Synthesis of short-/medium-chain-length poly(hydroxyalkanoate) blends by mixed culture fermentation of glycerol

Glycerol was used as a substrate in the bio-production of poly(hydroxyalkanoates) (PHAs) in an effort to establish an alternative outlet for glycerol and produce value-added products. Pseudomonas oleovorans NRRL B-14682 and Pseudomonas corrugata 388 grew and synthesized poly(3-hydroxybutyrate) (P3HB) and medium-chain-length PHA (mcl-PHA) consisting primarily of 3-hydroxydecanoic acid (C(10:0); 44 +/- 2 mol %) and 3-hydroxydodecenoic acid (C(12:1); 31 +/- 2 mol %), respectively, from glycerol at concentrations up to 5% (v/v). Cellular productivity maximized at 40% for P. oleovorans in 5% (v/v) glycerol and 20% for P. corrugata in 2% (v/v) glycerol after 72 h. Increasing the glycerol media concentration from 1% to 5% (v/v) caused a 61% and 72% reduction in the molar mass (M(n)) of the P3HB and mcl-PHA polymers, respectively. Proton-NMR analysis of the glycerol-derived P3HB revealed that the M(n) decrease was the result of esterification of glycerol onto the polymer in a chain terminating position. However, no evidence of glycerol-based chain termination was present in the mcl-PHA. The growth patterns of P. oleovorans and P. corrugata on glycerol permitted their use as mixed cultures to produce natural blends of P3HB and mcl-PHA. By incorporating a staggered inoculation pattern and varying the duration of the fermentations, P3HB/mcl-PHA ratios were achieved that varied from 34:66 to 96:4.     

The conversion of BTEX compounds by single and defined mixed cultures to medium-chain-length polyhydroxyalkanoate

Here, we report the use of petrochemical aromatic hydrocarbons as a feedstock for the biotechnological conversion into valuable biodegradable plastic polymers-polyhydroxyalkanoates (PHAs). We assessed the ability of the known Pseudomonas putida species that are able to utilize benzene, toluene, ethylbenzene, p-xylene (BTEX) compounds as a sole carbon and energy source for their ability to produce PHA from the single substrates. P. putida F1 is able to accumulate medium-chain-length (mcl) PHA when supplied with toluene, benzene, or ethylbenzene. P. putida mt-2 accumulates mcl-PHA when supplied with toluene or p-xylene. The highest level of PHA accumulated by cultures in shake flask was 26% cell dry weight for P. putida mt-2 supplied with p-xylene. A synthetic mixture of benzene, toluene, ethylbenzene, p-xylene, and styrene (BTEXS) which mimics the aromatic fraction of mixed plastic pyrolysis oil was supplied to a defined mixed culture of P. putida F1, mt-2, and CA-3 in the shake flasks and fermentation experiments. PHA was accumulated to 24% and to 36% of the cell dry weight of the shake flask and fermentation grown cultures respectively. In addition a three-fold higher cell density was achieved with the mixed culture grown in the bioreactor compared to shake flask experiments. A run in the 5-l fermentor resulted in the utilization of 59.6 g (67.5 ml) of the BTEXS mixture and the production of 6 g of mcl-PHA. The monomer composition of PHA accumulated by the mixed culture was the same as that accumulated by single strains supplied with single substrates with 3-hydroxydecanoic acid occurring as the predominant monomer. The purified polymer was partially crystalline with an average molecular weight of 86.9 kDa. It has a thermal degradation temperature of 350 degrees C and a glass transition temperature of -48.5 degrees C.     

Poly(ethylene glycol)-mediated molar mass control of short-chain- and medium-chain-length poly(hydroxyalkanoates) from Pseudomonas oleovorans

Three strains of Pseudomonas oleovorans, a well known poly(hydroxyalkanoate) (PHA) producer, were tested for the ability to control PHA molar mass and end group structure by addition of poly(ethylene glycol) (PEG) to the fermentation medium. Each strain of P. oleovorans - NRRL B-14682 (B-14682), NRRL B-14683 (B-14683), and NRRL B-778 (B-778) - synthesized a different type of PHA from oleic acid when cultured under identical growth conditions. Strain B-14682 produced poly(3-hydroxybutyrate) (PHB), while B-14683 synthesized a medium-chain-length PHA ( mcl-PHA) with a repeat unit composition ranging from C4 to C14 and some mono-unsaturation in the C14 alkyl side chains. Strain B-778 synthesized a mixture of PHB (95 mol%) and mcl-PHA (5 mol%). The addition of 0.5% (v/v) PEG (M(n) =200 g/mol, PEG-200) to the fermentation broth of strains B-14682 and B-778 resulted in chain termination through esterification at the carboxyl terminus of the PHB with PEG chain segments, thus reducing the molar mass by 54% and 23%, respectively. The molar mass of the mcl-PHA produced by strains B-14683 and B-778 also showed a 34% and 47% reduction in the presence of PEG-200, respectively, but no evidence of esterification was present. PEG-400 (M(n) =400 g/mol) had a reduced effect on PHA molar mass. In fact, the molar masses of the mcl-PHA derived from strain B-14683 and both the PHB and mcl-PHA from B-778 were unchanged by PEG-400. In contrast, the PHB produced by B-14682 showed a 35% reduction in molar mass in the presence of PEG-400.     

Production of medium-chain-length polyhydroxyalkanoates by sequential feeding of xylose and octanoic acid in engineered Pseudomonas putida KT2440

ABSTRACT: BACKGROUND: Pseudomonas putida KT2440 is able to synthesize large amounts of medium-chain-length polyhydroxyalkanoates (mcl-PHAs). To reduce the substrate cost, which represents nearly 50% of the total PHA production cost, xylose, a hemicellulose derivate, was tested as the growth carbon source in an engineered P. putida KT2440 strain. RESULTS: The genes encoding xylose isomerase (XylA) and xylulokinase (XylB) from Escherichia coli W3110 were introduced into P. putida KT2440. The recombinant KT2440 exhibited a XylA activity of 1.47 U and a XylB activity of 0.97 U when grown on a defined medium supplemented with xylose. The cells reached a maximum specific growth rate of 0.24 h-1 and a final cell dry weight (CDW) of 2.5 g L-1 with a maximal yield of 0.5 g CDW g-1 xylose. Since no mcl-PHA was accumulated from xylose, mcl-PHA production can be controlled by the addition of fatty acids leading to tailor-made PHA compositions. Sequential feeding strategy was applied using xylose as the growth substrate and octanoic acid as the precursor for mcl-PHA production. In this way, up to 20% w w-1 of mcl-PHA was obtained. A yield of 0.37 g mcl-PHA per g octanoic acid was achieved under employed conditions. CONCLUSIONS: Sequential feeding of relatively cheap carbohydrates and expensive fatty acids is a practical way to achieve more cost-effective mcl-PHA production. This study is the first reported attempt to produce mcl-PHA by using xylose as the growth substrate. Further process optimizations to achieve higher cell density and higher productivity of mcl-PHA should be investigated. These scientific exercises will undoubtedly contribute to the economic feasibility of mcl-PHA production from renewable feedstock.     

Polymerase C1 levels and poly(R-3-hydroxyalkanoate) synthesis in wild-type and recombinant Pseudomonas strains.

A functional antibody highly specific for polymerase C1 of Pseudomonas oleovorans GPo1 was raised and used to determine polymerase C1 levels in in vivo experiments. The polymerase C1 antibodies did not show a cross-reaction with polymerase C2 of P. oleovorans. In wild-type P. oleovorans GPo1 and Pseudomonas putida KT2442, amounts of 0.075 and 0.06% polymerase relative to total protein, respectively, were found. P. oleovorans GPo1(pGEc405), which contained additional copies of the polymerase C1-encoding gene under the control of its native promoter, contained 0.5% polymerase C1 relative to total protein. Polymerase C1 reached 10% of total cell protein when the polymerase C1-encoding gene was overexpressed through the P(alk) promoter in P. oleovorans GPo1(pET702, pGEc74). Amounts of poly(R-3-hydroxyalkanoate) (PHA) increased significantly under non-nitrogen-limiting conditions when additional polymerase C1 was expressed in P. oleovorans. Whereas P. oleovorans produced 34% (wt/wt) PHA under these conditions, a PHA level of 64% (wt/wt) could be reached for P. oleovorans GPo1(pGEc405) and a PHA level of 52% (wt/wt) could be reached for P. oleovorans GPo1(pET702, pGEc74) after induction, compared to a PHA level of 13% for the uninduced control. All recombinant Pseudomonas strains containing additional polymerase C1 showed small changes in their PHA composition. Larger amounts of 3-hydroxyhexanoate monomer and smaller amounts of 3-hydroxyoctanoate and -decanoate were found compared to those of the wild type. Two different methods were developed to quantify rates of incorporation of new monomers into preexisting PHA granules. P. oleovorans GPo1 cells grown under nitrogen-limiting conditions showed growth stage-dependent incorporation rates. The highest PHA synthesis rates of 9.5 nmol of C8/C6 monomers/mg of cell dry weight (CDW)/min were found during the mid-stationary phase, which equals a rate of production of 80 g of PHA/kg of CDW/h.     

Efficient production of medium-chain-length poly(3-hydroxyalkanoates) from octane by Pseudomonas oleovorans: economic considerations

Poly(3-hydroxyalkanoates) (PHA) have the potential to become a biodegradable alternative for conventional plastics. In order to produce PHA at competitive costs in comparison with commonly used plastics, efficient PHA production systems will have to be developed. Poly(3-hydroxybutyrate) fermentations are well developed and in actual use on an industrial scale; medium-chain-length PHA (mcl-PHA) production is less well described, although the vast majority of all PHA known today are mcl-PHA. This paper compares and describes mcl-PHA production systems with respect to the volumetric productivity, the cellular PHA content and the polymer yield on carbon substrates. Nitrogen was shown to be the most effective limitation to trigger PHA formation in P. oleovorans after different nutrient limitations had been compared. By using an economic model for the calculation of PHA production costs, we show that it should be possible to produce octane-based mcl-PHA on a large scale (more than 1000 tonnes/year) at costs below U.S. $ 10 kg⁻¹. Received: 4 April 1997 / Accepted: 20 May 1997     

Metabolic engineering and characterization of phaC1 and phaC2 genes from Pseudomonas putida KCTC1639 for overproduction of medium-chain-length polyhydroxyalkanoate

Two PHA synthase phaC1 and phaC2 genes cloned from the new strain Pseudomonas putida KCTC1639 were metabolically engineered for the overproduction of medium-chain-length polyhydroxyalkanoate (mcl-PHA). The overexpressed phaC1 and phaC2 genes in P. putida KCTC1639 were compared in terms of the biosynthesis of mcl-PHA, fatty acid assimilation, distribution of 3-hydroxylacyl monomer units, granular morphology, and thermophysical properties of the accumulated mcl-PHA. The biosynthesis of mcl-PHA was enhanced only by the overexpressed phaC1 gene up to 2.86-fold, in contrast, the phaC2 gene did not activate the biosynthesis of mcl-PHA. The overexpressed phaC1 gene tended to form enlarged, high molecular weight, and lower crystalline mcl-PHA granules, whereas the amplified phaC2 gene induced the fragmentation of mcl-PHA into a few small-sized granules. The transformant P. putida KCTC1639 overexpressing the phaC1 gene encoding PHA synthase I was cultivated by pH-stat fed-batch cultivation, and the concentration and content of mcl-PHA increased up to 8.91 g L-1 and 70.5%, respectively.     

Biosynthesis of synthons in two-liquid-phase media

The Pseudomonas oleovorans alkane hydroxylase and xylene oxygenase from Pseudomonas putida are versatile mono-oxygenases for stereo- and regioselective oxidation of aliphatic and aromatic hydrocarbons. Pseudomonas oleovorans and alkanol dehydrogenase deficient mutants of Pseudomonas have previously been used to produce alkanols from various alkanes and optically active epoxides from alkenes. Similarly, P. putida strains have been used to produce aromatic alcohols, aromatic acids, and optically active styrene oxides. A limitation in the use of Pseudomonas strains for bioconversions is that these strains can degrade some of the products formed. To counter this problem, we have constructed Escherichia coli recombinants, which contain the alk genes from the OCT plasmid of P. oleovorans [E. coli HB101 (pGEc47)] and the xylMA genes from the TOL plasmid of P. putida mt-2 [E. coli HB101 (pGB63)], encoding alkane hydroxylase and xylene oxygenase, respectively. Escherichia coli HB101 (pGEc47) was used to produce octanoic acid from n-octane and E. coli HB101 (pBG63) was put to use for the oxidation of styrene to styrene oxide in two-liquid phase biocatalysis at high cell densities. The alk(+) recombinant strain E. coli HB101 (pGEc47) was grown to 40 g/L cell dry mass in the presence of n-octane, which was converted to octanoic acid by the alkane oxidation system, the product accumulating in the aqueous phase. The xyl(+) recombinant E. coli HB101 (pBG63) was grown to a cell density of 26 g/L cell dry mass in the presence of around 7% (v/v) n-dodecane, which contained 2% (v/v) styrene. The recombinant E. coli (xyl(+)) converted styrene to (S)-(+)-styrene oxide at high enantiomeric excess (94% ee) and this compound partitioned almost exclusively into the organic phase. Using these high-cell-density two-liquid-phase cultures, the products accumulated rapidly, yielding high concentrations of products (50 mM octanoic acid and 90 mM styrene oxide) in the respective phases. (c) 1996 John Wiley & Sons, Inc.     

Engineering of stable recombinant bacteria for production of chiral medium-chain-length poly-3-hydroxyalkanoates.

In order to scale up medium-chain-length polyhydroxyalkanoate (mcl-PHA) production in recombinant microorganisms, we generated and investigated different recombinant bacteria containing a stable regulated expression system for phaC1, which encodes one of the mcl-PHA polymerases of Pseudomonas oleovorans. We used the mini-Tn5 system as a tool to construct Escherichia coli 193MC1 and P. oleovorans POMC1, which had stable antibiotic resistance and PHA production phenotypes when they were cultured in a bioreactor in the absence of antibiotic selection. The molecular weight and the polydispersity index of the polymer varied, depending on the inducer level. E. coli 193MC1 produced considerably shorter polyesters than P. oleovorans produced; the weight average molecular weight ranged from 67,000 to 70,000, and the polydispersity index was 2.7. Lower amounts of inducer added to the media shifted the molecular weight to a higher value and resulted in a broader molecular mass distribution. In addition, we found that E. coli 193MC1 incorporated exclusively the R configuration of the 3-hydroxyoctanoate monomer into the polymer, which corroborated the enantioselectivity of the PhaC1 polymerase enzyme.     

The microbial production of poly(hydroxyalkanoates) from tallow

The bacteria Pseudomonas oleovorans, P. resinovorans, P. putida, and P. citronellolis were evaluated for their ability to grow and produce poly(hydroxyalkanoates) (PHA) using tallow free fatty acids and tallow triglyceride as carbon substrates. Tallow free fatty acids supported cell growth and PHA production for all four organisms, yielding PHA contents of 18%, 15%, 19% and 3% of their cell dry weights for P. oleovorans, P.␣resinovorans, P. putida, and P. citronellolis respectively. Only P. resinovorans, however, was able to grow and produce PHA polymer, with cells attaining a PHA content of 15% of their cell dry weight, using unhydrolyzed tallow as the substrate. Extracts from 46-h cultures of P. resinovorans were found to have a higher esterase activity (12.80 units μl⁻¹min⁻¹) compared to the activities found for cultures of P. oleovorans, P. citronellolis, and P. putida ( < 0.03 units μl⁻¹min⁻¹). Polymer repeat-unit compositions were determined by GC analysis of the β-hydroxymethyl esters of hydrolyzed PHA, and ranged in carbon-chain lengths from C₄ to C₁₄, with some mono-unsaturation in the C₁₂ and C₁₄ side-chains. PHA compositions were similar for the polymers obtained from all four organisms, with repeat units of chain lengths C₈ and C₁₀ predominating. Received: 16 February 1996 / Received revision: 23 May 1996 / Accepted: 10 June 1996     

The role of the fatty acid beta-oxidation multienzyme complex from Pseudomonas oleovorans in polyhydroxyalkanoate biosynthesis: molecular characterization of the fadBA operon from P. oleovorans and of the enoyl-CoA hydratase genes phaJ from P. oleovorans and Pseudomonas putida

In order to investigate the role of the putative epimerase function of the beta-oxidation multienzyme complex (FadBA) in the provision of (R)-3-hydroxyacyl-CoA thioesters for medium-chain-length polyhydroxyalkanoate (PHA(MCL)) biosynthesis, the fadBA(Po) operon of Pseudomonas oleovorans was cloned and characterized. The fadBA(Po) operon and a class-II PHA synthase gene of Pseudomonas aeruginosa were heterologously co-expressed in Escherichia coli to determine whether the putative epimerase function of FadBA(Po) has the ability to provide precursors for PHA accumulation in a non-PHA-accumulating bacterium. Cultivation studies with fatty acids as carbon source revealed that FadBA(Po) did not mediate PHA(MCL) biosynthesis in the E. coli wild-type strain harboring a PHA synthase gene. However, PHA accumulation was strongly impaired in a recombinant E. coli fadB mutant, which harbored a PHA synthase gene. These data indicate that in pseudomonads FadBA does not possess the inherent property, based on a putative epimerase function, to provide the ( R)-enantiomer of 3-hydroxyacyl-CoA efficiently and that other linking enzymes are required to efficiently channel intermediates of beta-oxidation towards PHA(MCL) biosynthesis. However, the phaJ gene from P. oleovorans and from Pseudomonas putida, both of which encoded a 3- Re enoyl-CoA hydratase, was identified. The co-expression of phaJ(Po/Pp) with either a class-II PHA synthase gene or the PHA synthase gene from Aeromonas punctata in E. coli revealed that PhaJ(Po/Pp) mediated biosynthesis of either PHA(MCL), contributing to about 1% of cellular dry mass, or of poly(3-hydroxybutyrate- co-3-hydroxyhexanoate), contributing to 3.6% of cellular dry mass, when grown on decanoate. These data indicate that FadBA(Po)does not mediate the provision of (R)-3-hydroxyacyl-CoA, which resembles FadBA of non-PHA-accumulating bacteria, and that 3- Re enoyl-CoA hydratases are required to divert intermediates of fatty acid beta-oxidation towards PHA biosynthesis in P. oleovorans.     

Cytochrome Content of Two Pseudomonads Containing Mixed-Function Oxidase Systems

The cytochrome and nonheme iron protein content of two pseudomonads, Pseudomonas oleovorans and P. putida, containing mixed function oxidase systems was examined. The mixed function oxidase system of P. oleovorans and P. putida had previously been shown to be present in cells which had been grown on hexane and camphor, respectively, as energy source. The content of protoheme was found to increase significantly when the organisms were grown on the substrates for mixed function oxidation. The nonheme iron protein content increased significantly in the case of P. putida and was constant in P. oleovorans. The cytochrome c content was essentially constant in both pseudomonads. The content of cytochrome P-450 in P. putida increased from an immeasurably low amount to 0.15 nmoles per mg (dry weight). The content of cytochrome o in P. oleovorans increased by a factor of 4.5. P. oleovorans was not found to contain detectable quantities of cytochrome P-450 either in the presence or absence of the mixed function oxidase system.     

First-order kinetics analysis of monomer composition dependent polyhydroxyalkanoic acid degradation in Pseudomonas spp

The intracellular degradation of polyhydroxyalkanoic acid (PHA) in pseudomonads was investigated by first-order kinetics analysis using the initial rate method. One type of PHA was accumulated in five Pseudomonas spp., P. oleovorans, P. aeruginosa, P. fluorescens, P. citronellolis, and P. putida, by growing them on octanoic acid. The monomer compositions of the five PHA were not significantly different from one another: 85-90 mol % 3-hydroxyoctanoic acid (3HO), 7-12 mol % 3-hydorxycaproic acid (3HC), and 3-6 mol % 3-hydroxydecanoic acid (3HD). The first-order degradation rate constants (k(1)) for the octanoate-derived PHA (designated P(3HO)) in the five species were in a similar range between 0.060 and 0.088 h(-1). This may indicate the similar specificities of the five intracellular depolymerases. In addition, the similar k(1) among the different species may correlate with the high degree of amino acid sequence identities (over 85%) among the intracellular PHA depolymerase phaZ genes. Six other chemically different types of PHA were accumulated in P. putida from n-nonanoic acid, n-decanoic acid, 5-phenyvaleric acid, or 11-phenoxyundecanoic acid as a single or a mixed carbon source. The calculated k(1) values were characteristic to each PHA, reflecting their chemical structures. In comparison with P(3HO), an increase in the levels of the two minor monomers 3HC and 3HD as in P(21 mol % 3HC-co-56 mol % 3HO-co-23 mol % 3HD) significantly slowed the rate of intracellular degradation. From the comparison of k(1) values, it is suggested that the P. putida intracellular depolymerase is most active against P(3HO).     

Acetone extraction of mcl-PHA from Pseudomonas putida KT2440

A methodology was developed for the extraction of medium-chain-length poly-3-hydroxyalkanoates (mcl-PHA) from Pseudomonas putida. It was determined that if dry P. putida biomass containing mcl-PHA was washed in 20 volumes of methanol for 5 min followed by Soxhlet extraction in 10 volumes of acetone for 5 h, almost all of the PHA could be recovered with no detectable loss of molecular weight. Biomass containing higher amounts of PHA required less methanol during the pretreatment step but more acetone in the solvent extraction step than biomass containing less PHA. Further purification could be achieved by redissolving the PHA in acetone and reprecipitating in cold methanol. UV spectroscopy at 241 and 275 nm could be used as an indication of product purity.     

Synthesis and characterization of poly(3-hydroxyalkanoates) from Brassica carinata oil with high content of erucic acid and from very long chain fatty acids

Pseudomonas aeruginosa produced medium chain length poly(3-hydroxyalkanoates) (mcl-PHAs) when grown on substrates containing very long chain fatty acids (VLCFA, C>20). Looking for low cost carbon sources, we tested Brassica carinata oil (erucic acid content 35-48%) as an intact triglyceride containing VLCFA. Oleic (C18:1), erucic (C22:1), and nervonic (C24:1) acids were also employed for mcl-PHA production as model substrates. The polymers obtained were analyzed by GC of methanolyzed samples, GPC, 1H and 13C NMR, ESI MS of partially pyrolyzed samples, and DSC. The repeating units of such polymers were saturated and unsaturated, with a higher content of the latter in the case of the PHA obtained from B. carinata oil. Statistical analysis of the ion intensity in the ESI mass spectra showed that the PHAs from pure fatty acids are random copolymers, while the PHA from B. carinata oil is either a pure polymer or a mixture of polymers. Weight-average molecular weight varied from ca. 56,000 g/mol for the PHA from B. carinata oil and oleic acid, to about 120,000 g/mol for those from erucic and nervonic acids. The PHAs from erucic and nervonic acids were partially crystalline, with rubbery characteristics and a melting point (Tm) of 50°C, while the PHAs from oleic acid and from B. carinata oil afforded totally amorphous materials, with glass transition temperatures (Tg) of -52°C and -47°C, respectively.     

Kinetics of medium-chain-length polyhydroxyalkanoate production by a novel isolate of Pseudomonas putida LS46

Six bacteria that synthesize medium-chain-length polyhydroxyalkanoates (mcl-PHAs) were isolated from sewage sludge and hog barn wash and identified as strains of Pseudomonas and Comamonas by 16S rDNA gene sequencing. One isolate, Pseudomonas putida LS46, showed good PHA production (22% of cell dry mass) in glucose medium, and it was selected for further studies. While it is closely related to other P.?putida strains (F1, KT2440, BIRD-1, GB-1, S16, and W619), P.?putida LS46 was genetically distinct from these other strains on the basis of nucleotide sequence analysis of the cpn60 gene hypervariable region. PHA production was detected as early as 12?h in both nitrogen-limited and nitrogen-excess conditions. The increase in PHA production after 48?h was higher in nitrogen-limited cultures than in nitrogen-excess cultures. Pseudomonas?putida LS46 produced mcl-PHAs when cultured with glucose, glycerol, or C(6)-C(14) saturated fatty acids as carbon sources, and mcl-PHAs accounted for 56% of the cell dry mass when cells were batch cultured in medium containing 20?mmol/L octanoate. Although 3-hydroxydecanoate was the major mcl-PHA monomer (58.1-68.8?mol%) in P.?putida LS46 cultured in glucose medium, 3-hydroxyoctanoate was the major monomer produced in octanoate medium (88?mol%).     

Physiological Characterization and Genetic Engineering of Pseudomonas corrugata for Medium-Chain-Length Polyhydroxyalkanoates Synthesis from Triacylglycerols

Pseudomonas belonging to the rRNA-DNA homology group I produce medium-chain-length (mcl)-polyhydroxyalkanoates (PHA). We show that P. corrugata, a member of this group, accumulates 0.5–1.0 g of mcl-PHA/L of culture when grown on glucose (Gl) or oleic acid (Ol). The predominant monomers of Gl-PHA and Ol-PHA are β-hydroxydecanoate and β-hydroxyoctanoate, respectively. The molecular masses and polydispersity of P. corrugata PHAs are higher than those typically found with other Pseudomonas. We electrotransformed P. corrugata with a plasmid pCN51lip-1 carrying Pseudomonas lipase genes to generate strain III111-1. The recombinant strain grew on intact triacylglycerols (TAGs) to 1.9–2.7 g of cell-dry-weight/L of culture. The yields and the predominant repeat-units of PHAs obtained from the lard- and tallow-grown III111-1 were similar to those of Ol-PHA from wild-type cells. In contrast to other Pseudomonas species, P. corrugata III111-1 grown on TAGs at temperatures up to 36°C was not significantly affected with regard to cell yields, amounts of PHA produced, and the repeat unit compositions of the polymer. Received: 29 May 2001 / Accepted: 2 July 2001     

Improvement of the conversion of polystyrene to polyhydroxyalkanoate through the manipulation of the microbial aspect of the process: a nitrogen feeding strategy for bacterial cells in a stirred tank reactor

Pseudomonas putida CA-3 has been shown to accumulate the biodegradable plastic polyhydroxyalkanoate (PHA) when fed styrene or polystyrene pyrolysis oil as the sole carbon and energy source under nitrogen limiting growth conditions (67 mg nitrogen per litre at time 0). Batch fermentation of P. putida CA-3 grown on styrene or polystyrene pyrolysis oil in a stirred tank reactor yields PHA at 30% of the cell dry weight (CDW). The feeding of nitrogen at a rate of 1mg N/l/h resulted in a 1.1-fold increase in the percentage of CDW accumulated as PHA. An increase in the rate of nitrogen feeding up to 1.5mg N/l/h resulted in further increases in the percentage of the cell dry weight composed of PHA. However, feeding rates of 1.75 and 2mg N/l/h resulted in dramatic decreases in the percentage of cell dry weight composed of PHA. Interestingly nitrogen was not detectable in the growth medium after 16 h, in any of the growth conditions tested. A higher cell density was observed in cells supplied with nitrogen and thus further increases in the overall production of PHA were observed through nitrogen feeding. The highest yield of PHA was 0.28 g PHA per g styrene supplied with a nitrogen feeding rate of 1.5mg/l/h.     

Bacterial synthesis of polyhydroxyalkanoates containing aromatic and aliphatic monomers by Pseudomonas putida CA-3

Pseudomonas putida CA-3 has the ability to accumulate to high levels unique polyhydroxyalkanoate (PHA) heteropolymers composed of aromatic and aliphatic monomers. The majority of monomers are aromatic making up 98% of the polymer. (R)-3-hydroxyphenylvalerate and (R)-3-hydroxyphenylhexanoate are the most abundant monomers found in polymers accumulated from phenylalkanoic acids with an uneven and even number of carbons on the acyl side chain respectively. PHAs accumulated from phenylvaleric and phenylhexanoic acid were partially crystalline while all other PHAs were amorphous. Significant differences in the yield and PHA content of the cells occurred when different phenylalkanoic acids were supplied as growth substrates. Increasing the initial concentration of the growth substrate increased both the PHA content of the cells and the overall yield (g PHA/g carbon supplied) of PHA accumulated by P. putida CA-3 cells. The highest PHA content (% cell dry wt.) from an aromatic carbon source was 59% when 15mM phenylvaleric acid was supplied as the sole source of carbon and energy. This corresponded to a maximum PHA yield of 0.42 g PHA/g carbon supplied. In and attempt to increase the level of PHA accumulated from related growth substrates acrylic acid was added to the growth medium. However, the addition of various concentrations of acrylic acid to the growth medium had either no effect or decreased the PHA content of the cell accumulated from phenylalkanoic acids by P. putida CA-3.