抗夜蛾科苏云金芽孢杆菌WY-197菌株的生物学特性研究

苏云金芽孢杆菌 (Bacillusthuringiensis,Bt)WY 197菌株是从 4 0 0多株野生型Bt菌中筛选分离的1株对甜菜夜蛾和棉铃虫都具有高效杀虫活性的菌株。初步比较WY -197菌株和HD 1的形态特征、生理生化特性和伴孢晶体蛋白 ,结果表明 ,WY -197属于H3a3b3c血清型 (subsp .kurstaki) ;伴孢晶体形态主要为大小不一的菱形、小正方形。SDS -PAGE电泳图谱表明主要由 135ku和 6 5ku两种蛋白成分组成 ,在菌株生长形态、发酵培养特征、生理生化特性方面与生产菌株HD-1差别不大。采用生物测定的方法 ,进一步鉴定比较它们对甜菜夜蛾初孵、二龄、三龄幼虫和棉铃虫的毒效差异。结果表明 ,BtWY 197菌株发酵液对甜菜夜蛾初孵、二龄、三龄幼虫的LC50 分别为 0 .31、0 .6 1、2 .5 7μL/mL ,其中对甜菜夜蛾初孵幼虫的毒效是对照菌HD 1发酵液的 7倍 ,表明BtWY 197菌株对甜菜夜蛾三龄以下幼虫具有高毒力。对棉铃虫的毒力效价为 30 0 0IU/ μL ,略低于HD- 1菌株。     

星形孢菌素产生菌H41-38的发酵工艺条件

本研究对菌株H41-38发酵生产星形孢菌素的工艺进行了研究.结果表明:30℃、96h为菌株摇瓶培养最适条件.玉米淀粉和酵母粉为最适碳、氮源.采用Fractional factorial design方法确定培养基成分的重要因子:酵母粉和粗盐,然后利用爬坡路径试验和响应面分析法优化了发酵效价取得最大值时酵母粉和粗盐含量,发酵效价最大理论值为252.31μg/mL,摇瓶实测值为251.28μg/mL,其发酵水平比优化前提高了4.33倍.在30L发酵罐(300r/min、30℃、V空气=10L/min～15L/min)中扩大培养84h后发酵效价达到286.44μg/mL,比摇瓶培养效价提高了45.16μg/mL,其发酵参数变化曲线可指导生产罐的应用生产.     

培养方式对Xenorhabdus nematophila生长与抗菌活性的影响

为了明确不同培养方式对Xenorhabdus nematophilaYL001生长和抗菌活性的影响,提高YL001菌株的抗菌活性。采用分批发酵方式研究了摇瓶与发酵罐培养对置nematophila YL001生长和抗菌活性的影响。实验结果表明：在通气量2．5L／min、搅拌转速300r／min条件下,发酵罐的体积氧传递系数KLa明显高于摇瓶,通气及供氧状况好于摇瓶,细胞生长及代谢旺盛,细胞生长量较摇瓶发酵增加了23．9％;但由于pH变化幅度大,抗菌物质的活性单位仅达到摇瓶的发酵水平,为229U／mL。发酵罐pH控制初步研究表明,发酵过程中控制pH为7．5时,细胞生长量和抗菌活性达到23．71g/L和290U／mL,较不控制pH分别增加了21％和25％。通风对X.nematophila YL001生长和抗菌物质的产生有较大的影响,发酵罐培养时通气及供氧状况好于摇瓶,有利于YL001菌株的生长和抗菌物质的产生。     

发酵法生产L-精氨酸放大过程的工艺研究

本文报道了L-精氨酸产生菌株钝齿棒状杆菌突变株971．1继摇瓶发酵条件研究后所进行的2．6L台式发酵罐,2 0 0L和2000L通用发酵罐放大试验及其工艺条件研究的结果。试验表明,发酵PH值及供氧强度的合理控制对提高L-精氨酸的积累量非常重要。在所获得的工艺条件下,2000L发酵罐稳产试验的产酸率平均可达29.0mg/ml,最高32.0mg／ml。发酵液中L-精氨酸的提取收率平均为55．9％,最高可达66．04％。产品的质量符合药典标准。本文也对试验结果进行了分析与讨论。     

麦白霉素发酵培养基的改进

研究了淀粉水解液全部替代葡萄糖作为碳源发酵麦白霉素的工艺条件。用正交实验得出摇瓶培养基消毒后的最佳基质浓度为总糖5.0g/100mL,还原糖3.8g/100mL,氨基氮60mg/mL,溶解磷300μg/mL。以50L发酵罐进行实验,得出了麦白霉素的发酵代谢曲线和淀粉的适宜水解条件。经30t发酵罐放大实验结果表明,与葡萄糖作碳源相比,用淀粉水解液作碳源发酵麦白霉素,发酵单位提高23.0％,生产成本降低38.0％。     

苏云金芽孢杆菌发酵上清中增效物质生成的相关研究

利用BIOSTAT ^?-CL1 5L全自动发酵罐和 2 0t不锈钢发酵罐 ,对苏云金芽孢杆菌不同菌株 (GC-91 ,MP342 ,HD-1 )发酵上清液中增效物质的生成进行了研究 ,发现增效物质于对数生长期前期开始产生并积累 ,至对数生长期末期达到高峰 ,并保持稳定 ;不同菌株的发酵上清中增效物质生成量不同 ,其中GC-91最强 (增效倍数f=6.0 ) ,MP342次之 (f=3.7) ,HD 1最弱 (f=1.5 ) ;GC-91菌株上清液中增效物质生成曲线与晶体含量 ,效价代     

海洋中海藻糖产生菌的筛选及发酵条件优化

从180余份海水、海泥样品中筛选得到60株产海藻糖较高的菌株,编号为2-14的菌株海藻糖产量最高,为127.9mg/g cell。对2-14菌株进行形态特征、培养特征及生理生化试验,鉴定该菌株为红酵母属(Rhodotorula sp.)。研究摇瓶发酵条件对红酵母海藻糖产量的影响,结果为:初始pH5.5,发酵温度28℃,装液量75mL(250mL三角瓶中)。采用优化后发酵条件红酵母海藻糖产量为193.3mg/g cell,优化前对照值为132.1mg/g cell,优化后的结果是优化前的1.46倍。在5L发酵罐中培养得到最佳发酵时间为54h,发酵罐培养发酵液中海藻糖含量最高达2.5g/L,为摇瓶培养的1.6倍。     

一株产几丁质酶菌株的筛选及其产酶条件的研究

采用平板透明圈法从土壤中分离筛选到一株产几丁质酶放线菌株L12,用250mL摇瓶发酵初筛和复筛,酶活力为0.63U/mL。通过产酶条件实验,初步确定了该菌株较适产酶培养基和摇瓶发酵条件。条件优化后,30℃、250mL摇瓶发酵48h,几丁质酶活力达到1.06U/mL。     

L-色氨酸生产菌的选育及其发酵条件的研究

以代谢控制发酵理论为指导 ,对L -色氨酸产生菌的定向选育、摇瓶发酵条件、30L发酵罐发酵条件进行了研究。以谷氨酸棒杆菌Tx5 - 32 (Phe- +Tyr- )为出发菌株 ,经硫酸二乙酯 (DES)多次诱变处理 ,定向选育出一株L -色氨酸产生菌TQ2 2 2 3(Phe- +Tyr- +5 -MTr+5 -FTr+SGr+CINr)。以摇瓶分批发酵最优条件为基础 ,对菌株TQ2 2 2 3进行了 30L发酵罐分批发酵试验 ,该菌株发酵 6 4h ,产L -色氨酸 7.2 8g·L- 1 。     

海洋红酵母的液体培养

目的探讨提高海洋红酵母的液体高密度培养方法。方法在摇瓶培养条件下,测定温度、pH、装液量、接种量及摇床转速对海洋红酵母BY2菌株生长的影响,进一步放大培养至50L发酵罐,在培养过程流加氨水以控制pH稳定在5.3~5.5的条件下,考察不同葡萄糖浓度对海洋红酵母BY2菌株发酵菌量的影响。结果摇瓶最适培养条件为温度25℃,pH 5.5,接种量8%、装液量40mL/250mL三角瓶、摇床转速200r/min,在此培养条件下,24h时菌量达到8.9×108 CFU/mL;扩大至50L发酵罐,葡萄糖初始浓度为40、60、80、100g/L各罐20~24h时的菌量相应达到26.6×108、29.5×108、47.8×108、66.8×108 CFU/mL。结论提高初始葡萄糖浓度,流加氨水稳定发酵过程的pH,可以显著提高BY2菌株的发酵菌量。     

Scale-up of biopesticide production processes using wastewater sludge as a raw material

Studies were conducted on the production of Bacillus thuringiensis (Bt)-based biopesticides to ascertain the performance of the process in shake flasks, and in two geometrically similar fermentors (15 and 150 l) utilizing wastewater sludge as a raw material. The results showed that it was possible to achieve better oxygen transfer in the larger capacity fermentor. Viable cell counts increased by 38–55% in the bioreactor compared to shake flasks. As for spore counts, an increase of 25% was observed when changing from shake flask to fermentor experiments. Spore counts were unchanged in bench (15 l) and pilot scale (5.3–5.5 e⁺⁰⁸ cfu/ml; 150 l). An improvement of 30% in the entomotoxicity potential was obtained at pilot scale. Protease activity increased by two to four times at bench and pilot scale, respectively, compared to the maximum activity obtained in shake flasks. The maximum protease activity (4.1 IU/ml) was obtained in pilot scale due to better oxygen transfer. The Bt fermentation process using sludge as raw material was successfully scaled up and resulted in high productivity for toxin protein yield and a high protease activity.     

Culture condition improvement for whole-cell lipase production in submerged fermentation by Rhizopus chinensis using statistical method

Rhizopus chinensis CCTCC M201021 was a versatile strain capable of producing whole-cell lipase with synthetic activity in submerged fermentation. In order to improve the production of whole-cell lipase and study the culture conditions systematically, the combination of taguchi method and response surface methodology was performed. Taguchi method was used for the initial optimization, and eight factors viz., maltose, olive oil, peptone, K2HPO4, agitation, inoculum size, fermentation volume and pH were selected for this study. The whole-cell lipase activity yield was two times higher than the control experiment under initial optimal conditions, and four significant factors (inoculum, olive oil, fermentation volume and peptone) were selected to test the effect on the lipase production using response surface methodology. The optimal fermentation parameters for enhanced whole-cell lipase yield were found to be: inoculum 4.25 x 10(8) spores/L, olive oil 2.367% (w/v), fermentation volume 18 mL/250 mL flask, peptone 4.06% (w/v). Subsequent experimental trails confirmed the validity of the model. These optimal culture conditions in the shake flask led to a lipase yield of 13875 U/L, which 120% increased compare with the non-optimized conditions.     

Development of a stirred tank reactor system for the production of lignin peroxidases (ligninases) byPhanerochaete chrysosporium BKM-F-1767

Summary Lignin peroxidases produced byPhanerochaete chrysosporium have several important potential industrial applications based on their ability to degrade lignin and lignin-like compounds. A stirred tank reactor system for the production of lignin peroxidases is described here. Included in this study is an examination of the mechanics of pellet biocatalyst formation and the optimization of an acetate buffered medium. Higher levels of lignin peroxidase were obtained with acetate buffer compared to the other buffer systems tested. Concentrations of 0.05% (w/v) Tween 80 and 0.4 mM veratryl alcohol gave optimal lignin peroxidase activity in acetate buffered medium. In shake flask cultures, mycelial fragments in the inoculum aggregated into pellets during the first eight hours of incubation and thereafter increased in size through the eighth day. The agitation rate in shake flask cultures affected pellet size, the number of pellets formed, and lignin peroxidase activity. Transfer of fungal pellets from shake flask culture to a continuously oxygenated baffled stirred tank reactor (STR) resulted in production of high lignin peroxidase titres comparable to those of shake flask cultures when the agitation rate, oxygen dispersion and foaming were closely controlled.     

重组巴斯德毕赤酵母产米根霉α-淀粉酶发酵条件的研究

为了提高重组菌的淀粉酶表达量,以可分泌表达米根霉α-淀粉酶的甲醇快速利用型巴斯德毕赤酵母重组菌为基础,采用摇瓶发酵方式对影响重组菌表达淀粉酶的多个因素进行了研究和优化。摇瓶发酵条件确定为:温度为30℃,pH值为6.0,接种量为2.0(OD_(600)),甲醇补加方式采用前72 h发酵时间内每隔12h添加至终浓度为1.0%,72 h以后每隔24 h添加至终浓度为1.0%,在此条件下获得的淀粉酶最高表达量为47.5 U/mL,且在无机盐培养基中和有机氮源培养基中获得的淀粉酶发酵单位相当。以摇瓶发酵数据为基础确定15 L发酵罐放大实验条件为:无机盐培养基,温度为30℃,pH值为6.0,接种量为10%,甲醇流加方式采用DO—Start法控制,在此发酵条件下获得的淀粉酶表达量为440 U/mL,约为摇瓶发酵方式获得的淀粉酶表达量的9倍。     

里氏木霉双基因同步缺失菌株的构建与甘露聚糖酶表达研究

在里氏木霉中建立了一个快速的双基因位点同步同源重组新方法,较好解决了里氏木霉基因逐个敲除周期长等问题。研究以里氏木霉自身甘露聚糖酶基因（man5A）为重组表达的报告基因,通过一步转化,将该基因定点整合入纤维二糖水解酶Ⅰ（cbh1）基因位点,同时缺失主要的两个纤维素酶基因（cbh1、cbh2）,得到重组工程菌Man12。将重组工程菌Man12与出发菌株Tu6Δku70进行摇瓶发酵,结果显示,重组菌株的甘露聚糖酶产量比出发菌株提高10倍,而纤维素酶产量降低了60%,胞外总蛋白分泌水平降低了40%。Real-time PCR检测甘露聚糖酶基因（man5A）的转录水平,发现重组菌株较出发菌株提高了25倍。在里氏木霉中首次报道了通过一步转化实现两个基因同步定点整合的方法,对利用基因工程手段构建高效表达重组蛋白的里氏木霉工程菌株具有一定的指导意义。     

重组毕赤酵母生产β-葡萄糖苷酶发酵条件初步研究

为提高重组毕赤酵母(P.pastoris KM71/pPIC9K-bgl)生产β-葡萄糖苷酶的产量,在摇瓶条件下对重组P.pastoris产β-葡萄糖苷酶的发酵过程进行了优化,得到最佳的条件:生长阶段甘油浓度为30 g/L,接种量为10%,诱导阶段甲醇的初浓度为4%,过程补加甲醇0.5%,诱导温度30℃,pH7.5,诱导周期120 h,酶活可达到245 U/mL。在此基础上,在3 L发酵罐上进行初步放大,流加甘油提高细胞密度至OD_(600)为170,开始流加甲醇诱导,最终BGL酶活达到1 175 U/mL。比摇瓶提高了4.8倍,为β-葡萄糖苷酶工业化生产打下了坚实的基础。     

Selection of Leptospirillum ferrooxidans SRPCBL and development for enhanced ferric regeneration in stirred tank and airlift column reactor

Presence of Leptospirillum ferrooxidans plays significant role in ferric sulphate generation during bioleaching process. Thus, an attempt was made to select L. ferrooxidans from the polymetallic concentrate leachate and further developed it for enhanced ferric iron regeneration from the leachate in shake flask, stirred tank and column reactor. When ferric to ferrous iron ratio in the shake flask reached to 20:1, L. ferrooxidans out competed Acidithiobacillus ferrooxidans and accounted for more than 99% of the total population. The isolate was confirmed by 16S rRNA genes sequence analysis and named as L. ferrooxidans SRPCBL. When the culture was exposure to UV dose and the oxidation-reduction potential of the inoculation medium was adjusted to 40 0mV by ferrous:ferric iron ratio, the IOR reached to as high as 1.2 g/L/h in shake flask, even with initial ferrous iron concentration of 200 g/L. The chalcopyrite concentrate leachate containing 12.8, 15.7, and 42.0 g/L ferrous iron, ferric iron and copper, respectively was studied for ferric iron regeneration with the developed polymetallic resistant L. ferrooxidans SRPCBL in stirred tank and a developed biofilm airlift column, the highest IOR achieved were 2.20 g/L/h and 3.1 g/L/h, respectively, with ferrous oxidation efficiency of 98%. The ferric regeneration ability of the developed isolate from the leachate proves useful for a two-stage metal extraction process.     

Strain improvement and up scaling of phytase production by <Emphasis Type="Italic">Aspergillus niger</Emphasis> NCIM 563 under submerged fermentation conditions

Combination of physical and chemical mutagenesis was used to isolate hyper secretory strains of Aspergillus niger NCIM 563 for phytase production. Phytase activity of mutant N-1 and N-79 was about 17 and 47% higher than the parent strain. In shake flask the productivity of phytase in parent, mutant N-1 and N-79 was 6,181, 7,619 and 9,523 IU/L per day, respectively. Up scaling of the fermentation from shake flask to 3 and 14 L New Brunswick fermenter was studied. After optimizing various fermentation parameters like aeration, agitation and carbon source in fermentation medium the fermentation time to achieve highest phytase activity was reduced considerably from 14 days in shake flask to 8 days in 14 L fermenter. Highest phytase activity of 80 IU/ml was obtained in 1% rice bran–3.5% glucose containing medium with aeration 0.2 vvm and agitation 550 rpm at room temperature on 8th day of fermentation. Addition of either bavistin (0.1%), penicillin (0.1%), formalin (0.2%) and sodium chloride (10%) in fermented broth were effective in retaining 100% phytase activity for 8 days at room temperature while these reagents along with methanol (50%) and ethanol (50%) confer 100% stability of phytase activity at 4°C till 20 days. Among various carriers used for application of phytase in feed, wheat bran and rice bran were superior to silica and calcium carbonate. Thermo stabilization studies indicate 100% protection of phytase activity in presence of 12% skim milk at 70°C, which will be useful for its spray drying.