pH两阶段控制策略发酵生产重组角质酶

为提高基因工程菌Bacillus subtilis WSHB06-07发酵生产角质酶的产量和生产强度,考察了pH（5.5~8.0）对菌体生长和产酶的影响。基于不同pH发酵过程中菌体比生长速率及比产物合成速率的变化,确定了pH两阶段控制策略,即0~4 h时控制pH 7.5,4 h后将pH调至6.5。通过采用这一优化策略,角质酶酶活有了较大的提高,达170 U/mL,生产强度为16.9 kU/(L·h),比恒定pH 7.5控制模式下分别提高了122.6%和123.2%。     

pH对S-腺苷-L-蛋氨酸发酵的影响

研究了不同pH控制方式对S-腺苷-L-蛋氨酸(SAM)发酵过程及产量的影响。通过对发酵过程中不控制pH、控制恒定pH、两阶段控制pH和三阶段控制pH实验,研究了不同条件下对菌体干重、葡萄糖代谢和SAM产量的影响。控制合适的pH有利于菌体生长与SAM的生物合成,菌体生长最适pH为6.0,SAM转化最适pH为6.5,采用三阶段控制pH,使SAM产量比不控制pH提高了133%,比控制pH6.5提高了18.6%,比两阶段控制pH提高了10%。     

应用细胞透性化技术快速提取氧化葡萄糖杆菌胞内右旋糖酐糊精酶

将细胞透性化技术应用到右旋糖酐酶的提取检测过程中,根据单因素实验和正交试验设计确定了从氧化葡萄糖杆菌(Gluconobacter oxydans)细胞中提取胞内右旋糖酐糊精酶(DDase)的最佳方法:甘氨酸(Gly)质量分数15%,Triton X-100体积分数1%,菌悬液OD600为0.5~6.0,pH为6.81,冰浴处理时间1 h,透性化试剂的提取效率可达到酶活最大值的90%以上。与超声波细胞破碎法相比,该方法条件温和,酶的释放率较高并易于大量试样的平行实验操作。     

海洋红树林内生真菌产抗肿瘤活性化合物1403C发酵条件的优化

旨在考察pH、溶解氧和剪切力对Halorosellinia sp.( No.1403)发酵过程的影响.结果表明,在发酵中后期及整个发酵过程中控制发酵液的pH恒定对菌体的生长影响不明显,但在不同发酵时期控制不同的恒定pH值对1403C的产量影响较大.仅在发酵的前24h控制恒pH7.0,有利于菌丝的生长,但抑制1403C的生物合成,菌体干重为对照组的159.1％,1403C的产量仅为对照组的29.4％;从48 h开始控制恒pH7.0,有利于1403C的生物合成,菌体干重量为对照组的94％,1403C的产量为对照组的123.2％;适量的溶解氧和剪切力有利于1403C的生物合成;从48 h开始提高剪切力可获得较高的1403C产量,是对照组的151.8％.综上所述,在发酵至48 h时开始控制恒pH7.0,并适当增大剪切力,在整个发酵过程中控制适当充足的溶解氧有利于1403C的合成.     

右旋糖酐蔗糖酶工程菌株的构建及其培养条件的研究

[目的]右旋糖酐蔗糖酶是一种以蔗糖为底物,催化转移D-葡萄糖基生成α-葡聚糖或低聚糖的葡萄糖基转移酶.[方法]利用PCR扩增技术,将已获得的右旋糖酐蔗糖酶基因dexYG亚克隆到表达载体PET28a( )上,转化E.coli BL21(DE3),经过卡那霉素抗性筛选和酶切验证后,得到右旋糖酐蔗糖酶工程菌株BL21(DE3)/pET28-dexYG.[结果]经IPTG诱导该基因在E.coli BL21(DE3)中能有效表达,在诱导过程中菌体生长受到抑制.通过对培养时间、IPTG浓度、培养温度、菌浓(OD600)和pH值等产酶因素的优化考察,得到最佳培养条件为:培养时间5h、IPTG浓度0.5mmol/L、25℃、OD600值1.0和pH6.0.酶活力由最初的5.39U/mL提高到35.62U/mL,其中pH值对产酶活力影响最大,在pH6.0时的最高产酶活力是LB原始pH条件下最高酶活的3.5倍,并且pH值也是导致在诱导后期酶活迅速下降的主要原因之一.[结论]酶的表达和酶活的研究结果表明,构建的工程菌株能够异源高效表达右旋糖酐蔗糖酶,并且表现出较高的酶活力.     

Mn~(2+)对肠膜状明串珠菌产右旋糖酐的影响

肠膜状明串珠菌在其产生的右旋糖酐蔗糖酶的作用下,以蔗糖为原料转化合成右旋糖酐和产生果糖。着重进行了Mn~(2+)对肠膜状明串珠菌Lm-1226发酵产右旋糖酐影响的初步探索。对Mn~(2+)对肠膜状明串珠菌Lm-1226的生长,产果糖、右旋糖酐和右旋糖酐蔗糖酶,右旋糖酐蔗糖酶作用影响进行了研究。一定浓度的Mn~(2+)对肠膜状明串珠菌Lm-1226的生长具有促进作用; Mn~(2+)抑制肠膜状明串珠菌Lm-1226发酵产果糖和右旋糖酐,且Mn~(2+)浓度越高,抑制性越强; Mn~(2+)对肠膜状明串珠菌Lm-1226发酵产右旋糖酐蔗糖酶有抑制作用; Mn~(2+)对右旋糖酐蔗糖酶具有较强的激活作用,激活作用可达158%,最适Mn~(2+)浓度为5. 0 mmol/L。     

组成型表达粪产碱杆菌青霉素G酰化酶重组大肠杆菌发酵条件研究

目的:对重组大肠杆菌组成型表达粪产碱杆菌青霉素G酰化酶(AfPGA)进行了发酵条件研究。方法:在摇瓶和5L发酵罐中研究了(NH4)2SO4和葡萄糖浓度对质粒的分离稳定性及青霉素G酰化酶表达的影响。结果:该工程菌质粒具有分离不稳定性,培养基中无(NH4)2SO4时发酵过程中pH和糊精水解生成葡萄糖的浓度变化较小,细胞前期(0h-12h)的生长速率降低,质粒分离稳定性和青霉素G酰化酶的表达水平提高。发酵过程中维持低葡萄糖水平可以限制细胞的生长速率,提高质粒稳定性和促进青霉素G酰化酶的合成。采用混合碳源发酵,发酵培养基含糊精2g/L,12h后以1g/L.h恒速流加葡萄糖至35h,控制流加过程葡萄糖浓度0.1g/L左右,平均比生长速率为0.06h-1,发酵结束时质粒稳定性为86%,青霉素G酰化酶的表达水平达23 000U/L。结论:重组大肠杆菌组成型表达青霉素G酰化酶的研究对工业生产有一定指导意义。     

右旋糖酐酶的底物吸附

用35％乙醇保护,底物占旋糖酐能对右旋糖酐酶有效地吸附。采用0．2mol／L pH8．0的KzHPO4-KH2PO4缓冲液(内含30％乙醇)进行解吸,总同收率在80％以上。粗酶液经此过程提纯了9倍。低温对吸附有利。 在酶稳定范围内,pH对吸附影响不大。酶浓度过高,吸附效率下降。对稀酶液可连续多次吸附以达到浓缩目的。1．5％(W／V)的右旋糖酐使可得到满意的吸附效果,对五种不同来原的右旋糖酐酶吸附率都很高,但不同来源的底物适用情况差别很大。     

重组大肠杆菌右旋糖酐蔗糖酶的表达条件优化

通过设计正交实验,考察了培养基中各组分及其浓度对右旋糖酐蔗糖酶工程菌Escherichia coli BL21(DE3)/pET28-dexYG诱导产酶结果的影响。在获得最佳培养条件的基础上,考察温度、蔗糖浓度和pH值对右旋糖酐产量的影响。结果表明:菌浓OD600达到2.0时,加入异丙基硫代-β-D-呋喃半乳糖苷(IPTG)至0.25mmol/L,25°C诱导培养4h,产酶活力最高,达到110.16U/mL,蔗糖浓度对产量的影响比较显著。研究结果得到高效表达的培养条件,为实现该酶的工业化应用打下了基础。     

3-羟基丙酸分批发酵过程中的pH控制策略研究

本文利用重组大肠杆菌以甘油为底物发酵合成3．羟基丙酸,考察了不同pH对3．羟基丙酸产量及菌体生长的影响,发现在pH6．5条件下,细胞比生长速率达到最大值,延迟期也相对较短;而pH7．0有利于3-羟基丙酸的合成,控制pH7．0可以使3-羟基丙酸产量达到7．39g／L。基于不同pH条件下对细胞比生长速率和3-羟基丙酸比生成速率的分析,提出3．羟基丙酸分批发酵过程中的pH控制策略,即在发酵过程前5h将pH控制在6．5,5h～15h控制pH为7．0,此时有利于细胞生长;而后在15h-25h控制pH为7．5,25h后控制pH为7．0,从而使细胞具有较高的3．羟基丙酸比合成速率。在此控制策略下经过34h发酵3-羟基丙酸的终产量达到8．76g／L,比pH7．0条件下的3-羟基丙酸产量提高了18．54％。     

A shaken disposable bioreactor system for controlled insect cell cultivations at milliliter‐scale

While wave‐mixed and stirred bag bioreactors are common devices for rapid, safe insect cell culture‐based production at liter‐scale, orbitally shaken disposable flasks are mainly used for screening studies at milliliter‐scale. In contrast to the two aforementioned bag bioreactor types, which can be operated with standard or disposable sensors, shaker flasks have not been instrumented until recently. The combination of 250 mL disposable shake flasks with PreSens's Shake Flask Reader enables both pH and dissolved oxygen to be measured, as well as allowing characterization of oxygen mass transfer. Volumetric oxygen transfer coefficients (k_La‐values) for PreSens 250 mL disposable shake flasks, which were determined for the first time in insect cell culture medium at varying culture volumes and shaker frequencies, ranged between 4.4 and 37.9/h. Moreover, it was demonstrated that online monitoring of dissolved oxygen in shake flasks is relevant for limitation‐free growth of insect cells up to high cell densities in batch mode (1.6×10⁷ cells/mL) and for the efficient expression of an intracellular model protein.     

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。     

人三叶因子3在毕赤酵母中表达条件的研究

为提高人三叶因子 3 (HumanTrefoilfactor 3 ,hTFF3 )在毕赤酵母中的表达量 ,研究了转化子生长的培养条件 ,包括不同碳源对转化子生长的影响和接种量、甲醇浓度、pH值、摇瓶转速及不同诱导时间对人三叶因子 3表达的影响。结果表明转化子在生长阶段加入葡萄糖生长旺盛 ,培养 14h后OD₆₀₀ 就可达到 50。在 100mL生长培养基上的菌液以 1∶1接入诱导培养基时蛋白表达量最高 ;转化子在 1%的甲醇、pH60、摇瓶转速240r/min的条件下诱导4 8h ,菌体密度OD₆₀₀为 15 ,目的蛋白表达量达到 20mg L。用 5L发酵罐进行了高密度发酵 ,经2%甲醇32h诱导 ,最终菌体密度OD₆₀₀ 达到 120 ,每升发酵液中含目的蛋白100mg。     

溶氧对Blakeslea trispora分批发酵生产β-胡萝卜素的影响

在摇瓶和5 L发酵罐中研究了溶氧 (DO) 对Blakeslea trispora分批发酵生产β-胡萝卜素的影响,总结了5 L发酵罐中β-胡萝卜素发酵过程中溶氧的变化规律.结果表明,当500 mL摇瓶装液量为50 mL,转速为240 r/min条件下发酵生产β-胡萝卜素产量最大,达到3.416 g/L; 5 L发酵罐中,在搅拌转速为1 000 r/min,通气量为1.5 vvm的条件下,β-胡萝卜素的产量可达到3.712 g/L,略高于摇瓶,这可能是由于5 L发酵罐中的气液传递和混合状况好于摇瓶,促进了产物的合成.     

A highly efficient method for liquid and solid cultivation of the anaerobic hyperthermophilic eubacterium Thermotoga maritima

An efficient and economical medium--Thermotoga maritima basal medium (TMB)--was designed for the cultivation of T. maritima under either liquid or solid conditions. When the broth was flushed with N2 or CO2 throughout cell growth in a 10-L fermentor (pH controlled to 6.5), the maximum cell density (OD600) on TMB containing 1% glucose rose to 2.0 or higher (1.63 x 10(9) cells mL(-1)). Sheath-less cells observed by electron microscopy were captured during growth in the fermentor. Using a two-layer plating method, isolated single-well colonies were consistently obtained within 24 h on the TMB in modified tissue culture flasks. The minimal inhibitory chloramphenicol concentrations for T. maritima on TMB agar were 5 microg mL(-1) after 24 h and 48 h, and 25 microg mL(-1) at 72 h.     

Enterotoxin production by Vibrio cholerae and Vibrio mimicus grown in continuous culture with microbial cell recycle

We have examined the effect of complete cell recycle on the production of cholera toxin (CT) by Vibrio cholerae and CT-like toxin by Vibrio mimicus in continuous culture fermentations. Complete cell recycle was obtained by filtering culture fluids through Amicon hollow fibers with an exclusion limit of 100,000 daltons (H1P100-20) and returning the concentrated cell slurry to the fermentor. A single 1-liter laboratory fermentor system modified with this recycle loop was capable of producing over 20 liters of cell-free culture filtrate per day. Toxin production in this system was compared with yields obtained in traditional continuous cultures and in shake flask cultures. Yields of CT from V. cholerae 569B in the recycle fermentor were highest at the highest dilution rate employed (1.0 vol/vol per h). The use of complete cell recycle dramatically increased yields over those obtained in continuous culture and equaled those obtained in shake flasks. The concentration of CT in the filtrate was slightly less than half of that measured in culture fluids sampled at the same time. Similarly, V. mimicus 61892 grown in the presence of 50 micrograms of lincomycin per ml produced 280 ng of CT per ml in the recycle fermentor, compared with 210 ng/ml in shake flasks under optimal conditions. The sterile filtrate from this fermentation contained 110 ng/ml.     

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.     

Enterotoxin production by Vibrio cholerae and Vibrio mimicus grown in continuous culture with microbial cell recycle.

We have examined the effect of complete cell recycle on the production of cholera toxin (CT) by Vibrio cholerae and CT-like toxin by Vibrio mimicus in continuous culture fermentations. Complete cell recycle was obtained by filtering culture fluids through Amicon hollow fibers with an exclusion limit of 100,000 daltons (H1P100-20) and returning the concentrated cell slurry to the fermentor. A single 1-liter laboratory fermentor system modified with this recycle loop was capable of producing over 20 liters of cell-free culture filtrate per day. Toxin production in this system was compared with yields obtained in traditional continuous cultures and in shake flask cultures. Yields of CT from V. cholerae 569B in the recycle fermentor were highest at the highest dilution rate employed (1.0 vol/vol per h). The use of complete cell recycle dramatically increased yields over those obtained in continuous culture and equaled those obtained in shake flasks. The concentration of CT in the filtrate was slightly less than half of that measured in culture fluids sampled at the same time. Similarly, V. mimicus 61892 grown in the presence of 50 micrograms of lincomycin per ml produced 280 ng of CT per ml in the recycle fermentor, compared with 210 ng/ml in shake flasks under optimal conditions. The sterile filtrate from this fermentation contained 110 ng/ml.     

碱性果胶酶在重组毕赤酵母中高效表达的关键因素研究

为提高重组毕赤酵母生产碱性果胶酶的产量和生产强度,在摇瓶条件下优化了重组毕赤酵母生产碱性果胶酶的关键因素。结果表明,以下条件：初始甘油浓度40g／L、初始甲醇浓度3.1g甲醇／gDCW、每24h添加0.51g甲醇／gDCW、诱导表达周期72h、250mL三角瓶诱导培养基装液量30mL、初始pH6,0,最适于菌体生长与产物表达。在此基础上,7L罐上通过恒速流加甘油进一步提高细胞密度,诱导阶段甲醇采取前期恒速流加和后期DO-stat,发酵结束菌体干重达80g／L,酶活为217U／mL,比摇瓶结果提高了66.2％。     

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.