红谷霉素生料发酵工艺的研究

红谷霉素是链霉菌702发酵所产的一种生物活性物质,具有较强抗细菌活性。在摇瓶条件下,对链霉菌702生料发酵生产红谷霉素进行研究。采用单因素实验探索生料发酵工艺,筛选出摇瓶生料发酵条件为7.5%的种子接种量和添加抗菌剂1.5ml。在此条件下进行生料发酵,使红谷霉素摇瓶发酵产量达到1.46g/L,比常规灭菌发酵产量提高25.7%,实验结果表明红谷霉素生料发酵是一种潜在可行的发酵方法,不但可以很好的节约发酵成本,还可以提高发酵产量。     

固态间歇补料乙醇生料发酵新工艺

浓醪发酵是酒精生产的发展方向。与现行酒精厂普遍采用的热蒸煮工艺相比, 生料发酵技术的发展使得浓醪发酵更容易进行。本研究首次在生料发酵中直接采用固态原料间歇补料, 比较了STARGENTM生淀粉水解酶间歇补料工艺和传统无补料工艺, 并对不同补料方式进行了研究。结果表明: 与传统无补料生料发酵工艺相比, 在相同的干基配料浓度30%、相同的生料酶添加量0.22%(W/W)的条件下, 采用15%的起始配料浓度、发酵15~25 h进行间歇补料的新工艺, 酒精产量从17.06%提高到18.50%。该间歇补料优化工艺的建立, 丰富了生料发酵技术的应用。     

塔拉单宁水解酶产生条件的研究

微生物通过发酵产酶可以将植物单宁降解成小分子酚类化合物或其衍生物,但培养条件对其产酶影响很大。论文采用固态培养法,对黑曲霉产生塔拉单宁水解酶的条件进行了研究。结果表明,当培养液中塔拉单宁浓度为75 g/L、葡萄糖浓度为3 g/L、(NH4)2SO4浓度为0.2 g/L2、50 mL锥形瓶装液量为25 mL、惰性载体用量为5.6%(w/v)、起始pH为5.5、接种量为12%(v/v)、30℃培养72 h时,该黑曲霉产生的塔拉单宁水解酶活力可达到44.29 U/mL,是其自然条件下酶活力(24.09 U/mL)的1.84倍;没食子酸产率达到79.3%。研究结果对于揭示塔拉单宁生物降解的机理具有一定的参考价值。     

海洋Cellulophaga sp.QY201产生L-卡拉胶酶的发酵条件优化

目的:通过发酵条件优化,提高海洋Cellulophaga sp.QY201的L-卡拉胶酶产量.方法:采用正交试验分别时发酵条件、培养基配方进行优化.结果:该茵株最适培养基配方为(w/v):3%NaCl、0.5%MgSO4·7H2O、0.02%CaCl2、0.01%KCl、0.002%FeSO4、0.25%CaSein、0.15%Na2HPO4,0.2%NaNO3、0.25%L-卡拉胶.最佳培养条件为:培养基体积为70ml/250ml三角瓶,接种量为1%,25℃,90 r/min培养36 h.优化后酶活最高可迭2.64 U/ml,较优化前提高了22倍.结论:QY201最佳发酵条件的建立,为L-卡拉胶酶的大规模生产创造了条件.     

一株产生淀粉酶杆菌Bacillus sp. GEL-09的筛选、鉴定及发酵条件优化

【背景】生淀粉酶可以水解生淀粉颗粒,在酒精发酵、白酒、黄酒和食醋的生料酿造工业中具有广阔的应用前景。【目的】从自然环境中筛选产生淀粉酶的菌,对其发酵条件及酶性能进行考察,为淀粉生料发酵过程提供优良菌种和酶资源。【方法】取木薯田土壤,经过稀释、热处理、富集培养以及木薯淀粉平板筛选培养基初筛,摇瓶复筛得到产高效降解生淀粉酶的菌株;经过菌落形态、细胞染色观察以及16S rRNA基因序列比对进行鉴定;对筛选菌株的发酵培养基和发酵条件进行优化,并对酶蛋白进行分离纯化和酶学性质分析。【结果】分离到一株具有较高生淀粉酶水解活力的菌株GEL-09,经鉴定为芽胞杆菌Bacillus sp.GEL-09;该菌在最优发酵条件下培养96 h,胞外酶活力达到430.6 U/m L,是优化前的2.8倍;酶学性质分析发现该酶为中温、中性酶,最适温度和p H为50°C和7.0;生淀粉降解能力对比发现,该酶的生淀粉降解能力值为62.3%,显著高于细菌α-淀粉酶、生麦芽糖淀粉酶和甘薯β-淀粉酶对生淀粉的降解能力。【结论】Bacillus sp.GEL-09在生淀粉酶生产方面具有良好的开发应用前景。     

木薯淀粉原料生料酒精发酵的研究

利用木薯淀粉原料生料酒精发酵,对影响其发酵的主要因素进行单因素和正交试验,确定其发酵温度、pH值、料水比和发酵剂及氮磷添加量等最佳的工艺条件,结果表明:在木薯淀粉中添加占原料重0.4% 的尿素和0.2%的磷酸氢二钾、0.7% 的生料酒精发酵剂以及在料水比1:4、起始pH6.0、35℃条件下发酵5～6d,原料淀粉利用率和酒精产率分别达到85.3% 和48.4%.     

棘孢曲霉固态发酵柚皮产柚苷酶的条件优化

【目的】以柚皮为原料,优化棘孢曲霉利用柑橘加工副产物固态发酵柚苷酶的条件。【方法】采用高效液相色谱法检测酶活力,通过单因素试验考察固水比、装样量、接种量、温度对柚苷酶发酵的影响,用正交试验优化发酵条件。【结果】单因素试验结果的显著性分析表明培养基的固水比、装样量和培养温度对柚苷酶产量有显著性影响,而接种量影响不显著;经正交试验确定的优化条件是：固水比1:1 (质量体积比),装样量5 g/250 mL三角瓶,温度为30 °C,接种1 mL孢子悬浮液,发酵8 d。在此优化条件下,柚苷酶酶活力为8.19 IU/g干物质,比初始培养基产柚苷酶活力提高7.38倍。【结论】通过对固水比、装样量和发酵温度进行优化,大幅度提高了棘孢曲霉固态发酵柑橘加工副产物的柚苷酶产量,为柚苷酶的生产提供了一种高产发酵工艺。     

蛋白质谷氨酰胺酶的发酵及初步分离和应用研究

研究了不同发酵条件对于产吲哚金黄杆菌（Chryseobacterium indologenes）生产蛋白质谷氨酰胺酶能力的影响,酶的分离和初步的应用。通过考察种子的生长曲线,发酵的温度、转速、摇瓶装液量,碳源和氮源,得出最大产酶能力的发酵条件为：30℃,200r/min,装液量25ml/250ml,蔗糖为碳源,多聚蛋白胨为氮源,发酵10~12h。初步分离研究表明在4倍超滤浓缩和4倍乙醇沉淀条件下,酶活力回收率均为最高,分别为84.99%和76.07%。该酶与酪蛋白37℃温育2h时,酪蛋白的脱酰胺度为41.03%,到24h后,脱酰胺度不再增加,并且酪蛋白的溶解性也有所增加。     

黑曲霉固态发酵生产单宁酶的条件优化

研究采用响应面法优化黑曲霉固态发酵生产单宁酶的培养条件。应用Plackett—Burman试验筛选出重要影响因子：五倍子粉含量、（NH4）2SO4浓度以及接种孢子量,最陡爬坡试验逼近最大响应区域。应用Box．Behnken响应面试验对重要影响因子进一步优化。得到最佳培养条件：每250mL三角瓶中装入1．0g五倍子粉、4．4g稻壳和0．5g麸皮、液固比（mL／g）2：1且营养盐溶液组成为（NH4）2s0421g/L、MgSO4·7H2O1g／L、NaCl1g／L,培养基pH自然,接种5．7×10^7个孢子后在30℃温度下培养4d。在此条件下,单宁酶产量从40U／g提高到114U／g,3次重复验证性试验平均值为115U／g,验证了模型的可靠性。     

链霉菌A048产几丁质酶最佳发酵工艺研究

将链霉菌A048在完全培养基中培养至对数生长末期,离心洗涤收集菌丝体,然后接种入发酵产酶培养基中,进行二步发酵工艺牛产几丁质酶,几丁质酶活力比一步发酵工艺提高1．1倍,发酵周期共54h,比一步发酵工艺缩短66h;把菌丝体与几丁质粉共固定化,接入发酵产酶培养基中培养36h,几丁质酶活力比一步发酵工艺提高1．8倍,发酵周期缩短54h;在二步发酵工岂中另添加0．4％纤维素,几丁质酶活力可提高4倍,比一步发酵工艺提高10倍,酶活力达18．52U／mL。采用几丁质和纤维索双因子诱导二步发酵工艺可能是链霉菌A048生产几丁质酶的最佳工艺。     

Biosynthesis of tannin acyl hydrolase from tannin-rich forest residue under different fermentation conditions

Caesalpinia digyna, a tannin-rich forest residue, was used as substrate for production of tannase and gallic acid. Media engineering was carried out under solid-state fermentation, submerged fermentation and modified solid state fermentation conditions for optimum synthesis of tannase and gallic acid (based on 58% tannin content in the raw material). Tannase vis-à-vis gallic acid recovery under modified solid-state fermentation condition was maximum. Conversions of tannin to gallic acid under solid-state fermentation, submerged fermentation and modified solid-state fermentation conditions were 30.5%, 27.5% and 90.9%, respectively. Journal of Industrial Microbiology & Biotechnology (2000) 25, 29–38. Received 02 November 1999/ Accepted in revised form 12 February 2000     

1株产单宁酶细菌的分离鉴定及产酶条件研究

从富含单宁酸的土壤中分离筛选出1株产单宁酶的细菌,经过菌落形态观察和16S rDNA分子生物学鉴定,该细菌为肺炎克雷伯菌。对该菌所产胞外单宁酶的发酵条件进行了初步研究,得出最佳产酶条件：培养温度37℃,培养时间36 h,培养转速180 r/min,单宁酸含量2 g/L,最佳碳源为葡萄糖,最佳氮源为氯化铵,此时所产单宁酶活力为0.8 U/mL。     

Production of tannase from Aspergillus ruber under solid-state fermentation using jamun (Syzygium cumini) leaves

Tannase producing fungal strains were isolated from different locations including garbages, forests and orchards, etc. The strain giving maximum enzyme yield was identified to be Aspergillus ruber. Enzyme production was studied under solid state fermentation using different tannin rich substrates like ber leaves (Zyzyphus mauritiana), jamun leaves (Syzygium cumini), amla leaves (Phyllanthus emblica) and jawar leaves (Sorghum vulgaris). Jamun leaves were found to be the best substrate for enzyme production under solid-state fermentation (SSF). In SSF with jamun leaves, the maximum production of tannase was found to be at 30 °C after 96 h of incubation. Tap water was found to be the best moistening agent, with pH 5.5 in ratio of 1:2 (w/v) with substrate. Addition of carbon and nitrogen sources to the medium did not increase tannase production. Under optimum conditions as standardized here, the enzyme production was 69 U/g dry substrate. This is the first report on production of tannase by A. ruber, giving higher yield under SSF with agro-waste as the substrate.     

Optimisation of extracellular tannase production from <Emphasis Type="Italic">Paecilomyces variotii</Emphasis>

The tannase production by Paecilomyces variotii was confirmed by high performance thin layer chromatography (HPTLC), and substrate specificity of the tannase was determined by zymogram analysis in sodium dodecyl sulphate-polyacrylamide gel electrophoresis (SDS–PAGE). A clear band of activity observed after electrophoresis of culture filtrate in non-denaturing gels indicated the production of extracellular tannase by P. varoitii. HPTLC analysis revealed that gallic acid was the enzymatic degradation product of tannic acid during the fermentation process. The optimum condition for tannase production was at 72 h of incubation in shaking condition and addition of 1.5% tannic acid, 1% glucose and 0.2% sodium nitrate at temperature of 35°C and pH of 5–7. The production of extracellular tannase from Paecilomyces variotii was investigated under optimized conditions in solid-state fermentation (SSF), submerged fermentation (SmF) and liquid surface fermentation (LSF) processes. The maximum extracellular tannase production was obtained within 60 h of incubation under SSF followed by SmF and LSF.     

Production of tannase by Aspergillus niger Aa-20 in submerged and solid-state fermentation: influence of glucose and tannic acid

Tannase production by Aspergillus niger Aa-20 was studied in submerged (SmF) and solid-state (SSF) fermentation systems with different tannic acid and glucose concentrations. Tannase activity and productivity were at least 2.5 times higher in SSF than in SmF. Addition of high tannic acid concentrations increased total tannase activity in SSF, while in SmF it was decreased. In SmF, total tannase activity increased from 0.57 to 1.03 IU/mL, when the initial glucose concentration increased from 6.25 to 25 g/L, but a strong catabolite repression of tannase synthesis was observed in SmF when an initial glucose concentration of 50 g/L was used. In SSF, maximal values of total tannase activity decreased from 7.79 to 2.51 IU when the initial glucose concentration was increased from 6.25 to 200 g/L. Kinetic results on tannase production indicate that low tannase activity titers in SmF could be associated to an enzyme degradation process which is not present in SSF. Tannase titers produced by A. niger Aa-20 are fermentation system-dependent, favoring SSF over SmF. Journal of Industrial Microbiology & Biotechnology (2001) 26, 296–302. Received 07 July 2000/ Accepted in revised form 15 February 2001     

Co-production of tannase and gallic acid by a novel Penicillium rolfsii (CCMB 714)

Abstract

A novel tannase and gallic acid-producing Penicillium rolfsii (CCMB 714) was isolated from cocoa leaves from the South of Bahia. The influence of nutritional sources and the simultaneous effect of parameters involved in the fermentation process were available. Tannase (9.97 U?mL^?1) and gallic acid (9?mg mL^?1) production were obtained in 48?h by submerged fermentation in non-optimized conditions. Among the carbon sources, tested gallic acid and tannic acid showed the highest tannase production (p<.05) when compared with methyl gallate and glucose. After optimization using the temperature and tannic acid concentration as variables with the Central Compound Rotational Design (CCRD), the maximal tannase production (25.6?U mL^?1) was obtained at 29.8?°C and 12.7%, respectively, which represents an increase of 2.56 times in relation to the initial activity. The parameters optimized for the maximum production of gallic acid (21.51?mg mL^?1) were 30?°C and 10% tannic acid. P. rolfsii CCMB 714 is a new strain with a high tannase and gallic acid production and the gallic acid produced is very important, mainly for its applications in the food and pharmaceutical industry.     

Bioconversion of grape must into modulated gluconic acid production by Aspergillus niger ORS-4.410

AIMS: Analysis of regulators for modulated gluconic acid production under surface fermentation (SF) condition using grape must as the cheap carbohydrate source, by mutant Aspergillus niger ORS-4.410. Replacement of conventional fermentation condition by solid-state surface fermentation (SSF) for semi-continuous production of gluconic acid by pseudo-immobilization of A. niger ORS-4.410. METHODS AND RESULTS: Grape must after rectification was utilized for gluconic acid production in batch fermentation in SF and SSF processes using mutant strain of A. niger ORS-4.410. Use of rectified grape must led to the improved levels of gluconic acid production (80-85 g l(-1)) in the fermentation medium containing 0.075% (NH4)2HPO4; 0.1% KH2PO4 and 0.015% MgSO4.7H2O at an initial pH 6.6 (+/-0.1) under surface fermentation. Gluconic acid production was modulated by incorporating the 2% soybean oil, 2% starch and 1% H2O2 in fermentation medium at continuously high aeration rate (2.0 l min(-1)). Interestingly, 95.8% yield of gluconic acid was obtained when A. niger ORS-4.410 was pseudo-immobilized on cellulose fibres (bagasse) under SSF. Four consecutive fermentation cycles were achieved with a conversion rate of 0.752-0.804 g g(-1) of substrate into gluconic acid under SSF. CONCLUSIONS: Use of additives modulated the gluconic acid production under SF condition. Semi-continuous production of gluconic acid was achieved with pseudo-immobilized mycelia of A. niger ORS-4.410 having a promising yield (95.8%) under SSF condition. SIGNIFICANCE AND IMPACT OF THE STUDY: The bioconversion of grape must into modulated gluconic acid production under SSF conditions can further be employed in fermentation industries by replacing the conventional carbohydrate sources and expensive, energy consuming fermentation processes.     

Production of tannase by the immobilized cells of Bacillus licheniformis KBR6 in Ca-alginate beads

AIMS: The present study was aimed at finding the optimal conditions for immobilization of Bacillus licheniformis KBR6 cells in calcium-alginate (Ca-alginate) beads and determining the operational stability during the production of tannin-acyl-hydrolase (tannase) under semicontinous cultivation. METHODS AND RESULTS: The active cells of B. licheniformis KBR6 were immobilized in Ca-alginate and used for the production of tannase. The influence of alginate concentration (5, 10, 20 and 30 g l(-1)) and initial cell loading on enzyme production were studied. The production of tannase increased significantly with increasing alginate concentration and reached a maximum enzyme yield of 0.56 +/- 0.03 U ml(-1) at 20 g l(-1). This was about 1.70-fold higher than that obtained by free cells. The immobilized cells produced tannase consistently over 13 repeated cycles and reached a maximum level at the third cycle. Scanning electron microscope study indicated that the cells in Ca-alginate beads remain in normal shape. CONCLUSIONS: The Ca-alginate entrapment is a promising immobilization method of B. licheniformis KBR6 for repeated tannase production. Tannase production by immobilized cells is superior to that of free cells because it leads to higher volumetric activities within the same period of fermentation. SIGNIFICANCE AND IMPACT OF THE STUDY: This is the first report of tannase production from immobilized bacterial cells. The bacterium under study can produce higher amounts of tannase with respect to other fungal strains within a short cultivation period.