金针菇FV908菌株液体培养工艺的研究

通过单因子试验统计分析 ,优化筛选了适于金针菇 (Flammulinavelutipes)FV90 8的适宜培养基和摇瓶培养条件 ,结果表明 ,其适宜的液体培养基组成为玉米粉 5 .0 % ,麸皮 2 .0 % ,KH2 PO4 0 .1% ,MgSO4 ·7H2 O 0 .0 5 % ,10 μgVB1/ 10 0mL ,5 0 μgVB2 / 10 0mL ;适宜的摇瓶培养条件为 :培养基的起始pH 6 .0～ 7.0 ,5 0 0mL摇瓶装量为15 0mL ,接种量为 10 % ,培养温度 2 5℃ ,摇床转速为 12 0r/min ,菌丝干收率 39g/L。     

转萝卜过氧化物酶基因毕赤酵母株系培养条件的优化

为了提高转萝卜过氧化物酶基因RsPrx1毕赤酵母株系的表达产量,对培养条件进行优化。试验结果表明,26℃,pH7.4,甲醇浓度0.5%,通气面积1.5cm2,225r/min条件下,萝卜过氧化物酶RsPrx1表达量达50.95U/mL。在优化条件下,对培养基补充方式和菌株的遗传稳定性研究表明,彻底更换培养基较补充培养基提高3倍得率,转基因菌株遗传稳定性较高。     

地衣芽胞杆菌培养条件的研究

应用单因素和正交试验设计试验法对地衣芽胞杆菌在摇瓶水平上进行了培养基配方和培养条件的研究。结果表明：最适培养基配方为山芋淀粉1．0％,豆粕0．6％,玉米芯粉0．8％,K2HPO4 0．1％,MgSO40．1％。最适培养条件为37℃,摇床转速150r／min,250mL三角瓶装液50mL,接种量5．0％,振荡培养48h,pH7．0。在20L自动发酵罐中进行了扩大培养试验,考察溶氧对菌体生长的影响,并根据试验结果进一步扩大至1m^3发酵罐,通过控制搅拌速度和通气量,1m^3发酵罐中地衣芽胞杆菌培养液菌浓为7．2×10^9efu／mL,芽胞率达到90％。     

倍他洛尔立体拆分菌株培养条件优化

对倍他洛尔立体拆分菌株胶红酵(Rhodotorula mucilaginosa)DQ832198的培养基组成(碳源、氮源)和其它工艺条件(培养温度、初始pH、装液量)进行了研究。通过单因素试验和正交试验,确定了该菌株的最适培养条件为玉米浆1%、蛋白胨0.5%、甘油2%,初始pH 6.0,培养温度28℃,装液量为110 mL/250mL三角瓶。在此条件下,转化率达55.5%,比优化前提高了31.2%。     

灰树花深层发酵工艺条件的研究

灰树花摇瓶发酵较佳条件 :QF培养基 ,2 5℃ ,pH4 5,装量 60mL/50 0mL三角瓶 ,转速 1 0 0r/min。在种子培养基中加 0 4%的CMC ,可增加种子液菌丝的生长点 ,从而提高菌丝量。在 1 0L气升式发酵罐上放大试验 ,菌丝量对初糖的生物转化率在 2 4 %以上 ,对耗糖的转化率达 435%。菌丝体中多糖含量达 1 0 2 % ,发酵液中多糖含量为 1 38%。     

β-葡聚糖酶高产菌株BS9418F的选育及其发酵条件的研究

经60 Coγ射线辐照处理获得的诱变菌株芽孢杆菌BS9418F ,其产酶活力比出发菌株提高 30 %以上。该菌株以大麦粉 7%、玉米粉 3%、豆粕 3%及适量无机盐为培养基最佳配比 ,其最适培养条件为 :培养基初始 pH 7.0 ,摇瓶装量 5 0mL/ 30 0mL三角瓶 ,种龄 16～ 2 0h ,接种量 2 %～ 3% ,培养温度 36～ 37℃ ,发酵周期 40h。在优化条件下 ,摇瓶发酵产 β 葡聚糖酶活力高达 5 5 0 0u/mL以上 ,比出发菌株初始发酵水平提高了 4倍以上     

一株寡营养细菌胞外多糖的摇瓶发酵研究

从新疆的寡营养环境——古尔班通古特沙漠中分离到一株寡营养细菌Azotobacter sp．(1～15mg碳/L培养基),通过进行Azotobacter sp．菌的单因子优化培养基的试验、摇瓶培养工艺条件的优化试验(培养温度、培养时间、初始pH值、溶氧量),确定了菌种生长与营养需求等主要因子与胞外多糖产量、粘度的关系,结果表明,摇瓶发酵的最适宜条件为:以蔗糖为碳源,碳酸钙含量为2g/L,初始pH值为7左右,种龄72～84h,磷酸二氢钾、硫酸镁的含量分别为0．3g/L、0．1g/L,接种体积分数15%,于37℃摇瓶培养72h,250mL摇瓶装液量为50mL,在适宜条件下粘多糖的产量最大可达到1145．94μg/mL,粘性可达9200 mPa·s。     

均匀设计法对产几丁质酶细菌C4发酵条件的优化

系统研究了碳源,氮源,起始pH值、培养基装量、培养温度和时间等因素对细菌C4产几丁质酶的影响。结果表明,碳、氮源分别以胶体几丁质、KNO和蛋白胨最好;在起始pH值7．6—8．5,培养基装量为三角瓶体积的12％,培养温度28℃,振荡培养(180r／min)5d时最有利于几丁质酶的产生。在此基础上通过均匀设计法优化了发酵培养基配方。优化后的培养基配方为：胶体几丁质1．5％,蛋白胨0．55％,KNO3 0．3％,MgSO4 0．09％,Tween80 0．005％。在该条件下,几丁质酶活力达2．68U／mL,比在原基础培养条件下的酶活力提高90．1％。     

戊糖乳杆菌31-1菌株产细菌素发酵条件优化

对戊糖乳杆菌31-1产细菌素的条件进行了优化,分别研究了培养温度,培养基起始pH值,培养基碳源、氮源,刺激因子等因素对细菌素产量的影响。组合因素优化结果得到最佳培养基与培养条件为：乳糖30g、胰胨15g、豆胨20g、牛肉膏30g、蛋白胨20g、吐温801mL、磷酸氢二钾2g、乙酸钠5g、柠檬酸铵2g、硫酸镁0．58g、硫酸锰0．25g,蒸馏水定容至1000mL,30℃培养24h,培养起始pH为6．5。在此条件下培养细菌素效价可达到640AU／mL,与起始培养基相比细菌素产量提高了8倍。     

暹罗芽胞杆菌FJAT-45551用于农业生物防治的优化培养

以具有防病促长且抑菌谱广的暹罗芽胞杆菌(Bacillus siamensis)FJAT-45551为出发菌株,分别以生物量和发酵液的青枯雷尔氏菌和尖孢镰刀菌抑菌活性为指标,通过单因子和正交试验对其培养基成分和发酵培养条件进行优化,从而提高其抑菌活性。结果表明,优化后的培养基配方为:麸皮20 g/L,蛋白胨25 g/L,MgSO_4·H_2O 0. 2 g/L,CaCl_20. 1 g/L,FeSO_4·7H_2O 0. 1 g/L,NaH_2PO_4·H_2O 0. 5 g/L,K_2HPO_40. 5 g/L;最适发酵培养条件为:接种量1%、摇床转速130 r/min、温度20℃、装液量50 mL(250 mL的摇瓶装液50 mL)、初始pH值为6. 0。在优化的发酵条件下,FJAT-45551发酵液对番茄青枯病菌(Ralstorinia solanacearum)FJAT-91的抑菌圈直径达30. 82 mm,较优化前的抑菌圈直径增加了9. 09 mm,抑菌活性提高了41. 83%。     

Application of factorial designs for optimization of cyclodextrin glycosyltransferase production from Klebsiella pneumoniae pneumoniae AS-22.

Production of cyclodextrin glycosyltransferase (CGTase) from Klebsiella pneumoniae pneumoniae AS-22 was optimized in shake flasks using a statistical experimental design approach. Effect of various components in the basal medium, like carbon, nitrogen, phosphorus, and mineral sources as well as initial pH and temperature, were tested on enzyme production. The optimum concentrations of the selected media components were determined using statistical experimental designs. Two level fractional factorial designs in five variables, namely, dextrin, peptone, yeast extract, ammonium dihydrogen orthophosphate, and magnesium sulphate concentrations were constructed. The optimum medium composition thus found consisted of 49.3 g/L dextrin, 20.6 g/L peptone, 18.3 g/L yeast extract, 6.7 g/L ammonium dihydrogen orthophosphate, and 0.5 g/L magnesium sulphate. The maximum CGTase activity obtained was 21.4 U/mL in 28 h of incubation. The cell growth and CGTase production profiles were studied with the optimized medium in shake flasks and in 1-L fermenters. It was observed that the enzyme production was growth associated both in shake flask and in fermenter, although it was slower in shake flask. The maximum CGTase activity obtained in the fermenter was 32.5 U/mL in 16 h. The optimized medium resulted in about 9-fold increase in the enzyme activity as compared to that obtained in the basal medium in shake flask as well as in fermenter.     

Scaleup of ajmalicine production by plant cell cultures of Catharanthus roseus

The effect of scaleup on he production of ajmalicine by a Catharanthus roseus cell suspension culture in a selected induction medium were studied. In preliminary experiments it was observed that the culture turned brown and the production was inhibited upon transfer from a shake flask to a stirred bioreactor with forced aeration. Two factors were recognized as the potential origin of the differences between shake flask and bioreactor cultures: gas composition and mechanical shear forces. These factors were studied separately.By recirculating a large part of the exhaust gas, a comparable gas regime was obtained in a bioreactor as occurred in a shake flask cultures. This resulted in the absence of browning and a similar pattern of ajmalicine production as observed in shake flasks. The effect of shear forces could not be demonstrated. However, the experiments showed that the culture may be very sensitive to liquid phase concentrations of gaseous compounds. The effects of k(L)a, aeration rate, CO(2) production rate, and influent gas phase CO(2) concentration on the liquid phase CO(2) concentration are discussed. (c) 1993 John Wiley & Sons, Inc.     

Interaction of cultural conditions and end-product distribution in Bacillus subtilis grown in shake flasks

Summary A culture of Bacillus subtilis, in which the relative production of acetoin (Ac) and butanediol (Bu) is highly sensitive to oxygen tension as well as to mixing conditions, was used to evaluate several culture conditions in 500-ml shake flasks. The concentration ratio of these metabolites (Ac/Bu) produced in a defined period of culture time was used as a parameter for comparative purposes. The influence of working volume, shaking speed, broth viscosity and the presence of baffles were evaluated. Using unbaffled flasks it was found that working volume had the most influence on oxygenation in shake flasks, especially below 10%, where differences in Ac/Bu ratios up to ten times could be measured. Shaking speed played an important role only at values higher than 400 rpm or when small working volumes were used. The addition of xanthan gum decreased the Ac/Bu ratio nearly four times under equivalent working conditions and also diminished the influence of shaking speed. In general, Ac/Bu was higher when sulphite oxygen transfer rate (OTR) values were higher. However, the test culture was able to detect differences which were not evident using the OTR method. Comparing Ac/Bu ratios in stirred fermentors from the literature, it seems that similar oxygenation conditions can be reached in non-baffled shake flasks only at very high shaking speeds using small working volumes. With baffled flasks, our data suggest that better oxygenation and mixing can be achieved in shake flasks if compared with those obtained in stirred fermentors at conventional power inputs.     

Reproducing shake flasks performance in stirred fermentors: production of alginates by Azotobacter vinelandii

Keeping equal the initial power drawn (0.27 W l(-1)) in shake flasks and in a stirred fermentor did not reproduce the behaviour of alginate production by Azotobacter vinelandii. A lower mean molecular weight (1.1x10(6) Da) of the polymer was obtained in the bioreactor as compared to that obtained in shake flasks (1.9x10(6) Da). The reasons for this can reside in the fact that the evolution of the power drawn in the shake flasks could be considerably different to that observed in the stirred bioreactor. A drastic drop in the specific power drawn is expected in the shake flasks as a consequence of the increased viscosity, which caused the liquid not following the movement of the shaker. This was supported by the fact that cultures developed in the fermentor at lower initial power drawn (as low as 0.027-0.056 W l(-1)) or in a culture in which the power drawn was deliberately reduced along cultivation, produced alginates with similar molecular characteristics as that obtained in shake flasks.     

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.     

Disposable orbitally shaken TubeSpin bioreactor 600 for Sf9 cell cultivation in suspension

Disposable orbitally shaken TubeSpin bioreactor 600 tubes (TS600s) were recently developed for the bench-scale cultivation of animal cells in suspension. Here we compared batch cultures of Sf9 insect cells in TS600s, spinner flasks, and shake flasks. Superior cell growth was observed in TS600s and shake flasks as compared with spinner flasks, and more favorable oxygen-enriched cell culture conditions were observed in TS600s as compared with either spinner or shake flasks. The results demonstrated the suitability of TS600s as a disposable vessel for the cultivation of Sf9 cells in suspension.     

Comparison of p-Nitrophenol Biodegradation in Field and Laboratory Test Systems

Acclimation of microbial communities exposed to p-nitrophenol (PNP) was measured in laboratory test systems and in a freshwater pond. Laboratory tests were conducted in shake flasks with water, shake flasks with water and sediment, eco-cores, and two sizes of microcosm. The sediment and water samples used in the laboratory experiments were obtained from the pond. After a 6-day acclimation period, PNP was biodegraded rapidly in the pond. When the pond was treated with PNP a second time, biodegradation began immediately. The acclimation periods in laboratory test systems that contained sediment were similar to that in the pond. The acclimation period was threefold longer in shake flasks without sediment. PNP was biodegraded more slowly by microbial communities acclimated in the laboratory than it was in the pond, and the rate of biodegradation varied with the type of test. The number of bacteria able to mineralize PNP increased by 3 orders of magnitude in the pond during the acclimation period. Similar increases accompanied acclimation in the laboratory systems.     

以摇瓶所得摄氧率为基准进行发酵放大

通过设计特殊摇瓶,用亚硫酸盐法测出摇瓶口纱布层氧通透率的基础上,在实际发酵情况下通过测定瓶内气、液相氧的变化得出其发酵过程中的摄氧率(OUR)及氧传递系数(K_La)。以特制摇瓶取得的菌体CUR为基准进行发酵过程和发酵罐的放大。通过质谱仪在线检测及采样分析,研究了3种不同供气流量及搅拌转速下的放大结果。摇瓶与发酵罐在菌体OUR、菌体产量方面吻合很好,而在整个放大过程中,发现摇瓶与发酵罐内的氧传递系数(K_La)、溶解氧(C_L)差异较大。     

Stimulation of citric acid production in Aspergillus niger by addition of viscous substances in shake culture

When glucose (120mg/ml) was used as a carbon source, Aspergillus niger Yang no. 2. showed a markedly low citric acid productivity in shake culture (15.4 mg/ml) but a high productivity in semi-solid and surface cultures (72.3 mg/ml and 67.6 mg/ml, respectively). Since the viscosity of the medium was assumed to be one of the important factors for citric acid productivity in shake culture, the effects of the addition of viscous substances on citric acid productivity of strain Yang no. 2 were examined. The addition of 2.0–6.0 mg gelatin/ml as a viscous additive to the medium containing glucose as a carbon source increased slightly the medium viscosity but substantially increased the citric acid productivity in shake culture to levels of 52.0–53.3 mg/ml, about 3.4 times as much as that without gelatin. However, no influence of gelatin addition was observed in semi-solid and surface cultures, i.e. under static cultivation conditions. Different mycelial morphologies of the strain were observed when cultivations were done in shake culture with or without the addition of gelatin. Addition of 5.0 mg agar/ml, 5.0 mg carageenan/ml, 2.5 mg carboxymethylcellulose/ml and 2.5 mg polyethylene glycol 6000/ml, to the medium containing glucose as a carbon source also increased the citric acid productivity in shake culture to levels of 39.2–54.7 mg/ml. Since Yang no. 2 does not utilize these viscous substances, these results suggested that the viscous substances functioned as protectants for the mycelium from physiological stresses due to shaking and as a consequence resulted in a remarkably increased citric acid productivity in shake culture.     

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.