Production of poly-3-hydroxybutyrate by Bacillus sp. JMa5 cultivated in molasses media

A strain of Bacillus sp. coded JMa5 was isolated from molasses contaminated soil. The strain was able to grow at a temperature as high as 45°C and in 250 g/l molasses although the optimal growth temperature was 35–37°C. Cell density reached 30 g/l 8 h after inoculation in a batch culture with an initial concentration of 210 g/l molasses. Under fed-batch conditions, the cells grew to a dry weight of 70 g/l after 30 h of fermentation. The strain accumulated 25–35%, (w/w) polyhydroxybutyrate (PHB) during fermentation. PHB accumulation was a growth-associated process. Factors that normally promote PHB production include high ratios of carbon to nitrogen, and carbon to phosphorus in growth media. Low dissolved oxygen supply resulted in sporulation, which reduced PHB contents and dry weights of the cells. It seems that sporulation induced by reduced supply of nutrients is the reason that PHB content is generally low in the Bacillus strain.     

Optimizing conditions for poly(β-hydroxybutyrate) production by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis> LC1 in batch culture with sucrose as carbon source

Halomonas boliviensis LC1 is able to accumulate poly(β-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.%.     

Poly(3-hydroxybutyrate) synthesis from glycerol by a recombinant Escherichia coli arcA mutant in fed-batch microaerobic cultures

Poly(3-hydroxybutyrate) (PHB) synthesis was analyzed under microaerobic conditions in a recombinant Escherichia coli arcA mutant using glycerol as the main carbon source. The effect of several additives was assessed in a semi-synthetic medium by the ‘one-factor-at-a-time’ technique. Casein amino acids (CAS) concentration was an important factor influencing both growth and PHB accumulation. Three factors exerting a statistically significant influence on PHB synthesis were selected by using a Plackett–Burman screening design [glycerol, CAS, and initial cell dry weight (CDW) concentrations] and then optimized through a Box–Wilson design. Under such optimized conditions (22.02 g l⁻¹ glycerol, 1.78 g l⁻¹ CAS, and 1.83 g l⁻¹ inoculum) microaerobic batch cultures gave rise to 8.37 g l⁻¹ CDW and 3.52 g l⁻¹ PHB in 48 h (PHB content of 42%) in a benchtop bioreactor. Further improvements in microaerobic PHB accumulation were obtained in fed-batch cultures, in which glycerol was added to maintain its concentration above 5 g l⁻¹. After 60 h, CDW and PHB concentration reached 21.17 and 10.81 g l⁻¹, respectively, which results in a PHB content of 51%. Microaerobic fed-batch cultures allowed a 2.57-fold increase in volumetric productivity when compared with batch cultures. Electronic supplementary material The online version of this article (doi:) contains supplementary material, which is available to authorized users. An erratum to this article can be found at     

Production of poly(3-hydroxybutyrate) by solid-state fermentation with <Emphasis Type="Italic">Ralstonia eutropha</Emphasis>

The use of solid-state fermentation is examined as a low-cost technology for the production of poly(hydroxyalkanoates) (PHAs) by Ralstonia eutropha. Two agroindustrial residues (babassu and soy cake) were evaluated as culture media. The maximum poly(hydroxybutyrate) (PHB) yield was 1.2 mg g^–1 medium on soy cake in 36 h, and 0.7 mg g^–1 medium on babassu cake in 84 h. Addition of 2.5% (w/w) sugar cane molasses to soy cake increased PHB production to 4.9 mg g^–1 medium in 60 h. Under these conditions, the PHB content of the dry biomass was 39% (w/w). The present results indicate that solid-state fermentation could be a promising alternative for producing biodegradable polymers at low cost.Revisions requested 31 August 2004; Revisions received 12 October 2004     

Production of 1,3-propanediol by <Emphasis Type="Italic">Clostridium butyricum</Emphasis> VPI 3266 using a synthetic medium and raw glycerol

Growth inhibition of Clostridium butyricum VPI 3266 by raw glycerol, obtained from the biodiesel production process, was evaluated. C. butyricum presents the same tolerance to raw and to commercial glycerol, when both are of similar grade, i.e. above 87% (w/v). A 39% increase of growth inhibition was observed in the presence of 100 g l^–1 of a lower grade raw glycerol (65% w/v). Furthermore, 1,3-propanediol production from two raw glycerol types (65% w/v and 92% w/v), without any prior purification, was observed in batch and continuous cultures, on a synthetic medium. No significant differences were found in C. butyricum fermentation patterns on raw and commercial glycerol as the sole carbon source. In every case, 1,3-propanediol yield was around 0.60 mol/mol glycerol consumed.     

Preparation and characterization of native poly(3-hydroxybutyrate) microspheres from Ralstonia eutropha

An efficient process for the preparation of poly(3-hydroxybutyrate) (PHB) microspheres with a narrow size distribution was developed. PHB was produced by a fed-batch culture of Ralstonia eutropha using fructose syrup as the sole carbon source. After autoclaving the bacteria, PHB granules, which accumulated in the cells, were isolated by a detergent/hypochlorite treatment and then spray-dried to obtain the microspheres. The diameters of the PHB microspheres ranged from 0.6 to 1.1 m and the weight-average molecular weights were approximately 50000 with polydispersity indexes of 5.0. The microspheres had a porous internal structure with an average porosity value of 72% and efficiently blocked UV light shorter than 220 nm. When isosorbide dinitrate was used as a model drug, the optimal drug loading concentration of the microspheres for controllable retardation was 3% (w/w). Almost 80% of the loaded drug (3%, w/w) was released within 12 h with typical sustained drug release behaviors.     

Sugarcane molasses and yeast powder used in the Fructooligosaccharides production by Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611

Different concentrations of sucrose (3–25% w/v) and peptone (2–5% w/v) were studied in the formulation of media during the cultivation of Aspergillus japonicus-FCL 119T and Aspergillus niger ATCC 20611. Moreover, cane molasses (3.5–17.5% w/v total sugar) and yeast powder (1.5–5% w/v) were used as alternative nutrients for both strains’ cultivation. These media were formulated for analysis of cellular growth, β-Fructosyltransferase and Fructooligosaccharides (FOS) production. Transfructosylating activity (U _t ) and FOS production were analyzed by HPLC. The highest enzyme production by both the strains was 3% (w/v) sucrose and 3% (w/v) peptone, or 3.5% (w/v) total sugars present in cane molasses and 1.5% (w/v) yeast powder. Cane molasses and yeast powder were as good as sucrose and peptone in the enzyme and FOS (around 60% w/w) production by studied strains.     

Effect of amino acid supplementation on the synthesis of poly(3-hydroxybutyrate) by recombinant pha Sa + Escherichia coli

The effect of different amino acid supplements to the basal medium on poly(3-hydroxybutyrate) (PHB) accumulation by recombinant pha _Sa ⁺ Escherichia coli (ATCC: PTA-1579) harbouring the poly(3-hydroxybutyrate)-synthesizing genes from Streptomyces aureofaciens NRRL 2209 was studied. With the exception of glycine and valine, all other amino acid supplements brought about enhancement of PHB accumulation. In particular, cysteine, isoleucine or methionine supplementation increased PHB accumulation by 60, 45 and 61% respectively by the recombinant E. coli as compared with PHB accumulation by this organism in the basal medium. The effect of co-ordinated addition of assorted combinations of these three amino acids on PHB accumulation was studied using a 2³ factorial design. The three-factor interaction analyses revealed that the effect of the three amino acids on PHB accumulation by the recombinant E. coli was in the order of cysteine > methionine > isoleucine. The defined medium supplemented with cysteine, methionine and isoleucine at the concentration of 150 mgl^–1 each and glycerol as the carbon source was the optimum medium that resulted in the accumulation of about 52% PHB of cell dry weight.     

Exposure of Fischerella [Mastigocladus] to high and low temperature extremes: strain evaluation for a thermal mitigation process

In conjunction with a proposed algal cultivation scheme utilizing thermal effluent, twelve Fischerella strains were tested for tolerance to temperatures above and below their growth range. Exposure to 65 °C or 70 °C for 30 min caused bleaching and death of most or all cells. Effects of 60 °C exposure for periods of up to 2 h ranged from undetectable to severe for the various strains. Chlorophyll a content typically decreased 21–22% immediately following 60 °C or 65 °C (1 h) exposure. However, the 60 °C-shocked cultures regained normal Chl a content after 24 h at 45 °C, whereas Chl a in 65 °C-shocked cultures immediately lost visible autofluorescence and was later degraded. Exposure to 15 °C virtually stopped growth of all strains during a 48 h exposure period. Most strains grew as rapidly as 45 °C controls when restored to 45 °C, while a few strains recovered more slowly. Comparison with dark-incubated controls indicated that photooxidative damage did not occur during cold shock. Certain strains exhibited relatively rapid recovery from both heat and cold exposure, thus meeting the temperature tolerance criteria for the proposed algal cultivation process.     

Optimization of cell growth and poly(3-hydroxybutyrate) accumulation on date syrup by a Bacillus megaterium strain

Optimal growth and PHB accumulation in Bacillus megaterium occurred with 5% (w/v) date syrup or beet molasses supplemented with NH₄Cl. When date syrup and beet molasses were used alone without an additional nitrogen source, a cell density of about 3gl^–1 with a PHB content of the cells of 50% (w/w) was achieved. NH₄NO₃ followed by ammonium acetate and then NH₄Cl supported cell growth up to 4.8gl^–1, whereas PHB accumulation was increased with NH₄Cl followed by ammonium acetate, NH₄NO₃ and then (NH₄)₂SO₄ to a PHB content of nearly 42% (w/w). Cultivation of B.megaterium at 30l scale gave a PHB content of 25% (w/w) of the cells and a cell density of 3.4gl^–1 after 14h growth.     

Phase partition of gaseous hexane and surface hydrophobicity of Fusarium solani when grown in liquid and solid media with hexanol and hexane

The filamentous fungus, Fusarium solani, was grown in liquid and solid culture with glucose, glycerol, 1-hexanol and n-hexane. The partition coefficient with gaseous hexane (HPC) in the biomass was lower when grown in liquid medium with 1-hexanol (0.4) than with glycerol (0.8) or glucose (1) The HPC for surface growth were 0.2 for 1-hexanol, 0.5 for glycerol, 0.6 for glucose, and 0.2 for F. solani biomass obtained from a biofilter fed with gaseous n-hexane. These values show a 200-fold increase in n-hexane solubility when compared to water (HPC = 42). Lower HPC values can be partially explained by increased lipid accumulation with 1-hexanol, 10.5% (w/w) than with glycerol (8.5% w/w) or glucose (7.1% w/w). The diameter of the hyphae diminished from 3 μm to 2 μm when F. solani was grown on solid media with gaseous n-hexane thereby doubling the surface area for gaseous substrate exchange. The surface hydrophobicity of the mycelia increased consistently with more hydrophobic substrates and the contact angle of a drop of water on the mycelial mat was 113° when grown on n-hexane as compared to 75° with glucose. The fungus thus adapts to hydrophobic conditions and these changes may explain the higher uptake of gaseous hydrophobic substances by fungi in biofilters.     

Continuous cultures of Clostridium acetobutylicum: culture stability and low-grade glycerol utilisation

Continuous cultures of two strains of Clostridium acetobutylicum were stable for over 70 d when grown on glucose/glycerol mixtures. Butanol was the major fermentation end-product, accounting for 43 to 62% (w/w) of total products. Low-grade glycerol [65% (w/v) purity] could replace commercial glycerol [87% (w/v) purity], leading to a similar fermentation pattern: a butanol yield of 0.34 (mol/mol), a butanol productivity of 0.42 g l^–1 h^–1 and a 84% (w/w) glycerol consumption were attained when cultures were grown at pH 6 and D = 0.05 h^–1; butanol accounted for 94% (w/w) of total solvents. These values are among the highest reported in literature for C. acetobutylicum simple chemostats.     

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     

Effects of inoculum concentration,temperature, and carbon sources on tannase production during solid state fermentation of cashew apple bagasse

In this study, the optimization of tannase production by solid state fermentation was investigated using cashew apple bagasse (CAB), an inexpensive residue produced by the cashew apple agroindustry, as a substrate. To accomplish this, CAB was enriched with 2.5% (w/w) tannic acid and 2.5% (w/w) ammonium sulphate and then moistened with water (60 mL/100 g of dry CAB). The influence of inoculum concentration (10⁴ to 10⁷ spores/g), temperature (20, 25, 30, and 35°C) and several additional carbon sources (glucose, starch, sucrose, maltose, analytical grade glycerol, and glycerol produced during biodiesel production) on enzyme production by Aspergillus oryzae was then evaluated. Supplementation with maltose and glycerol inhibited tannase synthesis, which resulted in lower enzyme activity. Starch and sucrose supplementation increased enzyme production, but decreased the enzyme productivity. The maximum tannase activity (4.63 units/g of dry substrate) was obtained at 30°C, using 10⁷ spores/g and 1.0% (w/v) sucrose as an additional carbon source.     

A fundamental dual regulatory role of citrate on the biosyntheses of thuringiensin and poly-<Emphasis Type="Italic">β</Emphasis>-hydroxybutyrate in <Emphasis Type="Italic">Bacillus thuringiensis</Emphasis> YBT-032

The production of α-ketoglutarate, adenine, thuringiensin production rate and thuringiensin yield on glucose consumed increased by 22%, 36%, 40% and 40%, respectively, in presence of 2 g citrate/l. However, citrate decreased pyruvate production, poly-β-hydroxybutyrate (PHB) production rate and PHB yield by 62%, 31% and 45%, respectively. The activities of pyruvate kinase and glucose-6-phosphate dehydrogenase were 36%–45% lower and 50%–120% higher than those of the control, respectively. The results suggest that citrate regulated the carbon flux to synthesis of adenine present in thuringiensin with a higher efficiency of utilization of glucose by decreasing PHB synthesis.     

Glycerol production in relation to the ATP pool and heat production rate of the yeasts Debaryomyces hansenii and Saccharomyces cerevisiae during salt stress

Changes in glycerol production and two parameters related to energy metabolism i. e. the heat production rate and the ATP pool, were assayed during growth of Saccharomyces cerevisiae and Debaryomyces hansenii in 4 mM and 1.35 M NaCl media. For both of the yeasts, the specific ATP pool changed during the growth cycle and reached maximum values around 10 nmol per mg dry weight in both types of media. The levels of glycerol were markedly enhanced by high salinity. In the presence of 1.35 M NaCl, D. hansenii retained most of its glycerol produced intracellularly, while S. cerevisiae extruded most of the glycerol to the environment. The intracellular glycerol level of S. cerevisiae equalled or exceeded that of D. hansenii, however, with values never lower than 3 mol per mg dry weight at all phases of growth. When D. hansenii was grown at this high salinity the intracellular level of glycerol was found to correlate with the specific heat production rate. No such correlation was found for S. cerevisiae. We concluded that during salt stress, D. hansenii possesses the capacity to regulate the metabolism of glycerol to optimize growth, while S. cerevisiae may not be able to regulate when exposed to different demands on the glycerol metabolism.     

Functional role of granule-associated genes, phaP and phaR, in poly-β-hydroxybutyrate biosynthesis in recombinant E. coli harboring phbCAB operon

The expression characteristic of two granule-associated genes, phaP and phaR, in a recombinant E. coli harboring the phbCAB operon was investigated. Polybetamydroxybutyrate (PHB) accumulation increased up from 16% to 57% (w/w) after transformation of the granule-associated genes due to the stabilization of PHB granules rather than by a direct effect on PHB biosynthetic enzymes. The morphology of PHB granules also varied depending on the transformed phaP and phaR genes.     

Glycerol as substrate for biomass and β-carotene production byRhodotorula lactosa

Glycerol was used as the sole carbon and energy source for growingRhodotorula lactosa. The maximum biomass yield (0.53 g/g substrate) was obtained after 20 h with 21.5 g glycerol/l; growth was inhibited with 28.0 g glycerol/l and cell morphology was changed. At this time, the cells were not pigmented. After 48 h of cultivation, -carotene was at 1.8 mg/g dry cells, yielding 22.0 mg/l. When cells were grown for 20 h, washed, suspended in distilled water and aerated for 24 hours, more -carotene (2.66 mg/g dry cells or 28.0 mg/l of the original culture) was produced. Cell protein content after 48 h was 36 to 38% (w/w) before extraction and 45 to 47% (w/w) for acetone-extracted cells.     

Repeated Batch Cultivation of Ralstonia eutropha for Poly (β-hydroxybutyrate) Production

Batch cultivation of Ralstonia eutropha NRRL B14690 attained 21 g biomass l⁻¹ and 9.4 g poly(β-hydroxybutyrate) l⁻¹ (0.45 g PHB g⁻¹ dry wt⁻¹) in 60 h. Repeated batch operation (empty-and-fill protocol) to remove 20% (v/v) of the culture broth and to supplement an equal volume of fresh media resulted in 49 g biomass l⁻¹ and 25 g PHB l⁻¹ (0.51 g PHB g⁻¹ dry wt⁻¹) with an overall productivity of 0.42 g PHB l⁻¹ h⁻¹ in 67 h. In the two cycles of repeated batch fermentation there was a 3-fold increase in productivity as compared to batch.     

Effect of simple and complex carbon sources,low temperature culture and complex carbon feeding policies on poly-3-hydroxybutyric acid (PHB) content and molecular weight (Mw) from Azotobacter chroococcum 6B

The molecular weight (M _w) of poly-3-hydroxybutyrate (PHB), produced by shake-flask culture of Azotobacter chroococcum showed little variation with increasing glucose concentration as carbon source (being in the range of 400–500 kDa), while M _w increased from 300–400 to 640 kDa when grown with increasing concentration of sugar cane molasses. Molecular weight increased nearly 30% from 48 to 72 h culture time when 5% molasses as carbon source was used, while with glucose the highest M _w was reached at 48 h. Under fermentor cultivation A. chroococcum produced PHB with a relatively high M _w of 1590 kDa at 53 h culture time when grown in modified Burk's medium with glucose as carbon source at an initial C/N ratio (molar basis) of 69 under fermentor cultivation. A batch glucose-grown ammonium-limited fermentor culture was repeatedly fed with sugar cane molasses (initial C/N ratio 69) and it was observed that PHB content curve decreased at a slower rate than in the fed-batch culture in which glucose and sucrose were not consumed in the culture medium after the feed.