Growth-associated production of poly-3-hydroxybutyrate byBacillus mycoides

Bacillus mycoides strain RIJ B-017, a growth-associated poly-3-hydroxybutyrate (PHB) producer was grown on sucrose-containing media. PHB accumulated in cells up to 72% of dry cell mass. The overall maximum value of PHB yield (Y _p/s) and productivities (Q _p andq _p) 250 mg_p/g_s, 120 mg_p L⁻¹ h⁻¹ and 30 mg_p g_x ⁻¹ h⁻¹, respectively, were obtained at 15 g/L sucrose. Differential scanning calorimeter heating curve showed two peaks, one at 95.9 °C and another at 165.4°C with a shoulder around 154.6 °C. The viscosity-average molar mass in chloroform at 27°C was 505 kDa. The carbon content of PHB was 55.4% of the mass.     

Optimization of polyhydroxybutyrate production from a wild type and two mutant strains of Rhodobacter sphaeroides using statistical method

Interaction studies using central composite design (CCD) gave the optimum concentrations of acetate at 4 g l(-1) and (NH4)2SO4 at 0.01 g l(-1) with an optimum temperature of 35 degrees C. Rhodobacter sphaeroides N20 gave the highest PHB (7.8 g l(-1)) and biomass (DCW) (8.2 g l(-1)) values compared to the wild type strain and the mutant strain U7. The CCD results predicted that the optimum medium for the mutant strain N20 consisted of 3.90 g l(-1) acetate, 0.01 g l(-1) (NH4)2SO4 at 33.5 degrees C (R2=0.985). Validation of this model by culturing the mutant strain in this optimum medium exhibited similar values of PHB (7.76 g l(-1)), biomass (8.32 g l(-1)) and the PHB content in the cell 93.2% of DCW. Similar amounts of PHB were also obtained in batch fermentations using a 5-l bioreactor. The effect of pH and aeration rate was also studied and the optimum values were found to be pH 7.0 with an aeration rate of 1.0 vvm. Under these optimal conditions, strain N20 produced the highest amount of PHB production (8.76 g l(-1)), PHB content (95.4% of DCW) as well as the product yield (Yp/x) (0.72). These results are the highest values ever obtained from photosynthetic bacteria reported so far.     

Effect of total nutrient feed on production of poly-3-hydroxybutyrate by Methylobacterium sp. ZP24 grown on sugars

Methylobacterium sp. ZP24 is able to produce poly-3-hydroxybutyrate (PHB) from sucrose and lactose. As the production of PHB is growth-associated, a strategy of intermittent feeding of sugars and other nutrients was assessed for obtaining high yields of the polymer. Higher PHB synthesis was obtained at increased sugar feed rates. Cellular PHB contents of 63% and 71%, with productivities of up to 0.354 and 0.645 g PHB/l h were obtained from sucrose and lactose, respectively. A short-duration semicontinuous production level of up to 2.4 g PHB/l h was achieved in the lactose fermentation. Journal of Industrial Microbiology & Biotechnology (2000) 25, 276–279. Received 06 June 2000/ Accepted in revised form 31 August 2000     

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.     

Screening and identification of polyhydroxyalkanoates producing bacteria and biochemical characterization of their possible application

Polyhydroxyalkanoates (PHAs) accumulating bacteria were isolated under various selective conditions such as pH, salt concentrations and types of heavy metal. Fifty strains of bacterial isolates were found to belong to Bacillus, Proteus, Pseudomonas, Aeromonas, Alcaligenes and Chromobacterium, based on phenotypical features and genotypic investigation. Only twenty five bacterial isolates were selected and observed for the production of PHAs. Interestingly, bacteria belonging to Firmucutes Bacillus sp. produced a high amount of PHAs. The maximum PHAs were accumulated by B. licheniformis PHA 007 at 68.80% of dry cell weight (DCW). Pseudomonas sp., Aeromonas sp., Alcaligenes sp. and Chromobacterium sp. were recorded to produce a moderate amount of PHAs, varying from 10.00-44.32% of DCW. The enzymatic activity was preliminarily analyzed by the ratio of the clear zone diameter to colony diameter. Bacillus gave the highest ratio of hydrolysis zone which corresponds to the highest hydrolytic enzyme activities. Bacillus licheniformis PHA 007 had the highest lipase and protease activity at 2.1 and 5.1, respectively. However, the highest amylase activity was observed in Bacillus sp. PHA 023 at 1.4. Determination of metabolic characteristics was also investigated to check for their ability to consume a wide range of substrates. Bacillus, Aeromonas sp. and Alcaligenes sp. had great ability to utilize a variety of substrates. To decrease high PHA cost, different sources of cheap substrates were tested for the production of PHAs. Bacillus cereus PHA 008 gave the maximal yield of PHA production (64.09% of DCW) when cultivated in anaerobically treated POME. In addition, the accumulation of PHA copolymers such as 3-hydroxyvalerate and 3-hydroxyhexanoate was also observed in Bacillus and Pseudomomas sp. strain 012 and 045, respectively. Eight of the nine isolates accumulated a significant amount of PHAs when inexpensive carbon sources were used as substrates. Here it varied from 1.69% of DCW by B. licheniformis PHA 007 to 64.09% of DCW by B. cereus PHA 008.     

Production and characterization of PHB from two novel strains of Bacillus spp. isolated from soil and activated sludge

The present study reports two bacteria, designated 87I and 112A, which were isolated from soil and activated sludge samples from Hyderabad, India, and that are capable of producing poly-3-hydroxybutyrate (PHB). Based on phenotypical features and genotypic investigations, these microorganisms were identified as Bacillus spp. Their optimal growth occurred between 28°C and 30°C and pH 7. Bacillus sp. 87I yielded a maximum of 70.04% dry cell weight (DCW) PHB in medium containing glucose as carbon source, followed by 55.5% DCW PHB in lactose-containing medium, whereas Bacillus sp. 112A produced a maximum of 67.73% PHB from glucose, 58.5% PHB from sucrose, followed by 50.5% PHB from starch as carbon substrates. The viscosity average molecular mass (M _v) of the polymers from Bacillus sp. 87I was 513 kDa and from Bacillus sp. 112A was 521 kDa. All the properties of the biopolymers produced by the two strains 87I and 112A were characterized.     

Poly(3-hydroxybutyrate) production by Bacillus cereus SPV using sugarcane molasses as the main carbon source

The main hindrance in the use of polyhydroxyalkanoates (PHAs) as a replacement for existing petroleum-based plastics is their high production cost. The carbon source accounts for 50% of the cost for PHA production. Thus, increasing the yield and productivity of PHAs on cheap substrates is an important challenge for biotechnologists to support the commercialization and further applications of these polymers. In this study, we have investigated the use of an agricultural raw material, sugarcane molasses, as the main carbon source for poly(3-hydroxybutyrate) (P(3HB)) production by Bacillus cereus SPV. These studies were carried out in both shaken flasks and 2 L bioreactors. Various conditions were evaluated for their effects on biomass and P(3HB) accumulation. A high polymer yield was obtained, 61.07% dry cell weight (DCW) in a 1 L shaken flask study and 51.37% DCW in a 2 L fermenter study. These yields are 50% higher than previously observed with Bacillus cereus SPV. Hence, the results are encouraging and show that sugarcane molasses are a promising carbon source for an economical and commercially viable production of P(3HB).     

Poly(3-hydroxybutyrate) synthesis by recombinant Escherichia coli arcA mutants in microaerobiosis

We assessed the effects of different arcA mutations on poly(3-hydroxybutyrate) (PHB) synthesis in recombinant Escherichia coli strains carrying the pha synthesis genes from Azotobacter sp. strain FA8. The arcA mutations used were an internal deletion and the arcA2 allele, a leaky mutation for some of the characteristics of the Arc phenotype which confers high respiratory capacity. PHB synthesis was not detected in the wild-type strain in shaken flask cultures under low-oxygen conditions, while ArcA mutants gave rise to polymer accumulation of up to 24% of their cell dry weight. When grown under microaerobic conditions in a bioreactor, the arcA deletion mutant reached a PHB content of 27% +/- 2%. Under the same conditions, higher biomass and PHB concentrations were observed for the strain bearing the arcA2 allele, resulting in a PHB content of 35% +/- 3%. This strain grew in a simple medium at a specific growth rate of 0.69 +/- 0.07 h(-1), whereas the deletion mutant needed several nutritional additives and showed a specific growth rate of 0.56 +/- 0.06 h(-1). The results presented here suggest that arcA mutations could play a role in heterologous PHB synthesis in microaerobiosis.     

Kinetic studies and biochemical pathway analysis of anaerobic poly-(R)-3-hydroxybutyric acid synthesis in Escherichia coli

Poly-(R)-3-hydroxybutyric acid (PHB) was synthesized anaerobically in recombinant Escherichia coli. The host anaerobically accumulated PHB to more than 50% of its cell dry weight during cultivation in either growth or nongrowth medium. The maximum specific PHB production rate during growth-associated synthesis was approximately 2.3 +/- 0.2 mmol of PHB/g of residual cell dry weight/h. The by-product secretion profiles differed significantly between the PHB-synthesizing strain and the control strain. PHB production decreased acetate accumulation for both growth and nongrowth-associated PHB synthesis. For instance under nongrowth cultivation, the PHB-synthesizing culture produced approximately 66% less acetate on a glucose yield basis as compared to a control culture. A theoretical biochemical network model was used to provide a rational basis to interpret the experimental results like the fermentation product secretion profiles and to study E. coli network capabilities under anaerobic conditions. For example, the maximum theoretical carbon yield for anaerobic PHB synthesis in E. coli is 0.8. The presented study is expected to be generally useful for analyzing, interpreting, and engineering cellular metabolisms.     

Microbial production of polyhydroxybutyrate with tailor-made properties: an integrated modelling approach and experimental validation

The microbial production of polyhydroxybutyrate (PHB) is a complex process in which the final quantity and quality of the PHB depend on a large number of process operating variables. Consequently, the design and optimal dynamic operation of a microbial process for the efficient production of PHB with tailor-made molecular properties is an extremely interesting problem. The present study investigates how key process operating variables (i.e., nutritional and aeration conditions) affect the biomass production rate and the PHB accumulation in the cells and its associated molecular weight distribution. A combined metabolic/polymerization/macroscopic modelling approach, relating the process performance and product quality with the process variables, was developed and validated using an extensive series of experiments and measurements. The model predicts the dynamic evolution of the biomass growth, the polymer accumulation, the consumption of carbon and nitrogen sources and the average molecular weights of the PHB in a bioreactor, under batch and fed-batch operating conditions. The proposed integrated model was used for the model-based optimization of the production of PHB with tailor-made molecular properties in Azohydromonas lata bacteria. The process optimization led to a high intracellular PHB accumulation (up to 95% g of PHB per g of DCW) and the production of different grades (i.e., different molecular weight distributions) of PHB.     

Production of PHB and P (3HB-co-3HV) biopolymers by <Emphasis Type="Italic">Bacillus megaterium</Emphasis> strain OU303A isolated from municipal sewage sludge

Bacillus megaterium strain OU303A isolated from municipal sewage sludge was selected for the study of biosynthesis of polyhydroxybutyrate (PHB) and polyhydroxybutyrate-co-hydroxyvalerate P (HB-co-HV) copolymer. The strain yielded a maximum of 62.43% DCW polymer in the medium containing glycerol as carbon source, which was followed by 58.63% DCW polymer in glucose containing medium. We found that this strain was capable of producing 2.5% hydroxyvalerate copolymer from a single carbon substrate, glucose. The strain showed an increase in the amount of HV monomer content, when the precursor for the copolymer was included in the fermentation medium. The characterization of the biopolymers was carried out using FTIR, GC-MS, H¹ NMR and DSC. This is the first report of B. megaterium strain producing HV copolymer, without the addition of any precursor in the fermentation medium.     

Poly(β-hydroxybutyric acid) thermoplastic production by Alcaligenes latus: Behavior of fed-batch cultures

Fed-batch culture of Alcaligenes latus, ATCC 29713, was investigated for producing the intracellular bioplastic poly(β–hydroxybutyric acid), PHB. Constant rate feeding, exponentially increasing feeding rate, and pH-stat fed batch methods were evaluated. pH-stat fed batch culture reduced or delayed accumulation of the substrate in the broth and led to significantly enhanced PHB productivity relative to the other modes of feeding. Presence of excessive substrate appeared to inhibit PHB synthesis, but not the production of cells. In fed-batch culture, the maximum specific growth rate (0.265?h^?1) greatly exceeded the value (0.075?h^?1) previously observed in batch culture of the same strain. Similarly, the maximum PHB production rate (up to 1.15?g?·?l^?1?·?h^?1) was nearly 8-fold greater than values observed in batch operations. Fed-batch operation was clearly superior to batch fermentation for producing PHB. A low growth rate was not a prerequisite for PHB accumulation, but a reduced or delayed accumulation of substrate appeared to enhance PHB accumulation. Under the best conditions, PHB constituted up to 63% of dry cell mass after 12?h of culture. The average biomass yield coefficient on sucrose was about 0.35, or a little less than in batch fermentations. The highest PHB concentrations attained were about 18?g?·?l^?1.     

Large-scale production and efficient recovery of PHB with desirable material properties, from the newly characterised Bacillus cereus SPV

A newly characterised Bacillus strain, Bacillus cereus SPV was found to produce PHB at a concentration of 38% of its dry cell weight in shaken flask cultures, using glucose as the main carbon source. Polymer production was then scaled up to 20 L batch fermentations where 29% dry cell weight of PHB was obtained within 48 h. Following this, a simple glucose feeding strategy was developed and the cells accumulated 38% dry cell weight of PHB, an increase in the overall volumetric yield by 31% compared to the batch fermentation. Sporulation is the cause of low PHB productivity from the genus Bacillus [Wu, Q., Huang, H., Hu, G.H., Chen, J., Ho, K.P., Chen, G.Q., 2001. Production of poly-3-hydroxybutyrate by Bacillus sp. JMa5 cultivated in molasses media. Antonie van Leeuwenhoek 80, 111-118]. However, in this study, acidic pH conditions (4.5-5.8) completely suppress sporulation, in accordance with Kominek and Halvorson [Kominek, L.A., Halvorson, H.O., 1965. Metabolism of poly-beta-hydroxybutyrate and acetoin in Bacillus cereus. J. Bacteriol. 90, 1251-1259], and result in an increase in the yield of PHB production. This observation emphasises the potential of the use of Bacillus in the commercial production of PHB and other PHAs. The recovery of the PHB produced was optimised and the isolated polymer characterised to identify its material properties. The polymer extracted, was found to have similar molecular weight, polydispersity index and lower crystallinity index than others reported in literature. Also, the extracted polymer was found to have desirable material properties for potential tissue engineering applications.     

Biotechnological conversion of agro-industrial wastewaters into biodegradable plastic, poly beta-hydroxybutyrate

Waste activated sludge generated from a combined dairy and food processing industry wastewater treatment plant was evaluated for its potential to produce biodegradable plastic, poly beta-hydroxybutyric acid (PHB). Deproteinized jowar grain-based distillery spentwash yielded 42.3% PHB production (w/w), followed by filtered rice grain-based distillery spentwash (40% PHB) when used as substrates. Addition of di-ammonium hydrogen phosphate (DAHP) resulted in an increase in PHB production to 67% when raw rice grain-based spentwash was used. Same wastewater, after removal of suspended solids by filtration and with DAHP supplementation resulted in lower PHB production (57.9%). However, supplementing other wastes with DAHP led to a substantial decrease in PHB content in comparison to what was observed in the absence of DAHP.     

废弃活性污泥中产聚羟基脂肪酸酯菌株Bacillus sp. PB-3的发酵条件优化

通过尼罗红染色法结合荧光显微镜镜检,从废弃活性污泥中分离得到1株高产聚羟基脂肪酸酯(PHAs)的菌株Bacillus sp.PB-3,经气相色谱法鉴定该菌株胞内产物为聚β-羟基丁酸酯(PHB)。对培养基成分及发酵条件优化后,获得最佳培养方案:12 g/L的葡萄糖为C源,2 g/L的牛肉膏为N源,初始pH 7.5,培养基装液量80 mL,转速为200 r/min,37℃培养48 h,PHB质量分数可达菌体干质量的32.09%,比优化前提高30%。     

ENHANCED BIOSYNTHESIS OF POLY(3-HYDROXYBUTYRATE) FROM POTATO STARCH BY Bacillus cereus STRAIN 64-INS IN A LABORATORY-SCALE FERMENTER

To decrease the polyhydroxyalkanoate (PHA) production cost by supplying renewable carbon sources has been an important aspect in terms of commercializing this biodegradable polymer. The production of biodegradable poly(3-hydroxyalkanoates) (PHA) from raw potato starch by the Bacillus cereus 64-INS strain isolated from domestic sludge has been studied in a lab-scale fermenter. The bacterium was screened for the degradation of raw potato starch by a starch hydrolysis method and for PHA production by Nile blue A and Sudan black B staining. Shake-flask cultures of the bacterium with glucose [2% (w/v)] or raw potato starch [2% (w/v)] produced PHA of 64.35% and 34.68% of dry cell weight (DCW), respectively. PHA production was also carried out in a 5-L fermenter under control conditions that produced 2.78 g/L of PHA and PHA content of 60.53% after 21 hr of fermentation using potato starch as the sole carbon source. Gas chromatography–mass spectroscopy (GC-MS) analyses confirmed that the extracted PHA contained poly(3-hydroxybutyrate) (PHB) as its major constituent (>99.99%) irrespective of the carbon source used. The article describes, for what we believe to be the first time, PHB production being carried out without any enzymatic or chemical treatment of potato starch at higher levels by fermentation. More work is required to optimize the PHB yield with respect to starch feeding strategies.     

Banana waste as substrate for α-amylase production by Bacillus subtilis (CBTK 106) under solid-state fermentation

 Bacillus subtilis CBTK 106, isolated from banana wastes, produced high titres of α-amylase when banana fruit stalk was used as substrate in a solid-state fermentation system. The effects of initial moisture content, particle size, cooking time and temperature, pH, incubation temperature, additional nutrients, inoculum size and incubation period on the production of α-amylase were characterised. A maximum yield of 5 345 000 U mg^-1 min^-1 was recorded when pretreated banana fruit stalk (autoclaved at 121 °C for 60 min) was used as substrate with 70% initial moisture content, 400 μm particle size, an initial pH of 7.0, a temperature of 35 °C, and additional nutrients (ammonium sulphate/sodium nitrate at 1.0%, beef extract/peptone at 0.5%, glucose/sucrose/starch/maltose at 0.1% and potassium chloride/sodium chloride at 1.0%) in the medium, with an inoculum-to-substrate ratio of 10% (v/w) for 24 h. The enzyme yield was 2.65-fold higher with banana fruit stalk medium compared to wheat bran. Received: 18 April 1995/Received last revison: 6 May 1996/Accepted: 9 May 1996     

Comparison of recombinant Escherichia coli strains for synthesis and accumulation of poly-(3-hydroxybutyric acid) and morphological changes

A stable high-copy-number plasmid pSYL105 containing the Alcaligenes eutrophus polyhydroxyalkanoic acid (PHA) biosynthesis genes was constructed. This plasmid was transferred to seven Escherichia coli strains (K12, B, W, XL1-Blue, JM109, DH5alpha, and HB101), which were subsequently compared for their ability to synthesize and accumulate ploy- (3-hydroxybutyric acid) (PHB). Growth of recombinant cells and PHB synthesis were investigated in detail in Luria-Bertani (LB) medium containing 20 g/L glucose. Cell growth, the rate of PHB synthesis, the extent of PHB accumulation, the amount of glucose utilized, and the amount of acetate formed varied from one strain to another. XL1-Blue (pSYL105) and B (pSYL105) synthesized PHB at the fastest rate, which was ca. 0.2 g PHB/g true cell mass-h, and produced PHB up to 6-7 g/L. The yields of cell mass, true cell mass, and PHB varied considerably among the strains. The PHB yield of XL1-Blue (pSYL105) in LB plus 20 g/L glucose was as high as 0.369 g PHB/g glucose. Strains W (pSYL105) and K12 (pSYL105) accumulated the least amount of PHB with the lowest PHB yield at the lowest synthesis rate. JM109 (pSYL105) accumulated PHB to the highest extent (85.6%) with relatively low true cell mass (0.77 g/L). Considerable filamentation of cells accumulating PHB was observed for all strains except for K12 and W, which seemed to be due either to the overexpression of the foreign PHA biosynthesis enzymes or to the accumulation of PHB. (c) 1994 John Wiley & Sons, Inc.     

Cultivation engineering of microbial bioplastics production

Abstract Theoretical yields of poly- d (−)-3-hydroxybutyrate (PHB) from several carbon sources have been estimated from biochemical pathways leading to PHB. In estimating the yields, a special emphasis is made on recycling (or regeneration) of NADP⁺ which is the co-substrate of acetoacetyl-CoA reductase, one of three key enzymes involved in the biosynthesis of PHB. As a NADP⁺-regenerating enzyme, glucose-6-phosphate dehydrogenase or isocitrate dehydrogenase is conceived. Theoretical and observed yields have been compared when polyhydroxyalkanoates (PHA) were synthesized from methanol and from n -amyl alcohol by a methylotroph, Paracoccus denitrificans .
An equation, which predicts the overall yield of PHB when allowance is made for non-PHB biomass formation in actual bacterial PHB production, has been derived as a function of both theoretical yields and PHB content of the total dry cell mass. The ratio of the overall (yield) to be theoretical yield is roughly proportional to the PHB content. A novel specific PHB formation rate on the basis of the residual biomass (total biomass-PHB contained) was proposed. The specific PHB formation rate decreased according to a mono-molecular decay model whose decay constant depended solely on the C/N ratio of the feed solution. From this model, an equation has been derived to calculate the volumetric productivity of PHB on the assumption that the total amount of the residual biomass is unchanged in the nitrogen-deficient PHB formation phase. Also, a graphical procedure has been shown to calculate the volumetric productivity of PHB. A comparison has been made between several data of PHB productivities that have been calculated from the literature.     

The Effect of Energy Substrates on PHB Accumulation of Acidiphilium cryptum DX1-1

The effect of glucose and elemental sulfur on the growth and PHB accumulation of Acidiphilium cryptum DX1-1 was investigated. Meanwhile, the differential expressions of 19 genes related with PHB accumulation, sulfur metabolism and carbon fixed in heterotrophy, phytotrophy and mixotrophy were studied by RT-qPCR. The results showed that strain DX1-1 could accumulate PHB with sulfur as the energy substance and atmospheric CO₂ as carbon resource. Glucose could improve the growth of strain DX1-1 cultured in medium with sulfur as the energy substance, and almost all the key enzyme-encoding genes related with PHB, sulfur metabolism and carbon fixed were basically up-regulated. PHB polymerase (Arcy_3030), ribulose-bisphosphate carboxylase (Acry_0825), ribulose-phosphate-epimerase (Acry_0022), and cysteine synthase A (Acry_2560) played important role in PHB accumulation, the modified expression of which could influence the PHB yield. With CO₂ as carbon resource, the main initial substance of PHB accumulation for strain DX1-1 was acetyl-CoA, instead of acetate with the glucose as the carbon resource. Because of accumulating PHB by fixed atmospheric CO₂ while independent of light, A. cryptum DX1-1 may have specifically potential in production of PHB.