Production of carotenoids by β-ionone-resistant mutant of <Emphasis Type="Italic">Xanthophyllomyces dendrorhous</Emphasis> using various carbon sources

Batch culture kinetics of the red yeast, Xanthophyllomyces dendrorhous SKKU 0107, revealed reduction in biomass with glucose and lower intracellular carotenoid content with fructose. Figures were different when compared to sucrose, which is a disaccharide of glucose and fructose. In contrast, specific growth rate constant stayed between 0.094~0.098 h⁻¹, irrespective of the carbon sources employed. Although the uptake rate of glucose was found to be 2.9-fold faster than that of fructose, sucrose was found to be a more suitable carbon source for the production of carotenoids by the studied strain. When sugar cane molasses was used, both the specific growth rate constant and the intracellular carotenoid content decreased by 27 and 17%, respectively. Compared with the batch culture using 28 g/L sugar cane molasses, fed-batch culture with the same strain resulted in a 1.45-fold higher cell yield together with a similar level of carotenoid content in X. dendrorhous SKKU 0107.     

Poly(3-hydroxybutyrate) production by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis> in fed-batch culture

High poly(3-hydroxybutyrate) (PHB) content and volumetric productivity were achieved by fed-batch culture of Halomonas boliviensis using a defined medium. Initial shake flask cultivations in a minimal medium revealed that the growth of H. boliviensis was supported only when the medium was supplemented with aspartic acid, glycine, or glutamine. Addition of 0.1% (w/v) glutamine in the medium resulted in the highest cell dry weight (CDW; 3.9 g l⁻¹). Glutamine was replaced by the less expensive monosodium glutamate (MSG) in the medium without any notable change in the final cell density. Effect of initial concentrations of NH₄Cl and K₂HPO₄ on cell growth and PHB accumulation by H. boliviensis was then analyzed using a fed-batch fermentation system. The best conditions for PHB production by H. boliviensis were attained using 0.4% (w/v) NH₄Cl and 0.22% (w/v) K₂HPO₄ and adding MSG intermittently to the fermentor. Poly(3-hydroxybutyrate) content and CDW reached 90 wt.% and 23 g l⁻¹, respectively, after 18 h of cultivation. In order to increase CDW and PHB content, MSG, NH₄Cl, and K₂HPO₄ were initially fed to the fermentor to maintain their concentrations at 2%, 0.4%, and 0.22% (w/v), respectively, and subsequently their feed was suppressed. This resulted in a CDW of 44 g l⁻¹, PHB content of 81 wt.%, and PHB volumetric productivity of 1.1 g l⁻¹ h⁻¹.     

Production of PHB by a Bacillus megaterium strain using sugarcane molasses and corn steep liquor as sole carbon and nitrogen sources

Poly(hydroxybutyric acid) (PHB) and other biodegradable polyesters are promising candidates for the development of environment-friendly, totally biodegradable plastics. The use of cane molasses and corn steep liquor, two of the cheapest substrates available in Egypt, may help to reduce the cost of producing such biopolyesters. In this work, the effect of different carbon sources was studied. Maximum production of PHB was obtained with cane molasses and glucose as sole carbon sources (40.8, 39.9 per mg cell dry matter, respectively). The best growth was obtained with 3% molasses, while maximum yield of PHB (46.2% per mg cell dry matter) was obtained with 2% molasses. Corn steep liquor was the best nitrogen source for PHB synthesis (32.7 mg per cell dry matter), on the other hand, best growth was observed when ammonium chloride, ammonium sulphate, ammonium oxalate or ammonium phosphate were used as nitrogen sources.     

Incorporation of polyethylene glycol in polyhydroxyalkanoic acids accumulated by Azotobacter chroococcum MAL-201

Azotobacter chroococcum MAL-201 (MTCC 3853), a free-living nitrogen-fixing bacterium accumulates poly(3-hydroxybutyric acid) [PHB, 69% of cell dry weight (CDW)] when grown on glucose and poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [PHBV with 19.2 mol% 3HV] when grown on glucose and valerate. Use of ethylene glycol (EG) and/or polyethylene glycols (PEGs) of low molecular weight as sole carbon source were detrimental to A. chroococcum growth and polymer yields. PEG-200, however, in the presence of glucose was incorporated into the polyhydroxyalkanoate (PHA) polymer. Addition of PEG-200 (150 mM) to culture medium during mid-log phase growth favored increased incorporation of EG units (12.48 mol%) into the PHB polymer. In two-step culture experiments, where valerate and PEG simultaneously were used in fresh medium, EG was incorporated most effectively in the absence of glucose, leading to the formation of a copolymer containing 18.05 mol% 3HV and 14.78 mol% EG. The physico-mechanical properties of PEG-containing copolymer (PHBV–PEG) were compared with those of the PHB homopolymer and the PHBV copolymer. The PHBV–PEG copolymer appeared to have less crystallinity and greater flexibility than the short-chain-length (SCL) PHA polymers.     

Effect of nutritional supplements on bio-plastics (PHB) production utilizing sugar refinery waste with potential application in food packaging

Abstract

Polyhydroxyalkanoates (PHAs) are intracellular carbon and energy storage reserve material stored by gram-negative bacteria under nutrient limitation. PHAs are best alternative biodegradable plastics (bio-plastics) due to their resemblance to conventional synthetic plastic. The present study investigated the synergistic effect of nutritional supplements (amino acid and vitamin) on the PHA production by Alcaligenes sp. NCIM 5085 utilizing a sugar refinery waste (cane molasses) under submerged fermentation process. Initially, the effect of individual factor on PHA yield was studied by supplementing amino acids (cysteine, isoleucine, and methionine), vitamin (thiamin), and cane molasses at varying concentration in the production medium. Further, the cultivation medium was optimized by varying the levels of cane molasses, methionine and thiamin using response surface methodology to enhance the PHA yield. The maximum PHA yield of 70.89% was obtained under the optimized condition, which was then scaled up on 7.5?L-bioreactor. Batch cultivation in 7.5?L-bioreactor under the optimized condition gave a maximum PHA yield and productivity of 79.26% and 0.312 gL^?1 h^?1, respectively. The PHA produced was subsequently characterized as PHB by FTIR. PHB extracted was of relatively high molecular weight and crystallinity index. DSC analysis gave T_g, T_m, and X_c of 4.2, 179?°C and 66%, respectively. TGA analysis showed thermal stability with maximized degradation occurring at 302?°C, which is above the melting temperature (179?°C) of the purified polymer. The extracted polymer, therefore, possessed desirable material properties to be used in food packaging.     

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     

Improvement of erythromycin production by Saccharopolyspora erythraea in molasses based medium through cultivation medium optimization

In the present work, erythromycin production was carried out in submerged culture using Saccharopolyspora erythraea. Different experiments were conducted to optimize the cultivation medium through the change of carbon and nitrogen sources to cheaper one in order to reduce the cost of medium and to utilize sugar cane molasses as one of major sugar industry by-products in Egypt. It was found that the addition of sugar cane molasses a sole carbon source at a concentration of 60 g/l accompanied by corn steep liquor (as organic N-source) in combination with ammonium sulphate (as inorganic N-source) gave the maximal erythromycin production. The antibiotic production in this medium reached about 600 mg/l which is about 33% higher than the value obtained in glucose based medium. On the other hand, the addition of n-propanol in concentration of 1% (v/v) increased the antibiotic production reaching about 720 mg/l after 144 h. Concluding, the new medium formulation based on cheap carbon source, sugar cane molasses, was a good alternative solution for the production of erythromycin economically.     

Effect of carbon source and concentration on the molecular mass of poly(3-hydroxybutyrate) produced by Methylobacterium extorquens and Alcaligenes eutrophus

In shake-flask culture, Methylobacterium extorquens accumulated poly(3-hydroxybutyrate) (PHB) possessing a substantially higher weight-average molecular mass (M_W) than previously reported for this organism. The M_W of PHB produced by M. extorquens was dependent on the initial concentration of methanol or sodium succinate, used as sole carbon sources. The highest M_W values (0.6 and 1.7 × 10⁶) were obtained with low initial concentrations of methanol or sodium succinate (4.0 and 3.0 g l^–1, respectively) and the latter substrate always yielded PHB of higher M_W than that produced from methanol. Thus PHB with an M_W in the range 0.2–1.7 × 10⁶ could be produced by selection of the carbon source and its concentration. In contrast to the findings with M. extorquens, the M_W of PHB produced by Alcaligenes eutrophus was high (1.1–1.6 × 10⁶) and generally unaffected by the choice or concentration of the carbon source. The use of glycerol as sole carbon source did, however, result in the accumulation of PHB with a markedly lower M_W (5.5–8.5 × 10⁵) than that produced from other sole carbon sources by this organism under similar conditions. Correspondence to: A. J. Anderson     

Effect of growth conditions on the molecular weight of poly-3-hydroxybutyrate produced by <Emphasis Type="Italic">Azotobacter chroococcum</Emphasis> 7B

It has been shown that poly-3-hydroxybutyrate (PHB) of predetermined molecular weight can be obtained by varying the growth conditions of the producer strain, Azotobacter chroococcum 7B: pH, temperature, aeration, presence of sodium acetate as an additional carbon source, or growth on crude complex carbon sources (molasses, vinasse, or starch). High-molecular-weight polymer can be obtained at pH 7.0, optimal for the culture (1485 kDa), temperature 30–37°C (1600–1450 kDa, respectively), and low aeration (2215 kDa). The following factors decrease PHB MW: pH deviation to the acidic (pH 6.0, 476 kDa) or alkaline (pH 8.0, 354 kDa) range or lower temperature (20°C, 897 kDa). Introduction of additional carbon source (sodium acetate) at concentrations in the medium varying from 0 to 5 g/l provides an original method of production of PHB with predetermined MW in a wide range, from 270 to 1515 kDa, with high PHB content in the cell.     

Production of poly(3-hydroxybutyrate) from inexpensive substrates

Two inexpensive substrates, starch and whey were used to produce poly(3-hydroxybutyrate) (PHB) in fed-batch cultures of Azotobacter chroococcum and recombinant Escherichia coli, respectively. Oxygen limitation increased PHB contents in both fermentations. In fed-batch culture of A. chroococcum, cell concentration of 54 g l⁻¹ with 46% PHB was obtained with oxygen limitation, whereas 71 g l⁻¹ of cell with 20% PHB was obtained without oxygen limitation. The timing of PHB biosynthesis in recombinant E. coli was controlled using the agitation speed of a stirred tank fermentor. A PHB content of 80% could be obtained with oxygen limitation by increasing the agitation speed up to only 500 rpm.     

Enhancing polyhydroxybutyrate production from high cell density fed-batch fermentation of Bacillus megaterium BA-019

This study demonstrated the improved polyhydroxybutyrate (PHB) production via high cell density cultivation of Bacillus megaterium BA-019 with balanced initial total sugar concentration and carbon to nitrogen (C/N) weight ratio. In the 10 L stirred fermentor operated at 30 °C, pH 7.0, 600 rpm, and 1.0 vvm air, with the initial total sugar concentration of 60 g/L and urea at the C/N weight ratio of 10:1, 32.48 g/L cell biomass with the corresponding PHB weight content of 26.94 % and volumetric productivity of 0.73 g/L h were obtained from batch cultivation. Continuing cultivation by intermittent feeding of the sugarcane molasses along with urea at the C/N weight ratio of 12.5:1 gave much improved biomass and PHB production (90.71 g/L biomass with 45.84 % PHB content and 1.73 g/L h PHB productivity). Similar biomass and PHB yields were obtained in the 90 L stirred fermentor when using the impeller tip speed as the scale-up criterion.     

Poly-3-hydroxybutyrate production byAzotobacter chroococcum

Thirty-seven soil isolates and mutants ofAzotobacter chroococcum tested for poly-3-hydroxybutyrate (PHB) production using Sudan black B staining method were found to be positive. One mutant showed a higher number of PHB-producing cells and maximum number of granules per cell. Using 2% glucose and 15 mmol/L ammonium acetate, PHB production was found to be maximum at 36 and 48 h of growth under submerged cultivation and under stationary cultivation, respectively. PHB production was found to be higher on sucrose and commercial sugar (as carbon sources) as compared to glucose and mannitol. As commercial sugar is cheaper than sucrose it was selected as carbon source for PHB production, that being found to be maximum at 1% concentration. Inorganic nitrogen sources seemed to have no stimulatory effect on the production of PHB. However, ammonium acetate (15 mmol/L) was found to be best for PHB production. Peptone (0.2 %) gave a better yield of PHB under both growth conditions. Using all optimized conditions, PHB production was studied in ten selected strains. Two of them were found to be best PHB producers under both growth conditions, one producing 621 and 740 μg/g dry mass under submerged cultivation and under stationary cultivation, respectively, while the second one produced 589 and 733 μg/g.     

Poly(β-hydroxybutyrate) production by a moderate halophile,Halomonas boliviensis LC1

The moderate halophile Halomonas boliviensis, isolated from a Bolivian saline soil sample, was able to accumulate poly(β-hydroxybutyrate) (PHB) when grown under conditions of nutrient limitation and excess carbon source. The concentration of sodium chloride in the medium influenced the cell-growth, -size, and rate of PHB accumulation. Cultivation in shake flasks led to a PHB accumulation of about 54 wt.% with respect to cell dry weight at 4.5% (w/v) NaCl in a medium with butyric acid and sodium acetate as carbon sources. The production of PHB was substantially improved to a maximum value of 88 wt.% during cultivation under controlled conditions of pH and oxygen concentration in a fermentor. The use of glucose and sucrose, respectively, as carbon source could also lead to the production of PHB at an average level of 55 wt.%.     

Enhanced poly(L-malic acid) production from pretreated cane molasses by Aureobasidium pullulans in fed-batch fermentation

Poly(L-malic acid) (PMA) is a natural polyester with many attractive properties for biomedical application. However, the cost of PMA production is high when glucose is used as a carbon source. To solve this problem, cane molasses as a low-cost feedstock was applied for the production of PMA. Six pretreatment methods were applied to cane molasses before fermentation. Pretreatment with combined tricalcium phosphate, potassium ferrocyanide, and sulfuric acid (TPFSA) removed significant amounts of metal ions from cane molasses. The PMA concentration increased from 5.4?g/L (untreated molasses) to 36.9?g/L (TPFSA-pretreated molasses) after fermentation in shake flasks. A fed-batch fermentation strategy was then developed. In this method, TPFSA-pretreated cane molasses solution was continuously fed into the fermentor to maintain the total sugar concentration at 20?g/L. This technique generated approximately 95.4?g/L PMA with a productivity of 0.57?g/L/hr. The present study indicated that fed-batch fermentation using pretreated cane molasses is a feasible technique for producing high amounts of PMA.     

Polyhydroxybutyrate production by Saccharophagus degradans using raw starch as carbon source

Biosynthesis of poly(3‐hydroxybutyrate) (PHB) from raw starch as the carbon source by the polysaccharide‐digesting bacteria Saccharophagus degradans was investigated in a fed‐batch culture. The production and properties of the PHB synthesized from starch were compared to those obtained using glucose as carbon source. In fed‐batch cultures, S. degradans accumulated 21.35 and 17.46% of PHB, using glucose or starch as carbon source, respectively. The physical properties of the biopolymer produced from each carbon source were similar between them. Molecular mass, melting temperature and heat of fusion were 54.23 kDa, 165.61°C and 59.59 J/g, respectively, using glucose; and 57.07 kDa, 174.31°C and 67.66 J/g, respectively, using starch. This is the first work describing the capability of S. degradans to utilize raw starch as the sole carbon source for the production of PHB.     

Poly(3-hydroxybutyrate) (PHB) synthesis by recombinant Escherichia coli harbouring Streptomyces aureofaciens PHB biosynthesis genes: effect of various carbon and nitrogen sources

Recombinant Escherichia coli (ATCC:PTA-1579) harbouring poly(3-hydroxybutyrate) (PHB) synthesising genes from Streptomyces aureofaciens NRRL 2209 accumulates PHB. Effects of different carbon and nitrogen sources on PHB accumulation by recombinant E. coli were studied. Among the carbon sources used glycerol, glucose, palm oil and ethanol supported PHB accumulation. No PHB accumulated in recombinant cells when sucrose or molasses were used as carbon source. Yeast extract, peptone, a combination of yeast extract and peptone, and corn steep liquor were used as nitrogen sources. The maximum PHB accumulation (60% of cell dry weight) was measured after 48 h of cell growth at 37 degrees C in a medium with glycerol as the sole carbon source, and yeast extract and peptone as nitrogen sources. Scanning electron microscopy of the PHB granules isolated from recombinant E. coli revealed these to be spherical in shape with a diameter ranging from 0.11 to 0.35 pm with the mean value of 0.23 +/- 0.06 pm.     

Effect of anaerobic promoters on the microaerobic production of polyhydroxybutyrate (PHB) in recombinant <Emphasis Type="Italic">Escherichia coli</Emphasis>

Nine anaerobic promoters were cloned and constructed upstream of PHB synthesis genes phbCAB from Ralstonia eutropha for the micro- or anaerobic PHB production in recombinant Escherichia coli. Among the promoters, the one for alcohol dehydrogenase (P _adhE ) was found most effective. Recombinant E. coli JM 109 (pWCY09) harboring P _adhE and phbCAB achieved a 48% PHB accumulation in the cell dry weight after 48 h of static culture compared with only 30% PHB production under its native promoter. Sixty-seven percent PHB was produced in the dry weight (CDW) of an acetate pathway deleted (Δpta deletion) E. coli JW2294 harboring the vector pWCY09. In a batch process conducted in a 5.5-l NBS fermentor containing 3 l glucose LB medium, E. coli JW2294 (pWCY09) grew to 7.8 g/l CDW containing 64% PHB after 24 h of microaerobic incubation. In addition, molecular weight of PHB was observed to be much higher under microaerobic culture conditions. The high activity of P _adhE appeared to be the reason for improved micro- or anaerobic cell growth and PHB production while high molecular weight contributed to the static culture condition.     

PHB accumulation in Nostoc muscorum under different carbon stress situations

Use of algae for intracellular poly-β-hydroxybutyrate (PHB) accumulation for bioplastic production offers an opportunity in economic efficiency by reduced costs. The cyanobacterium Nostoc muscorum is a PHB accumulator which presents a great potential as raw material supplier because of short generation cycles. Here, we examined a range of experimental conditions including different growth conditions of phosphate-starved cells with the addition of external carbon sources. The highest, absolute PHB accumulation was measured in a phosphate-starved medium with 1% (w/w) glucose and 1% (w/w) acetate. PHB accumulated inside algae cells. After 23 days of growth in phosphate-starved medium, 1 L of culture contained up to 145.1 mg PHB. The highest PHB accumulation based on the cell dry weight was in an experiment with aeration and CO₂ addition. The intracellular level of PHB was up to 21.5% cell dry weight after 8 days.     

Enhancement of poly-3-hydroxybutyrate (PHB) productivity by the two-stage supplementation of carbon sources and continuous feeding of NH4Cl

Gluconate and glucose were selected as the carbon substrates in the production of poly-3-hydroxybutyrate (PHB). Gluconate was utilized to maximize the specific growth rate during the first stage of cell growth, whereas glucose was used to maximize PHB biosynthesis during the second stage of PHB accumulation. The sequential feeding of gluconate and glucose resulted in a 50% enhancement of PHB productivity as compared to the cultures cultivated on glucose alone. In conjunction with secondary glucose uptake, the presence of a trace amount of ammonium increased the rate of PHB biosynthesis during the stage of PHB accumulation. Via the feeding of 0.03 mmol/h of NH₄Cl solution prior to the exhaustion of the initial amount of NH₄Cl, PHB productivity was significantly enhanced as compared to the cultures raised on glucose alone. The glucose-grown culture evidenced a higher level of NADPH during the NH₄Cl-exausted PHB accumulation stage than was observed in the gluconate-grown culture, which reflects that the reason of higher PHB production observed when glucose was used as a carbon source. NH₄Cl feeding following the depletion of initial NH₄Cl resulted in elevated levels of both ATP and NADPH, which increased the PHB biosynthesis rate, and also in a decrease in the level of NADH, which reflected the alleviation of the inhibitory effects on the cells caused by nitrogen depletion. Electronic Supplementary Material  Supplementary material is available for this article at and is accessible for authorized users.     

Effect of nitrogen starvation on ammonium-inhibition of nitrogenase activity in Azotobacter chroococcum

When Azotobacter chroococcum cells grown in batch culture under N₂-fixing conditions were transferred to a medium lacking a nitrogen source, the cellular C/N ratio, the amount of alginic acid released into the external medium and the rate of endogenous respiration increased appreciably after 6 h to the exclusion of dinitrogen, whereas nitrogenase activity did not undergo any significant change. Nitrogen deficiency caused a decrease in the ammonium inhibition of nitrogenase activity from 95% inhibition at zero time to 14% after 6 h incubation under dinitrogen starvation, with no difference in the rate of ammonium utilization by N₂-fixing and N₂-starved cells being observed. This suggests that a balance of nitrogen and carbon assimilation is necessary for the ammonium inhibition of nitrogenase activity in A. chroococcum to take place.