Sarote Sirisansaneeyakul

Screening of yeasts for production of xylitol from d-xylose

Abstract Candida mogii ATCC 18364 was selected for a xylitol producer ( Y P S =0.62 g/g ) from 11 strains of d -xylose utilizing yeasts. Systematic kinetic studies are presented for growth and xylitol formation in synthetic medium using d -xylose as the carbon and energy source. Xylitol is produced from d -xylose under aerobic as well as oxygen-limiting conditions, but not in the absence of oxygen. It can be seen from the exprimental results that the concentrations of d -xylose and dissolved oxygen have a strong influence on the yield and rate for product formation. A maximum product yield was obtained when initial d -xylose concentration and specific oxygen uptake rate were 53 g/l and 0.5 mmol O2/g/h, respectively. Kinetic studies of d -xylose uptake, d -xylose reductase and xylitol dehydrogenase were performed to explain the complex regulatory properties of C. mogii during aerobic and oxygen-limited xylitol formation.

Carbon-to-nitrogen ratio affects the biomass composition and the fatty acid profile of heterotrophically grown Chlorella sp. TISTR 8990 for biodiesel production

Chlorella sp. TISTR 8990 was cultivated heterotrophically in media with various initial carbon-to-nitrogen ratios (C/N ratio) and at different agitation speeds. The production of the biomass, its total fatty acid content and the composition of the fatty acids were affected by the C/N ratio, but not by agitation speed in the range examined. The biomass production was maximized at a C/N mass ratio of 29:1. At this C/N ratio, the biomass productivity was 0.68gL(-1)d(-1), or nearly 1.6-fold the best attainable productivity in photoautotrophic growth. The biomass yield coefficient on glucose was 0.62gg(-1) during exponential growth. The total fatty acids (TFAs) in the freeze-dried biomass were maximum (459mgg(-1)) at a C/N ratio of 95:1. Lower values of the C/N ratio reduced the fatty acid content of the biomass. The maximum productivity of TFAs (186mgL(-1)d(-1)) occurred at C/N ratios of 63:1 and higher. At these conditions, the fatty acids were mostly of the polyunsaturated type. Allowing the alga to remain in the stationary phase for a prolonged period after N-depletion, reduced the level of monounsaturated fatty acids and the level of polyunsaturated fatty acids increased. Biotin supplementation of the culture medium reduced the biomass productivity relative to biotin-free control, but had no effect on the total fatty acid content of the biomass.

Biosorption of nonylphenol on dead biomass of Rhizopus arrhizus encapsulated in chitosan beads

The nonylphenol (NP) biosorption and desorption potential for fungal biomass used under batch conditions was investigated using kinetics and isotherm models. Fungal biomass of Rhizopus arrhizus TISTR 3610 exhibited preferential uptake of NP, an endocrine disrupting chemicals. Sporangiospores, asexual spores, were immobilised in chitosan beads. The biosorption data of NP on the moist heat inactivated R. arrhizus-chitosan beads were analyzed using four popular adsorption isotherms and, by using non-linear least-regression with the solver add-in in Microsoft Excel, correlated in order with the Fritz-Schluender>Redlich-Peterson>Freundlich>Langmuir isotherms. The pseudo first-order kinetics was found to have the best fit with the experimental data. The diffusivity of NP in the R. arrhizus-chitosan beads was calculated using the shrinking core model, and the diffusivity values were in the ranges of 2.3736x10(-4)-1.8950x10(-4) cm(2) s(-1). Desorption to recover the adsorbed NP from the beads was performed in methanol and was best described using a pseudo second-order kinetic model.

Characterization of a new oxygen-insensitive azoreductase from Brevibacillus laterosporus TISTR1911: Toward dye decolorization using a packed-bed metal affinity reactor

This study reports the identification of a new bacterial azoreductase from Brevibacillus laterosporus TISTR1911, its heterologous production in Escherichia coli, the biochemical characterization and immobilization for use in dye biodegradation processes. The recombinant azoreductase (BrAzo) is a monomeric FMN oxygen-insensitive enzyme with a molecular mass of 23 kDa showing a broad specificity for the reduction of synthetic azo dyes. Double hexahistidine-tagged BrAzo was immobilized onto a nickel chelating column and methyl orange was used to assess its degradation potential using a packed-bed reactor. The dye degradation is described by an exponential model in a downstream batchwise continuous flow mode operated with recycling. The complete degradation of methyl orange (170 μM at 600 mL/h) was achieved in 3 h and continued over 9 cycles. Coupling the immobilized BrAzo with glucose dehydrogenase for NADH regeneration yielded a shorter 1.5 h-degradation period that was maintained throughout 16 cycles.

Production of theabrownins using a crude fungal enzyme concentrate.

Theabrownins were produced from infusions of sun-dried green tea leaves using a crude enzyme concentrate of Aspergillus tubingensis TISTR 3647. This fungus had been isolated from a solid state fermentation of Pu-erh type tea. The crude enzyme concentrate contained activities of peroxidase, catechol oxidase and laccase. The enzyme concentrate effectively oxidized the phenolic compounds in green tea infusion to theabrownins. A theabrownins concentration of 56.0g/L was obtained in 44h. The reaction mixture contained the green tea infusion and crude enzyme concentrate in the volume ratio of 1: 0.205. The tea infusion had been produced using 200g of tea leaves per liter of distilled water. The reaction was carried out in a stirred bioreactor at 37°C with an aeration rate of 1 vvm, an agitation speed of 250rpm and a controlled pH of 7.0. Peroxidase, catechol oxidase, and laccase acted synergistically to convert the phenolic compounds in green tea infusion to theabrownins. Previously, theabrownins had been produced from green tea infusions only by using live fungal cultures. Production using the microorganism-free enzyme concentrate was comparable to production using the fungus A. tubingensis TISTR 3647. The proposed novel production process using the fungal crude enzymes and green tea infusion, offers a more controlled, reproducible and highly productive option for commercial production of theabrownins.

Microbial production of poly-γ-glutamic acid

Poly-γ-glutamic acid (γ-PGA) is a natural, biodegradable and water-soluble biopolymer of glutamic acid. This review is focused on nonrecombinant microbial production of γ-PGA via fermentation processes. In view of its commercial importance, the emphasis is on l-glutamic acid independent producers (i.e. microorganisms that do not require feeding with the relatively expensive amino acid l-glutamic acid to produce γ-PGA), but glutamic acid dependent production is discussed for comparison. Strategies for improving production, reducing costs and using renewable feedstocks are discussed.

Lipase-Catalysed Polymerization of Lactic Acid and the Properties of the Polymer

Lipase-catalysed polymerization is an emerging green alternative method for the synthesis of polylactic acid (PLA) from lactic acid (LA) monomer. Use of the lipase catalyst avoids the need for potentially toxic chemical catalysts. The concentration of the lipase enzyme is one of several factors which influence the polymerization process. This paper reports on the effects of the lipase concentration on the characteristics of the low molecular weight polylactic acid (PLA) formed via lipase-catalyzed polymerization of lactic acid. The polylactic acid products made by this method are characterized by Fourier Transform Infrared Spectroscopy (FTIR). Low molecular weight polylactic acid could be successfully produced from commercial lactic acid by using the commercial lipase Lipozyme TL IM at 50 °C in a 5-hour reaction.

Furfural and glucose can enhance conversion of xylose to xylitol by Candida magnoliae TISTR 5663.

Xylitol production from xylose by the yeast Candida magnoliae TISTR 5663 was enhanced by supplementing the fermentation medium with furfural (300mg/L) and glucose (3g/L with an initial mass ratio of glucose to xylose of 1:10) together under oxygen limiting conditions. In the presence of furfural and glucose, the final concentration of xylitol was unaffected relative to control cultures but the xylitol yield on xylose increased by about 5%. Supplementation of the culture medium with glucose alone at an initial concentration of 3g/L, stimulated the volumetric and specific rates of xylose consumption and the rate of xylitol production from xylose. In a culture medium containing 30g/L xylose, 300mg/L furfural and 3g/L glucose, the volumetric production rate of xylitol was 1.04g/L h and the specific production rate was 0.169g/g h. In the absence of furfural and glucose, the volumetric production rate of xylitol was ∼35% lower and the specific production rate was nearly 30% lower. In view of these results, xylose-containing lignocellulosic hydrolysates contaminated with furfural can be effectively used for producing xylitol by fermentation so long as the glucose-to-xylose mass ratio in the hydrolysate does not exceed 1:10 and the furfural concentration is ≤300mg/L.

Benzoate-induced stress enhances xylitol yield in aerobic fed-batch culture of Candida mogii TISTR 5892

Production of the natural sweetener xylitol from xylose via the yeast Candida mogii TISTR 5892 was compared with and without the growth inhibitor sodium benzoate in the culture medium. Sodium benzoate proved to be an uncompetitive inhibitor in relatively poorly oxygenated shake flask aerobic cultures. In a better controlled aerobic environment of a bioreactor, the role of sodium benzoate could equally well be described as competitive, uncompetitive or noncompetitive inhibitor of growth. In intermittent fed-batch fermentations under highly aerobic conditions, the presence of sodium benzoate at 0.15gL(-1) clearly enhanced the xylitol titer relative to the control culture without the sodium benzoate. The final xylitol concentration and the average xylitol yield on xylose were nearly 50gL(-1) and 0.57gg(-1), respectively, in the presence of sodium benzoate. Both these values were substantially higher than reported for the same fermentation under microaerobic conditions. Therefore, a fed-batch aerobic fermentation in the presence of sodium benzoate is promising for xylitol production using C. mogii.

Ohmic heating pretreatment of algal slurry for production of biodiesel

Suspensions of the model microalga Chlorella sp. TISTR 8990 were pretreated by ohmic heating to facilitate release of lipids from the cells in subsequent extraction and lipase-mediated transesterification to biodiesel. After ohmic pretreatment, the moist biomass was suspended in a system of water, hexane, methanol and immobilized lipase for extraction of lipids and simultaneous conversion to biodiesel. The ohmic pretreatment was optimized using an experimental design based on Taguchi method to provide treated biomass that maximized the biodiesel yield in subsequent extraction-transesterification operation. The experimental factors were the frequency of electric current (5-105 Hz), the processing temperature (50-70 °C), the algal biomass concentration in the slurry (algal fresh weight to water mass ratio of 1-3) and the incubation time (1-3 min). Extraction-transesterification of the pretreated biomass was carried out at 40 °C for 24 h using a reaction systems of a fixed composition (i.e. biomass, hexane, methanol, water and immobilized enzyme). Compared to control (i.e. untreated biomass), the ohmic pretreatment under optimal conditions (5 Hz current frequency, 70 °C, 1:2 mass ratio of biomass to water, incubation time of 2-min) increased the rate of subsequent transesterification by nearly 2-fold.