Effect of agitation speed on the synthesis of Mucor miehei acid protease

Different experiments using Mucor miehei CBS 370.65 were carried out to study the effect of agitation speed on the production of the mold acid protease. The experiments were conducted in shake flasks at a fixed substrate concentration of 58 g l⁻¹ of total carbohydrates and at shaker speeds from 80 to 380 rev min⁻¹. Enzyme production was found to be directly proportional to the shaker speeds, with the highest concentration of enzyme of 1,400 Soxhlet Rennet units (SU) ml⁻¹ obtained at 380 rev min⁻¹. The yield of product to substrate at 380 rev min⁻¹ was determined to be 27,081.0 SU g⁻¹ substrate and the productivity of the process was 221 SU g⁻¹ h⁻¹. Enzyme production was partially growth associated, and glucose supported both cell growth and enzyme production. Product formation and cell concentration were directly related to the rate of substrate consumption. The rate of product formation decreased when product started to accumulate, suggesting that the process was affected by feedback repression.     

The effect of acetic acid concentration on the growth and production of gamma-linolenic acid byMucor circinelloides CBS 203.28 in fed-batch culture

The effect of different initial acetic acid concentrations on the growth of and lipid and gamma-linolenic acid (GLA) production byMucor circinelloides CBS 203.28 was determined in a 14 litre stirred tank reactor operated in a fedbatch, pH-stat mode with acetic acid as carbon source and pH titrant. Increased acetic acid concentrations in the culture resulted in a significant increase in the crude oil content of the biomass. By contrast, all the other parameters such as the biomass concentration, GLA and oil yield on acetic acid, the GLA content of the biomass and oil, the growth rate and volumetric rate of GLA production decreased with an increase in acetic acid concentration. The best results were obtained with acetic acid at 2 g/1, which gave 39.8 mg GLA/g biomass and 15.6% GLA in the neutral lipid fraction, amounting to 340 mg GLA/1 culture. A decrease in the glyco- and phospho-lipid fractions during the cultivation coincided with an increase in the neutral lipid fraction. The GLA content of the biomass remained within rather narrow limits of 3.5% to 4% of the biomass, irrespective of the oil content of the biomass. The fatty acid profile was not greatly affected by the acetic acid concentration. The hyphae of the fungus were characterized by the accumulation of large intracellular oil droplets and some septa delimited the hyphae.     

Enhanced sunflower oil utilization and gamma-linolenic acid production by Mucor circinelloides f.circinelloides CBS 108.16 in the presence of acetate

World Journal of Microbiology and Biotechnology -     

Sedimentation properties of chitosomes fromMucor rouxii

Summary This study was undertaken to assess the distribution and localization of chitin synthetase in a fungal cell and to evaluate the sedimentation behavior of chitosomes (microvesicular containers of chitin synthetase). Chitosomes were isolated from cell-free extracts of yeast cells ofMucor rouxii by rate-zonal and isopycnic sedimentation in sucrose density gradients. Because of their small size and low density, chitosomes were effectively separated from other subcellular particles. Rate-zonal sedimentation was a suitable final step for isolating chitosomes as long as ribosomes had been eliminated by enzymic digestion. By isopycnic centrifugation, chitosomes could be separated directly from a crude cell-free extract; they cosedimented with a sharp symmetrical peak of chitin synthetase at a buoyant density of d=1.14–1.15g/cm³; the only significant contaminants were particles of fatty acid synthetase complex. From such sedimentations, we estimated that 80–85% of the chitin synthetase activity in the cell-free extract was associated with chitosomes; the rest was found in two smaller peaks sedimenting at d=1.19–1.20 and d=1.21–1.22 (5–10%), and in the cell wall fraction (5–10%). By consecutive rate-zonal and isopycnic sedimentations, chitosome preparations with relatively few contaminating particles were obtained. Potassium/sodium phosphate buffer (pH 6.5)+MgCl₂ was the most effective isolation medium for chitosomes. Other buffers such as TRIS-MES+MgCl₂ led to massive aggregation of chitosomes and a change in sedimentation properties. This tendency of chitosomes to aggregate could explain why most of the chitin synthetase activity of a fungus is sometimes found associated with other subcellular structures,e.g., plasma membrane.     

Directional Modifications of Resibufogenin by Mucor subtilissimus and Pseudomonas aeruginosa

Directional modifications of resibufogenin 1 by Mucor subtilissimus and Pseudomonas aeruginosa were carried out. The substrate was hydroxylated at C-12 by M. subtilissimus AS 3.2454, from which a major product 12-hydroxyresibufogenin 2 was obtained. Then product 2 was dehydrogenated by P. aeruginosa AS 1.860, which resulted in a new compound 12β-hydroxy-3-keto-resibufogenin 3.     

cDNA cloning,expression, and enzymatic activity of a novel endogenous cellulase from the beetle Batocera horsfieldi

In this study, we report a novel cellulase [β-1,4-endoglucanase (EGase), EC 3.2.1.4] cDNA (Bh-EGase II) belonging to the glycoside hydrolase family (GHF) 45 from the beetle Batocera horsfieldi. The Bh-EGase II gene spans 720 bp and consists of a single exon coding for 239 amino acid residues. Bh-EGase II showed 93.72% protein sequence identity to Ag-EGase II from the beetle Apriona germari. The GHF 45 catalytic site is conserved in Bh-EGase II. Bh-EGase II has three putative N-glycosylation sites at 56–58 (N–K–S), 99–101 (N–S–T), and 237–239 (N–Y–S), respectively. The cDNA encoding Bh-EGase II was expressed in baculovirus-infected insect BmN cells and Bombyx mori larvae. Recombinant Bh-EGase II from BmN cells and larval hemolymph had an enzymatic activity of approximately 928 U/mg. The enzymatic catalysis of recombinant Bh-EGase II showed the highest activity at 50 °C and pH 6.0.     

Ethanol and value‐added byproducts from rice straw by dimorphic fungus Mucor hiemalis

Different morphologies of Mucor hiemalis were induced and used for the production of ethanol and biomass from rice straw through a separate hydrolysis and fermentation process. The yield of enzymatic hydrolysis was improved from 40.4% for the untreated straw to 80–93% by employing sodium hydroxide and concentrated phosphoric acid pretreatments with or without ultrasonication. The best hydrolysis performance was achieved after pretreatment by sodium hydroxide assisted with ultrasonication. The ethanol yields from the hydrolysates were 0.39–0.44 g/g depending on the pretreatment method and the fungus morphology. The yeast‐like form of the fungus showed faster glucose assimilation and slightly higher ethanol yield compared to the other morphologies. The biomass yield of mostly yeast‐like cells was more than the other morphologies (0.202–0.282 g/g glucose). Moreover, the biomass of the yeast‐like cells had more protein content (46.7–52.4 %) compared to filamentous cells (37.7–46.3 %). The cell wall, alkali‐insoluble material (AIM) of the biomass, represented 16.3–20.1% of the biomass. On average, total chitin‐chitosan content of AIM of the biomass of purely filamentous, mostly filamentous, mostly yeast‐like, and purely yeast‐like forms of the fungus was 0.460, 0.373, 0.330, and 0.336 g/g AIM of the biomass, respectively.     

Lead biosorption by different morphologies of fungus Mucor indicus

Biosorption characteristics of Pb⁺² ions from aqueous solution were investigated using fungus Mucor indicus biomass treated with NaOH. Biosorption was measured as a function of biomass morphology, pH, biomass concentration, contact time, and metal concentration. The morphology of M. indicus biomass was manipulated towards filamentous or yeast-like forms. The highest and lowest biosorption capacities were observed for purely filamentous and yeast-like forms, respectively. Models of Langmuir, Freundlich, Temkin, and Scachard were applied to describe adsorption isotherm and fitted appropriately. Biosorption kinetics was successfully described using Ho’s pseudo-second-order model. Maximum and minimum values of biosorption capacity of Pb²⁺ were 22.1 and 12.1 mg g⁻¹ for purely filamentous and yeast-like morphologies, respectively. Increasing pH resulted in higher biosorption of Pb⁺² ions up to pH 5.5. Biosorption capacity of individual Pb⁺² ions was reduced in the presence of other metal ions in bi- or multi-metal ion experiments. Metal ions adsorption by the biomass could be eluted effectively with HNO₃.