Production,optimization and characterization of polyhydroxybutyrate,a biodegradable plastic by Bacillus spp.

Poly-β-hydroxybutyrate (PHB) is the intracellular lipid reserve accumulated by many bacteria. The most potent terrestrial bacterium Bacillus cereus SE-1 showed more PHB accumulating cells (22.1 and 40% after 48 and 72 h) than that of the marine Bacillus sp. CS-605 (5 and 33% after 48 and 72 h). Both the isolates harbored phbB gene and the characteristics C=O peak was observed in the extracted PHB by Fourier transformed infrared spectroscopy analysis. Maltose was found to be the most suitable carbon source for the accumulation of PHB in B. cereus SE-1. The extracted PHB sample from B. cereus SE-1 was blended with a thermoplastic starch (TS) and an increased thermoplasticity and decreased crystallinity were observed after blending in comparison to the standard PHB. The melting temperature (T_m), melting enthalpy (?Hf), and crystallinity (X_c) of the blended PHB sample were found to be 109.4 °C, 64.58 J/g, and 44.23%, respectively.     

钩端螺旋体聚Beta羟基丁酸(PHB)生物合成途径分析

【目的】致病型问号钩端螺旋体(问号钩体, Leptospira interrogans)和腐生型双曲钩体(L. biflexa)能够大量合成菌体内贮藏物, 这可能是钩体在营养贫瘠环境中长时间存活的主要原因之一。本研究对钩体聚Beta羟基丁酸(PHB)贮藏物进行定性定量测定, 通过基因组分析补充定义PHB合成主要功能基因, 并采用分子生物学方法初步证明PHB合成途径的完整性, 为进一步研究PHB合成与钩体抗逆能力的关系奠定基础。【方法】采用脂类特异性尼罗红染色法和浓硫酸氧化-紫外分光光度计测定法, 对问号钩体和双曲钩体的PHB贮藏物进行定性定量测定; 采用生物信息学方法(BLAST和InterProscan/InterPro2Go), 通过同源性分析和功能结构域搜索寻找钩体基因组中的PHB合成相关基因; 最后采用克隆测序和定量RT-PCR技术检测相关基因表达情况, 初步验证生物信息学预测结果。【结果】尼罗红染色和氧化后比色定量实验证明钩体合成细菌常见贮藏物PHB, 问号钩体合成量为菌体干重的42%?45%, 双曲钩体合成量为64%?68%。尽管已公布的多个钩体基因组中均没有定义完整的PHB合成途径, 但本研究通过综合生物信息学分析, 在问号钩体和双曲钩体中鉴定了PHB合成途径的主要功能基因(phbC)。克隆测序和定量RT-PCR证实钩体转录表达大部分PHB合成相关基因(phbA/B/C), 说明钩体内该生物途径基本完整, 且部分高水平表达基因可能是钩体主要的PHB合成相关基因。【结论】问号钩体和双曲钩体均可合成PHB贮藏物, 且具有基本完整的PHB合成生物途径。     

Upstream process optimization of polyhydroxybutyrate (PHB) by Alcaligenes latus using two-stage batch and fed-batch fermentation strategies

This research focused on optimizing the upstream process time for production of polyhydroxybutyrate (PHB) from sucrose by two-stage batch and fed-batch fermentation with Alcaligenes latus ATCC 29714. The study included selection of strain, two-stage batch fermentations with different time points for switching to nitrogen limited media (14, 16 or 18?h) and fed-batch fermentations with varied time points (similar to two stage) for introducing nitrogen limited media. The optimal strain to produce PHB using sucrose as carbon source was A. latus ATCC 29714 with maximum-specific growth rate of 0.38?±?0.01?h^?1 and doubling time of 1.80?±?0.05?h. Inducing nitrogen limitation at 16?h and ending second stage at 26?h gave optimal performance for PHB production, resulting in a PHB content of 46.7?±?12.2?% (g PHB per g dry cell weight) at the end of fermentation. This was significantly higher (P?≤?0.05) (approximately 7?%) than the corresponding fed batch run in which nitrogen limitation was initiated at 16?h.     

Production of tyrosinase by Auricularia auricula using low cost fermentation medium

Low cost fermentation media using agricultural by-products (wheat bran extract, rice bran extract and soybean meal extract) as a major nutrient source, were evaluated for the production of tyrosinase from the fungus Auricularia auricula in submerged culture. In single-factor experiments, three components (wheat bran extract, casein and CuSO₄) were chosen to further optimize medium composition using response surface methodology (RSM). The central composite experimental results showed the following optimum medium composition: wheat bran extract 36.0 %, casein 1.1 g/l and CuSO₄ 0.13 g/l. Under these conditions, the highest tyrosinase activity was 17.22 U/ml, which was 2.1 fold higher than that obtained using the non-optimized medium. The present study is the first to report the statistical optimization of medium composition for production of tyrosinase by A. auricula using cheaper wheat bran extract as a major nutrient source. These results might provide a reference for the development of a cost-effective medium for commercial production of tyrosinase.     

Novel and economical purification of recombinant proteins: intein-mediated protein purification using in vivo polyhydroxybutyrate (PHB) matrix association

This work combines two well-established technologies to generate a breakthrough in protein production and purification. The first is the production of polyhydroxybutyrate (PHB) granules in engineered strains of Escherichia coli. The second is a recently developed group of self-cleaving affinity tags based on protein splicing elements known as inteins. By combining these technologies with a PHB-specific binding protein, a self-contained protein expression and purification system has been developed. In this system, the PHB-binding protein effectively acts as an affinity tag for desired product proteins. The tagged product proteins are expressed in E. coli strains that also produce intracellular PHB granules, where they bind to the granules via the PHB-binding tag. The granules and attached proteins can then be easily recovered following cell lysis by simple mechanical means. Once purified, the product protein is self-cleaved from the granules and released into solution in a substantially purified form. This system has been successfully used at laboratory scale to purify several active test proteins at reasonable yield. By allowing the bacterial cells to effectively produce both the affinity resin and tagged target protein, the cost associated with the purification of recombinant proteins could be greatly reduced. It is expected that this combination of improved economics and simplicity will constitute a significant breakthrough in both large-scale production of purified proteins and enzymes and high-throughput proteomics studies of peptide libraries.     

Recovery of polyhydroxybutyrate (PHB) from Cupriavidus necator biomass by solvent extraction with 1,2‐propylene carbonate

An integrated procedure for the recovery of polyhydroxybutyrate (PHB) produced by Cupriavidus necator based on the extraction with 1,2‐propylene carbonate was evaluated. The effect of temperature (100–145°C) and contact time (15–45 min), precipitation period, and biomass pretreatments (pH shock and/or thermal treatments) on PHB extraction efficiency and polymer properties was evaluated. The highest yield (95%) and purity (84%) were obtained with the combination of a temperature of 130°C and a contact time of 30 min, with a precipitation period of 48 h. Under these conditions, PHB had a molecular weight of 7.4×10⁵, which was the highest value obtained. Lower values (2.2×10⁵) were obtained for higher temperatures (145°C), while lower temperatures resulted in incomplete extraction yields (45–54%). No further yield improvement was achieved with the pH/heat pretreatments, but the polymer's molecular weight was increased to 1.3×10⁶. The PHB physical properties were not significantly affected by any of the tested procedures, as shown by the narrow ranges obtained for the glass transition temperature (4.8–5.0°C), melting temperature (170.1–180.1°C), melting enthalpy (77.8–88.5 J/g) and crystallinity (55–62%). 1,2‐Propylene carbonate was shown to be an efficient solvent for the extraction of PHB from biomass. The precipitation procedure was found to highly influence the polymer recovery and its molecular weight. Although polymer molecular weight and purity were improved by applying pH/heat pretreatment to the biomass, the procedure involves the use of large amounts of chemicals, which increases the recovery costs and makes the process environmentally unfriendly.     

Lipases provide a new mechanistic model for polyhydroxybutyrate (PHB) synthases: characterization of the functional residues in Chromatium vinosum PHB synthase

Polyhydroxybutyrate (PHB) synthases catalyze the conversion of beta-hydroxybutyryl coenzyme A (HBCoA) to PHB. These enzymes require an active site cysteine nucleophile for covalent catalysis. A protein BLASTp search using the Class III Chromatium vinosum synthase sequence reveals high homology to prokaryotic lipases whose crystal structures are known. The homology is very convincing in the alpha-beta-elbow (with the active site nucleophile)-alpha-beta structure, residues 131-175 of the synthase. A conserved histidine of the Class III PHB synthases aligns with the active site histidine of the lipases using the ClustalW algorithm. This is intriguing as this histidine is approximately 200 amino acids removed in sequence space from the catalytic nucleophile. Different threading algorithms suggest that the Class III synthases belong to the alpha/beta hydrolase superfamily which includes prokaryotic lipases. Mutagenesis studies were carried out on C. vinosum synthase C149, H331, H303, D302, and C130 residues. These studies reveal that H331 is the general base catalyst that activates the nucleophile, C149, for covalent catalysis. The model indicates that C130 is not involved in catalysis as previously proposed [Müh, U., Sinskey, A. J., Kirby, D. P., Lane, W. S., and Stubbe, J. (1999) Biochemistry 38, 826-837]. Studies with D302 mutants suggest D302 functions as a general base catalyst in activation of the 3-hydroxyl of HBCoA (or a hydroxybutyrate acyl enzyme) for nucleophilic attack on the covalently linked thiol ester intermediate. The relationship of the lipase model to previous models based on fatty acid synthases is discussed.     

Model-based intensification of a fed-batch microbial process for the maximization of polyhydroxybutyrate (PHB) production rate

An integrated metabolic–polymerization–macroscopic model, describing the microbial production of polyhydroxybutyrate (PHB) in Azohydromonas lata bacteria, was developed and validated using a comprehensive series of experimental measurements. The model accounted for biomass growth, biopolymer accumulation, carbon and nitrogen sources utilization, oxygen mass transfer and uptake rates and average molecular weights of the accumulated PHB, produced under batch and fed-batch cultivation conditions. Model predictions were in excellent agreement with experimental measurements. The validated model was subsequently utilized to calculate optimal operating conditions and feeding policies for maximizing PHB productivity for desired PHB molecular properties. More specifically, two optimal fed-batch strategies were calculated and experimentally tested: (1) a nitrogen-limited fed-batch policy and (2) a nitrogen sufficient one. The calculated optimal operating policies resulted in a maximum PHB content (94% g/g) in the cultivated bacteria and a biopolymer productivity of 4.2 g/(l h), respectively. Moreover, it was demonstrated that different PHB grades with weight average molecular weights of up to 1513 kg/mol could be produced via the optimal selection of bioprocess operating conditions.

     

Development of a structured dynamic model for the production of polyhydroxybutyrate (PHB) in Azohydromonas lata cultures

The development of an accurate model representation of the fermentative production of polyhydroxybutyrate (PHB) is a prerequisite for the optimal operation and control of the microbial process. In the present work, a macroscopic model is developed to quantify the intracellular production of PHB in Azohydromonas lata bacteria. The proposed two-compartment structured model provides an accurate prediction of the metabolic and macroscopic phenomena occurring in A. lata bacterial cultures. Precisely, the proposed dynamic model accounts for biomass growth, polymer accumulation, carbon and nitrogen sources utilization and oxygen mass transfer rates. It is shown that the model can closely describe the time evolution of the bacterial culture via its direct comparison with experiments performed in flasks or/and a bioreactor. Moreover, it is shown that the model can be used as a simulation tool for process optimization and scaling-up studies of the PHB fermentative production in A. lata cultures.     

Production of green biodegradable plastics of poly(3-hydroxybutyrate) from renewable resources of agricultural residues

This work describes potential opportunities for utilization of agro-industrial residues to produce green biodegradable plastics of poly(3-hydroxybutyrate) (PHB). Wheat straws were examined with good efficacy of carbon substrates using Cupriavidus necator. Production was examined in separate hydrolysis and fermentation (SHF) in the presence and absence of WS hydrolysis enzymes, and in simultaneous saccharification and fermentation (SSF) with enzymes. Results showed that production of PHB in SSF was more efficient in terms of viable cell count, cell dry weight, and PHB production and yield compared to those of SHF and glucose-control cultures. While glucose control experiment produced 4.6 g/L PHB; SSF produced 10.0 g/L compared to 7.1 g/L in SHF when utilizing enzymes during WS hydrolysis. Results showed that most of sugars produced during the hydrolysis were consumed in SHF (~98 %) compared to 89.2 % in SSF. Results also demonstrated that a combination of glucose and xylose can compensate for the excess carbon required for enhancing PHB production by C. necator. However, higher concentration of sugars at the beginning of fermentation in SHF can lead to cell inhibition and consequently catabolite repressions. Accordingly, results demonstrated that the gradual release of sugars in SSF enhanced PHB production. Moreover, the presence of sugars other than glucose and xylose can eliminate PHB degradation in medium of low carbon substrate concentrations in SSF.     

Production of poly-beta-hydroxybutyrate (PHB) by Vibrio spp. isolated from marine environment

Bacteria isolated from marine sediments were screened for their ability to accumulate polyhydroxyalkanoates. Among the isolates, four Vibrio spp. (strain M11, M14, M20 and M31) were studied in detail. All synthesized intracellular lipid inclusions during growth on diverse carbon sources including acetate, glycerol, succinate, glucose and sucrose. The inclusions were identified to be poly-beta-hydroxybutyrate (PHB) using gas chromatography and nuclear magnetic resonance analysis. No other type of polyhydroxyalkanoates (PHAs) was found to be accumulated by these marine isolates, suggesting that the diversity of PHAs produced in marine environments may be not as versatile as found in other environments. Strain M11 accumulated PHB in concentrations as high as 41% of cell dry weight when grown in medium containing 4% of sodium chloride. One of the Vibrio spp. was identified to be closely related to Vibrio natriegens (98% identity) by partial 16S rDNA sequence homology. V. natriegens has the shortest generation time (9.8 min) of any bacterium and this characteristic may be an exploitable trait for the industrial production of PHB.     

Enhanced polyhydroxybutyrate (PHB) production via the coexpressed phaCAB and vgb genes controlled by arabinose PBAD promoter in Escherichia coli

Aim: To develop an approach to enhance polyhydroxybutyrate (PHB) production via the coexpressed phaCAB and vgb genes controlled by arabinose P_BAD promoter in Escherichia coli. Method and Results: The polyhydroxyalkanoates (PHAs) synthesis operon, (phaCAB), from Ralstonia eutropha was overexpressed under the regulation of the arabinose P_BAD promoter in Escherichia coli, and the vgb gene encoding bacterial haemoglobin from Vitreoscilla stercoraria (VHb) was further cloned at downstream of phaCAB to form an artificial operon. The cell dry weight (CDW), PHB content and PHB concentration were enhanced around 1·23‐, 1·57‐, and 1·93‐fold in the engineered cell harbouring phaCAB–vgb (SY‐2) upon 1% arabinose induction compared with noninduction (0% arabinose). Furthermore, by using a recombinant strain harbouring P_BAD promoter‐vgb along with native promoter‐phaCAB construction, the effect of vgb expression level on PHB biosynthesis was positive correlation. Conclusions: The results exploit the possibility to improve the PHB production by fusing the genes phaCAB–vgb from different species under the arabinose regulation system in E. coli. It also demonstrates that increase in VHb level enhances the PHB production. Significance and Impact of the Study: We were successful in providing a new coexpressed system for PHB synthesis in E. coli. This coexpressed system could be regulated by arabinose inducer, and is more stable and cheaper than other induced systems (e.g. IPTG). Furthermore, it could be applied in many biotechnology or fermentation processes.     

Production of targeted poly(3-hydroxyalkanoates) copolymers by glycogen accumulating organisms using acetate as sole carbon source

One of the main limitations in bacterial polyhydroxyalkanoate (PHA) production with mixed cultures is the fact that primarily polyhydroxybutyrate (PHB) homopolymers are generated from acetate as the main carbon source, which is brittle and quite fragile. The incorporation of different 3-hydroxyalkanoate (HA) components into the polymers requires the addition of additional carbon sources, leading to extra costs and complexity. In this study, the production of poly(3-hydroxybutyrate (3HB)-co-3-hydroxyvalerate (3HV)-co-3-hydroxy-2-methylvalerate (3HMV)), with 7-35C-mol% of 3HV fractions from acetate as the only carbon source was achieved with the use of glycogen accumulating organisms (GAOs). An enriched GAO culture was obtained in a lab-scale reactor operated under alternating anaerobic and aerobic conditions with acetate fed at the beginning of the anaerobic period. The production of PHAs utilizing the enriched GAO culture was investigated under both aerobic and anaerobic conditions. A polymer content of 14-41% of dry cell weight was obtained. The PHA product accumulated by GAOs under anaerobic conditions contained a relatively constant proportion of non-3HB monomers (30+/-5C-mol%), irrespective of the amount of acetate assimilated. In contrast, under aerobic conditions, GAOs only produced 3HB monomers from acetate causing a gradually decreasing 3HV fraction during this aerobic feeding period. The PHAs were characterized by gel permeation chromatography (GPC) and differential scanning calorimetry (DSC). The data demonstrated that the copolymers possessed similar characteristics to those of commercially available poly(3HB-co-3HV) (PHBV) products. The PHAs produced under solely anaerobic conditions possessed lower melting points and crystallinity, higher molecular weights, and narrower molecular-weight distributions, compared to the aerobically produced polymers. This paper hence demonstrates the significant potential of GAOs to produce high quality polymers from a simple and cheap carbon source, contributing considerably to the growing research body on bacterial PHA production by mixed cultures.     

Unraveling the function of the Rhodospirillum rubrum activator of polyhydroxybutyrate (PHB) degradation: the activator is a PHB-granule-bound protein (phasin)

Efficient hydrolysis of native poly(3-hydroxybutyrate) (nPHB) granules in vitro by soluble PHB depolymerase of Rhodospirillum rubrum requires pretreatment of nPHB with an activator compound present in R. rubrum cells (J. M. Merrick and M. Doudoroff, J. Bacteriol. 88:60-71, 1964). Edman sequencing of the purified activator (17.4 kDa; matrix-assisted laser desorption ionization-time of flight mass spectrometry) revealed identity to a hypothetical protein deduced from a partially sequenced R. rubrum genome. The complete activator gene, apdA (activator of polymer degradation), was cloned from genomic DNA, expressed as a six-His-tagged protein in recombinant Escherichia coli (M(r), 18.3 x 10(3)), and purified. The effect of ApdA on PHB metabolism was studied in vitro and in vivo. In vitro, the activity of the activator could be replaced by trypsin, but recombinant ApdA itself had no protease activity. Comparative sodium dodecyl sulfate-polyacrylamide gel electrophoresis analysis of the protein patterns of trypsin- and ApdA-treated nPHB granules isolated from different PHB-accumulating bacteria showed that trypsin activated nPHB by removing proteins of the surface layer of nPHB regardless of the origin of nPHB, but ApdA bound to and interacted with the surface layer of nPHB in a nonproteolytic manner, thereby transforming nPHB into an activated form that was accessible to the depolymerase. In vivo, expression of ApdA in E. coli harboring the PHB biosynthetic genes, phaCBA, resulted in significant increases in the number and surface/volume ratio of accumulated PHB granules, which was comparable to the effect of phasin proteins, such as PhaP in Ralstonia eutropha. The amino acid sequence of ApdA was 55% identical to the amino acid sequence of Mms16, a magnetosome-associated protein in magnetotactic Magnetospirillum species. Mms16 was previously reported to be a GTPase with an essential function in magnetosome formation (Y. Okamura, H. Takeyama, and T. Matsunaga, J. Biol. Chem. 276:48183-48188, 2001). However, no GTPase activity of ApdA could be demonstrated. We obtained evidence that Mms16 of Magnetospirillum gryphiswaldense can functionally replace ApdA in R. rubrum. Fusions of apdA and mms16 to gfp or yfp were functionally expressed, and both fusions colocalized with PHB granules after conjugative transfer to R. rubrum. In conclusion, ApdA in vivo is a PHB-bound, phasin-like protein in R. rubrum. The function of Mms16 in magnetotactic bacteria requires further clarification.     

Microbial synthesis of rhamnolipids by Pseudomonas aeruginosa (ATCC 10145) on waste frying oil as low cost carbon source

Vegetable edible oils and fats are mainly used for frying purposes in households and the food industry. The oil undergoes degradation during frying and hence has to be replaced from time to time. Rhamnolipids are produced by microbial cultivation using refined vegetable oils as a carbon source and Pseudomonas aeruginosa (ATCC 10145). The raw material cost accounts for 10-30% of the overall cost of biosurfactant production and can be reduced by using low-cost substrates. In this research, attention was focused on the preparation of rhamnolipids, which are biosurfactants, using potential frying edible oils as a carbon source via a microbial fermentation technique. The use of low-cost substrates as a carbon source was emphasized to tilt the cost of production for rhamnolipids. The yield was 2.8 g/L and 7.5 g/L from waste frying oil before and after activated earth treatment, respectively. The crude product contained mainly dirhamnolipids, confirmed by thin-layer chromatography (TLC), high-performance liquid chromatography (HPLC), liquid chromatography-mass spectroscopy (LC-MS), and (1)H-nuclear magnetic resonance (NMR). Hence, the treatment can be used to convert waste frying oil as a low-cost substrate into a cost-effective carbon source.     

合成聚β-羟基丁酸(PHB)鞘细菌的分离、鉴定与筛选

通过富集培养和划线分离等手段从活性污泥中分离筛选到一株合成PHB鞘细菌FQ4 0 ,其生物学特征为 :杆菌 ,大小 (0 .6～ 1.5 ) μm× (1.5～ 5 .5 ) μm ;革兰氏染色阴性 ;具衣鞘 ,丝状体很长 ,偶见假分枝 ;亚端生鞭毛 ;胞内具PHB颗粒 ;菌落为光滑型和丝状型两种。经鉴定该菌株为鞘细菌类球衣菌属中的浮游球衣菌 (Sphaerotilusnatans)。对其合成PHB研究表明 :细胞内可积累大量的PHB颗粒 ,含量可达细胞干重的 30 .5 %。     

Production of gold nanoparticles by biogenesis using bacteria

Diazotrophic cyanobacteria Anabaena sp. PCC 7120, four Nostoc strains, and two Azotobacter species (A. vinelandii and A. chroococcum) were found to produce gold nanoparticles (GNP) under nitrogen fixation conditions. GNP biogenesis occurred at AuHCl₄ concentrations from 0.1 to 1 mM. In the cultures of unicellular cyanobacteria Synechococcus sp. PCC 7942 and Synechocystis sp. PCC 6803 incapable of nitrogen fixation, no GNP were formed at the same concentrations of gold salts. The plasmon resonance band peak was located at 552 nm. This position is characteristic of spherical GNP 10 to 30 nm in size. Small amounts of GNP were also formed in the culture liquid supernatants of the tested nitrogen-fixing bacteria at AuHCl₄ concentrations from 0.25 to 0.5 mM.