Synthesis of biodegradable polyesters by Gram negative bacterium isolated from Malaysian environment

A locally isolated Gram negative bacterium, Cupriavidus sp. USMAA9-39 was able to produce various types of biodegradable polyesters through a two-step cultivation process. These are copolymer poly(3-hydroxybutyrate-co-4-hydroxybutyrate) [P(3HB-co-4HB)], copolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] and terpolymer poly(3-hydroxybutyrate-co-3-hydroxyvalerate-co-4-hydroxybutyrate) [P(3HB-co-3HV-co-4HB)]. These polymers were synthesized by this bacterium when grown with a combination of some carbon sources. The biosynthesis of P(3HB-co-4HB) was achieved by using carbon sources such as γ-butyrolactone or 1,4-butanediol or by a combination of oleic acid with either γ-butyrolactone or 1,4-butanediol. Meanwhile, poly(3-hydroxybutyrate-co-3-hydroxyvalerate) was produced using 1-pentanol or valeric acid or by a combination of oleic acid with either 1-pentanol or valeric acid. When γ-butyrolactone or 1,4-butanediol with either valeric acid or 1-pentanol were used as mixed carbon sources, P(3HB-co-3HV-co-4HB) terpolymer were produced. The presence of 3HB, 3HV or/and 4HB monomers were confirmed by gas chromatography and nuclear magnetic resonance (NMR) spectroscopy.     

Purification and Characterization of Fungal Poly(3-hydroxybutyrate) Depolymerase from Paecilomyces lilacinus F4-5 and Enzymatic Degradation of Poly(3-hydroxybutyrate-co-3-hydroxyvalerate) Film

Summary Poly(3-hydroxybutyrate) [P(3HB)] depolymerase was purified from a poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)]-degrading fungus, Paecilomyces lilacinus F4-5 by hydrophobic and ion exchange column chromatography, and showed a molecular mass of 45 kDa. The optimum temperature and pH of the P(3HB) depolymerase were 50 °C and 7.0, respectively. The enzyme was stable for at least 30 min at temperatures below 40 °C, while the activity abruptly decreased over 55 °C. Enzymatic P(3HB-co-3HV) degradation showed a similar degradation pattern to that of film overlaid by fungal hyphae. It reflects that the fungal degradation of P(3HB-co-3HV) in soil is mainly caused by extracellular depolymerases.     

Fermentative production of P(3HB-co-3HV) from propionic acid by Alcaligenes eutrophus in fed-batch culture with pH-stat continuous substrate feeding method

The feeding of propionic acid for production of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) [P(3HB-co-3HV)] by Alcaligenes eutrophus ATCC17697 was optimized using a fed-batch culture system. The concentration of propionic acid was maintained at 3 g l^–1 as growth was inhibited by propionic acid in the broth. A pH-stat substrate feeding system was used in which propionic acid was fed automatically to maintain a pH of the culture broth at 7.0. By feeding a substrate solution containing 20% (w/v) propionic acid, 4.9% (w/v) ammonia water [at a molar ratio of carbon to nitrogen (C/N molar ratio) of 10] in cell growth phase, the concentration of propionic acid in the broth was maintained at 3 g l^–1 giving a specific growth rate of 0.4 h^–1. To promote P(3HB-co-3HV) production, two stage fed-batch culture which consisted of the stage for the cell growth and the stage for the P(3HB-co-3HV) accumulation was carried out. When the substrate solution whose C/N molar ratio was 50 was fed in P(3HB-co-3HV) accumulation phase, the cell concentration and the P(3HB-co-3HV) content in the cells reached 64 g l^–1 and 58% (w/w) in 55.5 h, respectively.     

Production of poly(3-hydroxybutyrate-<Emphasis Type="Italic">co</Emphasis>-3-hydroxyvalerate) P(3HB-<Emphasis Type="Italic">co</Emphasis>-3HV) with a broad range of 3HV content at high yields by <Emphasis Type="Italic">Burkholderia sacchari</Emphasis> IPT 189

The biosynthesis of poly(3-hydroxybutyrate-co-3-hydroxyvalerate) from sucrose and propionic acid by Burkholderia sacchari IPT 189 was studied using a two-stage bioreactor process. In the first stage, this bacterium was cultivated in a balanced culture medium until sucrose exhaustion. In the second stage, a solution containing sucrose and propionic acid as carbon source was fed to the bioreactor at various sucrose/propionic acid (s/p) ratios at a constant specific flow rate. Copolymers with 3HV content ranging from 40 down to 6.5 (mol%) were obtained with 3HV yield from propionic acid (Y _3HV/prop) increasing from 1.10 to 1.34 g g⁻¹. Copolymer productivity of 1 g l⁻¹ h⁻¹ was obtained with polymer biomass content rising up to 60% by increasing a specific flow rate at a constant s/p ratio. Increasing values of 3HV content were obtained by varying the s/p ratios. A simulation of production costs considering Y _3HV/prop obtained in the present work indicated that a reduction of up to 73% can be reached, approximating US$ 1.00 per kg which is closer to the value to produce P3HB from sucrose (US$ 0.75 per kg).     

The use of norbornene derivatives in the synthesis of conformationally constrained peptides and pseudo-peptides

Summary The desymmetrisation ofendo-norborn-5-ene-2,3-dicarboxylic anhydride by proline esters has been used to prepare conformationally constrained pseudo-peptides with two peptide chains parallel to one another. A Curtius rearrangement on the desymmetrication adduct produced the corresponding isocyanate which was used to prepare both a peptide incorporating anendo-2-amino-3-carboxy-norborn-5-ene unit, and a pseudo-peptide with two peptide chains parallel to one another but offset by the presence of a urea unit. The conformational analysis of the resulting peptides was carried out, and the norbornene unit was found to induce the formation of β-turns and parallel β-sheets.     

A new acylated flavonol diglycoside from <Emphasis Type="Italic">Atriplex littoralis</Emphasis>

A new acetylated flavonol glycoside: patuletin 3-O-[5′″-O-feruloyl-β-D-apiofuransyl (1′″→2′′)-β-D-glucopyranoside] (2), together with a known patuletin 3-O-β-D-glucopyranoside (1) were isolated from the aerial part of Artiplex littoralis L. (Chenopodiacease). Their structures were elcidated by acid hydrolysis and spectroscopic methods including UV, ¹H, ¹³C NMR and ESI-MS for both compounds, additionally 2D-NMR, HSQC, HMBC experiments were performed for 2.     

Biotechnological approaches for the production of polyhydroxyalkanoates in microorganisms and plants - a review

The increasing effect of non-degradable plastic wastes is a growing concern. Polyhydroxyalkanoates (PHAs), macromolecule-polyesters naturally produced by many species of microorganisms, are being considered as a replacement for conventional plastics. Unlike petroleum-derived plastics that take several decades to degrade, PHAs can be completely bio-degraded within a year by a variety of microorganisms. This biodegradation results in carbon dioxide and water, which return to the environment. Attempts based on various methods have been undertaken for mass production of PHAs. Promising strategies involve genetic engineering of microorganisms and plants to introduce production pathways. This challenge requires the expression of several genes along with optimization of PHA synthesis in the host. Although excellent progress has been made in recombinant hosts, the barriers to obtaining high quantities of PHA at low cost still remain to be solved. The commercially viable production of PHA in crops, however, appears to be a realistic goal for the future.     

Isolation and purification of proteins from the symbiosome membrane of yellow lupine root nodules

A unique feature of the symbiotic association between legume plants and rhizobia is the plant-derived membrane which separates the symbionts within root nodule; this membrane is termed the peribacteroid membrane (PBM). Although this membrane plays a vital role in facilitating transport and other processes in nodules, little is known about the proteins that are associated with and are an integral part of it. The objective of this work was to apply modern methods of protein purification to the characterisation of proteins of peribacteroid membrane from nodules of yellow lupine (Lupines luteus). The 17-kDa protein was isolated from purified peribacteroid membrane using size exclusion and ion exchange chromatography (FPLC). The N-terminal amino acid sequence of this protein was determined; the sequence does not match any of the previously reported lupine and other legume sequences. Following detergent solubilisation of purified peribacteroid membrane, integral proteins of 15 to 20 kDa were purified by size exclusion chromatography.