Mass production of poly-β-hydroxybutyric acid by fully automatic fed-batch culture of methylotroph

Summary Fifty-one methylotrophs were checked with respect to their ability of poly--hydroxybutyric acid (PHB) production from methanol. One of them, Pseudomonas sp. K, was chosen from its good growth on a minimum synthetic medium. Optimal temperature and pH for its growth were 30° C and 7.0, respectively. Concentrations of PO ₄ ^3- and NH ₄ ⁺ in the medium should be kept at low levels. PHB formation was stimulated by deficiency of nutrient such as NH ₄ ⁺ , SO ₄ ^2- , Mg²⁺, Fe²⁺ or Mn²⁺. Among them, nitrogen deficiency was chosen from its effectiveness and easiness for PHB accumulation.The microorganism was cultivated to produce a large amount of poly--hydroxybutyric acid (PHB) from methanol by means of microcomputer-aided fully automatic fed-batch culture technique. During the cultivation, temperature, dissolved oxygen concentration (DO), and methanol concentration in the culture broth were maintained at 30° C 2.5±0.5 ppm and 0.5±0.2 g/l, respectively. Other nutrients, nitrogen source and mineral ions, were also controlled to maintain their initial concentrations in the medium during cell growth phase. When the high cell concentration was achieved (160 g/l), feedings of ammonia and minerals were stopped and only methanol was supplied successively to accumulate PHB. At 175 h, high concentration of PHB (136 g/l) was obtained and total cell concentration became 206 g/l. DO must be maintained above the critical level during the PHB formation phase, too. PHB yield from methanol (g PHB/g methanol) was 0.18 and the maximum PHB content reached 66% of dry weight. Solid PHB produced by the strain had the melting point of 176° C and the average molecular weight of 3.0x10⁵.     

Optimization of poly(β-hydroxybutyric acid) recovery from Alcaligenes latus: combined mechanical and chemical treatments

Recovery of the intracellular bioplastic poly(β-hydroxybutyric acid) or PHB from fed-batch cultured Alcaligenes latus, ATCC 29713, was examined using combinations of chemical and mechanical treatments to disrupt the cells. Chemical pretreatments used sodium chloride and sodium hydroxide. For salt pretreatment the cells were exposed to NaCl (8?kg?m^?3) and heat (60?°C, 1 h), cooled to 4?°C, and mechanically disrupted. For alkaline treatments, the cells were exposed to sodium hydroxide (0.025–0.8 kg?NaOH per kg biomass) and mechanically disrupted at ambient temperature. A combined treatment with sodium chloride (8 kg m^?3), heat (60?°C, 1 h), and alkaline pH shock (pH 11.5, 1?min) was also tested. Mechanical disruption employed a continuous flow bead mill (2,800 rpm agitation speed, 90?ml?min^?1 slurry flow rate, 512 m mean bead diameter, bead loadings of 80% or 85% of chamber volume). Disruption was quantified by protein release. Over most of the disruption period, the release of PHB was approximately proportional to protein release. Regardless of the pretreatment or bead load, the disruption obeyed first order kinetics; hence, the rate of protein release was directly proportional to the amount of unreleased protein. Relative to untreated biomass, pretreatment always produced earlier protein release during milling. Pretreatment with a minimum of 0.12?kg NaOH per kg biomass was necessary to enable complete disruption within three passes (85% bead load). Untreated biomass required more than twice as many passes. Irrespective of the chemical pretreatment, the bead loading strongly influenced the disruption rate which was higher at the higher loading. Alkaline hydrolysis associated PHB loss was observed, but it could be limited to insignificant levels by immediate neutralization of disrupted homogenates.     

Kinetics and effect of nitrogen source feeding on production of poly-β-hydroxybutyric acid by fed-batch culture

Summary A kinetic study of the production of poly--hydroxybutyric acid (PHB) by a fed-batch culture of Protomonas extorquens showed that a nitrogen source was necessary even in the PHB production phase. The effect of ammonia feeding on PHB production was consequently investigated. The nitrogen source (ammonia water) was supplied at a low constant feeding rate after the growth phase in which cell mass concentration reached 60 g/l. Feeding with a small quantity of ammonia resulted in a more rapid increase in intracellular PHB content than was the case without ammonia feeding. Excessive feeding of ammonia, however, caused not only degradation of accumulated PHB but also reduction of microbial PHB synthetic activity.     

Mass production of poly-β-hydroxybutyric acid by fed-batch culture with controlled carbon/nitrogen feeding

Summary The effect of the ratio of methanol to ammonia, in the feeding solution the C/N ratio, on microbial PHB production was investigated. A constant C/N ratio regulated both the PHB content and the specific rate of PHB production. The results indicated that to produce the maximum PHB effectively in a short time the C/N ratio should be controlled automatically according to the increase in PHB content. Variation of the PHB content was estimated by tracing the timecourse of CO₂ concentration in exhaust gas. When the cell concentration reached 70 g/l, C/N ratio was gradually increased from the initial C/N ratio of 10 (mol methanol/mol ammonia). At 121 h, concentration of PHB reached 136 g/l, which was the maximum level so far obtained. The reaction time was considerably shortened compared with our previous study (175 h). Furthermore, PHB concentration reached 149 g/l at 170 h and total cell concentration became 233 g/l. PHB yield from methanol was 0.20 (g PHB/g methanol), which was also superior to the previous result of 0.18.     

High frequency transformation of Alcaligenes eutrophus producing poly-β-hydroxybutyric acid by electroporation

Summary A strain of Alcaligenes eutrophus producing poly--hydroxybutyric acid was successfully transformed by the electroporation. The plasmid used was a broad host range plasmid pKT230 conferring kanamycin resistance. The optimum yield of transformant was 0.8×10²/g DNA when 50 l competent cells at 10¹⁰/ml were pulsed by 11.5 kV/cm for 5 ms with 1 g DNA. Plasmid DNA in the A. eutrophus transformant was stably maintained as a monomeric structure.     

Poly(β-L-malic acid) production by diverse phylogenetic clades of Aureobasidium pullulans

Poly(β-L-malic acid) (PMA) is a natural biopolyester that has pharmaceutical applications and other potential uses. In this study, we examined PMA production by 56 strains of the fungus Aureobasidium pullulans representing genetically diverse phylogenetic clades. Thirty-six strains were isolated from various locations in Iceland and Thailand. All strains from Iceland belonged to a newly recognized clade 13, while strains from Thailand were distributed among 8 other clades, including a novel clade 14. Thirty of these isolates, along with 26 previously described strains, were examined for PMA production in medium containing 5% glucose. Most strains produced at least 4 g PMA/L, and several strains in clades 9, 11, and 13 made 9–11 g PMA/L. Strains also produced both pullulan and heavy oil, but PMA isolated by differential precipitation in ethanol exhibited up to 72% purity with no more than 12% contamination by pullulan. The molecular weight of PMA from A. pullulans ranged from 5.1 to 7.9 kDa. Results indicate that certain genetic groups of A. pullulans are promising for the production of PMA.     

Optimized production of L-β-hydroxybutyric acid by a mutant of Yarrowia lipolytica

A mutant strain of Yarrowia lipolytica was developed which produced 8.0 g l--hydroxybutyric acid l^–1 from butyric acid in a batch culture. The optimum culture conditions in the fermenter for maintenance of a high cell activity, determined by chemostat analyses, were a specific growth rate of 0.06 h^–1, a glucose concentration of 2.0 g l^–1, and a butyric acid concentration of 8.1 g l^–1. A fed-batch fermentation was performed under these conditions resulting in an l--hydroxybutyric acid yield of 31 g l^–1.     

Production of poly-β-hydroxybutyric acid from carbon dioxide by Alcaligenes eutrophus ATCC 17697T

The characteristics of PHB production from carbon dioxide by autotrophic culture of Alcaligenes eutrophus ATCC 17697^T using a recycled gas closed circuit culture system under the condition of oxygen limitation were investigated. Cell concentration increased to more than 60 g/l after 60 h of cultivation, while the PHB concentration reached 36 g/l. PHB accumulation in the oxygen-limited culture was superior than that in an ammonium-deficient culture. The PHB produced was identified as a homopolymer of d-3-hydroxybutyrate by ¹H and ¹³C NMR analysis. The stoichiometry for PHB production from CO₂ under the oxygen limitation condition was indicated to be as follows: 33H₂ + 12O₂ + 4CO₂ → C₄H₆O₂ + 30H₂O. This stoichiometry shows that the hydrogen consumption per one mole of CO₂ for PHB production is larger than that for cell formation.     

Dynamics and modeling on fermentative production of poly (β-hydroxybutyric acid) from sugars via lactate by a mixed culture of Lactobacillus delbrueckii and Alcaligenes eutrophus

The mixed culture system was considered in the present research where sugars such as glucose were converted to lactate by Lactobacillus delbrueckii and the lactate was converted to poly β-hydroxybutyrate (PHB) by Alcaligenes eutrophus in one fermentor. For the modeling of the effect of NH₃ concentration on the cell growth of A. eutrophus and PHB production rates, metabolic flux distributions were computed at two culture phases of cell growth and PHB production periods. It was found that the NADPH, generated through isocitrate dehydrogenate in TCA cycle, was predominantly utilized for the reaction from α-ketoglutalate to glutamate when NH₃ was abundant, while it tended to be utilized for the PHB production through acetoacetyl CoA reductase as NH₃ concentration decreased. This phenomenon was reflected in the development of mathematical model. In the mixed culture experiments, the two phases were observed, namely the lactate production phase due to L. delbrueckii and the lactate consumption phase due to A. eutrophus. The lactate concentration could be estimated on-line by the amount of NaOH solution and HCl solution supplied to keep the culture pH at constant level. Several mixed culture experiments were conducted to see the dynamics of the system. Finally, a mathematical model which can describe the dynamic behavior of the present mixed culture was developed and the model parameters were tuned for fitting the experimental data. The model may be used for several purposes such as control, optimization, and understanding process dynamics etc.     

Expression of the Alcaligenes eutrophus poly(β-hydroxybutyric acid)-synthetic pathway in Pseudomonas sp.

The 12.5-kb EcoRI restriction fragment PP1 of Alcaligenes eutrophus strain H16, which encodes for -ketothiolase, NADP-dependent acetoacetyl-CoA reductase and poly(-hydroxybutyric acid)-synthase was mobilized to six different species of the genus Pseudomonas belonging to the rRNA homology group I. Pseudomonas aeruginosa, P. fluorescens, P. putida, P. oleovorans, P. stutzeri and P. syringae, which are unable to synthesize and accumulate poly(-hydroxybutyric acid), PHB, were employed as recipients. Whereas the A. eutrophus PHB-synthetic enzymes were only marginally expressed in P. stutzeri, they were readily expressed in the other species. For example, the specific activity of PHB-synthase was 1.8 U/g protein in transconjugants of P. stutzeri but was between 21 and 77 U/mg protein in transconjugants of the other species. All recombinant strains harboring plasmid pVK101::PP1 except those of P. stutzeri accumulated PHB; the PHB content of the cells grown on gluconate under nitrogen limitation varied between 8 and 24.3% of the cellular dry mass.Abbreviations PHB poly(-hydroxybutyric acid) - PHA poly(hydroxyalkanoic acid)     

Fermentative production of poly-β-hydroxybutyric acid from xylose by a two-stage culture method employing Lactococcus lactis IO-1 and Alcaligenes eutrophus

Summary A two-stage culture method employing Lactococcus.lactis IO-1 and Alcaligenes eutrophus was developed for production of poly--hydroxybutyric acid (PHB) from xylose. In this method, xylose was converted to L-lactic acid and acetic acid by L.lactis IO-1, and then the organic acids were converted to PHB by A.eutrophus. When the supernatant of the IO-1 culture broth, containing 10 g·dm^-3 L-lactate derived from xylose, was used as medium for A. eutrophus, the concentration of cells increased to 8.5 g·dm^-3 in 24 h and 55% of the content in the cells by weight was PHB.     

Manipulation of the genes for poly-β-hydroxybutyric acid synthesis in Alcaligenes eutrophus

Summary In order to establish the molecular breeding system in Alcaligenes eutrophus producing poly--hydroxybutyric acid (PHB), phbCAB genes from A. eutrophus were recombined into the E. coli-A. eutrophus shuttle vector and directly transferred into A. eutrophus by the electroporation. In A. eutrophus transformants, recombinant plasmids were stably maintained and enzyme activities for PHB biosyntheses were elevated 1.4–2.7 fold by the cloned genes.     

Production of poly(β-hydroxybutyric acid) and exopolysaccharide by Azotobacter beijerinckii WDN-01

The physico-chemical factors influencing the production of poly(-hydroxybutyric acid) [PHB] and exopolysaccharide (EPS) by a yellow pigmented Azotobacter beijerinckii strain WDN-01 were investigated. Under N-free condition with excess carbon, PHB accumulation attained its maximum at the late exponential phase followed by a sharp decline while EPS production was more or less parallel with growth. Polymer synthesis, however, was carbon-source-specific, the highest yield of PHB (2.73 g/l) and EPS (1.5 g/l) was obtained with 3% (w/v) glucose and mannitol respectively. Organic N-sources enhanced PHB production significantly, but inorganic nitrogenous compounds were inhibitory to both PHB and EPS synthesis. At optimum K₂HPO₄ concentration, the polymer yield was attributed to biomass yield. Oxygen-limiting conditions, irrespective of carbon sources favoured production of PHB and EPS.     

Formal kinetics of poly-β-hydroxybutyric acid (PHB) production in Alcaligenes eutrophus H 16 and Mycoplana rubra R 14 with respect to the dissolved oxygen tension in ammonium-limited batch cultures

Summary Under chemolithoautotrophic growth conditions with the organism Alcaligenes eutrophus H16 the exponential growth phase is characterized by two different growth rates, each associated with different specific rates of ammonium consumption. On the basis of the analytical determination of Poly--hydroxybutyric acid (PHB), it can be conclusively shown that PHB is synthesized even during the exponential growth phase at a specific rate proportional to the specific growth rates of total biomass. After complete consumption of ammonium, the increase of biomass is exclusively due to PHB synthesis, whereas protein and rest biomass (cell dry weight minus PHB) remain constant. After an extended period of fermentation, the PHB content reaches a saturation value. The transient phase between the growth and the storage phase is very short in comparison to the duration of the whole fermentation. In the case of Alcaligenes eutrophus, strain H 16, high concentrations of dissolved oxygen strongly influence growth as well as PHB synthesis.Abbrevations ^cO₂,L concentration of oxygen in the liquid phase (dissolved oxygen tension: d.o.t) - ^cH₂,L concentration of hydrogen in the liquid phase - ^cCO₂,L concentration of carbon dioxide in the liquid phase - S limiting substrate, concentration of - X total biomass, concentration of; total cell dry weight - P product; PHB, concentration of - R rest biomass: X-P, concentration of - ^rX dX/dt growth rate - ^rP dP/dt rate of PHB synthesis - ^rR dR/dt rate of rest biomass production - ^r0 ^dcO₂,L/dt rate of oxygen consumption - X dX/dt·1/X=r_X·1/X specific growth rate - P dP/dt·1/P=r_P·1/P specific rate of product formation - R dR/dt·1/R=r_R·1/R specific rate of rest biomass formation - r₀/R specific respiration rate     

Excretion of pyruvate by mutants of Alcaligenes eutrophus,which are impaired in the accumulation of poly(β-hydroxybutyric acid) (PHB), under conditions permitting synthesis of PHB

Summary Mutants of Alcaligenes eutrophus, which are defective in the intracellular accumulation of poly(-hydroxybutyric acid), PHB, were cultivated in the presence of excess carbon source after growth had ceased due to depletion of ammonium, sulphate, phosphate, potassium, magnesium, or iron. Under these conditions all mutants excreted large amounts of pyruvate into the medium. Excretion of pyruvate occurred with lactate, gluconate or fructose as carbon sources; the highest rate of pyruvate excretion (8 mmol/1 per hour) was obtained with lactate. The rate of pyruvate excretion by strain N9A-PHB^-02-HB^-1 on gluconate amounted to 2.5–6.3 mmol/g protein per hour depending on the depleted nutrient. The ratios of the molar rates for the utilization of the substrates versus those for the excretion of pyruvate were 1.9, 1.0 or 0.7, respectively. Wild-type strains did not excrete even traces of pyruvate, but accumulated PHB. Depending on the limiting nutrient, strain N9A accumulated PHB at a rate of 0.21–0.49 g/g protein per hour. On a molar basis (-hydroxybutyrate monomers versus pyruvate) the ratios for the rates for accumulation of PHB in the wild-type and for excretion of pyruvate in PHB-negative mutants were 0.9–1.4. The fermentation enzymes alcohol dehydrogenase and lactate dehydrogenase were not synthesized in cells starved of a nutrient; they were only detectable in cells cultivated under conditions of restricted oxygen supply. The latter conditions caused accumulation of PHB in the wild-type and excretion of pyruvate by the PHB-negative mutant.     

Effect of levulinic acid on cell growth and poly-β-hydroxyalkanoate production by Alcaligenes sp. SH-69

Summary Following growth of Alcaligenes sp. SH-69 on glucose as a sole carbon source for the production of poly--hydroxyalkanoates (PHAs), relatively low levels of levulinic acid (LA) were detected. Experiments were carried out in batch and continuous culture, and the effects of LA addition on growth and PHA synthesis were determined. Significant stimulatory effects were observed, greater than those for propionic acid addition. In N-limited two stage continuous culture, a maximal PHA content of 38.3 % (w/w) was achieved with a polyhydroxyvalerate (PHV) content of 23.5 % (molar basis) at D=0.078 l/h. This resulted from the controlled addition of LA at 0.5 g/L/h in the presence of excess glucose.     

Poly(β-hydroxybutyrate) production in oilseed leukoplasts of Brassica napus

Polyhydroxyalkanoates (PHAs) comprise a class of biodegradable polymers which offer an environmentally sustainable alternative to petroleum-based plastics. Production of PHAs in plants is attractive since current fermentation technology is prohibitively expensive. The PHA homopolymer poly(β-hydroxybutyrate) (PHB) has previously been produced in leaves of Arabidopsis thaliana (Nawrath et al., 1994, Proc Natl Acad Sci USA 91: 12760–12764). However, Brassica napus oilseed may provide a better system for PHB production because acetyl-CoA, the substrate required in the first step of PHB biosynthesis, is prevalent during fatty acid biosynthesis. Three enzymatic activities are needed to synthesize PHB: a β-ketothiolase, an acetoacetyl-CoA reductase and a PHB synthase. Genes from the bacterium Ralstonia eutropha encoding these enzymes were independently engineered behind the seed-specific Lesquerella fendleri oleate 12-hydroxylase promoter in a modular fashion. The gene cassettes were sequentially transferred into a single, multi-gene vector which was used to transform B. napus. Poly(β-hydroxybutyrate) accumulated in leukoplasts to levels as high as 7.7% fresh seed weight of mature seeds. Electron-microscopy analyses indicated that leukoplasts from these plants were distorted, yet intact, and appeared to expand in response to polymer accumulation. Received: 26 May 1999 / Accepted: 16 June 1999     

Effect of propionic acid on poly (β-hydroxybutyric-co-β-hydroxyvaleric) acid production byAlcaligenes eutrophus

Summary The effect of propionic acid on poly(-hydroxybutyric-co--hydroxyvaleric)acid P(HB-co-HV) copolymer production byAlcaligenes eutrophus ATCC 17699 supplied with fructose and propionic acid under nitrogen limited conditions was studied. The growth ofA. eutrophus was almost completely inhibited when the concentraion, of propionic acid exceeds 1.5 g/L. Specific production rate of HV unit was highest when propionic acid concentration was 0.5 g/L. In batch culture, pH change occurs in proportion to the consumption of propionic acid. Optimal concentration of propionic acid was maintained during the production phase by using a pH-stat feeding method and a total polymer content higher than 70% and the relative HV content upto 50% could be achieved.     

Continuous production of D-β-hydroxyisobutyric acid from methacrylic acid by Candida rugosa

Summary Continuous production of D- -hydroxyisobutyric acid (D-HIBA) from methacrylic acid (MA) using Candida rugosa IFO 0750 was most efficient under ammonium-limited conditions, whereas D-HIBA was not detected under glucose-limited conditions. As high as 21.5 g D-HIBA/l with 55% molar conversion yield from MA was obtained at a dilution rate of 0.04 h^-1.