Extracellular xylanase production by Fusarium species in solid state fermentation

Fusarium sp. has been shown to be a promising organism for enhanced production of xylanases. In the present study, xylanase production by 21 Fusarium sp. isolates (8 Fusarium culmorum, 4 Fusarium solani, 6 Fusarium verticillioides and 3 Fusarium equiseti) was evaluated under solid state fermentation (SSF). The fungal isolate Fusarium solani SYRN7 was the best xylanase producer among the tested isolates. The effects of some agriculture wastes (like wheat straw, wheat bran, beet pulp and cotton seed cake) and incubation period on xylanase production by F. solani were optimized. High xylanase production (1465.8 U/g) was observed in wheat bran after 96 h of incubation. Optimum pH and temperature for xylanase activity were found to be 5 and 50 degrees C, respectively.     

Cellulase and xylanase production by Trichoderma reesei Rut C-30

Summary When grown on cellulose or xylan, Trichoderma reesei (strain Rut C-30) produced extra-cellular enzymes which could hydrolyze both cellulose and xylan to their respective monosaccharides. At low O₂ saturation, -glucosidase activity is greatly reduced for cellulose-grown but not xylan-grown cells.     

木霉T6木聚糖酶固态发酵中试生产条件研究

木聚糖酶 (ＸｙｌａｎａｓｅＥＣ .3.2 .1 .8)是一类重要的木糖苷键水解酶 ,对于降解半纤维素起着重要作用[1,2 ] 。该酶在工业上具有巨大的潜在应用价值。在饲料工业上 ,该酶可以提高畜禽对饲料的利用率[3 ] ;在食品工业上 ,该酶的水解产物寡木糖是一类保健食品[4] ,还可用于制备食品增稠剂和澄清果汁 ;在制浆造纸工业上 ,纸浆经过木聚糖酶处理后 ,可降低卡伯值 ,减少含氯漂白剂用量[5 6] ,从而降低环境污染。国外对木聚糖酶的研究起步较早 ,美国、加拿大等发达国家已经进入商品化生产 ,市场需求不断扩大。国内也有对该酶生产的研究 ,但未…     

Effect of pH on production of xylanase by Trichoderma reesei on xylan- and cellulose-based media

Trichoderma reesei VTT-D-86271 (Rut C-30) was cultivatedon media based on cellulose and xylan as the main carbon source in fermentors with different pH minimum controls. Production of xylanase was favoured by a rather high pH minimum control between 6.0 and 7.0 on both cellulose- and xylan-based media. Although xylanase was produced efficiently on cellulose as well as on xylan as the carbon source, significant production of cellulose was observed only on the cellulose-based medium and best production was at lower pH (4.0 minimum). Production of xylanase at pH 7.0 was shown to be dependent on the nature of the xylan in the cultivation medium but was independent of other organic components. Best production of xylanase was observed on insoluble, unsubstituted beech xylan at pH 7.0. Similar results were obtained in laboratory and pilot (200-l) fermentors. Downstream processing of the xylanase-rich, low-cellulose culture filtrate presented no technical problems despite apparent autolysis of the fungus at the high pH. Enzyme produced in the 200-l pilot fermentor was shown to be suitable for use in enzyme-aided bleaching of kraft pulp. Due to the high xylanase/cellulase ratio of enzyme activities in the culture filtrate, pretreatment for removal of cellulase activity prior to pulp bleaching was unnecessary. Correspondence to: M. J. Bailey     

Effect of carbon and nitrogen sources on xylanase production by Trichoderma harzianum 1073 D3

In order to determine the effect of different carbon and nitrogen sources on xylanase production by Trichoderma harzianum 1073 D3, xylan in the xylanase production medium was replaced with different carbon sources. In order to reduce production time, glucose was added to the production media containing xylan. The effects of sucrose, maltose and lactose were investigated and maximum xylanase activity was observed in the presence of sucrose. Ammonium sulphate was the most appropriate inorganic nitrogen source for xylanase production and urea increased xylanase activity slightly.     

The use of canola meal as a substrate for xylanase production by Trichoderma reesei

Summary Tests made utilizing canola meal as a substrate for the production of xylanase indicate that Trichoderma reesei produced this enzyme in similar or better yields from canola meal than from Solka-floc, xylan or glucose. The maximum xylanase activity obtained from canola meal was 210 IU/ml in 9–12 days. The enzyme system produced using canola meal also contained a higher proportion of acetyl-xylan esterase, cellulase, and xylosidase activities. This system was more than or equally efficient as that produced using Solka-floc in hydrolysing canola meal, corn cobs, corn and wheat brans, straw, and larchwood xylan to fermentable sugars. Offprint requests to: Z. Duvnjak     

樟绒枝霉(Malbranchea cinnamomea)固体发酵产木聚糖酶的发酵条件优化

[目的] 研究樟绒枝霉(Malbranchea cinnamomea) CAU521利用农业废弃物固体发酵产木聚糖酶的发酵条件.[方法]采用单因素试验法优化影响菌株产酶的各个条件,包括碳源种类、氮源种类、初始pH、初始水分含量、培养温度及发酵时间共6个因素.[结果]获得的最佳产酶条件为:稻草为发酵碳源、2％(W/W)的酵母提取物为氮源、初始pH 7.0、初始水分含量80％和发酵温度45℃.在此条件下发酵6d后木聚糖酶的酶活力达到13 120 U/g干基碳源.[结论]樟绒枝霉固体发酵产木聚糖酶的产酶水平高,生产成本低,具有潜在的工业化应用前景.     

液态发酵条件下拟康宁木霉8985产纤维素酶能力初探

液态发酵条件下,以微晶纤维素为唯一碳源,比较了拟康宁木霉Trichoderma koningiopsis 8985和里氏木霉T.reesei QM9414产纤维素酶的能力。8985发酵12 h开始产生纤维素酶,36 h时酶活达到产酶峰值的50%,此时QM9414尚未诱导产酶。测定8985发酵84 h时上清液中滤纸纤维素酶、羧甲基纤维素酶、β-葡萄糖苷酶和木聚糖酶的酶活分别为1.06、3.62、1.80和6.67 IU/mL,分别是QM9414上述酶活的1.72、1.70、6.35和1.12倍。8985滤纸纤维素酶酶活的最适反应条件为pH 4.5,反应温度50℃,在Fe³⁺(≤4 mmol/L)和Cu²⁺(0–10 mmol/L)存在条件下酶活稳定。     

Purification and characterization of pectinesterase and polygalacturonase from Trichoderma reesei

Abstract Exopolygalacturonase, endopolygalacturonase and pectinesterase were separated from culture filtrates of Trichoderma reesei QM9414 by Sephadex chromatography. Exopolygalacturonase was characterized by specific cleavage of pectic acid to form d -galactopyranuronic acid, and by the hydrolysis of oligomers (highest reaction rate at pentamer). Polygalacturonase exhibited 2 pH-optima peaks (at 4.8 and 5.1) and 10 bands with enzyme activity by isoelectric focusing (IEF) (p I 4.6–8.5). Pectinesterase showed a pH-optimum at 7.6, and 6 enzyme-activity bands on an IEF zymogram which seemed identical with those of higher plants (tomato, alfalfa).     

Solid state fermentation for L-glutamic acid production using Brevibacterium sp.

Summary Solid state fermentation system was used to cultivate Brevibacterium sp. on sugar cane bagasse impregnated with a medium containing glucose, urea, mineral salts and vitamins for producing L-glutamic acid. Maximum yields (80 mg glutamic acid per g dry bagasse with biomass and substrate - mg/gds) were obtained when bagasse of mixed particle size was moistened at 85–90 % mositure level with the medium containing 10 % glucose. This is the first report on the cultivation of Brevibacterium sp. in solid cultures for production of glutamic acid.     

Improvement of xylanase production in solid state fermentation by alkali-tolerant Aspergillus fumigatus MKU1 using a fractional factorial design

Optimization of media for the maximum production of xylanase by Aspergillus fumigatus MKUI was carried out using De Meo's fractional factorial design with seven components such as NaNO3, K2HPO4, MgSO4, FeSO4. KCl, peptone and yeast extract. A. fumigatus produced a maximum of 700 U/gds of enzyme after 48 hr of incubation (before optimization). After two steps of optimization, the medium designed favoured a 2.8 fold (1950 U/gds) increase in xylanase production by A. fumigatus. Optimized medium for Aspergillus fumigatus contained (g/l) NaNO3, 15; K2HPO4, 15; MgSO4, 5; FeSO4, 0.009; KCI, 0.5; peptone, 20; and yeast extract, 10.     

Production of cellulase and xylanase by a wild strain of Trichoderma viride

Summary The production of cellulase and xylanase was investigated with a newly isolated strain of Trichoderma viride BT 2169. The medium composition was optimized on a shake-flask scale using the Graeco-Latin square technique. The temperature and time for optimal growth and production of the enzymes in shake cultures were optimized using a central composite design. The temperature optima for maximal production of filter paper cellulase (FPase), xylanase and -gluosidase were 32.8°, 34.7° and 31.1° C, respectively, and the optimum times for production of these enzymes were found to be 144, 158 and 170 h, respectively. The optimized culture medium and conditions (33° C) gave 0.55 unit of FPase, 188.1 units of xylanase and 3.37 units of -glucosidase per milliliter of culture filtrate at 144 h of shake culture. Among different carbon sources tested, the maximum enzyme activities were produced with sulphite pulp and all three enzymes were produced irrespective of the carbon sources used. Batch fermentation in a laboratory fermentor using 2% sulphite pulp allowed the production of 0.61 unit of FPase, 145.0 units of xylanase and 2.72 units of -glucosidase. In a fed-batch fermentation on 6% final Avicel concentration FPase and -glucosidase were 3.0 and 2.4 times higher respectively than those in batch fermentation on 2% Avicel. The pH and temperature optima as well as pH and temperature stabilities of T. viride enzymes were found to be comparable to T. reesei and some other fungal enzymes.     

Determination of some physiological factors affecting xylanase production from Trichoderma harzianum 1073 D3

In this study, different Trichoderma strains were tested and Trichoderma harzianum 1073 D3 was found to be the most potent xylanase producer. Then some cultural parameters, namely, incubation time, substrate concentration, initial culture pH and temperature were optimized in order to increase xylanase production from Trichoderma harzianum 1073 D3. The optimum incubation time was found to be 13 days. It was concluded that 1% xylan concentration is suitable for high xylanase production rate. The optimum temperature and pH were found to be 30 degrees C and 7, respectively. Also, it was determined that agitation during growth was suitable for efficient production.     

Regulation of the production of polygalacturonase by Aspergillus terreus

The synthesis of polygalacturonase (PG) (EC 3.2.1.15) by a strain of Aspergillus terreus was induced by polygalacturonic acid and repressed by glucose, galactose or fructose even in the presence of the inducer. The production of PG increased when the mycelium was washed free of glucose and incubated in a glucose-free medium containing the inducer, a fact that indicated the reversibility of the repression mechanism. When Actinomycin D and cycloheximide were added to the culture medium, the synthesis of PG ceased. PG synthesis increased 43% with the addition of methionine and 64% both with leucine and with tyrosine. Specific productivity with leucine was 210% higher than that of the control as against 149% with methionine and 70% with tyrosine. The results obtained suggest that PG synthesis is regulated by leucine.     

Molecular characterisation of Trichoderma species using SRAP markers

Trichoderma are commonly used as bio control agents in various agro ecosystems. They are known to produce a variety of compounds that induce resistance responses in plants. Among different species of Trichoderma, T. harzianum, T. viride, T. koningii and T. hamatum are commercially used as bio control agents. In the present study, four commercially important species of Trichoderma isolated from coffee ecosystem were screened with sequence related amplified polymorphism (SRAP) markers. Among 48 SRAP primer pairs tested, 29 primers were polymorphic and generated 316 distinct scorable fragments. Out of 347 amplified fragments, 177 fragments were found polymorphic with an average of 6.10 fragments per primer combination. The average polymorphism information content (PIC) and resolving power (Rp) of the 29 polymorphic SRAP primer pair were 0.42 and 14.62, respectively. The UPGMA dendrogram clearly divided Trichoderma species into two broad clusters. The highest homology (83.0%) was observed between T. viride and T. Harzianum and the lowest homology (74.0%) was observed between T. Harzianum and T. konangii. Further, among 29 polymorphic SRAP markers screened, four primer pairs (ME1-EM3, ME1-EM20, ME1-EM22 and ME2-EM4) produced unique fragments specific to each species. These markers can be useful in easy and rapid identification of the species.     

Regulation of the production of polygalacturonase by Aspergillus niger

Synthesis of ethylene in static cultures as well as the effect of endogenous and exogenous ethylene on the synthesis of polygalacturonase byAspergillus niger were determined. This strain produced maximum ethylene amounts when cultured at 30 °C for 3 d. The effect of adding ethylene precursors (citrate-cycle intermediates) on ethylene production was investigated. Best intracellular and extracellular polygalacturonase production was obtained with 2-oxoglutaric, pyruvic and fumaric acids, and with glutamic acid too. Addition of ethylene to the culture medium also increased the synthesis of polygalacturonase, although to a lower degree than when glutamic acid was added.     

Solid-state fermentation for xylanase production by Thermoascus aurantiacus using response surface methodology

We investigated xylanase production by Thermoascus aurantiacus using semisolid fermentation. Multivariant statistical approaches were employed to evaluate the effects of several variables (initial moisture in the medium, cultivation time, inoculum level, and bagasse mass) on xylanase production. The initial moisture content and bagasse mass were the most important factors affecting xylanase activity. The xylanase activity produced by the fungus under the optimized conditions (81% moisture content and 17 g bagasse) was found to be 2700 U per gram of initial dry matter, whereas its value predicted by a polynomial model was 2400 U per gram of initial dry matter. Received: 4 December 1998 / Received revision: 15 March 1999 / Accepted: 16 May 1999     

Solid-state production of polygalacturonase by Aspergillus sojae ATCC 20235

The effect of solid substrates, inoculum and incubation time were studied using response surface methodology (RSM) for the production of polygalacturonase enzyme and spores in solid-state fermentation using Aspergillus sojae ATCC 20235. Two-stage optimization procedure was applied using D-optimal and face-centered central composite design (CCD). Crushed maize was chosen as the solid substrate, for maximum polygalacturonase enzyme activity based on D-optimal design. Inoculum and incubation time were determined to have significant effect on enzyme activity and total spore (p<0.01) based on the results of CCD. A second order polynomial regression model was fitted and was found adequate for individual responses. All two models provided an adequate R(2) of 0.9963 (polygalacturonase) and 0.9806 (spores) (p<0.001). The individual optimum values of inoculum and incubation time for maximum production of the two responses were 2 x 10(7) total spores and 5-6 days. The predicted enzyme activity (30.55 U/g solid) and spore count (2.23 x 10(7)spore/ml) were very close to the actual values obtained experimentally (29.093 U/g solid and 2.31 x 10(7)spore/ml, respectively). The overall optimum region considering the two responses together, overlayed with the individual optima. Solid-state fermentation provided 48% more polygalacturonase activity compared to submerged fermentation under individually optimized conditions.     

Production of xylanase by immobilized Trichoderma reesei SAF3 in Ca-alginate beads

In the present study, the optimum conditions for the production of xylanase by immobilized spores of Trichoderma reesei SAF3 in calcium alginate beads were determined. The operational stability of the beads during xylanase production under semi-continuous fermentation was also studied. The influence of alginate concentration (1, 2, 3, and 4%) and initial cell loading (100, 200, 300, 400, and 500 beads per flask) on xylanase production was considered. The production of xylanase was found to increase significantly with increasing concentration of alginate and reached a maximum yield of 3.12 ± 0.18 U ml⁻¹ at 2% (w/v). The immobilized cells produced xylanase consistently up to 10 cycles and reached a maximum level at the forth cycle (3.36 ± 0.2 U ml⁻¹).