chromatography and nuclear magnetic resonance (NMR) spectroscopy.