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.     

Production of poly-β-hydroxybutyrate by thermophilic cyanobacterium, Synechococcus sp. MA19, under phosphate-limited conditions

Synechococcus sp. MA19, grown autotrophically under phosphate-limited conditions at 50 °C, produced poly--hydroxybutyrate (PHB) when intracellular phosphate content was 0.043–0.076mmol per g of cellular components. In the culture for 260h using Ca₃(PO₄)₂ as a phosphate source, strain MA19 accumulated PHB at 55% (w/w) of the dry cells and the amount of PHB produced was 2.4gl^–1 which was almost twice that without Ca₃(PO₄)₂ addition.     

Production of 2,3-butanediol from wood hydrolysate byKlebsiella pneumoniae

2,3-Butanediol was produced at 12g/l (27% w/w yield) from the reducing sugars in wood hydrolysate byKlebsiella pneumoniae NRRL B-199. Ethanol was present at 4 g/l and acetoin at 0.4 g/l. Optimum conditions for a 48 h fermentation were pH 6.0, 30°C and 50 g reducing sugars/l. Adding 1% (w/v) malt extract to the medium-enhanced butanedlol production to 13.3 g/l (yield 29%) without changing ethanol production.

---

Résumé On a produit 12 g/l de 2,3-butanediol (27% de rendement en poids) à partir des sucres réducteurs dans un hydrolysat de bois au moyen deKlebsiella pneumoniae NRRL B-199. L'éthanol était présent à raison de 4 g/l et l'acétoïne de 0.4 g/l. Les conditions optimum pour une fermentation de 48 h étainent les suivantes: pH 6.0, 30°C, et 50 g de sucres réducteurs par litre. L'ajout de 1% (p/v) d'extrait de malt au millieu accroît la production de butanediol jusqu'à 13.3 g/l (29% de rendement) sans changer la production d'éthanol.

     

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.     

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(γ-glutamic acid) (PGA), or poly(β-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 × 10⁵ g mol⁻¹ and a polydispersity of about 1.4. Received: 3 December 1999 / Received revision: 22 February 2000 / Accepted: 25 February 2000     

Production of fuel alcohol by Saccharomyces strains from tropical habitats

Summary Strains of Saccharomyces spp. from tropical substrates tolerated temperatures up to 40 ° C, sucrose concentrations up to 50% (w/v) and ethanol concentrations up to 20 g/L in fermentation conditions. Strain TD200 tolerated 20 g/l of ethanol. The ethanol produced by strain DR1459 was comparable to that of industrial strain HTYM-81. These strains have potential use for the production of fuel alcohol.     

Zobellella denitrificans strain MW1, a newly isolated bacterium suitable for poly(3-hydroxybutyrate) production from glycerol

Aims: To search for new bacteria for efficient production of polyhydroxyalkanoates (PHAs) from glycerol. Methods and Results: Samples were taken from different environments in Germany and Egypt, and bacteria capable of growing in mineral salts medium with glycerol as sole carbon source were enriched. From a wastewater sediment sample in Egypt, a Gram‐negative bacterium (strain MW1) was isolated that exhibited good growth and that accumulated considerable amounts of polyhydroxybutyrate (PHB) from glycerol and also from other carbon sources. The 16S rRNA gene sequence of this isolate exhibited 98·5% and 96·2% similarity to Zobellella denitrificans strain ZD1 and to Zobellella taiwanensis strain ZT1 respectively. The isolate was therefore affiliated as strain MW1 of Z. denitrificans. Strain MW1 grows optimally on glycerol at 41°C and pH 7·3 and accumulated PHB up to 80·4% (w/w) of cell dry weight. PHB accumulation was growth‐associated. Although it was not an absolute requirement, 20 g l^?1 sodium chloride enhanced both growth (5 g cell dry weight per litre) and PHB content (87%, w/w). Zobellella denitrificans strain MW1 is also capable to accumulate the poly(3‐hydroxybutyrate‐co‐3‐hydroxyvalerate) copolymer if sodium propionate was used as cosubstrate in addition to glycerol. Conclusions: A new PHB‐accumulating strain was isolated and identified. This strain is able to utilize glycerol for growth and PHB accumulation to high content especially in the presence of NaCl that will enable the utilization of waste glycerol from biodiesel industry. Significance and Impact of the Study: This study is the first report on accumulation of PHA in a member of the new genus Zobellella. Furthermore, utilization of glycerol as the sole carbon source for fast growth and PHB biosynthesis, growth in the presence of NaCl and high PHB contents of the cells will make this newly isolated bacterium a potent candidate for industrial production of PHB from crude glycerol occurring as byproduct during biodiesel production.     

Enhancement of succinic acid production by osmotic-tolerant mutant strain of Actinobacillus succinogenes

Fermentation and succinic acid production by Actinobacillus succinogenes YZ0819 was inhibited by high NaCl. To enhance the resistance of this strain to osmotic stress, an NaCl-tolerant mutant strain of A. succinogenes (CH050) was screened and selected through a continuous culture using survival in 0.7 M NaCl as the selection criterion. Using Na₂CO₃ as the pH regulator and glucose as the carbon source in batch fermentation, the isolated osmo-resistant stain, A. succinogenes CH050, produced up to 66 g/l succinic acid with a yield of 73.37% (w/w). The concentration of succinic acid and mass yield were increased by 37.5 and 4.37%, respectively, compared to the parent strain. The dry cell weight reached 10.1 g/l, which is 37% higher than that of the parent strain. The high tolerance of A. succinogenes CH050 to osmotic stress increased improved the succinic acid production from batch fermentation.     

Trehalose accumulation from corn starch by Saccharomycopsis fibuligera A11 during 2-l fermentation and trehalose purification

In this study, corn starch was used as the substrate for cell growth and trehalose accumulation by Saccharomycopsis fibuligera A11. Effect of different aeration rates, agitation speeds, and concentrations of corn starch on direct conversion of corn starch to trehalose by S. fibuligera A11 were examined using a Biostat B2 2-l fermentor. We found that the optimal conditions for direct conversion of corn starch to trehalose by this yeast strain were that agitation speed was 200 rpm, aeration rate was 4.0 l/min, concentration of corn starch was 2.0% (w/v), initial pH was 5.5, fermentation temperature was 30°C. Under these conditions, over 22.9 g of trehalose per 100 g of cell dry weight was accumulated in the yeast cells, cell mass was 15.2 g/l of the fermentation medium, 0.12% (w/v) of reducing sugar, and 0.21% (w/v) of total sugar were left in the fermented medium within 48 h of the fermentation. It was found that trehalose in the yeast cells could be efficiently extracted by the hot distilled water (80°C). After isolation and purification, the crystal trehalose was obtained from the extract of the cells.     

Ethanol and glycerol production under aerobic conditions by wild-type,respiratory-deficient mutants and a fusion product of Saccharomyces cerevisiae

Summary Experiments were performed to investigate growth, ethanol and glycerol production by wild-type strains (RHO) and respiratory-deficient (rho) mutants of Saccharomyces cerevisiae. Furthermore protoplasts were fused in order to enhance the fermentation capacity of a flocculent strain. At high substrate conditions, 150 g/l of saccharose, there is no difference in cell growth. However, at a glucose concentration of 10–20 g/l the mutants grow much slower. After 3 days of incubation at 28° C in a complete medium the viability of the two strains is the same. In minimal medium on the other hand the number of viable cells of the mutant is 100-fold reduced. All mutants tested showed a higher specific activity of alcohol dehydrogenase (ADH I) and an enhanced production of glycerol compared with the wild-type strain. By protoplast fusion a modified flocculent strain was obtained with higher specific activity of ADH I and a reduced biosynthesis of glycerol. However, the yields of ethanol (75–78%) are about the same for the wild-type strain and the rho mutants under aerobic conditions in absence of catabolite repression.     

Bimutation breeding of Aspergillus niger strain for enhancing β-mannanase production by solid-state fermentation

A parent strain Aspergillus niger LW-1 was mutated by the compound mutagenesis of vacuum microwave (VMW) and ethyl methane sulfonate (EMS). A mutant strain, designated as A. niger E-30, with high- and stable-yield β-mannanase was obtained through a series of screening. The β-mannanase activity of the mutant strain E-30, cultivated on the basic fermentation medium at 32 °C for 96 h, reached 36,675 U/g dried koji, being 1.98-fold higher than that (18,501 U/g dried koji) of the parent strain LW-1. The purified E-30 β-mannanase, a glycoprotein with a carbohydrate content of 19.6%, had an apparent molecular weight of about 42.0 kDa by SDS–PAGE. Its optimal pH and temperature were 3.5 and 65 °C, respectively. It was highly stable at a pH range of 3.5–7.0 and at a temperature of 60 °C and below. The kinetic parameters K_m and V_max, toward locust bean gum and at pH 4.8 and 50 °C, were 3.68 mg/mL and 1067.5 U/mg, respectively. The β-mannanase activity was not significantly affected by an array of metal ions and EDTA, but strongly inhibited by Ag⁺ and Hg²⁺. In addition, the hydrolytic conditions of konjak glucomannan using the purified E-30 β-mannanase were optimized as follows: konjak gum solution 240 g/L (dissolved in deionized water), hydrolytic temperature 50 °C, β-mannanase dosage 120 U/g konjak gum, and hydrolytic time 8 h.     

Pilot-scale production of butanol by Clostridium beijerinckii BA101 using a low-cost fermentation medium based on corn steep water

To improve the economic competitiveness of the acetone/butanol/ethanol fermentation process, glucose/corn steep water (CSW) medium was used on a pilot scale for the production of solvents. The production of butanol by the Clostridium beijerinckii NCIMB 8052 parent strain and the solvent-hyperproducing BA101 mutant was compared. In a 20-l fermentation using 5% glucose/CSW medium,  C. beijerinckii 8052 produced 8.5 g butanol/l and 5 g acetone/l, while  C. beijerinckii BA101 produced 16 g butanol/l and 7.5 g acetone/l. Further studies were carried out on a larger scale using an optimized 6% glucose/CSW medium. In a 200-l pilot-scale fermentor,  C. beijerinckii 8052 produced 12.7 g butanol/l and 6 g acetone/l following 96 h of fermentation.  C. beijerinckii BA101 produced 17.8 g/l and 5.5 g/l butanol and acetone respectively, following 130 h of fermentation. These results represent a 40% increase in final butanol concentration by the C. beijerinckii BA101 mutant strain when compared to the 8052 parent strain. The total solvents (acetone, butanol, and ethanol) produced by C. beijerinckii NCIMB 8052 and BA101 in a 200-l fermentation were 19.2 g/l and 23.6 g/l respectively. This is the first report of pilot-scale butanol production by the solvent-hyperproducing C. beijerinckii BA101 mutant employing an inexpensive glucose/CSW medium. Received: 26 May 1998 / Received revision: 21 September 1998 / Accepted: 11 October 1998     

Production of poly-β-hydroxybutyrate on molasses by recombinant Escherichia coli

Beet molasses successfully replaced glucose as sole carbon source to produce poly--hydroxybutyrate by a recombinant Escherichia coli strain (HMS174/pTZ18u-PHB). The fermentation with molasses was cheaper than with glucose. The final dry cell weight, PHB content and PHB productivity were 39.5 g/L, 80% (w/w) and 1 g/Lh, respectively, in a 5 L stirred tank fermenter after 31.5 h fed-batch fermentation with constant pH and dissolved O2 content. © Rapid Science Ltd. 1998     

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 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.     

The influence of poly-β-hydroxybutyrate accumulation on cell volume and buoyant density in alcaligenes eutrophus

Accumulation of poly--hydroxybutyrate (PHB) was studied in Alcaligenes eutrophus strain N9A. Under nitrogen limitation and heterotrophic conditions, the cells accumulated PHB at a rate of 50 fg cell^-1 h^-1. Volume increased from 1.208 to 3.808 m³ and buoyant density from 1.110 to 1.145 pg m^-3 with an increase in PHB from 0 up to 1.699 pg cell^-1. Volume was found to change linearly with PHB content. The changes were due to increases in cell width and not in cell length. PHB explained 93% of the changes in cellular volume. The relationship between density and PHB was hyperbolic. PHB explained 96% of the changes in density. When a mutant strain unable to accumulate PHB was analyzed together with the wild type, the PHB-less mutant and the wild type showed densities of 1.100 pg m^-3 and 1.120 pg m^-3, respectively, in gradients of 65% Percoll. In sucrose gradients, nevertheless, the results were reversed. This discrepancy was explained by the high osmolarity of sucrose which gives artificial results. Thus, we conclude that Percoll is a more suitable medium than sucrose to measure the density of live bacterial cells.Abbreviation PHB poly--hydroxybutyrate     

Optimization of whey fermentation in a shaken-flask fermenter

Summary A composite design technique was used to optimize the fermentation of whey by Kluyveromyces fragilis IMAT 1872. The experimental variables (temperature T, salts NP, yeast-extract YE and lactose level L), but not pH, were found to be significant at a level of 5%. The optimal operating conditions were determined (T=36.4°C, pH=5.1, NP=0.47% w/v, YE=0.114% w/v, and L=24.75 g/l). Temperature and lactose level exhibited a great influence on the biomass yield about the stationary point. Canonical analysis showed that these variables are not mutually independent. The optimal conditions will be used as starting point for a factorial design on a jar fermenter.     

Reducing sugar accumulation from alkali pretreated sugar cane bagasse using Cellulomonas

Summary An active cellulolytic culture was obtained following growth of the Cellulomonas strain CS1-17 for 24 h at 32° C on 1 or 2% alkali pretreated sugar cane bagasse. Environmental conditions were then varied to favour reducing sugar accumulation from fresh alkali pretreated bagasse added to the 24 h culture medium at 75 g/l. After incubation for an additional 48 h at 37° C under anaerobic, aerobic and aerobic+0.2% sodium azide conditions, reducing sugar was accumulated at 22.8, 23.7 and 25.6 g/l respectively. Approximately 83% of this release occurred during the first 18 h of incubation and the reducing sugar released contained approximately 14% xylose, 35% glucose, and 26% cellobiose. Addition of exogenous cellobiase resulted in conversion of the cellobiose to glucose.     

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.     

Production of cellulase and xylanase by a wild strain of Trichoderma viride

Summary The production of cellulase and xylanase was investigated with a newly isolated strain of Trichoderma viride BT 2169. The medium composition was optimized on a shake-flask scale using the Graeco-Latin square technique. The temperature and time for optimal growth and production of the enzymes in shake cultures were optimized using a central composite design. The temperature optima for maximal production of filter paper cellulase (FPase), xylanase and -gluosidase were 32.8°, 34.7° and 31.1° C, respectively, and the optimum times for production of these enzymes were found to be 144, 158 and 170 h, respectively. The optimized culture medium and conditions (33° C) gave 0.55 unit of FPase, 188.1 units of xylanase and 3.37 units of -glucosidase per milliliter of culture filtrate at 144 h of shake culture. Among different carbon sources tested, the maximum enzyme activities were produced with sulphite pulp and all three enzymes were produced irrespective of the carbon sources used. Batch fermentation in a laboratory fermentor using 2% sulphite pulp allowed the production of 0.61 unit of FPase, 145.0 units of xylanase and 2.72 units of -glucosidase. In a fed-batch fermentation on 6% final Avicel concentration FPase and -glucosidase were 3.0 and 2.4 times higher respectively than those in batch fermentation on 2% Avicel. The pH and temperature optima as well as pH and temperature stabilities of T. viride enzymes were found to be comparable to T. reesei and some other fungal enzymes.     

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.