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Metabolic engineering of Aeromonas hydrophila for the enhanced production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate).

Wild-type Aeromonas hydrophila 4AK4 produced 35-45 wt.% poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (PHBHHx) consisting of 10-15 mol% 3-hydroxyhexanoate (3HHx). To enhance PHBHHx production, vgb gene encoding Vitreoscilla haemoglobin or fadD gene encoding Escherichia coli acyl-CoA synthase was co-expressed with polyhydroxyalkanoates (PHA) synthesis-related genes including phbAB from Wautersia eutropha and phaPCJ from A. hydrophila. Expression of vgb increased PHBHHx content from 46 to 53 wt.% without affecting the polymer monomers composition, whereas fadD increased both PHBHHx content from 46 to 64 wt.% and its 3HHx fraction from 15 to 24 mol%. Co-expression of vgb or fadD gene with PHA-synthesis-related genes generally increased PHBHHx content over 60 wt.%. Co-expression of phbAB with vgb increased PHBHHx content and concentration up to about 70 wt.% and 4.0 g l-1, respectively. Fermentor study also showed that in the recombinants harboring vgb, CDW, PHBHHx concentration and productivity were significantly elevated up to 54 g l-1, 28.5 g l-1 and 0.791 g l-1 h-1, respectively, suggesting that vgb could promote PHA synthesis. In this strain, lac promoter could be used to constitutively express foreign genes such as phbA and phbB encoding beta-ketothiolase and NADPH-dependent acetoacetyl-CoA reductase of W. eutropha, respectively, without use of IPTG. The results showed that combined expression of different genes was a successful strategy to enhance PHA production, which could be useful for strain development to construct other recombinant PHA-producing strains.

3-Hydroxybutyric Acid↗

Transcriptional analysis of Ralstonia eutropha genes related to poly-(R)-3-hydroxybutyrate homeostasis during batch fermentation.

Poly-(R)-3-hydroxybutyrate (PHB) homeostasis in Ralstonia eutropha takes place at the interface of the cytosol and the hydrophobic PHB granule. PHB synthesis and degradation are therefore intimately linked to the process of granule assembly and breakdown. Unraveling this time-dependent three-dimensional process requires an understanding of the kinetics of synthesis of relevant proteins. Reverse transcriptase quantitative PCR and quantitative Western blotting were carried out on batch cultures of R. eutropha H16 in order to gain insight into how expression of the PHB-related genes phaA, phaB, phaC, phaP, phaR, phaZ1a, phaZ1b, and phaZ1c changed during a cell growth phase, a PHB production phase, and a PHB utilization phase. phaA, phaB, phaC, phaR, and phaZ1a were transcribed throughout cell growth, PHB production, and PHB degradation. PHB-mediated induction of PhaP expression was shown to occur at the transcriptional level, with transcript levels increasing during PHB production and decreasing during PHB utilization. Levels of PhaP correlated strongly with levels of PHB. Levels of phaZ1b transcript and protein increased sharply during production and decreased during degradation, but transcript accumulation did not depend on PHB production as in the case of phaP. No evidence of phaZ1c expression was found under the experimental conditions used in this study.

Bacterial Proteins↗

The role of PHB metabolism in the symbiosis of rhizobia with legumes.

The carbon storage polymer poly-beta-hydroxybutyrate (PHB) is a potential biodegradable alternative to plastics, which plays a key role in the cellular metabolism of many bacterial species. Most species of rhizobia synthesize PHB but not all species accumulate it during symbiosis with legumes; the reason for this remains unclear, although it was recently shown that a metabolic mutant of a nonaccumulating species retains the capacity to store PHB in symbiosis. Although the precise roles of PHB metabolism in these bacteria during infection, nodulation, and nitrogen fixation are not determined, the elucidation of these roles will influence our understanding of the metabolic nature of the symbiotic relationship. This review explores the progress that was made in determining the biochemistry and genetics of PHB metabolism. This includes the elucidation of the PHB cycle, variations in PHB metabolism among rhizobial species, and the implications of these variations, while proposing a model for the role of PHB metabolism and storage in symbiosis.

Fabaceae↗

Production of polyhydroxyalkanoates from methanol by a new methylotrophic bacterium Methylobacterium sp. GW2.

A new bacterial strain, isolated from groundwater contaminated with explosives, was characterized as a pink-pigmented facultative methylotroph, affiliated to the genus Methylobacterium. The bacterial isolate designated as strain GW2 was found capable of producing the homopolymer poly-3-hydroxybutyrate (PHB) from various carbon sources such as methanol, ethanol, and succinate. Methanol acted as the best substrate for the production of PHB reaching 40 % w/w dry biomass. PHB accumulation was observed to be a growth-associated process, so that there was no need for two-step fermentation. Optimal growth occurred at 0.5 % (v/v) methanol concentration, and growth was strongly inhibited at alpha concentration above 2 % (v/v). Methylobacterium sp. strain GW2 was also able to accumulate the copolyester poly-3-hydroxybutyrate-poly-3-hydroxyvalerate (PHB/HV) when valeric acid was supplied as an auxiliary carbon source to methanol. After 66 h, a copolymer content of 30 % (w/w) was achieved with a PHB to PHV ratio of 1:2. Biopolymers produced by strain GW2 had an average molecular weight ranging from 229,350 to 233,050 Da for homopolymer PHB and from 362,430 to 411,300 Da for the copolymer PHB/HV.

Biopolymers↗

Optimizing conditions for poly(beta-hydroxybutyrate) production by Halomonas boliviensis LC1 in batch culture with sucrose as carbon source.

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

Culture Techniques↗

Versatile sugar and valerate metabolic pathways in Paraburkholderia xenovorans LB400 enable tailored poly(3-hydroxybutyrate-co-3-hydroxyvalerate) production.

Poly(3-hydroxybutyrate) and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) polymers are accumulated by diverse prokaryotes. Their distinct monomer compositions enable their use as tailored bioplastics. The aims were to characterize the poly(3-hydroxybutyrate) and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) synthesis by Paraburkholderia xenovorans LB400 using different sugars and valerate, and to gain genome-oriented insights into polyhydroxyalkanoate production. d-Glucose, d-mannitol, d-gluconate, and d-xylose were evaluated as sole carbon sources or supplemented with valerate. Polyhydroxyalkanoates synthesized by strain LB400 were characterized through GC-MS, GC-FID, FTIR, and 1H and 13C-NMR. P. xenovorans LB400 reached 1.00-1.39 g L-1 of dry cell weight (DCW) with a P(3HB) content of 21-43% w w-1 when grown on different sugars. The addition of valerate to the sugar-grown LB400 cultures yielded a DCW of 1.79 to 2.29 g L-1 and a P(3HB-co-3HV) content of 50.0‒51.2% w w-1, with varying 3HV compositions (28‒43 mol%). The highest 3HV incorporation was observed with d-xylose and valerate. Genomic analyses of strain LB400 revealed key elements of sugar metabolism influencing growth, polymer accumulation, and monomer composition. LB400 genome encodes the PhaJ-like R-specific hydratase and FadJ epimerase, which are potentially useful for modulating copolymer composition. PHA production under bioreactor conditions was evaluated. In a bioreactor fed with d-glucose, LB400 achieved a P(3HB) concentration of 2.2 g L-1. These findings highlight the metabolic versatility of P. xenovorans LB400 in utilizing diverse sugars to produce either P(3HB) or tailor-made P(3HB-co-3HV), supporting the development of bioplastics for specific applications. KEY POINTS: • Strain LB400 produced P(3HB-co-3HV) from various sugars and valerate. • Sugar type drives LB400 PHA copolymer synthesis and composition. • Strain LB400 PHA production was scaled up to a bioreactor.

Polyesters↗

Economic considerations in the production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) by bacterial fermentation.

The process for the production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB/V)] by bacterial fermentation and its recovery was analysed. The effects of various factors such as P(3HB/V) content, P(3HB/V) productivity, P(3HB/V) yield and 3-hydroxyvalerate (3HV) fraction in P(3HB/V) on the production cost of P(3HB/V) were examined. The increase in the 3HV yield on a carbon source did not significantly decrease the production cost when the 3HV fraction was 10 mol%, because the cost of the carbon substrate for 3HV was relatively small in terms of the total cost. However, at a 3HV fraction of 30 mol%, the 3HV yield on a carbon source had a significant effect on the total P(3HB/V) production cost. The production cost of P(3HB/V) increased linearly with the increase in the 3HV fraction in P(3HB/V).

Alcaligenes↗

Polymer production by two newly isolated extremely halophilic archaea: application of a novel corrosion-resistant bioreactor.

A novel corrosion-resistant bioreactor composed of polyetherether ketone (PEEK), tech glass and silicium nitrite ceramics was constructed and applied for the cultivation of two newly isolated, extremely halophilic archaea producing poly(gamma-glutamic acid) (PGA), or poly(beta-hydroxy butyric acid) (PHB), respectively. These bacteria were isolated from hypersaline soil close to Aswan (Egypt). The isolate strain 40, which is related to the genus Natrialba, produced large amounts of PGA when cultivated on solid medium. Culture conditions were optimised applying the corrosion-resistant bioreactor. PGA production was dependent on NaCl concentration and occurred about at 20% (w/v) NaCl in the medium. A maximum cell density of about 1.6 g cell dry matter/l was obtained when the bioreactor was stirred and aerated in a batch fermentation process using proteose-peptone medium. The supernatant was monitored with respect to PGA formation, and after 90 h a maximum of 470 mg/l culture volume was detected by HPLC analysis. Culture conditions were optimized for the isolate 56, which accumulated PHB as intracellular granules. Batch fermentations in the stirred and aerated bioreactor applying acetate and n-butyric acid as carbon sources led to cell density of 2.28 g cell dry matter/l and a maximum PHB accumulation contributing to about 53% of cellular dry weight. About 4.6 g PHB were isolated from 10.6 g dried cells of strain 56, which exhibited a weight average molar mass of 2.3 x 10(5) g mol(-1) and a polydispersity of about 1.4.

Archaea↗

Accumulation and mobilization of storage lipids by Rhodococcus opacus PD630 and Rhodococcus ruber NCIMB 40126.

The time course of the accumulation of triacylglycerols (TAGs) in Rhodococcus opacus PD630 or of TAGs plus polyhydroxyalkanoates (PHA) in Rhodococcus ruber NCIMB 40126 with gluconate or glucose as carbon source, respectively, was studied. In addition, we examined the mobilization of these storage compounds in the absence of a carbon source. R. opacus accumulated TAGs only after the exhaustion of ammonium in the medium, and, with a fixed concentration of the carbon source, the amounts of TAGs in the cells increased with decreasing concentrations of ammonium in the medium. When these cells were incubated in the absence of an additional carbon source, about 90% of these TAGs were mobilized and used as endogenous carbon source, particularly if ammonium was available. R. ruber accumulated a copolyester consisting of 3-hydroxybutyrate and 3-hydroxyvalerate already during the early exponential growth phase, whereas TAGs were synthesized and accumulated mainly during the late exponential and stationary growth phases. In the stationary growth phase, synthesis of TAGs continued, whereas PHA was partially mobilized. In the absence of an additional carbon source but in the presence of ammonium, mobilization of TAGs started first and was then paralleled by the mobilization of PHA, resulting in an approximately 90% and 80% decrease of these storage compounds, respectively. During the accumulation phase, interesting shifts in the composition of the two storage compounds occurred, indicating that the substrates of the PHA synthase and the TAG synthesizing enzymes were provided to varying extents, depending on whether the cells were in the early or late exponential or in the stationary growth phase.

Culture Media↗

A calorimetrically based method to convert toxic compounds into poly-3-hydroxybutyrate and to determine the efficiency and velocity of conversion.

A fed-batch method for converting toxic substrates into poly-3-hydroxybutyrate is presented. The method involves a series of batch-growth processes, regulated by adding small amounts of carbon substrate, during the course of which the concentration of the nitrogen source decreases and controls the distribution of the substrate-carbon assimilated. The addition of carbon substrate is controlled, and the small changes that occur in the growth pattern are interpreted using high-resolution reaction calorimetry. The method was tested with Ralstonia eutropha DSM 4058 growing on phenol, and Variovorax paradoxus DSM 4065 growing on sodium benzoate. The maximum carbon conversion efficiencies (CCEs) obtained, 23% and 27% respectively, were compared with the theoretically possible values.

Betaproteobacteria↗

Molecular mass of poly[(R)-3-hydroxybutyric acid] produced in a recombinant Escherichia coli.

Poly[(R)-3-hydroxybutyric acid] (PHB) was produced at 37 degrees C by a recombinant Escherichia coli harboring the Alcaligenes eutrophus biosynthesis phb-CAB genes in Luria-Bertani media containing glucose at 10-30 g/l at different pH values and the time-dependent changes in the molecular mass of PHB were studied. PHB polymers accumulated within cells while glucose was present in the medium. The number-average molecular mass of PHB decreased with time during the course of PHB accumulation, and the values for PHB were markedly dependent on the cultivation conditions of the E. coli, ranging from 0.5 MDa to 20 MDa. Under specific conditions (pH 6.0), E. coli produced PHB with an extremely high molecular mass (20 MDa). It has been suggested that a chain-transfer agent is generated in E. coli cells during the accumulation of PHB.

Acyltransferases↗

Trans activation of the Escherichia coli ato structural genes by a regulatory protein from Bacillus megaterium: potential use in polyhydroxyalkanoate production.

A Bacillus megaterium genomic fragment, which encoded an activator homologous to sigma 54 regulators and which was capable of activating Escherichia coli ato genes in trans, was detected in a gene library of B. megaterium screened for beta-ketothiolase activity. The fragment presented only one complete open reading frame (ORF1), which encoded a protein of 398 amino acids. The recombinant plasmid complemented mutations in the Escherichia coli atoC regulatory gene. The constitutive expression of the E. coli ato operon mediated by ORF1 could be useful for the synthesis of polyhydroxyalkanoates with different flexibility properties by recombinant E. coli strains.

Amino Acid Sequence↗

Poly-(3-hydroxybutyrate) production from whey by high-density cultivation of recombinant Escherichia coli.

Recombinant Escherichia coli strain GCSC 6576, harboring a high-copy-number plasmid containing the Ralstonia eutropha genes for polyhydroxyalkanoate (PHA) synthesis and the E. coli ftsZ gene, was employed to produce poly-(3-hydroxybutyrate) (PHB) from whey, pH-stat fed-batch fermentation, using whey powder as the nutrient feed, produced cellular dry weight and PHB concentrations of 109 g l-1 and 50 g l-1 respectively in 47 h. When concentrated whey solution containing 210 g l-1 lactose was used as the nutrient feed, cellular dry weight and PHB concentrations of 87 g l-1 and 69 g l-1 respectively could be obtained in 49 h by pH-stat fed-batch culture. The PHB content was as high as 80% of the cellular dry weight. These results suggest that cost-effective production of PHB is possible by fed-batch culture of recombinant E. coli using concentrated whey solution as a substrate.

Alcaligenes↗

Quantification of bacterial polyhydroxyalkanoic acids by Nile red staining.

The fluorescence properties of one chemically and seven biologically produced polyhydroxyalkanoic acid were investigated as film castings and in living cells respectively after staining with Nile red. All these polyesters show a similar fluorescence behaviour, revealing a clear fluorescence maximum at an excitation wavelength between 540 nm and 560 nm and an emission wavelength between 570 nm and 605 nm. This could be shown by the use of two-dimensional fluorescence spectroscopy and flow cytometry. The examination of native poly(3-hydroxybutyric acid), poly(3HB), granules isolated from cells of Ralstonia eutropha H16 showed that the addition of 6.0 micrograms Nile red is necessary for total staining of 1.0 mg granules. The fluorescence intensity at an excitation wavelength of 550 nm and an emission wavelength of 600 nm showed high correlation to the poly(3HB) concentration of grana suspensions at different grana concentrations. These results and the staining of cell suspensions during cultivation experiments revealed that Nile red has a high potential for the quantitative determination of hydrophobic bacterial polyhydroxyalkanoic acids.

Bacteriological Techniques↗

Exploitation of butyrate kinase and phosphotransbutyrylase from Clostridium acetobutylicum for the in vitro biosynthesis of poly(hydroxyalkanoic acid).

Active butyrate kinase (Buk) and phosphotransbutyrylase (Ptb) were purified in three steps: ammonium sulfate precipitation, hydrophobic chromatography on phenyl-Sepharose and affinity chromatography on Matrex Red A from recombinant Escherichia coli K2006 (pJC7). They were then successfully exploited for in vitro synthesis of 3-hydroxybutyryl-CoA (3HBCoA), 4-hydroxybutyryl-CoA (4HBCoA), 4-hydroxyvaleryl-CoA (4HVCoA) and poly(hydroxyalkanoic acid) (PHA). In addition, the ability of the PHA synthase of Chromatium vinosum, PhaEC(Cv), to use these CoA thioesters was evaluated. Combination of Buk and Ptb with PhaEC(Cv) established a new system for in vitro synthesis of poly(3-hydroxybutyric acid) [poly(3HB)]. In this system, 3-hydroxybutyric acid was converted to 3HBCoA by Buk and Ptb at the expense of ATP. Formation of 3HBCoA was further driven by the polymerization of 3HBCoA molecules to poly(3HB) by PHA synthase, and the released CoA was recycled by Ptb. This system therefore also ensured the regeneration of CoA. With ATP as the energy supply, which was hydrolyzed to ADP and phosphate, 2.6 mg poly(3HB) was obtained from a 1-ml reaction mixture containing 7.6 mg 3-hydroxybutyrate at the beginning. Studies showed that Ptb and PHA synthase were the rate-limiting steps in this system, and initial CoA concentrations ranging from 1 to 7 mM did not inhibit poly(3HB) synthesis. Synthesis of various polyesters of 3HB and 4HB with this system was also tested, and copolyesters containing 4HB of 1-46 mol % were obtained.

3-Hydroxybutyric Acid↗

Design of PCR primers and a gene probe for extensive detection of poly(3-hydroxybutyrate) (PHB)-degrading bacteria possessing fibronectin type III linker type-PHB depolymerases.

For rapid and sensitive detection of poly(3-hydroxybutyrate) (PHB)-degrading bacteria, a PCR primer set (PHB primers) and a gene probe (PHB probe) were designed, based on the homologous regions of six fibronectin type III linker domain-encoding sequences laid on a variety of PHB depolymerase genes listed in the GenBank. PCR using PHB primers amplified DNA fragments with the expected sizes from all the tested bacterial strains used for primer design; and all of the amplified fragments gave positive signals by Southern hybridization with the PHB probe. No amplified fragments were observed from negative controls. To evaluate the availability of the PHB primers and PHB probe, they were applied to 57 wild-type, PHB-degrading bacteria newly isolated from a variety of environments. The PHB primers amplified DNA fragments with expected sizes from 50 of the 57 wild-type strains, while the PHB probe showed positive signals against the amplified fragments from 47 strains. These results suggest that the primer and probe system established in this study can detect a considerable proportion of the potential PHB-degrading bacteria and can be applied to evaluate PHB-degradation potential in a natural environment, in combination with direct DNA extraction methods.

Bacteria↗

Integrated production of biodegradable plastic, sugar and ethanol.

Poly 3-hydroxybutyric acid (PHB) and related copolymers can be advantageously produced when integrated into a sugarcane mill. In this favorable scenario, the energy necessary for the production process is provided by biomass. Carbon dioxide emissions to the environment are photosynthetically assimilated by the sugarcane crop and wastes are recycled to the cane fields. The polymer can be produced at low cost considering the availability of a low-price carbon source and energy.

Biodegradation, Environmental↗

Industrial scale production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate).

Large scale production of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) [P(3HB-co-3HHx)] by Aeromonas hydrophila 4AK4 was examined in a 20,000 l fermentor. Cells were first grown using glucose as a carbon source, and polyhydroxyalkanoate (PHA) biosynthesis was triggered by the addition of lauric acid under conditions of limited nitrogen or phosphorus. When cells first grown in a medium containing 50 g glucose l(-1) were further cultivated after the addition of 50 g lauric acid l(-1) under phosphorus limitation, a final cell concentration, PHA concentration and PHA content of 50 g l(-1), 25 g l(-1), and 50 wt%, respectively, were obtained in 46 h, equivalent to PHA productivity of 0.54 g l(-1)t h(-1). The copolymer produced was found to be a random copolymer, and the 3HHx fraction was 11 mol%.

3-Hydroxybutyric Acid↗