Purification and properties of the β-fructofuranosidase from Kluyveromyces fragilis

The β-fructofuranosidase from Kluyveromyces fragilis was purified to one band on electrophoresis by 3 different methods. Two of the preparations were found to be impure by isoelectric focusing. This demonstrates the need for more than one criteria of homogeneity when purifying this enzyme. The enzyme was found to be a glycoprotein, stable at 50°C, with a pH optimum of 4.5. The cations Hg²⁺, Ag⁺, Cu²⁺ and Cd²⁺ exhibited a marked inhibition of the enzyme. Competitive inhibition was observed with the fructose analog 2,5-anhydro-D-mannitol suggesting that the enzyme is inhibited by the furanose form of fructose.     

Production of high fructose syrup from <Emphasis Type="Italic">Asparagus</Emphasis> inulin using immobilized exoinulinase from <Emphasis Type="Italic">Kluyveromyces marxianus</Emphasis> YS-1

Extracellular exoinulinase from Kluyveromyces marxianus YS-1, which hydrolyzes inulin into fructose, was immobilized on Duolite A568 after partial purification by ethanol precipitation and gel exclusion chromatography on Sephadex G-100. Optimum temperature of immobilized enzyme was 55 °C, which was 5 °C higher than the free enzyme and optimal pH was 5.5. Immobilized biocatalyst retained more than 90% of its original activity after incubation at 60 °C for 3 h, whereas in free form its activity was reduced to 10% under same conditions, showing a significant improvement in the thermal stability of the biocatalyst after immobilization. Apparent K _m values for inulin, raffinose and sucrose were found to be 3.75, 28.5 and 30.7 mM, respectively. Activation energy (E _a) of the immobilized biocatalyst was found to be 46.8 kJ/mol. Metal ions like Co²⁺ and Mn²⁺ enhanced the activity, whereas Hg²⁺ and Ag²⁺ were found to be potent inhibitors even at lower concentrations of 1 mM. Immobilized biocatalyst was effectively used in batch preparation of high fructose syrup from Asparagus racemosus raw inulin and pure inulin, which yielded 39.2 and 40.2 g/L of fructose in 4 h; it was 85.5 and 92.6% of total reducing sugars produced, respectively.     

Inulinase production by a marine yeast <Emphasis Type="Italic">Pichia guilliermondii</Emphasis> and inulin hydrolysis by the crude inulinase

Marine yeast strain 1, isolated from the surface of a marine alga, was found to secrete a large amount of inulinase into the medium. This marine yeast was identified as a strain of Pichia guilliermondii according to the results of routine yeast identification and molecular methods. The crude inulinase produced by this marine yeast worked optimally at pH 6.0 and 60°C. The optimal medium for inulinase production was seawater containing 4.0% (w/v) inulin and 0.5% (w/v) yeast extract, while the optimal cultivation conditions for inulinase production were pH 8.0, 28°C and 170 rpm. Under the optimal conditions, over 60 U ml⁻¹ of inulinase activity was produced within 48 h of fermentation in shake flasks. A large amount of monosaccharides and a trace amount of oligosaccharides were detected after the hydrolysis, indicating that the crude inulinase had a high exoinulinase activity.     

克鲁维酵母Y-85菊粉酶的纯化和性质

克鲁维酵母(Kluyveromyces sp.)Y-85产生的胞内菊粉酶(endocellular inulinase)和胞外菊粉酶(exocellular inulinase)粗酶液分别经PEG6000-磷酸盐缓冲液双水相抽提得部分纯化酶液。前者进一步用硫酸铵分级沉淀、Protein-PAK DEAE离子交换、Protein-PAK200SW凝胶过滤后得到两个菊粉酶组分EⅠ和EⅡ;后者采用DEAE-Sephacel离子交换、Sephadex G150凝胶过滤后得到菊粉酶Eexo。经Waters 650E蛋白纯化系统鉴定,三者均呈单一的对称峰;EⅠ和EⅡ达聚丙烯酰胺盘状凝胶电泳纯。EⅠ、EⅡ和Eexo的分子量分别为42kD、65kD和57kD;三者均为糖蛋白,多糖含量分别为30％、35％和25％;I/S(Inulinaseactivity/Sucrase activity)比值分别为0.086、0.078和0.072;三者均属外切菊粉酶。EⅠ、EⅡ和Eexo酶反应最适pH分别为4.6、4.5和4.6,最适温度分别为52℃、52℃和55℃;Ag^+、Hg^(2+)和PCMB对酶活性有强烈的抑制作用;三者水解菊芋粉糖液的产物均为果糖(86.5％)和葡萄糖(13.5％)。     

Inulinolytic activity of broths of Aspergillus niger ATCC 204447 cultivated in shake flasks and stirred tank bioreactor

It is the first detailed study of an inulinolytic fungus Aspergillus niger ATCC 204447 since its discovery, covering submerged cultivations both in shake flasks and a stirred tank bioreactor. Various carbon sources were applied to induce the inulinolytic activity in shake flask cultures. The highest volumetric and specific (per gram of biomass) activities (respectively 0.68 U/mL and 184 U g/X) were observed for the initial inulin and sucrose concentrations equal to 20 g/L. The fungus grew as large (>3 mm) spherical pellets. The influence of inoculum density and application of microparticle‐enhanced cultivation (MPEC) were studied in the batch bioreactor cultivations. Inoculum density moderately affected the inulinolytic activities, whose highest values were 0.7 U/mL and 165 U g/X at the lowest studied spore density of 3.33·10⁸ L^?1. Dispersed hyphae evolved in the bioreactor made the broth difficult to aerate due to high apparent viscosity (exceeding 200 Pa sⁿ at shear rate about 0.05 s^?1) and shear thinned properties (flow behavior index below 0.2). In MPEC (10 μm talc microparticles) the pellets of diameter between 1 and 2 mm were formed, which facilitated the aeration of the broth and increased the specific inulinolytic activity 3.5‐fold.     

Production,characterization and gene cloning of the extracellular enzymes from the marine-derived yeasts and their potential applications

In this review article, the extracellular enzymes production, their properties and cloning of the genes encoding the enzymes from marine yeasts are overviewed. Several yeast strains which could produce different kinds of extracellular enzymes were selected from the culture collection of marine yeasts available in this laboratory. The strains selected belong to different genera such as Yarrowia, Aureobasidium, Pichia, Metschnikowia and Cryptococcus. The extracellular enzymes include cellulase, alkaline protease, aspartic protease, amylase, inulinase, lipase and phytase, as well as killer toxin. The conditions and media for the enzyme production by the marine yeasts have been optimized and the enzymes have been purified and characterized. Some genes encoding the extracellular enzymes from the marine yeast strains have been cloned, sequenced and expressed. It was found that some properties of the enzymes from the marine yeasts are unique compared to those of the homologous enzymes from terrestrial yeasts and the genes encoding the enzymes in marine yeasts are different from those in terrestrial yeasts. Therefore, it is of very importance to further study the enzymes and their genes from the marine yeasts. This is the first review on the extracellular enzymes and their genes from the marine yeasts.     

Use of a sequential strategy of experimental design to optimize the inulinase production in a batch bioreactor

A potential application of inulinase in the food industry is the production of fructoligosaccharides (FOS) by the transfructosilation of sucrose. The FOSs present many interesting functional properties besides their ability to increase the shelf-life and flavor of many products. The use of an industrial medium represents a good alternative to producing inulinase at low cost, since the activity may improve, or at least remain the same, as that obtained using a synthetic medium. This work was an optimization study of the inulinase production by Kluyveromyces marxianus NRRL Y-7571 using industrial pre-treated culture medium in a bioreactor employing a sequential strategy of experimental design. Initially, a Plackett–Burman (Screening Design) design was used, where the studied variables were molasses, corn steep liquor, yeast extract concentration, and agitation and aeration rates. After the analysis of the effects, a central composite rotational design (CCRD) was carried out. The optimized condition for the inulinase production was: 250 g/l of molasses, 80 g/l of corn steep liquor, 6 g/l of yeast extract, 300 rpm of agitation and 1.5 vvm aeration rate, which resulted in an enzymatic activity of 1,317 ± 65 U/ml.     

Technical viability of the production,partial purification and characterisation of inulinase using pretreated agroindustrial residues

The present work aimed to study the viability of the use of sugarcane molasses and corn steep liquor (CSL) in a sequential inulinase production performing an up-stream pretreatment of these agroindustrial residues. A sequential strategy was used applying three central composite rotatable designs (CCRDs) to optimise medium composition, followed by a down-stream step. The medium containing 150 g L⁻¹ molasses, 50 g L⁻¹ CSL and 6 g L⁻¹ yeast extract, yielded a maximum inulinase production of 1,294 ± 7 U mL⁻¹, after 72 h of fermentation. A down-stream evaluation was carried out using an expanded bed of Streamline DAE resin (Pharmacia), with and without the up-stream treatment. The results showed that the enzyme could not be recovered from the non-pretreated medium, whereas a yield of 91% was obtained in the adsorption stage from the medium prepared with the up-stream treatment, showing the viability of producing the enzyme inulinase from agroindustrial residues using the integrated process.     

菊粉酶高活力菌株的筛选及其产酶研究

利用透明圈法从３０个菊粉酶活力菌株中筛选出两个高活力菌株Ｈ_８和Ｍ_８９,两菌株均鉴定为黑曲霉。Ｈ_８和Ｍ_８９产酶的最佳碳源是菊粉,Ｈ_８最适氮源是（ＮＨ_４）_２ＳＯ_４,Ｍ_８９以草酸胺最好,（ＮＨ_４）_２ＳＯ_４仅次于草酸胺。两菌株产酶的环境条件有一定差异,Ｈ