The effects of sodium bisulfite in extraction of PHB by hypochlorite

Summary Molecular weight of PHB becomes low when using a hypochlorite extraction method for PHB separation. This disadvantage was overcome by adding sodium bisulfite which is an anti-oxidant. The molecular weight drop was decreased from 30 % to 14 % by adding sodium bisulfite. It was also found that raising the pH to 12 and the addition of a surfactant resulted in the improvement of the PHB purity.     

A novel biological recovery approach for PHA employing selective digestion of bacterial biomass in animals

Applied Microbiology and Biotechnology - Polyhydroxyalkanoate (PHA) is a family of microbial polyesters that is completely biodegradable and possesses the mechanical and thermal properties of some...     

Anaerobic digestion of microalgal biomass with ultrasonic disintegration

The use of photosynthetic microalgae for nutrient removal and biofuel production has been widely discussed. Anaerobic digestion of waste microalgal biomass to produce biogas is a promising technology for bioenergy production. However, the methane yield from this anaerobic process was limited because of the hard cell wall of Chlorella vulgaris. The use of ultrasound has proven to be successful at improving the disintegration and anaerobic biodegradability of Chlorella vulgaris. Ultrasonic pretreatment in the range of 5–200 J ml⁻¹ was applied to waste microalgal biomass, which was then used for batch digestion. Ultrasound techniques were successful and showed higher soluble COD at higher applied energy. During batch digestion, cell disintegration due to ultrasound increased in terms of specific biogas production and the degradation rate. Compared to the untreated sample, the specific biogas production was increased in the ultrasound-treated sample by 90% at an energy dose of 200 J ml⁻¹. For the disintegrated samples, volatile solids reduction was also increased according to the energy input and degradation. These results indicate that the hydrolysis of microalgal cells is the rate-limiting step in the anaerobic digestion of microalgal biomass.     

Hypochlorite digestion method for efficient recovery of PHB from <Emphasis Type="Italic">Alcaligenes faecalis</Emphasis>

We reported the optimum amount of PHB accumulated by Alcaligenes faecalis during its 24 h growth under nitrogen deficient conditions. After 24 h incubation decrease in the amount of PHB was recorded. Hypochlorite digestion of biomass of organism followed by extraction with a solvent system consisting of 1:1 mixture of ethanol and acetone resulted in efficient recovery of PHB vis-à-vis earlier methods. This solvent system gave a high recovery yield, i.e. 5.6 gL⁻¹ vis-à-vis earlier reported yield, 1.34 gL⁻¹ (by same method), 0.63 gL⁻¹ (by chloroform extraction method) and 1.1 gL⁻¹ (by dispersion method).     

Structured modeling of the anaerobic digestion of biomass particulates

Anaerobic digestion of biological organic particulates to methane has been described by a structured mathematical model based on multiple-reaction stoichiometry, conventional material balances, and liquid phase equilibrium chemistry. A general stoichiometric treatment for any set of multiple biological reactions is derived based on a unit mass of oxggen equivalents of the reactions limiting substrate. The model agrees well with two existing experimental studies of anaerobic digestion of biomass particulates. Hypothetical computer simulations are presented to illustrate possible instabilities of the anaerobic process under various operating scenarios.     

Improved performance of anaerobic digestion ofSpirulina maxima algal biomass by addition of carbon-rich wastes

Mixtures of carbon-rich wastes andS. maxima algal biomass increase markedly the performance of anaerobic digestion. A mixture of 507 sewage sludge and algae increases the methane yield and the productivity over twofold. Peat hydrolyzate and sewage sludge, when added to algae, have shown a synergistic effect and spent sulfite liquor added at concentrations over 307 V/V has inhibited methanogenic activity.     

Detailed study of anaerobic digestion of Spirulina maxima algal biomass

Biomass of the blue-green alga Spirulina maxima was converted to methane using continuous stirred tank digesters with an energy conversion efficiency of 59%. Digesters were operated using once-a-day feeding with a retention time (theta) between 5 and 40 days, volatile solid concentrations (S(to)) between 20 and 100 kg VS/m(3), and temperatures between 15 and 52 degrees C. The results indicated a maximum methane yield of 0.35 m(3) (STP)/kg VS added at theta 30 days and S(to) 20 kg VS/m(3). Under such conditions, the energy conversion of the algal biomass to methane was 59%. The maximum methane production rate of 0.80 m(3) (STP)/m(3) day was obtained with theta= 20 days and S = 100 kg VS/m(3). The mesophilic condition at 35 degrees C produced the maximum methane yield and production rate. The process was stable and characterized by a high production of volatile acids (up to 23, 200 mg/L), alkalinity (up to 20, 000 mg/L), and ammonia (up to 7000 mg/L), and the high protein content of the biomass produced a well buffered environment which reduced inhibitory effects. At higher loading rates, the inhibition of methanogenic bacteria was observed, but there was no clear-cut evidence that such a phenomenon was due to nonionized volatile acids or gaseous ammonia. The kinetic analysis using the model proposed by Chen and Hashimoto indicated that the minimum retention time was seven days. The optimum retention time increased gradually from 11 to 16 days with an increase in the initial volatile solid concentration. The kinetic constant K decreased with the improvement in the digester performance and increased in parallel with the ammonia concentration in the culture media.     

Microbial and enzymatic improvement of anaerobic digestion of waste biomass

Metabolic activities of different microorganisms (Bacillus subtilis, B. licheniformis and Aspergillus niger) and hydrolytic enzymes (concentrations: 1 to 200 mg enzyme solids g^–1 feed) were studied individually and in combinations with respect to H₂ and methane production from damaged wheat grains. Bacillus subtilis, B. licheniformis and pre-existing hydrogen producers (control) produced 45 to 64 l H₂ kg^–1 total solids and subsequently, with the help of added methanogens, 155 to 220 l methane kg^–1 total solids could be produced. H₂ production from damaged wheat grains could be decreased to 28% or enhanced up to 152% with respect to control, by employing various microbial and enzymatic treatments. Similarly, it has been made possible to vary methane production capacities from as low as 17% to as high as 110% with respect to control.     

The recovery of poly(3-hydroxybutyrate) by using dispersions of sodium hypochlorite solution and chloroform

Summary To take advantage of both differential digestion by hypochlorite and solvent extraction, we used dispersions of sodium hypochlorite solution and chloroform in the recovery of microbial PHB. The treatment with hypochlorite alone caused such severe degradation and the molecular weight decreased drastically with increasing hypochlorite concentration. However, using the dispersion, the degradation of PHB was markedly diminished owing to theshielding effect of chloroform. In this case, we could obtain PHB of above 97% purity with a number average molecular weight of 1,000,000 comparable to the original molecular weight of 1,200,000.     

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.     

生物合成材料聚β-羟基丁酸(PHB)的研究进展

聚β-羟基丁酸(PHB)是原核微生物在碳、氮营养失衡的情况下,作为碳源和能源贮存在生物体内的一类热塑性聚酯.它作为微生物合成的可降解材料,除了具有与化学合成高分子相似的性质外,还具有一般化学合成高分子没有的性质,如光学活性好、透氧性低、抗紫外线辐射、生物可降解性、生物组织相容性、压电性和抗凝血性等,具有广阔的应用前景,越来越受到人们的关注.国内外的许多公司和科研机构纷纷开展可降解塑料的研发工作.着重介绍了PHB的理化性质、检测方法、生物合成、降解以及基因改良菌种方面的研究进展,同时对其应用、目前存在的问题以及可能的解决方案进行了讨论.     

Increased PHB productivity by high-cell-density fed-batch culture of Alcaligenes latus, a growth-associated PHB producer

Alcaligenes latus, a growth-associated PHB producer, was cultivated by a pH-stat modal fed-batch culture technique to attain high PHB productivity. Both sucrose solution and inorganic medium were fed in conjunction with the supply of ammonia solution which serves as a nitrogen source and as a means of pH control. Compositions of the inorganic medium were formulated by elemental analysis of A. latus cell mass. The effect on inoculum size was examined to reduce culture time. High concentrations of cell (142 g/L) and PHB (68.4 g/L) were obtained in a short culture time (18 h) with an inoculum size of 13.7 g/L. The PHB content and the PHB productivity at the end of the fed-batch culture were 50% of dry cell weight and 4.0 g PHB/(L . h), respectively. (c) 1996 John Wiley & Sons, Inc.     

Serum protein degradation by hypochlorite

The structural integrity of serum proteins: albumin, immunoglobulin G, transferrin, ceruloplasmin and superoxide dismutase, and the functional activity of the latter two enzymes after their interaction with hypochlorite were studied. It was shown that the interaction between the proteins and hypochlorite resulted in protein injury and degradation of their native structure. In the case of ceruloplasmin and transferrin, a practically complete protein "dissipation" occurred, the albumin and superoxide dismutase structures being injured in a lesser degree. The inactivation of ceruloplasmin was slower than that of superoxide dismutase. The protein degradation by hypochlorite seems to be the main factor restricting the ability of the proteins to act as antiinflammatory drugs.     

Ethanol production from biomass by repetitive solid-state fed-batch fermentation with continuous recovery of ethanol

To save cost and input energy for bioethanol production, a consolidated continuous solid-state fermentation system composed of a rotating drum reactor, a humidifier, and a condenser was developed. Biomass, saccharifying enzymes, yeast, and a minimum amount of water are introduced into the system. Ethanol produced by simultaneous saccharification and fermentation is continuously recovered as vapor from the headspace of the reactor, while the humidifier compensates for the water loss. From raw corn starch as a biomass model, 95 ± 3, 226 ± 9, 458 ± 26, and 509 ± 64 g l⁻¹ of ethanol solutions were recovered continuously when the ethanol content in reactor was controlled at 10–20, 30–50, 50–70 and 75–85 g kg-mixture⁻¹, respectively. The residue showed a lesser volume and higher solid content than that obtained by conventional liquid fermentation. The cost and energy for intensive waste water treatment are decreased, and the continuous fermentation enabled the sustainability of enzyme activity and yeast in the system.     

Collagen type II modification by hypochlorite

Oxidation of proteins is a common phenomenon in the inflammatory process mediated by highly reactive agents such as hypochlorite (HOCl/OCl(-)) produced by activated neutrophils. For instance, in rheumatoid arthritis hypochlorite plays an important role in joint destruction. One of the major targets for HOCl/OCl(-) is collagen type II (CII) - the primary cartilage protein. In our study, HOCl/OCl(-) mediated collagen II modifications were tested using various methods: circular dichroism (CD), HPLC, ELISA, dynamic light scattering (DLS), fluorimetry and spectrophotometry. It was shown that hypochlorite action causes deamination with consecutive carbonyl group formation and transformation of tyrosine residues to dichlorotyrosine. Moreover, it was shown that ammonium chloramine (NH(2)Cl) formed in the reaction mixture reacts with CII. However, in this case the yield of carbonyl groups and dichlorotyrosine is lower than that observed for HOCl/OCl(-) by 50%. CD data revealed that collagen II exists as a random coil in the samples and that chlorination is followed by CII fragmentation. In the range of low HOCl/OCl(-) concentrations (up to 1 mM) 10-90 kDa peptides are predominant whereas massive production of shorter peptides was observed for high (5 mM) hypochlorite concentration. DLS measurements showed that chlorination with HOCl/OCl(-) decreases the radius of collagen II aggregates from 30 to 6.8 nm. Taking into account the fact that chlorinated collagen is partially degraded, the DLS results suggest that smaller micelles are formed of the 10-90 kDa peptide fraction. Moreover, collagen chlorination results in epitope modification which affects CII recognition by anti-CII antibodies. Finally, since in the synovial fluid the plausible hypochlorite concentration is smaller than that used in the model the change of size of molecular aggregates seems to be the best marker of hypochlorite-mediated collagen oxidation.     

High rate anaerobic digestion of a petrochemical wastewater using biomass support particles

Anaerobic digestion of wastewater from a dimethyl terephthalate plant was studied in continuously stirred tank reactors with plastic net biomass support particles (BSP) at a level of 20% (v/v). The experimental results showed that the BSP system could treat the wastewater at a hydraulic retention time as low as 1.5 d, organic loading as high as 20 kg COD/m3/d and at acidic feed pH as low as 4.5 with 95% COD reduction and biogas production of about 8l/l/d, while the control system without support particles could not treat the wastewater above a 5-d hydraulic retention time, 5 kg COD/m3/d organic loading and a feed pH of 6.0. Thus, augmentation of BSP upgraded the performance of the conventional suspended growth system to an equivalent level to advanced reactors.     

Hydrolysis of native poly(hydroxybutyrate) granules (PHB), crystalline PHB, and artificial amorphous PHB granules by intracellular and extracellular depolymerases.

Native poly(hydroxybutyrate) (PHB) granules, purified PHB and artificial amorphous PHB granules were examined as putative substrates for hydrolysis by the intracellular depolymerase system of Rhodospirillum rubrum and the extracellular depolymerase of Pseudomonas lemoignei. The R. rubrum depolymerizing system requires pretreatment of granules with a heat stable 'activator' fraction; the activator can be replaced by mild trypsin treatment. Artificial granules were prepared with a cationic detergent, cetyltrimethylammonium bromide (CTAB) and an anionic detergent, (sodium cholate). Cholate and CTAB PHB granules were hydrolyzed by both enzyme systems; however, some differences were noted. Cholate granules were hydrolyzed in the absence of the R. rubrum activator fraction. Activator was required for the hydrolysis of CTAB granules but could be replaced by heparin in the extracellular depolymerase system but not in the intracellular depolymerase system. A Triton X-114 extract of native PHB granules inhibited the hydrolysis of trypsin-activated granules by the intracellular depolymerase. The inhibition was reversed by the activator fraction. Detergent extracts of granules activated with the R. rubrum activator were unable to inhibit the hydrolysis of trypsin-activated granules. These data suggest that the activator acts to modify an inhibitor present on native granules.