应用Coriolus vericolor菌丝球脱色染料及印染废水的研究

对白腐真菌(Coriolus vericolor)产生漆酶进行〖JP2〗了研究。发现该菌产漆酶的最适初始pH值为45。提高微量元素浓度或添加藜芦醇都可使C.versicolor的产酶能力增加,添加Tween80会有一定的抑制作用。采用C.versicolor菌丝球进行重复分批产酶试验,结果表明菌丝球的稳定性很好,同一批菌丝球可连续利用14次,平均每批酶活力可保持在672U/mL,产酶能力优于聚氨酯泡沫固定化菌丝。将粗酶液用于染料的脱色降解试验,在酶活力为3.3IU/mL〖JP〗,酸性橙浓度为500mg/L条件下,经过24h反应,脱色率达到98.5%;对含弱酸大红和卡布龙红的印染废水进行脱色试验,脱色率也达到了93%。     

枯草芽孢杆菌中性β-甘露聚糖酶的产生及性质

由土壤中分离出一株产中性β甘露聚糖酶的枯草芽孢杆菌(Bacillus subtilis),编号BM9602。该菌在液体培养条件下,产生中性β甘露聚糖酶。多糖能作为碳源,而单糖不能作为碳源;有机氮源优于无机氮源。产酶最适培养基组成：魔芋粉4%,牛肉蛋白胨和酵母膏各1%。产酶最适培养条件：培养基起始pH85,35℃,振荡培养36〖KG*3]h。以槐豆胶为底物,培养滤液中性β甘露聚糖酶活力为96IU/mL。酶在pH50～100和50℃下稳定;作用最适条件为pH60和50℃;水解魔芋粉和槐豆胶均产生寡聚糖。     

肝素酶产生菌的筛选及发酵条件

从土壤中筛选到一株活性较高的肝素酶产生菌株Corynebacterium sp.。培养及产酶最佳条件表明,最适培养基组成(g/L)：胰蛋白胨20,氯化钠1,磷酸氢二钾25,硫酸镁05,麦芽糖20,pH65。最适生长温度27℃,最佳产酶温度31℃。在500mL三角瓶中装40mL培养基,在30℃,200r/min摇床上培养24 h,每升发酵液可产酶1700u。     

固定化青霉素V酰化酶的制备及性质

尖镰孢(Fusarium oxysporum)FP941青霉素V酰化酶经γ氧化铝吸附洗脱、硫酸铵沉淀和脱盐处理后,固定在环氧丙烯聚合物载体上,湿固定化酶表现活力为217 IU/g,固定化产率为53%。固定化酶作用最适温度为55℃,最适pH为80;在pH50～110及50℃以下稳定;37℃使用25次后,酶活力保留90%。     

硫酸软骨素酶产生菌的筛选及酶的分离纯化

利用平板快速筛选法,从鱼腹中筛选到一株产生硫酸软骨素酶的细菌YH311,通过生物特性和生化反应试验考察,初步鉴定为温和气单胞菌（Aeromonas sobria）。培养至36h时,该菌株产酶达到高峰期,培养液的酶活力达09U/mL。利用超声波破碎菌体细胞,分别测定培养液和菌体细胞的酶活力,发现培养液的酶活力要远远大于菌体细胞的酶活力,显示该酶为分泌型表达,属于胞外酶。发酵液经离心后,上清液用硫酸铵分级沉淀,再分别经过CMCellulose、QAEsephadex A50和Sephadex G150层析柱进行逐级分纯,并跟踪酶活,最后获得硫酸软骨素酶。SDSPAGE检测为单一条带,其分子量约为80kD。     

枯草芽孢杆菌中性内切β-甘露聚糖酶的纯化及性质

枯草芽孢杆菌(Bacillus subtilis)BM9602产生的中性内切β甘露聚糖酶(endoβ1,4Dmannan mannanohydrolase,EC,3.2.1.78)经硫酸铵分级沉淀、DEAE纤维素(DE22)离子交换柱层析,得到电泳纯的样品,提纯了455倍,收率为59%。用SDSPAGE测得该酶的分子量为35kD。用PAGEIEF测得其等电点pI为45。酶反应的最适pH为5.8,最适温度为50℃。该酶在pH60～80,50℃以下稳定。金属离子Hg2+和Ag+对酶活性强烈抑制。酶对槐豆胶、羟丙基瓜胶、田菁胶和魔芋粉的Km值分别为38、149、113和24mg/mL,Vmax值分别为245、865、384和198μmol.min-1mg-1。酶水解甘露聚糖为甘露寡糖(不含单糖)。     

贝壳状革耳菌和黄孢平革菌固体培养酶系比较

白腐菌黄孢平革菌(Phanerochaete chrysosporium) 与贝壳状革耳菌(Panus conchatus)在类似自然状态的固体培养条件下酶的分泌情况有 较大差异。P.conchatus和P.chrysosporium的主要木素降解酶分别是漆酶和锰过氧化物酶 ;两种菌均产生较高水平的木聚糖酶;P.conchatus在整个培养过程中所产生的内切葡 聚糖酶、微晶纤维素酶和纤维二糖酶活力均比P.chrysosporium相应酶的活力低得多, 尤其是内切葡聚糖酶。研究结果初步揭示了P.conchaus降解木素的主要酶系及选择性降 解木素的原因。     

丝状真菌表达分泌系统中受体菌的构建

黑曲霉糖化酶高产菌株T21经紫外诱变后, 通过酪蛋白平板和蛋白酶活性测定筛选出胞外酸性蛋白酶活力仅为原株076%的菌株A.nigerT21-201,其生长特性和产糖化酶活力与原株基本一致。利用原生质体PEG法将含有报告基因vhb的表达分泌质粒Pgt10-vhb通过与选择标记质粒的共转化导入此蛋白酶部分缺陷株及其原株T21,检测在蛋白酶缺陷株Aspergillus niger T21-201 和原株T21中VHb的分泌表达,结果表明在A.nigerT21-201中VHb表达水平显著高于原株,但Northern blot却显示在两菌株中^vnb基因的转录水平近似,由此证明酸性蛋白酶缺陷对保护外源蛋白产生了显著效果。      

焦曲霉产木聚糖酶的研究*

从1144株真菌中筛选到一株产木聚糖酶活力较高的焦曲霉(Aspergillus ustus)。该菌株适宜的产酶条件为在4%麸皮液中添加0.5%葡萄糖,0.4%硝酸钠及0.1%氯化钠,30℃振荡培养6d,木聚糖酶活力可达2176 u/mL。酶反应的最适温度为55℃,最适pH为5.5,在pH5～8酶活力稳定。45℃保温1h,酶活力剩余35%。酶水解桦木木聚糖的Km值为4.3×10^-3g/mL,V_max值为4.9mg/(mL·min)。酶解产物以木三糖和木四糖为主,表明该酶是一种典型的内切糖苷酶。     

产气肠杆菌几丁质酶的分离纯化及性质研究

从自然罹病死亡的草原毛虫(Gynephorap ruoergnesis)体内分离到一株产气肠杆菌(Enterobacter aerogenes),它在几丁质的诱导下能产生较高活性的几丁质酶。发酵液经硫酸铵盐析、DEAE纤维素柱层析和Sephadex G-100柱层析分离出几丁质酶。用SDSPAGE测得该酶的分子量为425kD。水解几丁质的Km值为2.88mg/mL-1。酶反应的最适温度为55℃,最适pH值为60,金属离子对几丁质酶活性影响较大,其中Zn2+、Ba2+、Ca2+和Mn2+对酶有较强的激活作用,而Hg2+、Co2+和Mg2+则有较强的抑制作用。     

Enhanced cellulase production through random mutagenesis of Talaromyces pinophilus OPC4-1 and fermentation optimization

Reducing cellulase cost remains a major challenge for lignocellulose to fuel and chemical industries. In this study, mutants of a novel wild-type cellulolytic fungal strain Talaromyces pinophilus OPC4-1 were developed by consecutive UV irradiation, N-methyl-N`-nitro-N-nitrosoguanidine (NTG) and ethylmethane sulfonate (EMS) treatment. A potential mutant EMM was obtained and displayed enhanced cellulase production. Using Solka Floc cellulose as the substrate, through fed-batch fermentation, mutant strain T. pinophilus EMM generated crude enzymes with an FPase activity of 27.0 IU/mL and yield of 900 IU/g substrate. When corncob powder was used, strain EMM produced crude enzymes with an FPase activity of 7.3 IU/mL and yield of 243.3 IU/g substrate. In addition, EMM crude enzymes contained 29.2 and 16.3 IU/mL β-glucosidase on Solka Floc cellulose and corncob power, respectively. The crude enzymes consequently displayed strong biomass hydrolysis performance. For corncob hydrolysis, without supplement of any commercial enzymes, glucose yields of 591.7 and 548.6 mg/g biomass were obtained using enzymes produced from Solka Floc cellulose and corncob powder, respectively. It was 553.9 mg/g biomass using the commercial enzyme mixture of Celluclast 1.5 L and Novozyme 188. Strain T. pinophilus EMM was therefore a potential fungus for on-site enzyme production in biorefinery processes.     

中性内切型纤维素酶在毕赤酵母中高水平表达的研究

中性内切型纤维素酶在纺织及造纸工业具有重要的应用,为了进一步提高从我国草菇中克隆的一种新的中性内切型纤维素酶(EG1)在Pichiapastoris中的表达水平,我们进行了提高基因拷贝数及高密度发酵等多种手段实现其高水平表达的研究。在前期研究的基础上,利用对已整合eg1的重组子再转化的方法,从含有2000μgLZeocin的YPDSZ平板上筛选到高抗Zeocin转化子,在摇瓶培养条件下,该转化子表达量比原来提高了3.8倍,在pH4～8条件下均有稳定表达,接种量(OD600=5.0)表达水平最好,提高甲醇的诱导浓度对表达有显著的促进作用。用3.2L发酵罐进行了高密度发酵,甲醇诱导95.5h后达到最高值,比摇瓶培养再提高了6.4倍,因此利用高抗Zeocin转化子及高密度发酵的手段,使EG1的表达水平提高了34倍,蛋白表达量达8.80mgmL,EG1酶活达到543.36IUmL,实现了中性内切纤维素酶的高水平表达,本研究将大大促进建立我国纺织用纤维素酶大规模高效生产技术。     

应用Coriolus vericolor 菌丝球脱色染料及印染废水的研究

对白腐真菌（Coriolus vericolor）产生漆酶进行了研究。发现该菌产漆酶的最适初始pH值为4．5。提高微量元素浓度或添加藜芦醇都可使C.versiclor的产酶能力增加,添加Tween80会有一定的抑制作用。采用C.versicolor菌丝球进行重复分批产酶试验,结果表明菌丝球的稳定性很好,同一批菌丝球可连续利用14次,平均每批酶活力可保持在6．72U／mL,产酶能力优于聚氨酯泡沫固定化菌丝。将粗酶液用要料的脱色降解试验,在酶活力为3．3IU／mL,酸性橙浓度为500mg/L条件下,经过24h反应,脱色率达到98．5％;对含弱酸大红和卡布龙红的印染废水进行脱色试验,脱色率也达到了93％。     

Production of multi-fiber modifying enzyme from Mamillisphaeria sp. for refining of recycled paper pulp

Enzymatic modification of pulp is receiving increasing interest for energy reduction at the refining step of the paper-making process. In this study, the production of a multi-fiber modifying enzyme from Mamillisphaeria sp. BCC8893 was optimized in submerged fermentation using a response-surface methodology. Maximal production was obtained in a complex medium comprising wheat bran, soybean, and rice bran supplemented with yeast extract at pH 6.0 and a harvest time of 7 d, resulting in 9.2 IU/mL of carboxymethyl cellulase (CMCase), 14.9 IU/mL of filter paper activity (FPase), and 242.7 IU/mL of xylanase. Treatment of old corrugated container pulp at 0.2-0.3 IU of CMCase/g of pulp led to reductions in refining energy of 8.5-14.8%. The major physical properties were retained, including tensile and compression strength. Proteomic analysis showed that the enzyme was a complex composite of endo-glucanases, cellobiohydrolases, beta-1,4-xylanases, and beta-glucanases belonging to various glycosyl hydrolase families, suggestive of cooperative enzyme action in fiber modification, providing the basis for refining efficiency.     

Production of extracellular exoinulinase from Kluyveromyces marxianus YS-1 using root tubers of Asparagus officinalis

Root tubers of Asparagus officinalis were used as a source of raw inulin for the production of exoinulinase (EC 3.2.1.7) from Kluyveromyces marxianus YS-1. Root extract prepared at 10kg/cm2 pressure for 10min showed maximum inulinase production. Medium components and process parameters were standardized to improve the enzyme production. Inulinase yield of 40.2IU/mL in a medium containing raw inulin (3.5%), beef extract (2%), SDS (0.001%), Mn2+ (2.0mM), Mg2+ (1.5mM), Co2+ (2mM) and pH 6.5 has been obtained under agitation (150rpm) after 60h of incubation at 30 degrees C at shake flask level. After optimization, the enzyme production was 4.8 times more than the basal medium. To test the feasibility of raw inulin from A. officinalis for the production of inulinase, trials were also made in a bioreactor (1.5L). Inulinase activity of 50.2IU/mL was obtained from raw inulin (4.0%) under agitation (200rpm) and aeration (0.75vvm) at 30 degrees C after 60h of fermentation. Inulinase yield in bioreactor was almost six times higher than the basal medium used initially in shake flask.     

复合与合成培养基对大肠杆菌胞外生产α-环糊精葡萄糖基转移酶的影响

为实现来源于Paenibacillus macerans JFB05-01的α-环糊精葡萄糖基转移酶（α-CGT酶）的高效胞外表达,以含分泌型信号肽OmpA的大肠杆菌E.coli BL21（DE3）{pET-20b（+）/α-cgt}为研究对象,比较了其在不同诱导条件下复合与合成培养基中生长产酶的规律。结果表明在添加甘氨酸的条件下采用合成培养基,以0.8 g/L/h的乳糖进行流加诱导所得的胞外酶活和生产强度最高。在该条件下发酵30小时后胞外α-CGT酶的环化活性达113.0U/ml（水解活性为79 100.0IU/ml）,是复合培养基胞外产酶的2.3倍,完全满足工业化生产的需求。     

Production of cellulase enzymes and hydrolysis of steam-exploded wood

Steam-exploded aspen has been examined as a candidate feedstock for both cellulose production and enzymatic hydrolysis of wood. Batch and fed-batch cultivation methods were evaluated and compared with previous experiments using ball-milled, crystalline cellulose (Solka Floe). Batch cultivation of Trichoderma reesei Rut C-30 on 9 wt% water-washed aspen yielded enzyme productivities and activities comparable to those obtained on Solka Floe (40 FP IU/L-h; 7. 5 FP IU/mL). Fed-batch cultivation of Rut C-30 resulted in higher enzyme productivities and tilers than batch cultivation (50 FP IU/L-h; 15 FP IU/mL). However, the overall enzyme production performance was lower than on Solka Floe at comparable cellulose feeding rates and concentrations. This may be due to the accumulation of steam explosion by-products and lignin in the fermentor.The hydroiysis of water-washed steam-exploded aspen was performed at different enzyme loadings and wood concentrations. Glucose production, using 10 and 15wt% suspension, showed that while glucose concentration increased with wood load, the yield of glucose derived from cellulose decreased. With 10wt% suspensions, it was possible to obtain a cellous conversion to glucose above 95%. Low cellulose levels in the hydrolyzates indicated that the filter paper activity ratios (approximately 1.5), a significant result since the fungus was grown exclusively on wood. mIt also suggested that the observed yield decrease is more likely to be caused by glucose than cellobiose inhibition of the enzymes.     

Optimization of L-asparaginase production from novel Enterobacter sp., by submerged fermentation using response surface methodology

The culture conditions and nutritional rations influencing the production of extra cellular antileukemic enzyme by novel Enterobacter aerogenes KCTC2190/MTCC111 were optimized in shake-flask culture. Process variables like pH, temperature, incubation time, carbon and nitrogen sources, inducer concentration, and inoculum size were taken into account. In the present study, finest enzyme activity achieved by traditional one variable at a time method was 7.6 IU/mL which was a 2.6-fold increase compared to the initial value. Further, the L-asparaginase production was optimized using response surface methodology, and validated experimental result at optimized process variables gave 18.35 IU/mL of L-asparaginase activity, which is 2.4-times higher than the traditional optimization approach. The study explored the E. aerogenes MTCC111 as a potent and potential bacterial source for high yield of antileukemic drug.     

Production of alkali tolerant cellulase free xylanase in high levels by Bacillus pumilus SV-205

The fermentation conditions were optimized for hyper production of xylanase from Bacillus pumilus SV-205. The bacterium secretes high levels (7382.7±1200 IU/mL) of cellulase-free xylanase using wheat bran led to 21.63 fold increase in activity. A combination of yeast extract and peptone stimulated highest xylanase production (2448.0 IU/mL) as compared to other combinations. The most important characteristic of the enzyme is its high pH stability (100%) over a broad pH range of 6-11 for 24h. Thermostability studies revealed that enzyme retained 65% activity after an incubation of 2h at 60°C. The level of production is remarkable as compared to earlier reports.     

Studies on quantitative physiology of Trichoderma reesei with two-stage continuous culture for cellulose production

By employing a two-stage continuous-culture system, some of the more important physiological parameters involved in cellulose biosynthesis have been evaluated with an ultimate objective of designing an optimally controlled cellulose process. The two-stage continuous-culture system was run for a period of 1350 hr with Trichoderma reesei strain MCG-77. The temperature and pH were controlled at 32°C and pH 4.5 for the first stage (growth) and 28°C and pH 3.5 for the second stage (enzyme production). Lactose was the only carbon source for the both stages. The ratio of specific uptake rate of carbon to that of nitrogen, Q(C)/Q(N), that supported good cell growth ranged from 11 to 15, and the ratio for maximum specific enzyme productivity ranged from 5 to 13. The maintenance coefficients determined for oxygen, M_O, and for carbon source, M_C, are 0.85 mmol O₂/g biomass/hr and 0.14 mmol hexose/g biomass/hr, respectively. The yield constants determined are: Y_X/O = 32.3 g biomass/mol O₂, Y_X/C = 1.1 g biomass/g C or Y_X/C = 0.44 g biomass/g hexose, Y_X/N = 12.5 g biomass/g nitrogen for the cell growth stage, and Y_X/N = 16.6 g biomass/g nitrogen for the enzyme production stage. Enzyme was produced only in the second stage. Volumetric and specific enzyme productivities obtained were 90 IU/liter/hr and 8 IU/g biomass/hr, respectively. The maximum specific enzyme productivity observed was 14.8 IU/g biomass/hr. The optimal dilution rate in the second stage that corresponded to the maximum enzyme productivity was 0.026 ～ 0.028 hr^?1, and the specific growth rate in the second stage that supported maximum specific enzyme productivity was equal to or slightly less than zero.