Utilization of prawn waste for chitinase production by the marine fungus Beauveria bassiana by solid state fermentation

Prawn waste, a chitinous solid waste of the shellfish processing industry, was used as a substrate for chitinase production by the marine fungus Beauveria bassiana BTMF S10, in a solid state fermentation (SSF) culture. Theprocess parameters influencing SSF were optimized. A maximum chitinase yield of 248.0 units/g initial dry substrate (U/gIDS) was obtained in a medium containing a 5:1 ratio (w/v) of prawn waste/sea water, 1% (w/w) NaCl,2.5% (w/w) KH2PO4, 425–600m substrate particle size at 27°C, initial pH 9.5, and after 5 days of incubation. The presence of yeast extract reduced chitinase yield. The results indicate scope for the utilization of shellfish processing (prawn) waste for the industrial production of chitinase by using solid state fermentation.     

Production of fungal chitosan by solid substrate fermentation followed by enzymatic extraction

An improved method is described for the production of chitosan from mycelia of the fungus Gongronella butleri, grown by solid substrate fermentation on sweet potato. The chitosan was extracted subsequently by 11 M NaOH at 45 °C, and 0.35 M acetic acid at 95 °C. The resulting extract was clarified using a heat-stable, commercial -amylase. The yield (4–6 g/100 g mycelia) and relative number average molecular weight (44–54 kDa) of the chitosan increased with increasing duration of fungal growth up to the sixth day.     

Production of the fungal biocontrol agent Epicoccum nigrum by solid substrate fermentation: effect of water activity on accumulation of compatible solutes

Epicoccum nigrum conidia were produced by solid fermentation on wheat grains (cv. Rendeveaux and Brigadier) at different water activities (a_w). Conidial production was highest at high a_w(0.996) than at reduced a_w (0.98). However, conidial production at reduced a_w was improved when the a_w of the substrate was adjusted with a mixture of glycerol and water. Maximum levels ofconidiation were 7–11 × 10⁶ conidia g⁻¹ grain. The a_w of the solid substrate affected the pattern of accumulation of compatible solutes in the conidia. Mannitol was the main polyol in all conidialtypes. However, the amounts of mannitol were higher in conidia produced at high a_w. At reduced a_w the conidia of E. nigrum accumulated moreglycerol, which is more efficient in the osmorregulation proccess than mannitol. Arabitol accumulated in low amounts, specifically in conidia produced at the lower a_w, on cv. Rendeveaux but not on cv. Brigadier. Trehalose was detected in higher amounts in cv. Rendeveaux than in cv. Brigadier, andthe amounts were higher in conidia produced at high a_w. A significant amount of endogenous solutes was detected in the washing liquid used for the separation of the conidia. This revised version was published online in June 2006 with corrections to the Cover Date.     

Effect of operating conditions on solid substrate fermentation

In this work the effects of environmental parameters on the performance of solid substrate fermentation (SSF) for protein production are studied. These parameters are (i) air flow rate, (ii) inlet air relative humidity, (iii) inlet air temperature, and (iv) the heat transfer coefficient between the outer wall of the fermentor and the air in the incubator. The air flow is supplied to effect cooling of the fermented mass by evaporation of water. A dynamic model is developed, which permits estimation of biomass content, total dry matter, moisture content, and temperature of the fermented matter. The model includes the effects of temperature and moisture content on both the maximum specific growth rate and the maximum attainable biomass content. The results of the simulation are compared with actual experimental data and show good agreement with them. The most important conclusions are that (i) the evaporative cooling of the biomass is very effective for temperature control and (ii) the air flow rate and the heat transfer coefficient have strong effects but they affect the biomass morphology and are not controllable easily. Also, a simple technique for the determination of the optimum temperature and moisture content profile for cell protein production is applied. The simulated biomass production increases considerably employing the optimum temperature and moisture content profiles. The ultimate goal is to implement the determined effects of the environmental parameters on the SSF biomass production and the temperature and moisture variation profiles to effectively control the SSF and optimize the biomass production. (c) 1993 John Wiley & Sons, Inc.     

Synergism of cellulase enzymes in mixed culture solid substrate fermentation

Sugar cane bagasse was subjected to a mixed culture, solid substrate fermentation with Trichoderma reesei QM9414 and Aspergillus terreus SUK-1 to produce cellulase and reducing sugars. The highest cellulase activity and reducing sugar amount were obtained in mixed culture. The percentage of substrate degradation achieved employing mixed culture was 26% compared to 50% using separate cultures of the two molds. This suggests that the synergism of enzymes in mixed culture solid substrate fermentation have lower synergism than in pure culture.     

Standardization of the filter paper activity assay for solid substrate fermentation

The conditions of the filter paper activity (FPA) assay were standardized for solid substrate fermentation (SSF). The FPA is a relative measure of the overall cellulose hydrolysing capacity of microbial cellulase preparations, thus reliable and comparable data may be obtained only under standardized conditions. The standardization developed for submerged fermentation (SF) cannot be translated directly to SSF. In SSF, the FPA is strongly dependent on the extraction volume and on the dilution of the enzyme in the assay. The optimal extraction volume was substrate dependent in SSF of corn fiber, spent brewing grains and wheat straw for cellulase production by Trichoderma reesei Rut C30. Other cellulolytic enzyme assays (endoglucanase, beta-glucosidase and xylanase) were much less sensitive to the extraction volume.     

一株感染家蚕的高致病性白僵菌的筛选及发酵条件优化

【背景】球孢白僵菌是一种重要的昆虫病原真菌,通过侵染幼蚕可制备白僵蚕。白僵蚕中的生物活性物质在医疗、保健品及化妆品行业有着广泛的应用。【目的】从7株不同来源的白僵菌中筛选获得高毒力白僵菌并优化其发酵条件,为制备白僵蚕提供优质的菌种资源。【方法】从不同白僵蚕体内分离获得7株白僵菌菌株(SDJC-1、SDJC-2、SDJC-3、GXHC-1、SDND-BB、AT-3006和SQJC-1),通过生物学特性观察、产蛋白酶和几丁质酶活力分析及对家蚕的致死力等研究,筛选得到一株致病力高、性状优异的白僵菌株,并对其最适发酵条件进行探索。【结果】菌株SDJC-3的生物学性状优异,产孢量较高,家蚕致死率达75%,其制备的白僵蚕成品个头大且饱满,横截面丝腺环清晰,品质较好。通过对菌株SDJC-3进一步进行发酵优化,发现其最适生长温度为27℃、最优发酵转速为180 r/min、最适的发酵液体积占比为1/5 (250 mL培养瓶)。【结论】本研究将为人工利用白僵菌制备白僵蚕及提高其产量和品质提供理论基础。     

Optimization of phytase production by solid substrate fermentation

The production of phytase by three feed-grade filamentous fungi (Aspergillus ficuum NRRL 3135, Mucor racemosus NRRL 1994 and Rhizopus oligosporus NRRL 5905) on four commonly used natural feed ingredients (canola meal, cracked corn, soybean meal, wheat bran) was studied in solid substrate fermentation (SSF). A. ficuum NRRL 3135 had the highest yield [15 IU phytase activity/g dry matter (DM)] on wheat bran. By optimizing the supplementation of wheat bran with starch and (NH₄)₂SO₄, phytase production increased to 25 IU/g DM. Optimization was carried out by Plackett-Burman and central composite experimental designs. Using optimized medium, phytase, phosphatase, alpha-amylase and xylanase production by A. ficuum NRRL 3135 was studied in Erlenmeyer flask and tray SSF. By scaling up SSF from flasks to stationary trays, activities of 20 IU phytase activity/g DM were reproducibly obtained. Electronic Publication     

Enhanced lovastatin production by solid state fermentation ofMonascus ruber

The purpose of this study was to optimize the solid state cultivation ofMonascus ruber on sterile rice. A single-level-multiple-factor and a single-factor-multiple-level experimental design were employed to determine the optimal medium constituents and to optimize carbon and nitrogen source concentrations for lovastatin production. Simultaneous quantitative analyses of the β-hydroxyacid form and β-hydroxylactone for of lovastatin were performed by the high performance liquid chromatography (HPLC) method with a UV photodiode-array (PDA) detector. The total lovastatin yield (4≈6 mg/g, average of five repeats) was achieved by adding soybean powder, glycerol, sodium nitrate, and acetic acid at optimal composition of the medium increased by almost 2 times the yield observed prior to optimization. The experimental results also indicated that the β-hydroxylactone form of lovastatin (LFL) and the β-hydroxyacid form of lovastatin (AFL) simultaneously existed in solid state cultures ofMonascus ruber, while the latter was the dominant form in the middle-late stage of continued fermentation. These results indicate that optimized culture conditions can be used for industrial production of lovastatin to obtain high yields.     

Response surface optimization of mixed substrate solid state fermentation for the production of lovastatin by Monascus purpureus

The objective of this work is to enhance the production of lovastatin using Monascus purpureus MTCC 369 in mixed substrate solid state fermentation using various solid substrates and to optimize the combination of the solid substrates by response surface methodology. Solid state fermentation was conducted in a 250 mL Erlenmeyer flask at 30°C for 14 days with initial moisture content of 40% and inoculum size of 10% active culture. Barley, long grain rice and sago starch were found to be the suitable substrates producing maximum lovastatin of 193.7 mg, 190.2 mg and 180.9 mg/g of dry solids. These substrates were further used in various combinations as designed by the central composite design for enhancing the lovastatin production using Monascus purpureus. To the best of our knowledge this is the first report on the production of lovastatin using a mixed substrate solid state fermentation using Monascus purpureus.     

Statistical model based optimization of spore production by solid-state culture of Beauveria bassiana

A significant enhancement of spore production by solid-state culture of Beauveria bassiana was achieved via a statistical modeling and optimization approach. A two-level Plackett–Burman design was implemented to screen the significant medium components for spore production. Among the six variables tested, sucrose, NaNO₃, and H₃BO₃ were identified as the most significant factors (confidence levels above 95%) for spore production. The steepest ascent experiments were adopted to determine the optimal region of the medium composition. The developed second-order polynomial model predicted that the maximal spore production was 6.24×10⁹/g with the following optimal culture conditions: sucrose 34.7 g/L, NaNO₃ 52.8 g/L, and H₃BO₃ 79.6 µg/L. Finally the verification experiments were carried out and the maximal spore production reached 6.221×10⁹/g at the above optimal conditions. The spore production in the verification experiments was very close to that predicted by the model, indicating that the constructed second-order model had superior modeling and optimization ability and can be applied in the optimal spore production of Beauveria bassiana YP9 as a biological control agent.     

Degradation of the herbicide bentazon as related to enzyme production by Phanerochaete chrysosporium in two solid substrate fermentation systems

Enzyme production and degradation of the herbicide bentazon by Phanerochaete chrysosporium growing on straw (solid substrate fermentation, SSF) and the effect of nitrogen and the hydraulic retention time (HRT) were studied using a small bioreactor and batch cultures. The best degradation of bentazon was obtained in the low nitrogen treatments, indicating participation of the ligninolytic system of the fungus. The treatments that degraded bentazon also had manganese peroxidase (MnP) activity, which seemed to be necessary for degradation. Pure MnP (with Mn(II) and H₂O₂) did not oxidize bentazon. However, in the presence of MnP, Mn(II) and Tween 80, bentazon was slowly oxidized in a H₂O₂-independent reaction. Bentazon was a substrate of pure lignin peroxidase (LiP) and was oxidized significantly faster (22,000–29,000 times) as compared to the MnP-Tween 80 system. Although LiP was a better enzyme for bentazon oxidation in vitro, its role in the SSF systems remains unclear since it was detected only in treatments with high nitrogen and high HRT where no degradation of bentazon occurred. Inhibition of LiP activity may be due to phenols and extractives present in the straw.     

Bioprocess optimization of laccase production through solid substrate fermentation using Perenniporia tephropora-L168 and its application in bioremediation of triaryl-methane dye

Laccases are multi copper oxidases that can oxidize both phenolic and nonphenolic lignin related compounds. Consequently, there has been continuous demand for laccases for the oxidative degradation of phenolic dyes in effluents. In view of this, the present work was focused on laccase production by solid substrate fermentation using a newly isolated fungus Perenniporia tephropora-L168. To intensify the laccase production, the process parameters pH, nitrogen, inducer, and substrate: water ratio were optimized by using statistical model. A set of optimal conditions noted were pH 3, nitrogen 0.001 g/L; inducer 0.5% and substrate: water ratio (1:10), which yielded laccase 1,160 U/g. The crude laccase exhibited noteworthy potential to degrade a triaryl-methane dye especially Malachite green. Also, during bioremediation studies, the statistical process optimization could achieve 81% decolourization within 180 min. The laccase treatment brought chemical transformation in malachite green as evident from UV–Visible spectra, FTIR, HPLC while toxicity against bacteria and fungi was also reduced. During phytotoxicity study, effect of treated and untreated dye on germination of seed was analyzed. Interestingly, the germination index for Vigna aconitifolia and Vigna radiata was increased by two and fourfold, respectively. Overall, this work demonstrates optimized production of laccase using Perenniporia tephropora-L168 and its efficient bioremediation potential for triaryl-methane dye.     

Conidia production by <Emphasis Type="Italic">Beauveria bassiana</Emphasis> (for the biocontrol of a diamondback moth) during solid-state fermentation in a packed-bed bioreactor

Conidia of Beauveria bassiana CS-1, which have the potential for the control of the diamondback moth (Plutella xylostella), were produced by solid-state fermentation (SSF) using a packed-bed bioreactor with rice straw and wheat bran. As the packing density and the bed height were increased, the production of conidia decreased. In a packed-bed bioreactor under no aeration and no addition of polypropylene (PP) foam (control), the total average of conidia was 4.9 × 10⁸ g^-1. The production of conidia was affected more by the addition of PP foam as an inert support than forced aeration and was approx. 23 times higher than that of the control. The total average of conidia produced by B. bassiana was 1.1–1.2 × 10¹⁰ g^-1 . Revisions requested 6 September 2004/2 November 2004; Revisions received 1 November 2004/8 December 2004     

Solid substrate fermentation of lignite by the coal-solubilizing mould, Trichoderma atroviride, in a new type of bioreactor

Trichoderma atroviride CBS 349 is able to solubilize lignite. The mould was cultured under non-sterile conditions in a new type of bioreactor for solid substrate fermentation. German lignite (lithotype A, Bergheim) was used as complex solid substrate. Over 40 days 140 g of 1.5 kg lignite held in a 25 l-bioreactor was solubilized by the fungus.     

土壤中产木聚糖酶菌株的筛选及发酵条件优化

【背景】木聚糖广泛存在于木质纤维类生物质中,是世界上含量最丰富的半纤维素,利用产酶微生物对木质纤维类生物质进行发酵处理是木质纤维类生物质资源化和能源化的有效手段。【目的】通过产木聚糖酶菌株的筛选鉴定、酶学特性分析和发酵条件优化,获得开发多纤维农林废弃物生产新型多元化饲料添加剂的材料。【方法】利用青藏高原土壤筛选产木聚糖酶菌株,通过形态学观察和rDNAITS区域序列分析鉴定菌株XC70种属,对其所产酶的酶学特性及该菌的生长规律和产酶规律进行分析,并利用单因素法和正交试验法优化其发酵条件。【结果】菌株XC70经形态学和分子生物学方法鉴定为草酸青霉(Penicillium oxalicum)。菌株XC70所产木聚糖酶的最适反应条件为:pH 5.0,70°C,温度低于50°C时稳定性较好,具备一定的耐酸性,Na+和K+对木聚糖酶活力具有促进作用(P0.05),在发酵54 h后菌体量和上清液酶活力大小均达到高峰。经过单因素法和正交试验法优化后确定了该菌的最优发酵条件为:蛋白胨7 g/L,玉米秸秆50 g/L,KCl 4 g/L,培养基初始pH 4.0,28°C,摇床转速200r/min,接种量2%。在此发酵条件下,木聚糖酶活力可达到1 489.33U/mL,与优化前相比提高了3倍多。【结论】从青藏高原土壤中筛选获得的菌株XC70具有一定的产木聚糖酶能力,其所产生的酸性木聚糖酶可用于降解多纤维物质开发新型饲料添加剂,具有一定的应用潜力和开发价值。     

变温干燥固体发酵产物对球孢白僵菌分生孢子性能的影响

[目的]评价球孢白僵菌固体发酵产物的干燥温度对产后分生孢子性能的影响.[方法]采用28℃2和35℃组合的7种恒温或变温处理干燥发酵产物,分析收获的分生孢子质量.[结果]变温干燥可显著降低产后孢子粉的杂菌污染.干燥温度对活孢率和孢子萌发速度影响不一致.35℃恒温干燥5 h后活孢率与新鲜孢子无明显差异,但萌发中时缩短了9.3%.干燥处理提高了孢子对高温和紫外辐射的耐受性.适当的变温干燥比恒温干燥有利于增强孢子抗逆性.干燥温度影响分生孢子胞内海藻糖积累,但其含量与抗逆性无直接相关性.优化干燥温度可提高产后分生孢子毒力.在370～450孢子/mm2剂量下,经28℃ 24 h后升至35℃干燥2 h或35℃恒温干燥5 h的分生孢子对桃蚜的致死中时分别比新鲜孢子缩短了10.6 h和7.5 h.[结论]球孢白僵菌固体发酵产物的干燥温度是影响产后孢子粉杂菌污染、孢子活力、抗逆性和毒力的重要因素.     

Enhanced production of cellulases byPenicillium citrinum in solid state fermentation of cellulosic residue

Penicillium citrinum, using rice husks in a solid state fermentation, produced maximum cellulase yields (37 Units/g) after 12 days with a cellulose utilization of more than 70%. Enzyme yields were three times higher than in shake-flask cultures.     

Characterization of the growth and sporulation behavior of Penicillium roquefortii in solid substrate fermentation by material and bioenergetic balances

When Pencillium roquefortii is grown on two kinds of buckwheat, exhibiting a low [0.85 g water/g dry matter (DM), buckwheat A] and a high [1.5 g water/g initial dry matter (IDM), buckwheat B] water content, a marked difference in the mode of development of the fungus is observed. Material balances for buckwheat A show that growth does not stop because of nutrient exhaustion. Analysis of water balance shows that active growth proceeds with a permanent limitation by the turgor potential which disappears when the water activity of the substrate is close to 0.96, thus arresting growth. This limitation causes intensive water excretion from the system due to the lowering of the water activity of the substrate. The water content of the mycelium thus decreases from 79% at the beginning of the cultivation to 74% when the growth stops. This is linked to a substantial oxidative metabolism and a high sporulation efficiency, close to 0.85. The spores obtained have a low dry weight and a reduced nitrogen content. In the case of buckwheat B, the active growth is shown to stop because of available mineral nitrogen depletion. No significant decrease in the water activity of the substrate is found during the protein synthesis, and the turgor potential remains high at the end of this period. Culture proceeds with new wall synthesis; the sporulation efficiency remains high and the spores obtained exhibit a high dry weight and a high nitrogen content. The bioenergetic balances show that the P/O ratio varies with the kind of substrate used; its value is close to 1.56 for the low water medium and to 2.21 for the high one. The ATP yield Z is always close to 1, and fungal development occurs with limitations of both anabolism and catabolism on buckwheat B and only of anabolism and catabolism on buckwheat B and only of anabolism on buckwheat A.     

High-level xylanase production by alkaliphilic Bacillus pumilus ASH under solid-state fermentation

Bacillus pumilus ASH produced a high level of an extracellular and thermostable xylanase enzyme when grown using solid-state fermentation (SSF). Among a few easily available lignocellulosics tested, wheat bran was found to be the best substrate (5,300 U/g of dry bacterial bran). Maximum xylanase production was achieved in 72 h (5,824 U/g). Higher xylanase activity was obtained when wheat bran was moistened with deionized water (6,378 U/g) at a substrate-to-moisture ratio of 1:2.5 (w/v). The optimum temperature for xylanase production was found to be 37°C. The inoculum level of 15% was found to be the most suitable for maximum xylanase production (7,087 U/g). Addition of peptone stimulated enzyme production followed by yeast extract and mustard oil cake, whereas glucose, xylose and malt extract greatly repressed the enzyme activity. Repression by glucose was concentration-dependent, repressing more than 60% of the maximum xylanase production at a concentration of 10% (w/v). Cultivation in large enamel trays yielded a xylanase titre that was slightly lower to that in flasks. The enzyme activity was slightly lower in SSF than in SmF but the ability of the organism to produce such a high level of xylanase at room temperature and with deionized water without addition of any mineral salts in SSF, could lead to substantial reduction in the overall cost of enzyme production. This is the first report on production of such a high level of xylanase under SSF conditions by bacteria.