Production of two phase polyhydroxyalkanoic acid granules in Ralstonia eutropha.

To synthesize layered granules consisting of selected phases of polyhydroxybutyrate (PHB) homopolymer and PH(B-co-V) copolymer, Ralstonia eutropha was grown on fructose and limited quantities (1 g/l) of valeric acid. Exhaustion of the valerate resulted in a carbon source shift and a shift in the composition of polyhydroxyalkanoate (PHA) being synthesized within the cell. The synthesis rates were 0.030 g PH(B-co-V)/l per h and 0.033 g PHB/l per h, giving a copolymer composition of 48% HV. The valerate was exhausted at approximately 12 h at a rate of 0.0894 g/l per h after which only PHB was produced through the remaining 12 h at 0.033 g PHB/l per h from the remaining fructose, which was utilized at a constant rate of 0.0861 g/l per h throughout all 24 h of the experiment. Differential scanning calorimetry (DSC) of isolated granules showed two glass transitions, confirming the presence of two distinct polymer phases within the layered granules. Transmission electron microscopic images stained with RuO4 revealed a heavily stained copolymer core within a lighter stained PHB shell, confirming the expected morphology of granule composition. Thus, biosynthesis can be exploited for the control of domain sizes in layered granules, potentially providing metabolic control over the physical properties of the resultant polymer.     

Production of polyhydroxybutyrate by Ralstonia eutropha from protein hydrolysates

Polyhydroxybutyrate (PHB) was produced by Ralstonia eutropha DSM 11348 (formerly Alicaligenes eutrophus) in media containing 20–30 g l⁻¹ casein peptone or casamino acids as sole sources of nitrogen. In fermentations using media based on casein peptone, permanent growth up to a cell dry mass of 65 g l⁻¹ was observed. PHB accumulated in cells up to 60%–80% of dry weight. The lowest yields were found in media without any trace elements or with casamino acids added only. The residual cell dry masses were limited to 10–15 g l⁻¹ and did not contain PHB. The highest productivity amounted to 1.2 g PHB l⁻¹ h⁻¹. The mean molecular mass of the biopolymer was determined as 750 kDa. The proportion of polyhydroxyvalerate was less than 0.2% in PHB. The bioprocess was scaled up to a 300-l plant. During a fermentation time of 39 h the cells accumulated PHB to 78% w/w. The productivity was 0.98 g PHB l⁻¹ h¹. Received: 8 July 1998 / Accepted: 26 August 1998     

Production of unsaturated polyesters by Pseudomonas oleovorans

Pseudomonas oleovorans was grown separately on 3-hydroxy-6-octenoic acid and 3-hydroxy-7-octenoic acid as the only carbon source and under ammonium nutrient-limiting conditions to produce storage polyesters. The polyesters produced contained mainly unsaturated C8 units. Small amounts of both the saturated and the unsaturated C6 units were also present, but only about 1% of the saturated 3-hydroxyoctanoate units was detected. The polyester obtained from 3-hydroxy-6-octenoic acid, which was a mixture of the cis and trans isomers, also contained units with cis and trans double bonds. The weight average molecular weights of the polymers produced were in the range of 339,000-383,000 as determined by g.p.c. relative to polystyrene, with Mw/Mn ratios of 1.8-2.1. The mechanism of PHA formation from n-octene previously reported is discussed in relation to the present results, and the two were found to be in good agreement.     

Production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) from plant oil by engineered Ralstonia eutropha strains

The polyhydroxyalkanoate (PHA) copolymer poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) [P(HB-co-HHx)] has been shown to have potential to serve as a commercial bioplastic. Synthesis of P(HB-co-HHx) from plant oil has been demonstrated with recombinant Ralstonia eutropha strains expressing heterologous PHA synthases capable of incorporating HB and HHx into the polymer. With these strains, however, short-chain-length fatty acids had to be included in the medium to generate PHA with high HHx content. Our group has engineered two R. eutropha strains that accumulate high levels of P(HB-co-HHx) with significant HHx content directly from palm oil, one of the world's most abundant plant oils. The strains express a newly characterized PHA synthase gene from the bacterium Rhodococcus aetherivorans I24. Expression of an enoyl coenzyme A (enoyl-CoA) hydratase gene (phaJ) from Pseudomonas aeruginosa was shown to increase PHA accumulation. Furthermore, varying the activity of acetoacetyl-CoA reductase (encoded by phaB) altered the level of HHx in the polymer. The strains with the highest PHA titers utilized plasmids for recombinant gene expression, so an R. eutropha plasmid stability system was developed. In this system, the essential pyrroline-5-carboxylate reductase gene proC was deleted from strain genomes and expressed from a plasmid, making the plasmid necessary for growth in minimal media. This study resulted in two engineered strains for production of P(HB-co-HHx) from palm oil. In palm oil fermentations, one strain accumulated 71% of its cell dry weight as PHA with 17 mol% HHx, while the other strain accumulated 66% of its cell dry weight as PHA with 30 mol% HHx.     

Optimization of growth media components for polyhydroxyalkanoate (PHA) production from organic acids by Ralstonia eutropha

We employed systematic mixture analysis to determine optimal levels of acetate, propionate, and butyrate for cell growth and polyhydroxyalkanoate (PHA) production by Ralstonia eutropha H16. Butyrate was the preferred acid for robust cell growth and high PHA production. The 3-hydroxyvalerate content in the resulting PHA depended on the proportion of propionate initially present in the growth medium. The proportion of acetate dramatically affected the final pH of the growth medium. A model was constructed using our data that predicts the effects of these acids, individually and in combination, on cell dry weight (CDW), PHA content (%CDW), PHA production, 3HV in the polymer, and final culture pH. Cell growth and PHA production improved approximately 1.5-fold over initial conditions when the proportion of butyrate was increased. Optimization of the phosphate buffer content in medium containing higher amounts of butyrate improved cell growth and PHA production more than 4-fold. The validated organic acid mixture analysis model can be used to optimize R. eutropha culture conditions, in order to meet targets for PHA production and/or polymer HV content. By modifying the growth medium made from treated industrial waste, such as palm oil mill effluent, more PHA can be produced.     

Lipid and fatty acid metabolism in Ralstonia eutropha: relevance for the biotechnological production of value-added products

Lipid and fatty acid metabolism has been well studied in model microbial organisms like Escherichia coli and Bacillus subtilis. The major precursor of fatty acid biosynthesis is also the major product of fatty acid degradation (β-oxidation), acetyl-CoA, which is a key metabolite for all organisms. Controlling carbon flux to fatty acid biosynthesis and from β-oxidation allows for the biosynthesis of natural products of biotechnological importance. Ralstonia eutropha can utilize acetyl-CoA from fatty acid metabolism to produce intracellular polyhydroxyalkanoate (PHA). R. eutropha can also be engineered to utilize fatty acid metabolism intermediates to produce different PHA precursors. Metabolism of lipids and fatty acids can be rerouted to convert carbon into other value-added compounds like biofuels. This review discusses the lipid and fatty acid metabolic pathways in R. eutropha and how they can be used to construct reagents for the biosynthesis of products of industrial importance. Specifically, how the use of lipids or fatty acids as the sole carbon source in R. eutropha cultures adds value to these biotechnological products will be discussed here.     

Conversion of volatile fatty acids into polyhydroxyalkanoate by Ralstonia eutropha

Aims:  The aims of this study were to optimize condensed corn solubles (CCS) as a medium for growth of Ralstonia eutropha and to determine the effects of individual volatile fatty acids (VFAs) on polyhydroxyalkanoate (PHA) production .
Methods and Results:  A CCS medium of concentration 240 g l⁻¹ with a carbon : nitrogen ratio of 50 : 1 was developed as the optimal medium. Cultures were grown in 1-l aerated flasks at 250 rev min⁻¹ at 30°C for 120 h. Comparable growth rates were observed in CCS vs a defined medium. At 48 h, VFAs were fed individually at different levels. Optimal levels of all the acids were determined to maximize PHA production. An overall comparison of the VFAs indicated that butyric and propionic acids provided the best results.
Conclusion:  An optimized CCS medium supported growth of R. eutropha . Butyric and propionic acids were the most efficient carbon sources to maximize PHA production when added at the 5 g l⁻¹ level.
Significance and Impact of the Study:  The study shows that a byproduct of ethanol industry can be effectively used as a low cost medium for PHA production, thus partly reducing the cost of commercialization of biopolymers.     

Re-evaluation of the primary structure of Ralstonia eutropha phasin and implications for polyhydroxyalkanoic acid granule binding

Sequence analysis of several cDNAs encoding the phasin protein of Ralstonia eutropha indicated that the carboxyl terminus of the resulting derived protein sequence is different from that reported previously. This was confirmed by: (1) sequencing of the genomic DNA; (2) SDS-PAGE and peptide analysis of wild-type and recombinant phasin; and (3) mass spectrometry of wild-type phasin protein. The results have implications for the model proposed for the binding of this protein to polyhydroxyalkanoic acid granules in the bacterium.     

Production and purification of self-assembling peptides in Ralstonia eutropha

Self-assembling peptides have emerged as an attractive scaffold material for tissue engineering, yet the expense associated with solid phase chemical synthesis has limited their broad use. In addition, the fidelity of chemical synthesis constrains the length of polypeptides that can be produced homogeneously by this method. Template-derived biosynthesis by recombinant DNA technology may overcome both of these problems. However, recovery of polypeptides from recombinant protein expression systems typically involves multi-step purification schemes. In this study, we report an integrated approach to recombinantly produce and purify self-assembling peptides from the recently developed expression host Ralstonia eutropha. The purification is based on the specific affinity of carbohydrate binding modules (CBMs) to cellulose. In a first step, we identified CBMs that express well in R. eutropha by assembling a fusion library of green fluorescent protein (GFP) and CBMs and determining the fluorescence of cell-free extracts. Three GFP::CBM fusions were found to express at levels similar to GFP alone, of which two CBMs were able to mediate cellulose binding of the GFP::CBM fusion. These two CBMs were then fused to multiple repeats of the self-assembling peptide RAD16-I::E (N-RADARADARADARADAE-C). The fusion protein CBM::E::(RAD16-I::E)4 was expressed in R. eutropha and purified using the CBM's affinity for cellulose. Subsequent proteolytic cleavage with endoproteinase GluC liberated RAD16-I::E peptide monomers with similar properties to the chemically synthesized counterpart RAD16-I.     

Inhibitory effect of medium-chain-length fatty acids on synthesis of polyhydroxyalkanoates from volatile fatty acids by Ralstonia eutropha

Medium-chain-length fatty acids, such as nonanoic (9:0) and octanoic (8:0) acids, are more toxic to Ralstonia eutropha than volatile fatty acids such as acetic, propionic and butyric acids. Nonanoic acid was degraded to acetic and propionic acids via -oxidation by Ralstonia eutropha for cell growth and synthesis of polyhydroxyalkanoates (PHAs). In a mixture of the fatty acids, utilization of nonanoic acid was depressed by acetic and propionic acids, and vice versa. The PHA accumulation from the volatile fatty acids was decreased from 53% (w/w) of dry cell mass to 23% due to the nonanoic acid. Similar phenomena were also observed with octanoic acid and its metabolic intermediates, acetic and butyric acids.     

Production of poly(3-hydroxybutyrate) and poly(3-hydroxybutyrate-co-4-hydroxybutyrate) by Ralstonia eutropha from soybean oil

High-yield production of polyhydroxyalkanoates (PHAs) by Ralstonia eutropha KCTC 2662 was investigated using soybean oil and γ-butyrolactone as carbon sources. In flask culture, it was shown that R. eutropha KCTC 2662 accumulated PHAs during the growth phase. The optimum carbon to nitrogen ratio (C/N ratio) giving the highest cell and PHA yield was 20 g-soybean oil/g-(NH(4))(2)SO(4). The 4-hydroxybutyrate (4HB) fraction in the copolymer was not strongly affected by the C/N ratio. In a 2.5-L fermentor, a homopolymer of poly(3-hydroxybutyrate) [P(3HB)] was produced from soybean oil as the sole carbon source by batch and fed-batch cultures of R. eutropha with dry cell weights of 15-32 g/L, PHA contents of 78-83 wt% and yields of 0.80-0.82 g-PHA/g-soybean oil used. By co-feeding soybean oil and γ-butyrolactone as carbon sources, a copolymer of poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)] could be produced with dry cell weights of 10-21 g/L, yields of 0.45-0.56 g-PHA/g-soybean oil used (0.39-0.50g-PHA/g-carbon sources used) and 4HB fractions of 6-10 mol%. Higher supplementation of γ-butyrolactone increased the 4HB fraction in the copolymer, but decreased cell and PHA yield.     

Production of (3-hydroxybutyrate-co-3-hydroxyhexanoate) copolymer from coffee waste oil using engineered Ralstonia eutropha

Bioprocess and Biosystems Engineering - Polyhydroxyalkonate (PHA) is a type of polymer that has the potential to replace petro-based plastics. To make PHA production more economically feasible,...     

Ralstonia eutropha strain H16 as model organism for PHA metabolism and for biotechnological production of technically interesting biopolymers

The Gram-negative, facultative chemolithoautotrophic bacterium Ralstonia eutropha has been intensively investigated for almost 50 years. Today it is the best studied 'Knallgas' bacterium and producer of poly(3-hydroxybutyric acid). This polyester provides the basis for renewable resource-based biodegradable plastic materials and has attracted much biotechnological interest. The polymer is accumulated in large amounts in the cell and can be used for various applications ranging from replacement of fossil resource-based bulk plastics to high-value special purpose polymers. To further enhance productivity and to allow tailormade poly(hydroxyalkanoic acids) (PHA) with different monomer compositions by metabolic engineering, the knowledge of metabolic pathways and of the biochemical properties of the enzymes involved is essential. Furthermore, proteins covering the PHA granule surface, which are referred to as phasins, and fusions of these phasins to other proteins are promising candidates for various protein technologies. The recently published genome sequence of strain H16 allows researchers to take a closer look at the genetic potential of this versatile bacterium. R. eutropha is, however, not limited to PHAs and to PHA-related polymers like poly(mercaptoalkanoic acids) as it can also be employed for production of a range of other interesting polymers including polyamides like cyanophycin.     

Production of unusual bacterial polyesters by Pseudomonas oleovorans through cometabolism

Abstract Pseudomonas oleovorans is an adaptable, aerobic bacterium that can produce a wide range of storage polyesters (poly-β-hydroxyalkanoates, PHAs). With few exceptions, the PHAs obtained when this bacterium is grown with single organic substrates capable of polymer production are generally copolymers. With two different polymer-producing substrates the copolymers formed contain units derived from each substrate often in direct proportion to the amounts in the medium. With such substrates or with non-producing substrates, or with non-growth substrates, the ability of P. oleovorans to utilize different types of individual organic compounds can be classified into three different categories, as follows: group A—the organic compound can support both growth and polymer production; or group B—the organic compound can support growth but not polymer production; or group C—the organic compounds cannot support growth. For organic compounds in groups B and C, new and unusual copolymers containing units derived from these substrates can often be obtained if that compound is cofed with a good polymer-producing substrate for P. oleovorans , such as either octanoic acid or nonanoic acid. The PHAs obtained by this type of cometabolism from a variety of such substrates are described.     

Cloning and molecular organization of the polyhydroxyalkanoic acid synthase gene (phaC) of Ralstonia eutropha strain B5786

Class I polyhydroxyalkanoic acid (PHA) synthase gene (phaC) of Ralstonia eutropha strain B5786 was cloned and characterized. R. eutropha B5786 features the ability to synthesize multicomponent PHAs with short- and medium-chain-length monomers from simple carbohydrate substrate. A correlation was made between the molecular structure of PHA synthase and substrate specificity and the ability of strain-producers to accumulate PHAs of this or that structure. A strong similarity of PHA synthase of R. eutropha strain B5786 with PHA synthase of R. eutropha strain H16, which, as opposed to strain B5786, enables to incorporate medium chain length PHAs if hexanoate is used as carbon source, exhibited 99%. A correlation between the structure of PHA synthase of B5786 strain with synthases of microorganisms which synthesize short and medium chain length PHAs similarly to B5786 strain, showed an identity level from 26 to 41% (homology with synthase of Rhodospirillum rubrum makes 41%, Ectothiorhodospira shaposhnikovii makes 26%, Aeromonas punctata makes 40%, Thiococcus pfennigii makes 28%, Rhodococcus ruber makes 38%, and with PhaCl and PhaC2 synthases of Pseudomonas sp. 61–3 makes 34 and 37%, respectively). This allows for speaking about the absence of a direct connection between the molecular organization of PHA synthases and their functional abilities, namely, the ability to synthesize PHAs of a particular composition.     

Production of medium chain length polyhydroxyalkanoates by fed-batch culture of Pseudomonas oleovorans

Pseudomonas oleovorans was cultivated to produce medium chain length polyhydroxyalkanoates (MCL-PHAs) from octanoic acid and ammonium nitrate as carbon and nitrogen source, respectively, by a pH-stat fed-batch culture technique. The octanoate in the culture broth was maintained below 4 g l^–1 by feeding the mixture of octanoic acid and ammonium nitrate when the culture pH rose above 7.1. The final cell concentrations of 63, 55 and 9.5 g l^–1, PHA contents of 62, 75 and 67% of dry cell wt, and productivities of 1, 0.63 and 0.16 g l^–1 h^–1 were obtained when the C/N ratios in the feed were 10, 20 and 100 g octanoic acid g^–1 ammonium nitrate, respectively.     

A novel nitrilase from Ralstonia eutropha H16 and its application to nicotinic acid production

A novel aliphatic nitrilase, REH16, was found in Ralstonia eutropha H16 and overexpressed in Escherichia coli BL21(DE3), and its enzymatic properties were studied. The temperature and pH optima were 37 °C and 6.6, respectively, and the best thermostability of the nitrilase was observed at 25 °C, which preserved 95% of activity after 120 h of incubation. REH16 has a broad hydrolytic activity toward aliphatic and heterocyclic nitriles and showed high tolerance of 3-cyanopyridine; this enzyme could hydrolyze as high as 100 mM 3-cyanopyridine completely. To improve the 3-cyanopyridine conversion efficiency in an aqueous reaction system, water-miscible organic solvents were tested, and ethanol (10% v/v) was chosen as the optimal co-solvent. Finally, under optimized conditions, using the fed-batch reaction mode, total of 1050 mM 3-cyanopyridine was hydrolyzed completely in 20.8 h with eight substrate feedings, yielding 129.2 g/L production of nicotinic acid and thus showing a potential for industrial application.

     

Optimization of cyanophycin production in recombinant strains of Pseudomonas putida and Ralstonia eutropha employing elementary mode analysis and statistical experimental design

Elementary mode analysis was applied to simulate conditions for cyanophycin (CGP) biosynthesis and to optimize its production in bacteria. The conclusions from these simulations were confirmed by experiments with recombinant strains of the wild types and polyhydroxyalkanoate (PHA)-negative mutants of Ralstonia eutropha and Pseudomonas putida expressing CGP synthetase genes (cphA) of Synechocystis sp. strain PCC6308 or Anabaena sp. strain PCC7120. In particular, the effects of suitable precursor substrates and of oxygen supply as well as of the capability to accumulate PHA in addition to CGP biosynthesis were investigated. Since CGP consists of the amino acids aspartate and arginine, the tricarboxylic acid cycle (TCC), which provides intermediates for biosynthesis of these amino acids, seems to be important. Excretion of intermediates of the TCC upon cultivation at restricted oxygen supply and conversion of fumarate mainly to malate and to only little succinate in the absence of oxygen indicated that TCC intermediates for arginine and aspartate biosynthesis were provided by the oxidative or reductive parts of the TCC, respectively. The following important conclusions were made from the experiments and the simulations: (i) external arginine additionally supplied to the medium, (ii) oxygen limitation, and (iii) absence of PHA accumulation exerted positive effects on CGP accumulation. These conclusions were utilized to obtain CGP contents in the cells of as high as 17.9% (w x w(-1)) during cultivation of the investigated bacteria at the 30-L scale using mineral salts medium. Such high CGP contents were previously not obtained with these bacteria at a 30-L scale, even if complex media were used.     

Continuous Production of Long-Side-Chain Poly-β-Hydroxyalkanoates by Pseudomonas oleovorans

Shake flask experiments showed that Pseudomonas oleovorans began to be growth inhibited at 4.65 g of sodium octanoate liter^-1, with total inhibition at 6 g liter^-1. In chemostat studies with 2 g of ammonium sulfate and 8 g of octanoate liter^-1 in the feed, the maximum specific growth rate was 0.51 h^-1, and the maximum specific rate of poly-β-hydroxyalkanoate (PHA) production was 0.074 g of PHA g of cellular protein^-1 h^-1 at a dilution rate (D) of 0.25 h^-1. When the specific growth rate (μ) was <0.3 h^-1, the PHA composition was relatively constant with a C₄/C₆/C₈/C₁₀ ratio of 0.1:1.7:20.7:1.0. At μ > 0.3 h^-1, a decrease in the percentage of C₈ with a concomitant increase in C₁₀ monomers as μ increased was probably due to the effects of higher concentrations of unmetabolized octanoate in the fermentor. At D = 0.24 h^-1 and an increasing carbon/nitrogen ratio, the percentage of PHA in the biomass was constant at 13% (wt/wt), indicating that nitrogen limitation did not affect PHA accumulation. Under carbon-limited conditions, the yield of biomass from substrate was 0.76 g of biomass g of octanoate^-1 consumed, the yield of PHA was 0.085 g of PHA g of octanoate^-1 used, and 7.9 g of octanoate was consumed for each gram of NH₄⁺ supplied. The maintenance coefficient was 0.046 g of octanoate g of biomass^-1 h^-1. Replacement of sodium octanoate with octanoic acid appeared to result in transport-limited growth due to the water insolubility of the acid.     

Enzymatic recovery and purification of polyhydroxybutyrate produced by Ralstonia eutropha

Polyhydroxybutyrate (PHB) is the most studied among a wide variety of polyhydroxyalkanoates, bacterial biodegradable polymers known as potential substitutes for conventional plastics. This work aimed at evaluating the use of enzymes to recover and purify the PHB produced by Ralstonia eutropha DSM545. Screening experiments allowed the selection of trypsin, bromelain and lysozyme among six enzymes, based on their efficiency in lysing cells of a non-PHB producing R. eutropha strain. Then, process conditions for high efficiency in PHB purification from the DSM545 cells were searched for the enzymes previously selected. The best result was achieved with 2.0% of bromelain (enzyme mass per biomass), equivalent to 14.1 U ml(-1), at 50 degrees C and pH 9.0, resulting in 88.8% PHB purity. Aiming at improving the process efficiency and reducing the enzyme cost, experiments were carried out with pancreatin, leading to 90.0% polymer purity and an enzyme cost three times lower than the one obtained with bromelain. The molecular mass analysis of PHB showed no polymer degradation. Therefore, this work demonstrates the potential of using enzymes in order to recover and purify PHB and bacterial biopolymers in general.