里氏木霉与米根霉混合固态发酵产纤维素酶

以里氏木霉及米根霉单菌固态发酵为对象,考察不同混合发酵形式对里氏木霉与米根霉混合固态发酵产纤维素酶的影响。结果表明:同时接种里氏木霉与米根霉,试验考察的两菌种接种量比1∶1(以孢子个数计)及5∶1条件下,两菌未产生明显协同产酶作用。米根霉延时(24 h)接种且菌种量比5∶1以及米根霉延时(48 h)接种且菌种量比1∶1,2种发酵形式产酶情况类似,滤纸酶活(FPA)及羧甲基纤维素酶(CMCase)酶活相对米根霉单菌发酵有所提高,而β-葡萄糖苷酶(β-GA)酶活相对里氏木霉单菌固态发酵结束时分别增加4.66及4.40倍,可以发现两菌产生一定协同作用。在米根霉延时(48 h)接种且菌种量比5∶1的发酵形式下,FPA及CMCase在发酵第7天酶活分别达到44.04 IU/g、627.14 U/g(以1 g干曲计),分别是里氏木霉固态单菌发酵产酶达到稳定期时酶活的1.36和1.63倍,两菌产生了有效的协同作用。     

纤维素酶制备过程中不同底物、菌种的研究

比较用两个菌（黑氏木霉Ｔrichoderma reesei RutC-30及其改良菌种）和不同的纤维底物备纤维素酶解效果与酶系构成,研究表明,以玉米秸秆米为底物,发言奶菌种产酶时间比里氏木霉早２天,且改良菌种滤纸酶活要比里氏木霉高,分别为２．３９ＦＰＩＵ／mL和１．８５ＦＰＩＵ／mL,里木氏霉已实际运用到生产工艺中,如把改良菌种运用至生产工艺必将产生可观的经济效益。     

里氏木霉和鸡腿菇利用秸秆共发酵产木质降解酶

为了更好地利用农业废弃物,提高其综合利用率,减少传统化学方法及秸秆焚烧过程造成的环境污染,实验对鸡腿菇、黑曲霉和里氏木霉3株产木质纤维素降解酶系的菌株进行混合平板产酶筛选,结果显示鸡腿菇和里氏木霉平板培养相容性良好,且产酶量高。在相容性实验的基础上,对鸡腿菇和里氏木霉的最优产酶条件进行了研究。在最优条件下:鸡腿菇和里氏木霉接种比例按5:2,接种时间间隔为12h,26oC、150r/min下,发酵3d产漆酶活力达3267.2U/mL,比单独发酵提高106%。     

黑曲霉与里氏木霉固态混合发酵产β-葡萄糖苷酶

对黑曲霉NL02与里氏木霉RUT-C30固态混合发酵产β-葡萄糖苷酶的发酵培养基进行优化,研究培养基含水率、C源、N源、接种量、温度和2种菌种不同延长接种时间与接种比例对β-葡萄糖苷酶活力的影响。研究表明：麸皮17.5 g、玉米芯7.5 g、（NH4）2SO4 0.40 g、尿素0.37 g、黑曲霉孢子接入量为107个接种到250 mL三角瓶中,温度30 ℃、摇床转速100 r/min时,里氏木霉以105个孢子与黑曲霉同时接入,每克干曲所得β-葡萄糖苷酶的活力为132.45 IU,较黑曲霉单独培养时的104.35 IU提高了26.94%。     

甘蔗渣固态发酵产纤维素酶

以甘蔗渣和麸皮混合作为固态发酵产酶培养基,采用单因素优化实验对里氏木霉固态发酵产纤维素酶进行优化。结果表明,在50 m L体系培养基中,在底物绝干原料5.2 g、甘蔗渣与麸皮质量比7∶3、氮源((NH4)2SO4)7.5 g/L、产酶诱导物1.6 g/L、表面活性剂(聚乙二醇PEG6000)0.1 g、发酵起始p H 4.4、培养基中里氏木霉孢子接入量5×105个的条件下,温度30℃时发酵120 h,里氏木霉固态发酵产纤维素酶的酶活达76.39 IU/g,是起始优化前20.29 IU/g的3.76倍。     

一株高效降解纤维素菌株的筛选及其产酶能力研究

目的筛选并鉴定一种产纤维素酶能力较高的菌株,为纤维素的高效利用贮备菌源。方法用羧甲基纤维素钠(CMC-Na)平板筛选产纤维素酶菌株,通过LB培养基对其进行纯化,16SrDNA基因序列分析其分类地位,3,5-二硝基水杨酸法(DNS)测定其产酶能力。结果分离纯化得到的产纤维素酶菌株(S1)为芽胞杆菌属(Bacillus genus)的短小芽胞菌,在最佳产酶条件下产酶含量达到1 204U/mL,产纤维素酶能力与里氏木霉(Trichoderma reesei)相当,但其产酶速率较里氏木霉低。结论 S1是一株产纤维素酶能力较高的菌株,产酶条件温和,初步鉴定为一种新种,具有较高研究及应用价值。     

高效转化法定向进化里氏木霉的纤维素酶

优化了根癌农杆菌介导的里氏木霉的转化方法,得出转化的最适条件:共培养pH 5.3、共培养温度24℃、乙酰丁香酮浓度200μmol/L、根癌农杆菌OD660值0.8、里氏木霉孢子预萌发时间3 h。此时转化率为13 000个转化子(以107个里氏木霉孢子计),是未优化条件下的27倍以上。利用此高效转化法,结合强化纤维二糖水解酶基因II表达的操作,从324个转化子中筛选到了1株优良的里氏木霉转化子C10,发酵5 d后,纤维二糖水解酶活力达(122.44±5.91)U/m L,是初始菌株的5.4倍;滤纸酶活力达(28.92±2.45)IU/m L,是初始菌株的4.3倍。与初始菌株所产纤维素酶相比,转化子C10所产纤维素酶降解玉米秸秆和稻草的能力有明显的提高。本研究为里氏木霉的基因工程改造及其纤维素酶的定向进化提供了有价值的实验数据。     

固态混合发酵提高木聚糖酶和纤维素酶活力的研究

研究了接种比例、接种时间、碳源、氮源等因素对木霉和黑曲霉混合发酵产木聚糖酶和纤维素酶的影响。试验结果表明,当木霉和黑曲霉按4:6同时接种,以玉米芯3．75g、麸皮3．75g、葡萄糖37．5mg为混合碳源,Mandels营养盐11．5mL、添加NH_4NO_37．5mg为氮源,在84h产纤维素酶活力达到230IU/g干物质,木聚糖酶活力达到1308IU/g干物质,与两菌纯培养相比,纤维素酶活力提高163％,木聚糖酶活力提高79．5％。     

新颖阿魏酸酯酶在黑曲霉中异源表达及其应用

本研究依托桧状青霉的基因组学和蛋白组学数据,发现一种新型的阿魏酸酯酶。利用PCR技术成功扩增得到桧状青霉阿魏酸酯酶的基因,构建真菌表达盒通过原生质体的方法将其转化到黑曲霉中。通过SDS-PAGE检测和酶活力检测验证该阿魏酸酯酶成功地在黑曲霉胞外分泌表达。根据氨基酸序列相似性和底物特异性分析都显示该阿魏酸酯酶属于C型的阿魏酸酯酶,与常见的A型、B型阿魏酸酯酶性质区别较大。将成功表达阿魏酸酯酶的黑曲霉胞外酶液复配里氏木霉酶液后,水解不同生物质材料,纤维素水解效率均有大幅程度地提高,玉米秸秆,麦麸,玉米芯,木薯酒糟的水解效率分别提高68.8%,38.6%,15.6%和20.0%。该研究为新颖阿魏酸酯酶应用以及今后里氏木霉纤维素酶酶系复配提供新的思路。     

高效低成本纤维素酶诱导物的制备、筛选及应用

本研究利用玉米芯、甘蔗渣、脱木素木糖渣及粗纤维诱导里氏木霉产纤维素酶,对4种材料进行成份测定,然后以逐步添加的方式与微晶纤维素混合诱导里氏木霉产纤维素酶,和使用微晶纤维素诱导产酶对比,玉米芯含有的纤维素代替总纤维素的50%时,酶活力降低2个单位,蛋白减少0.8 g左右,其酶水解能力降低0.4%,对其产纤维素酶的水解能力没产生不利影响。甘蔗渣纤维素替代量可以达到30%,酶活力有1个单位的降低,蛋白分泌降低0.5 g左右,酶的水解能力提高7%左右。脱木素木糖渣纤维素替代量也可达到50%,酶活力和蛋白降低分别达到0.5个单位和0.2 g左右,酶水解能力降低了4.45%。粗纤维的利用可以达到100%替代,对里氏木霉产酶的酶活力影响有0.3个单位之差,水解能力降低1.625%。这说明这几种物质可以部分替代或者完全替代微晶纤维素,诱导里氏木霉发酵产纤维素酶,特别是由玉米芯和甘蔗渣制备的脱木素木糖渣和粗纤维有着较高的应用前景。该研究对降低纤维素酶的生产成本及其工业化应用具有重要意义。     

2种纤维素酶水解效果比较及酶蛋白组分分析

比较了自产纤维素酶和商品纤维素酶的水解效果,并采用超滤、层析、SDS-PAGE相结合的方法分析2种纤维素酶蛋白组分的差异。里氏木霉以纸浆为C源合成的自产纤维素酶的水解得率高于商品纤维素酶,自产纤维素酶水解48h的得率为66.24%,商品纤维素酶的得率为52.19%。自产纤维素酶中存在着Cel6A酶组分和XYNⅡ酶组分,而商品纤维素酶中没有检测到这2种酶组分。自产纤维素酶和商品纤维素酶的Cel1A酶组分和Cel7A酶组分间存在着分布和含量上的差异。自产纤维素酶在相对分子质量(2.5～3.5)×104范围内存在着几条蛋白条带,而商品纤维素酶则是在相对分子质量3.5×104附近存在着几条蛋白条带。     

Enhanced cellulolytic enzyme production by the synergism between Trichoderma reesei RUT-C30 and Aspergillus niger NL02 and by the addition of surfactants

Two improvement approaches comprising of a mixed culture of Trichoderma reesei and Aspergillus niger and the addition of surfactants were employed in this study in order to enhance cellulolytic enzyme production as well as to improve the composition. Different delay times of A. niger inoculation (0, 24, and 48 h) and inoculum ratios of T. reesei versus A. niger (1:1 and 5:1) derived six mixed culture forms, which were 0 h/1:1, 0 h/5:1, 24 h/1:1, 24 h/5:1, 48 h/1:1, and 48 h/5:1. It was found that the form 48 h/5:1 allowed the highest FPA, 3.30 ± 0.34 IU/mL, and a relatively high BGA, 1.01 ± 0.25 IU/mL, thereafter being selected for the subsequent improvement step addition of surfactants. Among the three surfactants, including Triton X-100, CHAPS and sodium taurocholate, the third one was found to be the best one giving rise to the highest FPA and BGA, 5.02 ± 0.40 and 1.48 ± 0.28 IU/mL, respectively. Differently sourced cellulases were compared in the enzymatic hydrolysis of steam-exploded corn stover (SECS). Moreover, the cellulase produced by the mixed culture form 48 h/5:1 using SECS as a substrate showed the highest yield at 80.93 ± 2.04%, indicating that the composition of this cellulase was improved by the mixed culture of T. reesei and A. niger. The results validate that these two improvement approaches are efficient and applicable in cellulase production.     

The enzymatic hydrolysis and fermentation of pretreated wheat straw to ethanol

Autohydrolysis and ethanol-alkali pulping were used as pretreatment methods of wheat straw for its subsequent saccharification by Trichoderma reesei cellulase. The basic hydrolysis parameters, i.e., reaction time, pH, temperature, and enzyme and substrate concentration, were optimized to maximize sugar yields from ethanol-alkali modified straw. Thus, a 93% conversion of 2.5% straw material to sugar syrup containing 73% glucose was reached in 48 h using 40 filter paper units/g hydrolyzed substrate. The pretreated wheat straw was then fermented to ethanol at 43 degrees C in the simultaneous saccharification and fermentation (SSF) process using T. reesei cellulase and Kluyveromyces fragilis cells. From 10% (w/v) of chemically treated straw (dry matter), 2.4% (w/v) ethanol was obtained after 48 h. When the T. reesei cellulase system was supplemented with beta-glucosidase from Aspergillus niger, the ethanol yield in the SSF process increased to 3% (w/v) and the reaction time was shortened to 24 h.     

一株产纤维素酶真菌的筛选、鉴定及酶学性质初步研究

经过初筛和复筛从土样中分离出1株高产纤维素酶真菌SNB9,经形态学和ITS序列分析。鉴定为黑曲霉（Aspergu Uusniger）。生长条件的测定显示该菌生长范围偏酸。发酵后纤维素酶的最适作用pH在4．0—5．0,最适作用温度在45—55℃。滤纸酶活为9．29U／mL,C,酶活为23．69U／mL,CMCase酶活为38．23U／mL,β-葡萄糖苷酶活为65．52U／mL。发酵液中除了纤维素酶,还发现有辅助酶,包括木聚糖酶、淀粉酶、果胶酶、蛋白酶。     

Study of a High-Yield Cellulase System Created by Heavy-Ion Irradiation-Induced Mutagenesis of Aspergillus niger and Mixed Fermentation with Trichoderma reesei

The aim of this study was to evaluate and validate the efficiency of ¹²C⁶⁺ irradiation of Aspergillus niger (A. niger) or mutagenesis via mixed Trichoderma viride (T. viride) culturing as well as a liquid cultivation method for cellulase production via mixed Trichoderma reesei (T. reesei) and A. niger culture fermentation. The first mutagenesis approach was employed to optimize yield from a cellulase-producing strain via heavy-ion mutagenesis and high-throughput screening, and the second was to effectively achieve enzymatic hydrolysis of cellulase from a mixed culture of mutant T. viride and A. niger. We found that ¹²C⁶⁺-ion irradiation induced changes in cellulase biosynthesis in A. niger but had no effect on the time course of the synthesis. It is notable that the exoglucanases (CBH) activities of A. niger strains H11-1 and H differed (6.71 U/mL vs. 6.01 U/mL) and were significantly higher than that of A. niger mutant H3-1. Compared with strain H, the filter paper assay (FPA), endoglucanase (EG) and β-glucosidase (BGL) activities of mutant strain H11-1 were increased by 250.26%, 30.26% and 34.91%, respectively. A mixed culture system was successfully optimized, and the best ratio of T. reesei to A. niger was 5:1 for 96 h with simultaneous inoculation. The BGL activity of the mixed culture increased after 72 h. At 96 h, the FPA and BGL activities of the mixed culture were 689.00 and 797.15 U/mL, respectively, significantly higher than those of monocultures, which were 408.70 and 646.98 U/mL for T. reesei and 447.29 and 658.89 U/mL for A. niger, respectively. The EG activity of the mixed culture was 2342.81 U/mL, a value that was significantly higher than that of monocultures at 2206.57 U/mL for T. reesei and 1727.62 U/mL for A. niger. In summary, cellulose production and hydrolysis yields were significantly enhanced by the proposed combination scheme.     

Kinetics of cellobiose hydrolysis using cellobiase composites from Ttrichoderma reesei and Aspergillus niger

The enzymatic hydrolysis of cellulose to glucose involves the formation of cellobiose as an intermediate. It has been found necessary(1) to add cellobiase from Aspergillus niger (NOVO) to the cellobiase component of Trichoderma reesei mutant Rut C-30 (Natick) cellulase enzymes in order to obtain after 48 h complete conversion of the cellobiose formed in the enzymatic hydrolysis of biomass. This study of the cellobiase activity of these two enzyme sources was undertaken as a first step in the formation of a kinetic model for cellulose hydrolysis that can be used in process design. In order to cover the full range of cellobiose concentrations, it was necessary to develop separate kinetic parameters for high- and low-concentration ranges of cellobiose for the enzymes from each organism. Competitive glucose inhibition was observed with the enzymes from both organisms. Substrate inhibition was observed only with the A. niger enzymes.     

Evaluation of culture conditions for cellulase production by two Trichoderma reesei mutants under solid-state fermentation conditions

Response surface methodology (RSM) was used to evaluate the effects of fermentation parameters for cellulase production by Trichoderma reesei QM9414 and T. reesei MCG77 in solid-state fermentation using rice bran as substrate. Initial pH, moisture content and temperature were optimized using filter paper activity (FPA) as response. Statistical analysis of the results for T. reesei QM9414 showed that only moisture content had significant effect on cellulase activity and had a linear effect on enzyme activity (maximum enzyme activities were obtained at 70% moisture content). The results for T. reesei MCG77 showed that temperature and moisture content were the most significant parameters for cellulase activity. The optimum cellulase production was in the temperature range of 25-30 degrees C and moisture content between 55% and 70%. After the optimization, the FPA in T. reesei MCG77 was increased by 2.5 folds compared to that of T. reesei QM9414.     

Enzymic saccharification of sugarcane bagasse pretreated by autohydrolysis-steam explosion

Pretreatment of bagasse by autohydrolysis at 200 degrees C for 4 min and explosive defibration resulted in the solubilization of 90% of the hemicellulose (a heteroxylan) and in the production of a pulp that was highly susceptible to hydrolysis by cellulases from Trichoderma reesei C-30 and QM 9414, and by a comercial preparation, Meicelase. Saccharification yields of 50% resulted after 24 h at 50 degrees C (pH 5.0) in enzymic digests containing 10% (w/v) bagasse pulps and 20 filter paper cellulase units (FPU). Saccharifications could be increased to more than 80% at 24 h by the addition of exogenous beta-glucosidase from Aspergillus niger. The crystallinity of cellulose in bagasse remained unchanged following autohydrolysis-explosion and did not appear to hinder the rate or extent of hydrolysis of cellulose. Autohydrolysis-exploded pulps extracted with alkali or ethanol to remove lignin resulted in lowere conversions of cellulose (28-36% after 25 h) than unextracted pulps. Alkali extracted pulps arising from autohydrolysis times of more than 10 min at 200 degrees C were less susceptible to enzymic hydrolysis than unextracted pulps and alkali-extracted pulps arising from short autohydrolysis times (e.g., 2 min at 200 degrees C). Autohydrolysis-explosion was as effective a pretreatment method as 0.25M NaOH (70 degrees C/2 h) both yielded pulps that resulted in high cellulose conversions with T. reesei cellulase preparations and Meicelase. Supplementation of T. reesei C-30 cellulose preparations with A. niger beta-glucosidases was effective in promoting the conversion of cellulose into glucose. A ration of FPU to beta-glucosidase of 1:1.25 was the minimum requirement to achieve more than 80% conversion of cellulose into glucose within 24 h. Other factors which influenced the extent of saccharification of autohydrolysis-exploded bagasse pulps were the enzyme-substrate ratio, the substrate concentration, and the saccharification mode.     

Enzyme regeneration during hydrolysis of steam-pretreated willow and requirement for cellulase complex composition

In order to reduce the total enzyme consumption in high-solids static hydrolysis of nonwashed steam-exploded willow Salix caprea by mixed cellulase of Trichoderma reesei + Aspergillus foetidus, two different approaches were proposed. In the first case, the enzyme activity adsorbed on residual solids after extended hydrolysis was used for hydrolysis of the newly added substrate. The initial mixing of fresh and hydrolyzed substrates was sufficient for the adsorbed enzyme redistribution and conversion of the new substrate portion, and permanent mechanical stirring was not required. Feeding of two additional portions of the exploded hardwood adjusted to pH 4 with dry caustic into the reactor with simultaneous replacement of accumulated sugars with fresh buffer (pH 4.5) resulted, on average, in a 90% conversion of cellulose at the final enzyme loading 8 IFPU per g ODM substrate, an average sugar concentration of 12%, and a glucose/xylose ratio of 5:1. In the second approach, weakly adsorbed cellulase fractions were used for static high-solids hydrolysis followed by their ultrafiltration recovery from the resultant sugar syrup. In contrast to the initial cellulase mixture whose residual activity in a syrup did not exceed 5-10% at the end of hydrolysis (48 h), up to 60% of weakly adsorbed enzyme fraction could be separated from sugar syrups by ultrafiltration and then reused. Weakly adsorbed enzymes displayed a hydrolysis efficiency of not less than 80% per IFPU enzyme consumed in extended hydrolysis of pretreated willow as compared to the original enzyme mixture. An electrophoretic study of the weakly adsorbed enzyme fraction identified T. reesei cellobiohydrolase II as the predominant component, whereas clear domination of T. reesei cellobiohydrolase I was found by electrophoresis of proteins tightly bound to hydrolysis residual solids.