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.     

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.     

Fermentative production of P(3HB-co-3HV) from propionic acid by Alcaligenes eutrophus in fed-batch culture with pH-stat continuous substrate feeding method

The feeding of propionic acid for production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] by Alcaligenes eutrophus ATCC17697 was optimized using a fed-batch culture system. The concentration of propionic acid was maintained at 3 g l^–1 as growth was inhibited by propionic acid in the broth. A pH-stat substrate feeding system was used in which propionic acid was fed automatically to maintain a pH of the culture broth at 7.0. By feeding a substrate solution containing 20% (w/v) propionic acid, 4.9% (w/v) ammonia water [at a molar ratio of carbon to nitrogen (C/N molar ratio) of 10] in cell growth phase, the concentration of propionic acid in the broth was maintained at 3 g l^–1 giving a specific growth rate of 0.4 h^–1. To promote P(3HB-co-3HV) production, two stage fed-batch culture which consisted of the stage for the cell growth and the stage for the P(3HB-co-3HV) accumulation was carried out. When the substrate solution whose C/N molar ratio was 50 was fed in P(3HB-co-3HV) accumulation phase, the cell concentration and the P(3HB-co-3HV) content in the cells reached 64 g l^–1 and 58% (w/w) in 55.5 h, respectively.     

Structure and properties of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) produced by Alcaligenes latus

Summary Random copolymers of 3-hydroxybutyrate (3HB) and 4-hydroxybutyrate (4HB) with a wide range of compositions varying from 0 to 83 mol% 4HB were produced by Alcaligenes latus from the mixed carbon substrates of 3-hydroxybutyric and 4-hydroxybutyric acids. The structure and physical properties of P(3HB-co-4HB) were characterized by¹H and¹³C NMR spectroscopy, gel-permeation chromatography, and differential scanning calorimetry. The isothermal radial growth rates of spherulites of P(3HB-co-4HB) were much slower than the rate of P(3HB) homopolymer. The enzymatic degradation rates of P(3HB-co-4HB) films by a PHB depolymerase were strongly influenced by the copolymer composition.     

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.     

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 and Characterization of Poly(3-hydroxybutyrate-co-3- hydroxyhexanoate) from Palm Oil Products in a Wautersia eutropha Mutant

Palm kernel oil, palm olein, crude palm oil and palm acid oil were used for the synthesis of poly (3-hydroxybutyrate-co-3-hydroxyhexanoate) [P(3HB-co-3HHx)] by a mutant strain of Wautersia eutropha (formerly Ralstonia eutropha) harboring the Aeromonas caviae polyhydroxyalkanoate (PHA) synthase gene. Palm kernel oil was an excellent carbon source for the production of cell biomass and P(3HB-co-3HHx). About 87% (w/w) of the cell dry weight as P(3HB-co-3HHx) was obtained using 5 g palm kernel oil/l. Gravimetric and microscopic analyses further confirmed the high PHA content in the recombinant cells. The molar fraction of 3HHx remained constant at 5 mol % regardless of the type and concentration of palm oil products used. The small amount of 3HHx units was confirmed by ¹³C NMR analysis. The number average molecular weight (M_n) of the PHA copolymer produced from the various palm oil products ranged from 27 0000 to 46 0000 Da. The polydispersity was in the range of 2.6–3.9.     

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.     

Studies on the biodegradability of polythioester copolymers and homopolymers by polyhydroxyalkanoate (PHA)-degrading bacteria and PHA depolymerases

The biodegradability of microbial polythioesters (PTEs), a novel class of biopolymers which were discovered recently and can be produced by polyhydroxyalkanoate (PHA)-accumulating bacteria, was studied. Using poly(3-hydroxybutyrate-co-3-mercaptopropionate) [poly(3HB-co-3MP)] as sole carbon source for screening, 22 new bacterial strains were isolated and characterized. Interestingly, none of the PHA-degrading bacteria was able to utilize the homopolymer poly(3MP) as a carbon source for growth or to form clear zones on poly(3MP)-containing agar plates. The extracellular PHA depolymerases from two strains ( Schlegelella thermodepolymerans, Pseudomonas indica K2) were purified to electrophoretic homogeneity and biochemically characterized. The PHA depolymerase of S. thermodepolymerans exhibited a temperate optimum of about 75°C to 80°C and was stable at 70°C for more than 24 h. Regarding the substrate specificities of the PHA depolymerase of S. thermodepolymerans, enzyme activities decreased significantly with increasing 3MP content of the copolymer substrates. Interestingly, no activity could be detected with homoPTEs consisting only of 3MP or of 3-mercaptobutyrate. Similar results were obtained with the PHA depolymerases PhaZ2, PhaZ5 and PhaZ7 of Paucimonas lemoignei which were also investigated. The PHA depolymerase of Ps. indica K2 did not cleave any of the investigated polymers containing 3MP. Gas chromatography, infrared and ¹H-NMR spectrometry and matrix-assisted laser desorption/ionization time-of-flight analysis revealed that 3MPs containing oligomers were enriched in the water-insoluble fraction remaining after partial digestion of poly(3HB-co-3MP) by purified poly(3HB) depolymerase of S. thermodepolymerans. In contrast, 3HB was enriched in the water-soluble fraction, which also contained 3HB-co-3MP dimer obtained by partial digestion of this copolymer by the enzyme. This study clearly indicates that PHA depolymerases are specific for oxoester linkages of PHAs and that the thioester bonds of PTEs cannot be cleaved by this type of enzyme.This publication is dedicated to Prof. Dr. Hans G. Schlegel in honor of his 80th birthday     

Characterization of new isolated <Emphasis Type="Italic">Ralstonia</Emphasis><Emphasis Type="Italic">eutropha</Emphasis> strain A-04 and kinetic study of biodegradable copolyester poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-4-hydroxybutyrate) production

A new isolated bacterial strain A-04 capable of producing high content of polyhydroxyalkanoates (PHAs) was morphologically and taxonomically identified based on biochemical tests and 16S rRNA gene analysis. The isolate is a member of the genus Ralstonia and close to Ralstonia eutropha. Hence, this study has led to the finding of a new and unexplored R. eutropha strain A-04 capable of producing PHAs with reasonable yield. The kinetic study of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] production by the R. eutropha strain A-04 was examined using butyric acid and γ–hydroxybutyric acid as carbon sources. Effects of substrate ratio and mole ratio of carbon to nitrogen (C/N) on kinetic parameters were investigated in shake flask fed-batch cultivation. When C/N was 200, that is, nitrogen deficient condition, the specific production rate of 3-hydroxybutyrate (3HB) showed the highest value, whereas when C/N was in the range between 4 and 20, the maximum specific production rate of 4-hydroxybutyrate (4HB) was obtained. Thus, the synthesis of 3HB was growth-limited production under nitrogen-deficient condition, whereas the synthesis of 4HB was growth-associated production under nitrogen-sufficient condition. The mole fraction of 4HB units increased proportionally as the ratio of γ–hydroxybutyric acid in the feed medium increased at any value of C/N ratio. Based on these kinetic studies, a simple strategy to improve P(3HB-co-4HB) production in shake flask fed-batch cultivation was investigated using C/N and substrate feeding ratio as manipulating variable, and was successfully proved by the experiments. The nucleotide sequence 1,378 bp reported in this study will appear in the GenBank nucleotide sequence database under accession number EF988626.     

Production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) in recombinant Corynebacterium glutamicum using propionate as a precursor

Lipopolysaccharides free P[3-hydroxybutyrate (3HB)-co-3-hydroxyvalerate (3HV)] production was achieved using recombinant Corynebacterium glutamicum harboring polyhydroxyalkanoate (PHA) biosynthetic genes from Ralstonia eutropha. Cells grown on glucose with feeding of propionate as a precursor of 3HV unit accumulated 8-47 wt% of P(3HB-co-3HV). The 3HV fraction in the copolymer was varied from 0 to 28 mol% depending on the propionate concentrations.     

Biocompatibility of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) copolyesters produced byAlcaligenes sp. MT-16

Poly(3-hydroxybutyrate-co-3-hydroxyvalerate), poly(3HB-co-3HV), copolyesters, with 3-hydroxyvalerate (3HV) contents ranging from 17 to 60 mol%, were produced byAlcaligenes sp. MT-16, and their biocompatibility evaluated by the growth of Chinese hamster ovary (CHO) cells and the adsorption of blood proteins and platelets onto their film surfaces. The number of CHO cells that adhered to and grew on these films was higher with increasing 3HV content. In contrast, the tendency for blood proteins and platelets to adhere to the copolyester surfaces significantly decreased with increasing 3HV content. Examination of the surface morphology using atomic force microscopy revealed that the surface roughness was an important factor in determining the biocompatibility of theses copolyesters. The results obtained in this study suggest that poly(3HB-co-3HV) copolyesters, with >30 mol% 3HV, may be useful in biocompatible biomedical applications.     

Degradation of microbial polyester poly(3-hydroxybutyrate) in environmental samples and in culture

Poly(3-hydroxybutyrate) [P(3HB)] test-pieces prepared from the polymer produced by Azotobacter chroococcum were degraded in natural environments like soil, water, compost and sewage sludge incubated under laboratory conditions. Degradation in terms of % weight loss of the polymer was maximum (45%) in sewage sludge after 200 days of incubation at 30°C. The P(3HB)-degrading bacterial cultures (36) isolated from degraded test-pieces showed different degrees of degradation in polymer overlayer method. The extent of P(3HB) degradation increases up to 12 days of incubation and was maximum at 30°C for majority of the cultures. For most efficient cultures the optimum concentration of P(3HB) for degradation was 0.3% (w/v). Supplementation of soluble carbon sources like glucose, fructose and arabinose reduced the degradation while it was almost unaffected with lactose. Though the cultures degraded P(3HB) significantly, they were comparatively less efficient in utilizing copolymer of 3-hydroxybutyrate and 3-hydroxyvalerate [P(3HB-co-3HV)].     

Production of copolymer consisting of 3-hydroxybutyrate and 3-hydroxyvalerate by fed-batch culture of Alcaligenes SP. SH-69

Summary Production of copolymer consisting of 3-hydroxybutyrate and 3-hydroxyvalerate [poly(3HB-co-3HV)] by fed-batch culture of Alcaligenes sp. SH-69 was investigated using glucose as a sole carbon source. Synthesis of poly(3HB-co-3HV) during the polymer accumulation stage was favored under dissolved oxygen tension at 20% and C/N ratio (mol glucose/mol ammonium) of 23.1. When conditions were optimal, 36 g liter^-1 of poly(3HB-co-3HV) containing 3.0 mol% of 3HV was produced. Decreasing C/N ratio resulted in an increase of 3HV fraction in the copolymer to a maximum level of 6.3 mol%.     

A New Beneficial Mutation in Pseudomonas sp. 61-3 Polyhydroxyalkanoate (PHA) Synthase for Enhanced Cellular Content of 3-Hydroxybutyrate-Based PHA Explored Using Its Enzyme Homolog as a Mutation Template

A newly isolated mutation (Gln508Leu) and a combination of it with previously discovered beneficial mutations in polyhydroxyalkanoate synthase 1 from Pseudomonas sp. 61-3 were found to enhance the production of poly(3-hydroxybutyrate) [P(3HB)] and poly(3HB-co-3-hydroxyalkanoate)s in recombinant Escherichia coli.     

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.     

Polyhydroxyalkanoate copolymers from forest biomass

The potential for the use of woody biomass in poly-β-hydroxyalkanoate (PHA) biosynthesis is reviewed. Based on previously cited work indicating incorporation of xylose or levulinic acid (LA) into PHAs by several bacterial strains, we have initiated a study for exploring bioconversion of forest resources to technically relevant copolymers. Initially, PHA was synthesized in shake-flask cultures of Burkholderia cepacia grown on 2.2% (w/v) xylose, periodically amended with varying concentrations of levulinic acid [0.07–0.67% (w/v)]. Yields of poly(β-hydroxybutyrate-co-β-hydroxyvalerate) [P(3HB-co-3HV)] from 1.3 to 4.2 g/l were obtained and could be modulated to contain from 1.0 to 61 mol% 3-hydroxyvalerate (3HV), as determined by ¹H and ¹³C NMR analyses. No evidence for either the 3HB or 4HV monomers was found. Characterization of these P(3HB-co-3HV) samples, which ranged in molecular mass (viscometric, M _v) from 511–919 kDa, by differential scanning calorimetry and thermogravimetric analyses (TGA) provided data which were in agreement for previously reported P(3HB-co-3HV) copolymers. For these samples, it was noted that melting temperature (T _m) and glass transition temperature (T _g) decreased as a function of 3HVcontent, with T _m demonstrating a pseudoeutectic profile as a function of mol% 3HV content. In order to extend these findings to the use of hemicellulosic process streams as an inexpensive carbon source, a detoxification procedure involving sequential overliming and activated charcoal treatments was developed. Two such detoxified process hydrolysates (NREL CF: aspen and CESF: maple) were each fermented with appropriate LA supplementation. For the NREL CF hydrolysate-based cultures amended with 0.25–0.5% LA, P(3HB-co-3HV) yields, PHA contents (PHA as percent of dry biomass), and mol% 3HV compositions of 2.0 g/l, 40% (w/w), and 16–52 mol% were obtained, respectively. Similarly, the CESF hydrolysate-based shake-flask cultures yielded 1.6 g/l PHA, 39% (w/w) PHA contents, and 4–67 mol% 3HV compositions. These data are comparable to copolymer yields and cellular contents reported for hexose plus levulinic acid-based shake-flask cultures, as reported using Alcaligenes eutrophus and Pseudomonas putida. However, our findings presage a conceivable alternative, forestry-based biorefinery approach for the production of value-added biodegradable PHA polymers. Specifically, this review describes the current and potential utilization of lignocellulosic process streams as platform precursors to PHA polymers including hemicellulosic hydrolysates, residual cellulose-derived levulinic acid, tall oil fatty acids (Kraft pulping residual), and lignin-derived aromatics.     

Enhanced production of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) copolymer and antimicrobial yellow pigmentation from Cupriavidus sp. USMAHM13 with antibiofilm capability

Antibiofilm polymers have the ability to inhibit bacterial biofilm formation, which is known to occur ubiquitously in the environment and pose risks of infection. In this study, production of P(3HB-co-4HB) copolymer and antimicrobial yellow pigment from Cupriavidus sp. USMAHM13 are enhanced through medium optimization. Before the improvement of yellow pigment production, screening for the best additional supplement was performed resulting in high-yield yellow pigmentation using yeast extract with optimum concentration of 2?g/L. Effects of different concentrations of 1,4-butanediol, ammonium acetate, and yeast extract were studied using central composite design. Under optimal conditions, 53?wt% of polyhydroxyalkanoate (PHA) content, 0.35?g/L of pigment concentration, and 5.87?g/L of residual biomass were achieved at 0.56?wt% C of 1,4-butanediol, 1.14?g/L of ammonium acetate, and 2?g/L of yeast extract. Antibiofilm tests revealed that the yellow pigment coated on P(3HB-co-4HB) copolymer had significant effect on the inhibition of bacteria proliferation and colonization from 6?hr onward reaching 100% inhibition by 12?hr, hence effectively inhibiting the biofilm formation.     

Production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) co-polymer by the diazotrophic cyanobacterium Aulosira fertilissima CCC 444

Accumulation of poly(3-hydroxybutyrate-co-3-hydroxyvalerate), P(3HB-co-3HV), a well-known co-polymer of polyhydroxyalkanoates family, was investigated in a N₂-fixing cyanobacterium, Aulosira fertilissima CCC 444, in presence of propionate and valerate in the culture medium. The most significant rise in P(3HB-co-3HV) co-polymer content up to 77 % of dry cell weight was recorded under 0.5 % fructose?+?0.4 % valerate supplementation depicting a productivity of 38 mg L^?1 day^?1, which was further increased by 2.5-fold, i.e., up to 95 mg L^?1 day^?1 under P deficiency. Surface analysis revealed a regular and smooth surface for P(3HB-co-3HV) co-polymer, against rugged and porous surface of the homopolymer of poly-β-hydroxybutyrate. X-ray diffraction showed semi-crystalline nature of the P(3HB-co-3HV) co-polymer. The thermal and mechanical properties of the co-polymer are comparable with the chemoheterotrophic bacterial polymers, thus opens up possibilities of using cyanobacterial PHAs in various fields.