Self-directing optimization of β-1,3-glucanase production by Trichoderma harzianum in batch culture

The self-directing optimization technique was employed to determine the optimal conditions for -1,3-glucanase production by Trichoderma harzianum in batch culture. A maximum -1,3-glucanase production of 0.910 U was obtained at a pH (controlled) of 4.9, an aeration rate of 0.9 1/(1)(min), and an agitator speed of 220 rev/min which were found to be the most suitable.     

Inulinase (β-fructofuranosidase) production by Kluyeromyces marxianus in batch culture

Summary Production of inulinase in batch fermentation using various carbon sources with Kluyermoyces marxianus was examined. Inulinase synthesis in the culture proceeded parallel to cell growth. Glucose, fructose and sucrose were inferior carbon sources for inulinase broduction. Highest production (212 U/mL) was achieved on inulin based media.     

The effect of dissolved oxygen tension on 11β- and 19-hydroxylation of Reichstein's Substance S by Pellicularia filamentosa

Summary The 11- and 19-hydroxylation enzyme(s) of Pellicularia filamentosa IFO 6298 have been shown to be inducible by Reichstein's Substance S. By using the protein synthesis inhibitor, cycloheximide, in fermenter culture the effects of dissolved oxygen tension (DOT) on enzyme induction and enzyme expression have been separately investigated. For both hydroxylations, an optimum DOT for induction has been shown at 15% of saturation, while the optimum for expression is at 30% of saturation. The results have been verified in the absence of cycloheximide. Thus, maximum rates of hydroxylation are achieved when induction is performed at low DOT, followed by elevation to ensure maximum expression.     

High yield purification of JNK1β1 and activation by in vitro reconstitution of the MEKK1 → MKK4 → JNK MAPK phosphorylation cascade

The c-Jun N-terminal kinase (JNK) pathway forms part of the mitogen-activated protein kinase (MAPK) signaling pathways comprising a sequential three-tiered kinase cascade. Here, an upstream MAP3K (MEKK1) phosphorylates and activates a MAP2K (MKK4 and MKK7), which in turn phosphorylates and activates the MAPK, JNK. The C-terminal kinase domain of MEKK1 (MEKK-C) is constitutively active, while MKK4/7 and JNK are both activated by dual phosphorylation of S/Y, and T/Y residues within their activation loops, respectively. While improvements in the purification of large quantities of active JNKs have recently been made, inadequacies in their yield, purity, and the efficiency of their phosphorylation still exist. We describe a novel and robust method that further improves upon the purification of large yields of highly pure, phosphorylated JNK1β1, which is most suitable for biochemical and biophysical characterization. Codon harmonization of the JNK1β1 gene was used as a precautionary measure toward increasing the soluble overexpression of the kinase. While JNK1β1 and its substrate ATF2 were both purified to >99% purity as GST fusion proteins using GSH-agarose affinity chromatography and each cleaved from GST using thrombin, constitutively-active MEKK-C and inactive MKK4 were separately expressed in E. coli as thioredoxin-His₆-tagged proteins and purified using urea refolding and Ni²⁺-IMAC, respectively. Activation of JNK1β1 was then achieved by successfully reconstituting the JNK MAPK activation cascade in vitro; MEKK-C was used to activate MKK4, which in turn was used to efficiently phosphorylate and activate large quantities of JNK1β1. Activated JNK1β1 was thereafter able to phosphorylate ATF2 with high catalytic efficiency.     

Kinetics and effect of nitrogen source feeding on production of poly-β-hydroxybutyric acid by fed-batch culture

Summary A kinetic study of the production of poly--hydroxybutyric acid (PHB) by a fed-batch culture of Protomonas extorquens showed that a nitrogen source was necessary even in the PHB production phase. The effect of ammonia feeding on PHB production was consequently investigated. The nitrogen source (ammonia water) was supplied at a low constant feeding rate after the growth phase in which cell mass concentration reached 60 g/l. Feeding with a small quantity of ammonia resulted in a more rapid increase in intracellular PHB content than was the case without ammonia feeding. Excessive feeding of ammonia, however, caused not only degradation of accumulated PHB but also reduction of microbial PHB synthetic activity.     

Optimization of uracil addition for curdlan (β-1→3-glucan) production by Agrobacterium sp.

Uracil, acting as a precursor of UDP-glucose, served as an activator on the production of curdlan with Agrobacterium sp. (ATCC 31750). The time of adding uracil was important to improve curdlan production. When uracil was added after ammonium depletion (at 26 h), it was used as a nitrogen source for cell growth. Although the cell concentration increased, the curdlan production was decreased. If uracil was added at 46 h, then uracil was degraded slowly but still activated curdlan production. With the addition of both sucrose (200 g) and uracil (1.5 g), the curdlan production was increased up to 93 g l^–1 after 160 h fermentation.     

Optimized methodology for extraction of (1 → 3)(1 → 6)-β-d-glucan from Saccharomyces cerevisiae and in vitro evaluation of the cytotoxicity and genotoxicity of the corresponding carboxymethyl derivative

The cell wall of Saccharomyces cerevisiae is an important source of β-d-glucan, a glucose homopolymer with immunostimulant properties. The standard methodologies described for its extraction involve acid and alkaline washings, which degrade part of its glucose chains and reduce the final yield. In the present study, an optimized methodology for extraction of β-d-glucan from S. cerevisiae cells, involving sonication and enzyme treatment, with a yield of 11.08 ± 0.19%, was developed. The high-purity (1 → 3)(1 → 6)-β-d-glucan was derivatized to carboxymethyl-glucan (CM-G). In vitro tests with CM-G in Chinese hamster epithelial cells (CHO-k1) did not reveal any cytotoxic or genotoxic effects or influences of this molecule on cell viability. The method described here is a convenient alternative for the extraction of (1 → 3)(1 → 6)-β-d-glucan under mild conditions without the generation of wastes that could be potentially harmful to the environment.     

The effect of temperature on growth and cellulase (β-1,4-endoglucanase) production in the compost fungusChaetomium thermophile var.dissitum

Chaetomium thermophile var.dissitum, isolated from an experimental urban refuse compost, had the following growth characteristics: Minimum temperature, 27±1°C; optimum, 45–50°C; maximum, 57±1°C; pH optimum 5.5–6.0.A number of carbohydrates could be used for growth, but cellulase formation measured with carboxymethylcellulose as substrate was initiated only on cellulose or xylan. With cellulose as the carbon source, cellulase accumulation in the culture filtrate followed closely that of growth, when the temperature was varied. pH optimum for the cellulase system was 5.0.The optimum temperature for cellulase activity with carboxymethylcellulose as substrate varied between 77°C with 1/2 h incubation time and 58°C with 10 h incubation time.With cotton as substrate, the optimum temperature was 58°C regardless of incubation time. Carboxymethylcellulose had a higher stabilizing effect on the enzyme than cotton. The temperature stability of the cellulase was highest at pH 6.0.     

The investigation of effect of organic carbon sources addition in anaerobic–aerobic (low dissolved oxygen) sequencing batch reactor for nutrients removal from wastewaters

The effect of addition of organic carbon sources (acetic acid and waste activated sludge alkaline fermentation liquid) on anaerobic–aerobic (low dissolved oxygen, 0.15–0.45 mg/L) biological municipal wastewater treatment was investigated. The results showed that carbon source addition affected not only the transformations of polyhydroxyalkanoates (PHA), glycogen, nitrogen and phosphorus, but the net removal of nitrogen and phosphorus. The removal efficiencies of TN and TP were, respectively, 61% and 61% without organic carbon source addition, 81% and 95% with acetic acid addition, and 83% and 97% with waste activated sludge alkaline fermentation liquid addition. It seems that the alkaline fermentation liquid of waste biosolids generated in biological wastewater treatment plant can be used to replace acetic acid as an additional carbon source to improve the anaerobic–aerobic (low dissolved oxygen) municipal wastewater nutrients removal although its use was observed to cause a slight increase of effluent BOD and COD concentrations.     

Cyclic (1→2)-β-d-Glucan-hydrolyzing Enzymes from Acremonium sp. 15 Purification and Some Properties of Endo-( 1 → 2)-α-d-glucanase and β-d-Glucosidase

Acremonium sp. 15 a fungus isolated from soil, produces an extracellular enzyme system degrading cyclic (1→2)-β-d-glucan. This enzyme was found to be a mixture of endo-(1→2)-β-d-glucanase and β-d-glucosidase. The (1→2)-β-d-glucanase was purified to homogeneity shown by disc-electrophoresis after SP-Sephadex column chromatography, Sephadex G-75 gel filtration, and rechromatography on SP-Sephadex. The molecular weight of the enzyme was 3.6 × 10⁴ by SDS-polyacrylamide gel electrophoresis. The isoelectric point of the enzyme was pH 9.6. The enzyme was most active at pH 4.0—4.5, and stable up to 40°C in 20 mm acetate buffer (pH 5.0) for 2 hr of incubation. This enzyme hydrolyzed only (l→2)-β-d-glucan and did not hydrolyze laminaran, curdlan, or CM-cellulose. The hydrolysis products from cyclic (1→2)-β-d-glucan were mainly sophorose.

The β-d-glucosidase was purified about 4000-fold. The rate of hydrolysis of the substrates by this β-d-glucosidase decreased in the following order: β-nitrophenyl-β-d-glucoside, sophorose, phenyl-β-d-glucoside, laminaribiose, and salicin. This enzyme has strong transfer action even at the low concentration of 0.75 mm substrate.     

Effect of levulinic acid on cell growth and poly-β-hydroxyalkanoate production by Alcaligenes sp. SH-69

Summary Following growth of Alcaligenes sp. SH-69 on glucose as a sole carbon source for the production of poly--hydroxyalkanoates (PHAs), relatively low levels of levulinic acid (LA) were detected. Experiments were carried out in batch and continuous culture, and the effects of LA addition on growth and PHA synthesis were determined. Significant stimulatory effects were observed, greater than those for propionic acid addition. In N-limited two stage continuous culture, a maximal PHA content of 38.3 % (w/w) was achieved with a polyhydroxyvalerate (PHV) content of 23.5 % (molar basis) at D=0.078 l/h. This resulted from the controlled addition of LA at 0.5 g/L/h in the presence of excess glucose.     

Paenibacillus curdlanolyticus B-6 xylanase Xyn10C capable of producing a doubly arabinose-substituted xylose, α-l-Araf-(1 → 2)-[α-l-Araf-(1 → 3)]-d-Xylp,from rye arabinoxylan

Paenibacillus curdlanolyticus B-6 Xyn10C is a single module xylanase consisting of a glycoside hydrolase family-10 catalytic module. The recombinant enzyme, rXyn10C, was produced by Escherichia coli and characterized. rXyn10C was highly active toward soluble xylans derived from rye, birchwood, and oat spelt, and slightly active toward insoluble wheat arabinoxylan. It hydrolyzed xylooligosaccharides larger than xylotetraose to produce xylotriose, xylobiose, and xylose. When rye arabinoxylan and oat spelt xylan were treated with the enzyme and the hydrolysis products were analyzed by thin layer chromatography (TLC), two unknown hydrolysis products, U1 and U2, were detected in the upper position of xylose on a TLC plate. Electrospray ionization mass spectrometry and enzymatic analysis using Bacillus licheniformis α-l-arabinofuranosidase Axh43A indicated that U1 was α-l-Araf-(1 → 2)-[α-l-Araf-(1 → 3)]-d-Xylp and U2 was α-l-Araf-(1 → 2)-d-Xylp, suggesting that rXyn10C had strong activity toward a xylosidic linkage before and after a doubly arabinose-substituted xylose residue and was able to accommodate an α-1,2- and α-1,3-linked arabinose-substituted xylose unit in both the −1 and +1 subsites. A molecular docking study suggested that rXyn10C could accommodate a doubly arabinose-substituted xylose residue in its catalytic site, at subsite −1. This is the first report of a xylanase capable of producing α-l-Araf-(1 → 2)-[α-l-Araf-(1 → 3)]-d-Xylp from highly arabinosylated xylan.     

Glycan modification of a thermostable recombinant (1-3,1-4)-β-glucanase secreted fromSaccharomyces cerevisiae is determined by strain and culture conditions

High level biosynthesis and secretion of the thermostable hybrid (1-3,1-4)--glucanase H(A16-M) has been achieved inSaccharomyces cerevisiae by means of the yeast vacuolar endoprotease B promoter (PRB1_p) and theBacillus macerans (1-3,1-4)--glucanase signal peptide. The N-glycans present on the yeast-secreted H(A16-M), denoted H(A16-M)-Y, were released by endoglycosidase H, and identified by proton NMR spectroscopy to be a homologous series of Man_8-13GlcNAc₂, although only traces of Man₉GlcNAc₂ were found. Therefore, processing of N-glycans on H(A16-M)-Y is similar to that on homologous proteins. Most of the N-glycans (88%) were neutral while the remainder were charged due to phosphorylation. Site-directed mutagenesis of Asn to Gln in two of the N-glycosylation sequons, and subsequent analysis of the N-glycans on the yeast-secreted proteins together with analysis of the N-glycans from the individual sites of H(A16-M)-Y suggest the presence of steric hindrance to glycan modification by the glycans themselves. H(A16-M)-Y produced under control of either the yeast protease B or the yeast 3-phosphoglycerate kinase promoter, each in two differentSaccharomyces strains revealed a dependence of N-glycan profile on both strain and culture conditions. The extent of O-glycosylation was found to be nine mannose units per H(A16-M)-Y molecule. An attempt to identify the linkage-sites for the O-glycans by amino acid sequencing failed, suggesting non-stoichiometric or heterogeneous O-glycosylation. The possible modes in which N-glycans might contribute to resistance of H(A16-M)-Y to irreversible thermal denaturation are discussed with respect to structural information available for H(A16-M)-Y. Abbreviations: AMY,B. amyloliquefaciens (1-3,1-4)--glucanse; MAC,B. macerans (1-3,1-4)--glucanase H(A16-M), H(A36-M), H(A78-M),H(A107-M) and H(A152-M), hybrid (1-3,1-4)--glucanases containing 16, 36, 78, 107 and 152 N-terminal amino acids, respectively, derived from AMY with the remaining amino acids derived from MAC; similar enzyme abbreviations followed by Y, e.g. H(A16-M)-Y, denote the enzymes secreted from yeast cells; PCR, polymerase chain reaction; PGK_p, yeast 3-phosphoglycerate kinase promoter; PRB1_p, yeast protease B promoter; LB, Luria-Bertani medium; SC, minimal medium; CNBr, cyanogen bromide; Endo H_f, endoglycosidase H fusion protein; PNGase F, peptide:N-glycosidase F; HPAEC; high pH anion exchange chromatography; HVE, high voltage paper electrophoresis; CPY, yeast carboxypeptidase Y.     

Optimizing conditions for poly(β-hydroxybutyrate) production by <Emphasis Type="Italic">Halomonas boliviensis</Emphasis> LC1 in batch culture with sucrose as carbon source

Halomonas boliviensis LC1 is able to accumulate poly(β-hydroxybutyrate) (PHB) under conditions of excess carbon source and depletion of essential nutrients. This study was aimed at an efficient production of PHB by growing H. boliviensis to high cell concentrations in batch cultures. The effect of ammonium, phosphate, and yeast extract concentrations on cell concentration [cell dry weight (CDW)] and PHB content of H. boliviensis cultured in shake flasks was assayed using a factorial design. High concentrations of these nutrients led to increments in cell growth but reduced the PHB content to some extent. Cultivations of H. boliviensis under controlled conditions in a fermentor using 1.5% (w/v) yeast extract as N source, and intermittent addition of sucrose to provide excess C source, resulted in a polymer accumulation of 44 wt.% and 12 g l⁻¹ CDW after 24 h of cultivation. Batch cultures in a fermentor with initial concentrations of 2.5% (w/v) sucrose and 1.5% (w/v) yeast extract, and with induced oxygen limitation, resulted in an optimum PHB accumulation, PHB concentration and CDW of 54 wt.%, 7.7 g l⁻¹ and 14 g l⁻¹, respectively, after 19 h of cultivation. The addition of casaminoacids in the medium increased the CDW to 14.4 g l⁻¹ in 17 h but reduced the PHB content in the cells to 52 wt.%.     

Studies on β-glucanases. Some properties of a bacterial endo-β-(1→3)-glucanase system

A commercial enzyme preparation, originally obtained from a Flavobacterium(Cytophaga), was fractionated by continuous electrophoresis, giving a protein fraction which hydrolysed laminarin, carboxymethylpachyman, barley β-glucan, lichenin and cellodextrin in random fashion. This enzymic activity was not very stable. Ion-exchange chromatography and molecular-sieve chromatography on Bio-Gel P-60 showed that this activity was due to two specific β-glucanases, an endo-β-(1→3)-glucanase and an endo-β-(1→4)-glucanase. The two enzymes occur in both high- and low-molecular-weight forms, the latter endo-β-(1→3)-glucanase having a molecular weight of about 16000.     

Formal kinetics of poly-β-hydroxybutyric acid (PHB) production in Alcaligenes eutrophus H 16 and Mycoplana rubra R 14 with respect to the dissolved oxygen tension in ammonium-limited batch cultures

Summary Under chemolithoautotrophic growth conditions with the organism Alcaligenes eutrophus H16 the exponential growth phase is characterized by two different growth rates, each associated with different specific rates of ammonium consumption. On the basis of the analytical determination of Poly--hydroxybutyric acid (PHB), it can be conclusively shown that PHB is synthesized even during the exponential growth phase at a specific rate proportional to the specific growth rates of total biomass. After complete consumption of ammonium, the increase of biomass is exclusively due to PHB synthesis, whereas protein and rest biomass (cell dry weight minus PHB) remain constant. After an extended period of fermentation, the PHB content reaches a saturation value. The transient phase between the growth and the storage phase is very short in comparison to the duration of the whole fermentation. In the case of Alcaligenes eutrophus, strain H 16, high concentrations of dissolved oxygen strongly influence growth as well as PHB synthesis.Abbrevations ^cO₂,L concentration of oxygen in the liquid phase (dissolved oxygen tension: d.o.t) - ^cH₂,L concentration of hydrogen in the liquid phase - ^cCO₂,L concentration of carbon dioxide in the liquid phase - S limiting substrate, concentration of - X total biomass, concentration of; total cell dry weight - P product; PHB, concentration of - R rest biomass: X-P, concentration of - ^rX dX/dt growth rate - ^rP dP/dt rate of PHB synthesis - ^rR dR/dt rate of rest biomass production - ^r0 ^dcO₂,L/dt rate of oxygen consumption - X dX/dt·1/X=r_X·1/X specific growth rate - P dP/dt·1/P=r_P·1/P specific rate of product formation - R dR/dt·1/R=r_R·1/R specific rate of rest biomass formation - r₀/R specific respiration rate     

The production of acidic,O-acylated cyclosophorans [cyclic (1→2)-β-d-glucans] by Agrobacterium and Rhizobium species

Acidic cyclosophorans [cyclic (1→2)-β-d-glucans] containing methylmalonic acid, or succinic acid, or both, were isolated by DEAE-cellulose chromatography from culture filtrates and cells of some strains of Agrobacterium radiobacter, Rhizobium phaseoli, and R. trifolii. The evidence suggests that one carboxyl group of the dicarboxylic acid is in ester linkage with an hydroxyl group of a sugar unit.     

Changes in (1→3)-β-glucanase activities during stipe elongation inCoprinus cinereus

Cell-free extracts and cell wall autolysates prepared from the stipes of basidiocarp ofCoprinus cinereus were examined for (13)--glucanase activities. Gel filtration revealed two major peaks and a minor one of (13)--glucanases in both of the preparations, the former ones being designated as glucanase I and glucanase II. Glucanase I with a molecular weight of 300,000 had activity towardp-nitrophenyl--d-glucoside (pNPG) as well as laminarin, whereas glucanase II with a molecular weight of 70,000 had no activity toward pNPG. Both enzymes had only negligible activity toward pustulan. During stipe elongation, the level of glucanase-II activity remarkably increased with increasing rate of the elongation, whereas that of glucanase-I activity remained almost constant, in both the cell-free extract and the cell wall autolysate. Near the end of stipe elongation, both glucanase activities were lowered in the cell wall autolysate, but remained high in the cell-free extract.