一株高产木聚糖酶真菌的筛选及酶学性质分析

从近百份土样中,首先筛选得到具有明显半纤维素水解活性透明圈的菌株564株,其中202株的木聚糖酶活力用96孔板筛选方法进行了验证。结果显示：基于96孔深孔板测定的酶活力与初筛测得的透明圈活力趋势一致。最终筛选得到一株高产木聚糖酶的菌株ECU2023,经核糖体rDNA内部转录间隔区的序列对比,鉴定为泡盛曲霉（Aspergillus awamori）。研究获得了其最佳培养条件：pH6．0,培养时间4d,C源为30～40g/L玉米芯粉。经过（NH4）2SO4沉淀和Superdex G-75凝胶过滤层析后,其中主要木聚糖酶成分的最适反应pH为6．0,最适反应温度为50℃。     

木聚糖酶高产菌株的鉴定及产酶条件的优化

目的:通过了解木聚糖酶高产菌株A79的遗传背景.并优化其产木聚糖酶的液体发酵条件,为下一步工业化生产和木聚糖酶制剂的研制奠定基础.方法:通过形态观察和18S rDNA基因的分子系统进化分析,对菌株A79进行鉴定;通过单因素和均匀设计试验,优化其产胞外木聚糖酶的液体发酵条件.结果:通过对18S rDNA基因的分子系统进化分析,菌株A79被鉴定为黑曲霉(Asperillus niger A79).其最佳产酶培养基为:玉米芯5.0%,麸皮0.5%.纤维物质1.O%,玉米浆1.1%.(NH4)2SO40.8%,蛋白胨0.8%,CaCO3 0.5%,KH2PO4 0.23%,MgSO4,·7H2O 0.08%,微量元素(MaIldels)0.08%,pH自然.最佳发酵条件为:接种量5%(2.0×107),28℃、250r/min振荡培养96h.结论:经优化培养,酶活力由前期的50 000u/ml提高到90000u/ml,增加了近50%.     

厌氧菌群SVY42产酶条件分析及产木聚糖酶菌株的分离鉴定

以美国内华达州大盆地温泉采集样品为材料,富集获得纤维素及半纤维素高效稳定降解厌氧菌群SVY42,以巨菌草、甘蔗渣、废菇筒、羧甲基纤维素钠、滤纸、木聚糖为碳源,分析菌群SVY42产内切葡聚糖酶(CMC酶)、β-葡萄糖苷酶和木聚糖酶的情况。在此基础上,以木聚糖为底物筛选高产木聚糖酶的菌株。菌群SVY42在以巨菌草作为碳源时的β-葡萄糖苷酶活最高为0.23 U/mL,以木聚糖作为碳源时CMC酶活和木聚糖酶活均为最高,分别为0.31 U/mL和0.35 U/mL。从菌群SVY42中筛选得到1株高产木聚糖酶厌氧菌株SVY42-1,该菌在最适温度41℃和pH 8.0条件下,其木聚糖酶活力为0.26 U/mL,对其进行16S rDNA序列系统进化分析,SVY42-1与已知菌株的最高同源性仅为93.81%,初步鉴定属于新属。     

混合菌株降解褐藻胶的筛选、鉴定及产酶条件优化

为获得仿刺参（Apostichopus japonicus）肠道菌群中可有效降解褐藻胶的混合菌株,以海藻酸钠为唯一碳源配制培养基,以透明圈法进行初筛,DNS法和紫外法复筛,从已驯化仿刺参肠道中筛选得到4株高酶活力褐藻胶降解菌株S1、S2、S10和S11,经16S rDNA序列分析、电镜观察,确定菌株S2与S11分别为微杆菌属（Microbacterium sp.）和微小杆菌属（Exiguobacterium sp.）。对该4株菌株分别进行混合培养,获得菌株S2与S11最佳配比组合,并通过单因素试验及响应面优化试验对影响混合菌株产酶条件的发酵初始pH值、NaCl质量浓度、装液量和发酵温度4个因素进行优化。得到混合菌株最佳产酶条件为pH 8,NaCl质量浓度为40 g/L,装液量80 mL,温度28 ℃。在最佳发酵条件下,混合菌株酶活力可达94.78 U/mL,相比于优化前提高了43.9%,优化后混合菌株的酶活力显著提高。     

黑曲霉A3菌株木聚糖酶粗酶制剂的制备和性质

本文研究了黑曲霉（AspergillusnigerA3）菌株固体发酵培养的产酶过程,发酵3d产木聚糖酶活最高,固体曲最适浸提比为1：7（W／V）,通过60％～65％饱和度的硫酸按盐析,获得的木聚糖酶活力最高。冻干酶粉活力为15400u/g,得率为71％,40℃烘干酶粉活力为15395U／g,得率为51％,酶反应最适温度55℃,最适pH4．6,保温1h半失活温度（t1／2）为54℃,酶对四种不同底物半纤维素水解作用的亲合性为鼓皮最强,稻草最弱。     

1株褐藻胶降解菌的筛选、鉴定及产酶条件优化

为获得可产生褐藻胶裂解酶并高效降解褐藻胶的菌株,以海藻酸钠为唯一碳源配制培养基,以透明圈法进行初筛,DNS法复筛,从海洋生物中筛选得到1株高酶活力褐藻胶降解菌株B12,经16S rDNA序列分析、生理生化试验、电镜观察,确定该菌为弧菌属(Vibrio sp.)。通过单因素试验及响应面优化试验对影响菌株生长和产酶条件的5个因素(发酵初始pH值、发酵温度、NaCl质量浓度、接种量和装液量)进行优化。得到该菌株最佳产酶条件:pH 6.52,发酵温度28.2℃,NaCl质量浓度20.1 g/L,接种量2.1%,装液量59.5 mL。在最佳发酵条件下,B12菌株酶活力可达91.68 U/mL,相比于优化前提高了38.5%。菌株开始产酶时间提前6 h, 4℃冷藏酶活力稳定性较好。     

果胶酶高产菌株EIM-4的鉴定及其液体发酵条件优化

目的：通过了解高产果胶酶菌株EIM-4的背景信息及优化其最适的产酶条件,为下一步工业化生产提供依据。方法：通过基于18S rDNA序列的系统发育进化分析对果胶酶高产菌进行鉴定,通过单因素试验和均匀设计获得最适产酶条件。结果：通过对18SrRNA基因的分子系统进化分析,菌株EIM-4被鉴定为黑曲霉（Aspergillus niger）。通过单因素和均匀设计试验确定最佳产酶培养基为（g/L）：橘皮粉32.9,黄豆粉10.7,（NH4）SO42.1,CaCO31.0,pH自然。结论：Aspergillus niger EIM-4的液体发酵产果胶酶的活力可达15159.82U/mL。     

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.     

一株高产木聚糖酶的枝链霉菌的分离鉴定及产酶

对1株高产木聚糖酶的链霉菌进行了鉴定并研究其木聚糖酶的生产过程及水解产物特点。分离得到1株产木聚糖酶的链霉菌Streptomyces sp.L2001,从形态学特征、培养特征和生理生化特征等方面对该菌株进行了鉴定。PCR扩增得到16S rDNA序列全长为1429bp,分析结果表明,菌株与Streptomyces rameus NBRC3782同源性达99.16%。结合传统生理生化实验结果鉴定为枝链霉菌。菌株液体发酵6d能产生842.0U/mL木聚糖酶活力。经HPLC分析酶解产物,结果显示木二糖、木三糖及木四糖含量之和高达93.5%,该酶适用于工业化生产低聚木糖。     

一株产胆固醇氧化酶的不动杆菌的筛选鉴定及特性研究

目的：筛选鉴定产胆固醇氧化酶的菌株并对其酶的性质及发酵条件进行初步的研究。方法：利用唯一碳源的胆固醇平板筛选,酶活测定比较得酶活力最高的菌株;生理生化试验结合16S rDNA序列分析鉴定其种属,单因素及正交实验优化培养基及发酵条件。结果：所得菌株H4与产不动杆菌（Acinetobacter）有最近的亲缘关系,其胆固醇氧化酶作用的最适温度和pH分别为37℃和8.0,金属离子Mg2＋、Zn2＋、Fe2＋对该酶具有一定激活作用,菌株产酶的最适培养基为（g/L）：胆固醇1.5,蔗糖5,蛋白胨7,硝酸铵3,吐温1.0,pH7.5;最适培养条件为33℃,15mL培养基/100mL三角瓶,摇床培养（200r/min）48h,优化后发酵液酶活达135.8U/L。结论：获得了1株产胆固醇氧化酶的菌株H4,并初步鉴定为不动杆菌（Acinetobacter）。     

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％。     

利用数学统计方法快速优化木聚糖酶液体发酵培养基

木聚糖是植物中半纤维素的主要成分,含量仅次于纤维素的可再生多糖资源。木聚糖酶的使用可以有效提高半纤维素的利用,降低原料成本,减少污染,保护生态环境。应用快速有效的数学统计方法对木聚糖酶生产菌黑曲霉（A8pergillus niger）FS418液体发酵培养基进行优化。首先采用Plackett-Burman设计对培养基中8因素进行筛选,获得影响产酶3个最重要的营养组分：蛋白胨、麸皮、甘蔗渣;然后采用响应面分析法对3个因素进行3水平的优化,得到它们的最佳组合：麸皮6.0％、蛋白胨0.2％、甘蔗渣0.4％。优化后液体发酵水平比初始设计有了较大提高,最终产酶水平达到5147.29U／mL、实测值与模型的预测值只有0.8％的误差。     

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     

离子注入选育高产木聚糖酶黑曲霉及其发酵条件研究

以黑曲霉A3为出发菌,利用离子注入技术选育出一株遗传性状稳定的木聚糖酶高产突变株AN497,其产酶水平较出发菌从野生型A3菌株的405.6IU/ml提高到586.2IU/ml,即酶产量增加了44.5%;对高产菌进行发酵条件优化,发现以玉米芯粉为主要碳源、用蔗糖代替葡萄糖作为附加碳源,对木聚糖酶的发酵具有明显的促进作用;采用复合的无机氮源 (NH4)2SO4和NaNO3,(1: 2)浓度以10g/L为宜;菌株对发酵通氧量具有较高的要求,摇瓶转速在230r/min时的产酶水平较200r/min要高;通过发酵条件的优化,高产菌株的产酶活力最高可达671.1IU/mL,比出发菌株的产酶量提高了65.5%。     

Xylanase production in solid state fermentation by Aspergillus niger mutant using statistical experimental designs

The initial moisture content, cultivation time, inoculum size and concentration of basal medium were optimized in solid state fermentation (SSF) for the production of xylanase by an Aspergillus niger mutant using statistical experimental designs. The cultivation time and concentration of basal medium were the most important factors affecting xylanase activity. An inoculum size of 5 x 10(5) spores/g, initial moisture content of 65%, cultivation time of 5 days and 10 times concentration of basal medium containing 50 times concentration of corn steep liquor were optimum for xylanase production in SSF. Under the optimized conditions, the activity and productivity of xylanase obtained after 5 days of fermentation were 5,071 IU/g of rice straw and 14,790 IU l(-1) h(-1), respectively. The xylanase activity predicted by a polynomial model was 5,484 IU/g of rice straw.     

Xylanase production using inexpensive agricultural wastes and its partial characterization from a halophilic <Emphasis Type="Italic">Chromohalobacter</Emphasis> sp. TPSV 101

A halophilic and alkali-tolerant Chromohalobacter sp. TPSV 101 with an ability to produce extracellular halophilic, alkali-tolerant and moderately thermostable xylanase was isolated from solar salterns. Identification of the bacterium was done based upon biochemical tests and 16S rRNA sequence. The culture conditions for higher xylanase production were optimized with respect to NaCl, pH, temperature, substrates and metal ions and additives. Maximum xylanase production was achieved in the medium with 20% NaCl, pH-9.0 at 40°C supplemented with 1% (w/v) sugarcane bagasse and 0.5% feather hydrolysate as carbon and nitrogen sources. Sugarcane bagasse (250 U/ml) and wheat bran (190 U/ml) were the best inducer of xylanase when used as carbon source as compared to xylan (61 U/ml). The xylanase that was partially purified by protein concentrator had a molecular mass of 15 kDa approximately. The xylanase from Chromohalobacter sp. TPSV 101 was active at pH 9.0 and required 20% NaCl for optimal xylanolytic activity and was active over a broad range of temperature 40–80°C with 65°C as optimum. The early stage hydrolysis products of sugarcane bagasse were xylose and xylobiose, after longer periods of incubation only xylose was detected.     

Response surface optimization of fermentation conditions for producing xylanase by <Emphasis Type="Italic">Aspergillus</Emphasis><Emphasis Type="Italic">niger</Emphasis> SL-05

Fermentation conditions were statistically optimized for producing extracellular xylanase by Aspergillus niger SL-05 using apple pomace and cotton seed meal. The primary study shows that culture medium with a 1:1 ratio of apple pomace and cotton seed meal (carbon and nitrogen sources) yielded maximal xylanase activity. Three significant factors influencing xylanase production were identified as urea, KH(2)PO(4), and initial moisture content using Plackett-Burman design study. The effects of these three factors were further investigated using a design of rotation-regression-orthogonal combination. The optimized conditions by response surface analysis were 2.5% Urea, 0.09% KH(2)PO(4), and 62% initial moisture content. The analysis of variance indicated that the established model was significant (P < 0.05), "while" or "and" the lack of fit was not significant. Under the optimized conditions, the model predicted 4,998 IU/g dry content, whereas validation experiments produced an enzymatic activity of xylanase at 5,662 IU/g dry content after 60 h fermentation. This study innovatively developed a fermentation medium and process to utilize inexpensive agro-industrial wastes to produce a high yield of xylanase.     

Production of cellulase-free thermostable xylanases by an isolated strain of Aspergillus niger PPI, utilizing various lignocellulosic wastes

A strain of Aspergillus niger PPI having prolific xylanolytic potential was isolated and the optimum conditions for maximum xylanase production was studied, resulting in the following: 4% substrate concentration, 10% v/v inoculum size, 72 h of incubation and pH 3.5–4.5 at 28 °C. The production profile of xylanase was examined with various lignocellulosics and maximum yield was achieved with oat. The hemicellulose content of wastes was also determined and oatmeal was found to have maximum hemicellulose content followed by wheat straw, sugarcane bagasse, rice husk and gram residue respectively. The enzyme showed maximum activity at pH 4 and temperature 60 °C. However, maximum stability was achieved at pH 3.5 and temperature 55 °C. Cellulase activity was found altogether absent in the enzyme broth.     

Improved xylanase production using apple pomace waste by Aspergillus niger in koji fermentation

Xylanase production by Aspergillus niger NRRL‐567 in solid‐state fermentation (koji fermentation) was optimized using 2⁴ factorial design and response surface methodology. The evaluated variables were the initial moisture level and concentration of inducers [veratryl alcohol (VA), copper sulphate (CS), and lactose (LAC)], leading to the response of xylanase production. Initial moisture level and LAC were found to be the most significant variable for xylanase production (p<0.05). The highest xylanase production was observed with 3578.8 ± 65.3 IU/gds (gram dry substrate) under optimal conditions using initial moisture of 85% (v/w), pH 5.0 and inducers VA (2 mM/kg), LAC 2% (w/w), and CS (1.5 mM/kg) after 48 h of incubation time. Higher xylanase activity of 3952 ± 78.3 IU/gds was attained during scale‐up of the process in solid‐state tray fermentation under optimum conditions after 72 h of incubation time. The present study demonstrates that A. niger NRRL‐567 can efficiently be used to achieve xylanase production with an economical and environmental benefit in solid‐state tray fermentation. The developed process can be used to develop an effective process for commercially feasible bioproduction of xylanases for speciality applications, such as conversion of lignocellulosic biomass to biofuels and other value‐added products.