L-苹果酸产生菌F-871变株合成延胡索酸酶的研究

温特曲霉AspergilluswentiiF-871是高效转化延胡索酸为L-苹果酸的变株,通过对其合成延胡索酸酶的因素进行研究,筛选了培养基主要营养元素有L-精氨酸、酪氨酸、丝氨酸、天冬氨酸、苏氨酸、赖氨酸及相应含量丰富的酵母粉、黄豆饼粉和玉米浆。该变株生长阶段条件为:pH6.0,温度2830℃,培养时间为24h,酶合成阶段最适条件:接种量15%,初始pH6.8,培养温度2830℃,装量8090ml/500ml,酶合成周期40h。在优化的培养条件下,F-871变株延胡索酸酶合成水平可达156.33u/g,100ml发酵液中的酶可将延胡索酸转化为L-苹果酸32.06g,比国内一步发酵法产酸88.5%提高约4倍,转化率由85%提高到106.87%,发酵周期由90h缩短至57h。     

L-苹果酸产生菌F-871变株合成延胡索酸酶的研究

温特曲霉Aspergillus wentii F-871是高效转化延胡索酸为L-苹果酸的变株,通过对其合成延胡索酸酶的因素进行研究,筛选了培养基主要营养元素有L-精氨酸、酪氨酸、丝氨酸、天冬氨酸、苏氨酸、赖氨酸及相应含量丰富的酵母粉、黄豆饼粉和玉米浆。该变株生长阶段条件为：pH6．0,温度2830℃,培养时间为24h,酶合成阶段最适条件：接种量15％,初始pH6．8,培养温度2830℃,装量8090ml／500ml,酶合成周期40h。在优化的培养条件下,F-871变株延胡索酸酶合成水平可达156．33u／g,100ml发酵液中的酶可将延胡索酸转化为L-苹果酸32．06g,比国内一步发酵法产酸88．5％提高约4倍,转化率由85％提高到106．87％,发酵周期由90h缩短至57h。     

温特曲霉转富马酸为L-苹果酸的初步研究*

从大量霉菌中选育到一株具有较高富马酸酶活性的温特曲霉(Aspergillus wentii) A5-61。在摇瓶培养条件下,32℃ 96小时,产L-苹果酸达10.49g/100ml,对富马酸的转化率达90.80%。利用菌体细胞,进行酶转化试验,结果表明：1.6g湿菌体接入25ml含富马酸10.0%（用NaOH中和至pH7.0）的转化液中,35℃16～24小时,连续转化三次,分别产生L—苹果酸9.61g/100ml、9.73g/100ml、6.93g/100ml。对菌体整体细胞酶学性质的研究表明,其最适反应温度35℃,最适反应pH7.0,Cu2＋对该酶有明显的抑制作用,该酶的Km＝0.154mol/L,Vmax＝0.0571mol/L·h。     

嗜热网球菌纤维二糖差向异构酶在枯草芽孢杆菌中的表达及发酵优化

通过化学方法合成嗜热网球菌(Dictyoglomus thermophilum)来源的纤维二糖差向异构酶基因ce,将其引入到载体pBSuL3-ce,构建重组质粒pBSuL3-ce并转化进枯草芽孢杆菌,发酵48h后测定胞内酶活为7. 5U/ml。酶学性质结果表明:该酶的最适pH为8. 5;最适温度为85℃,85℃的半衰期为120min。为降低发酵成本,对发酵培养基进行优化:以35g/L豆粕粉为氮源、5g/L甘油为碳源时,酶活力最高可达12. 3U/ml。依据摇瓶优化的条件在3L发酵罐中扩大培养,胞内酶活达到56U/ml,比摇瓶培养酶活提高了8倍。利用发酵所得酶制备乳果糖,在乳糖浓度为400g/L、反应温度为85℃、初始pH 8. 5、加酶量为20U/ml的条件下,乳果糖转化率可达51%。     

蚀木链霉菌KX6耐热内切葡聚糖酶的产生及酶学性质研究

从堆肥中筛选到一株产耐热内切葡聚糖酶的放线菌菌株,通过形态观察和16S rRNA序列分析,鉴定为蚀木链霉菌(Streptomyces Xylophagus)。实验中对其产酶的液态发酵条件进行了研究,碳源为1%（w/v）羧甲基纤维素钠,氮源为1%（w/v）豆粕粉,250ml三角瓶30 %装液量,接种量为2%,培养基初始pH为8.0,培养温度为40℃,200r/min培养48h后,发酵液中内切葡聚糖酶活达到0.538IU/ml。该酶的最适作用温度和pH分别为50℃和7.0,50℃下酶活保持1 h不变,60℃保温1h,仍有60%的原酶活性,pH为6.0~7.0酶活稳定,该酶属于一种耐热的中性内切葡聚糖酶。     

海洋真菌岩藻多糖酶的固态发酵条件研究*

本文对海洋真菌Dendryphiella arenaria(TM94)岩藻多糖酶的固态发酵条件进行了研究,主要内容包括碳源、氮源、添加物、起始pH、接种量及温度等.固态发酵最佳培养基组成麸皮7.5g,葡萄糖0.5g,海带粉0.6g,NaNO3为4g/L最佳培养条件为培养温度28℃,起始pH6,接种量3ml(孢子浓度为106个/ml).在28℃培养24h,酶活力可达35.5IU/g干培养基,比活力为1.39IU/mg蛋白质.对岩藻多糖酶酶学性质也进行了研究.     

β-甘露聚糖酶产生菌的分离、鉴定及产β-甘露聚糖酶最适条件的研究

以采集的土壤样品为试验材料,经过富集培养及分离纯化,筛选出2株产β-甘露聚糖酶的菌株.采用摇瓶培养分别测定其酶活力,其中1株菌株酶活力较高,酶活力达50.36 U/ml.生理生化性质鉴定及16S rDNA序列相似性结果表明该菌为假单孢菌(Pseudomonas sp.).产酶的最适条件研究发现,1 g/100 ml玉米粉,2 g/100 ml魔芋粉,pH6.0,32℃为最优产酶条件,酶活力达185.37 U/ml,是优化前的3.68倍.该菌产酶迅速,培养12 h后已达产酶高峰.粗酶的性质研究发现,该酶是一种酸性的甘露聚糖酶,作用的最适pH为4.0,最适反应温度为55℃;该酶的稳定性较好,在pH4.0～6.0、温度为40～55℃保持较好的稳定性.     

L-Gln高产突变菌株发酵条件的初步优化

将诱变实验筛选出的遗传稳定性高产突变株C.glutamicum N-U-6作为研究对象,采用单次单因子非统计优化技术确定了它在培养温度为30℃下250 mL的摇瓶培养条件为:150 g.L-1葡萄糖,最佳无机氮源及其浓度为:40 g.L-1NH4Cl;最佳有机氮源及其浓度:14 g.L-1尿素;玉米浆浓度:10 g.L-1,初始pH为7.2,装液量为30 mL,种龄为12 h,接种量为10%。谷氨酰胺产量达到37.21 g.L-1,比优化前的突变株(33.54 g.L-1)提高10.9%。     

无根根零R25和普通变形杆菌P1混合培养发酵L-苹果酸的研究

所筛的41株属于根霉属的菌株,均具有从葡萄糖产生延胡索酸的能力。其中,R25产延胡索酸能力最高,同时产生部分L-苹果酸。该菌株被鉴定为无根根霉(Rhizopus arrhizus)。普通变形杆菌(Protcus vulgaris) Pl具有强的延胡索酸酶活性：可将延胡索酸转化为L一苹果酸。     

D-泛解酸内酯水解酶产生菌的筛选及产酶条件研究

筛选到一株产D-泛解酸内酯水解酶的菌株,经鉴定为串珠镶孢霉菌（Fusarium monili-forme)SW-902。产酶条件研究表明,用甘油作碳源,蛋白胨作氮源,初始pH8.0,温度26℃,摇瓶培养3d,产酶量最高,在60L发酵罐中通风发酵45h,产菌丝体生物量7.18g干菌体/L,D-泛解酸内酯水解酶酶活力达到0.92IU/g干菌体。     

球孢白僵菌Bb174固态发酵产几丁质酶产酶及酶学特征研究

对球孢白僵菌(Beauveria bassiana)Bb174产几丁质酶进行了固态发酵条件及酶学特征的研究．结果表明,以4：1麸皮：蚕蛹粉、蛋白胨1g·L^-1作为产酶最适培养基,在7．5g培养基中接种3ml液态种子,自然pH下28℃培养2d,酶活可达最高,为126U·g^-1(干培养基)．粗酶液的最适反应温度为40℃,最适反应pH5．0,在30-70℃保温1h,得半失活温度48℃．在30--40℃、pH4～6范围内,酶的性质最稳定．根据Lineweaver-Burk作图法,得到该酶的动力学参数Km为0．52mg·ml^-1,Vm为0．7△E680·h^-1．     

Single-cell protein production from Jerusalem artichoke extract by a recently isolated marine yeast <Emphasis Type="Italic">Cryptococcus aureus</Emphasis> G7a and its nutritive analysis

After crude protein of the marine yeast strains maintained in this laboratory was estimated by the method of Kjehldahl, we found that the G7a strain which was identified to be a strain of Cryptococcus aureus according to the routine identification and molecular methods contained high level of protein and could grow on a wide range of carbon sources. The optimal medium for single-cell protein production was seawater containing 6.0 g of wet weight of Jerusalem artichoke extract per 100 ml of medium and 4.0 g of the hydrolysate of soybean meal per 100 ml of medium, while the optimal conditions for single-cell protein production were pH 5.0 and 28.0°C. After fermentation for 56 h, 10.1 g of cell dry weight per liter of medium and 53.0 g of crude protein per 100 g of cell dry weight (5.4 g/l of medium) were achieved, leaving 0.05 g of reducing sugar per 100 ml of medium and 0.072 g of total sugar per 100 ml of medium total sugar in the fermented medium. The yeast strain only contained 2.1 g of nucleic acid per 100 g of cell dry weight, but its cells contained a large amount of C_16:0 (19.0%), C_18:0 (46.3%), and C_18:1 (33.3%) fatty acids and had a large amount of essential amino acids, especially lysine (12.6%) and leucine (9.1%), and vitamin C (2.2 mg per 100 g of cell dry weight). These results show that the new marine yeast strain was suitable for single-cell protein production.     

短小芽孢杆菌(Bacillus pumilus) WHK4以羽毛粉为底物产蛋白酶条件的优化

探索Bacillus pumilusWHK4以羽毛粉为底物产酶的最佳条件和最佳培养基组成。以羽毛粉发酵培养基为基础,首先采用单因子试验考察底物浓度、初始pH、接种量、外加碳源、外加氮源对WHK4产酶活力的影响。在单因子试验的基础上采用正交试验设计对底物浓度、温度、初始pH、接种量、外加(NH4)2SO4、外加麦芽糖进行优化。结果显示:Bacillus pumilusWHK4最佳的产酶条件为初始pH7.38,菌龄16 h,接种量5%,37℃。最佳的培养基组成为:1 L基础发酵培养基,40.0 g羽毛粉,10.0 g(NH4)2SO4和10.0 g麦芽糖。在优化的条件下Bacillus pumilusWHK4 24 h产蛋白酶活力为每毫升90 U。对培养条件和培养基的优化为Bacillus pumilusWHK4产蛋白酶的分离纯化奠定了基础。     

球孢白僵菌Bb174固态发酵产几丁质酶产酶及酶学特征研究

对球孢白僵菌(Beauveria bassiana)Bb174产几丁质酶进行了固态发酵条件及酶学特征的研究.结果表明,以4:1麸皮:蚕蛹粉、蛋白胨1g·L^-1作为产酶最适培养基,在75g培养基中接种3ml液态种子,自然pH下28℃培养2d,酶活可达最高,为126U·g^-1(干培养基).粗酶液的最适反应温度为40℃,最适反应pH5.0,在30～70℃保温1h,得半失活温度48℃.在30～40℃、pH4～6范围内,酶的性质最稳定.根据Lineweaver-Burk作图法,得到该酶的动力学参数K_m为0.52mg·ml^-1,V_m为0.7△E₆₈₀·h^-1.     

Fermentation of fumarate and L-malate by Clostridium formicoaceticum.

The fermentation of fumarate and L-malate by Clostridium formicoaceticum was investigated. Growing and nongrowing cells degraded fumarate by dismutation to succinate, acetate, and CO2; on the other hand, only small amounts of succinate were detected when the organism was grown on L-malate. This dicarboxylic acid was mainly converted to acetate and CO2. The fermentation balances were modified if bicarbonate or formate were present in the medium. When C. formicoaceticum was grown in the presence of both dicarboxylic acids, fumarate was consumed before L-malate. The latter was mainly converted to acetate, whereas fumarate was fermented to acetate and succinate. Molar growth yields were determined to be 6 g of dry weight per mol of fumarate and 8 g of dry weight per mol of L-malate fermented.     

Production of carboxylic acids from hydrolyzed corn meal by immobilized cell fermentation in a fibrous-bed bioreactor

Corn meal hydrolyzed with amylases was used as the carbon source for producing acetic, propionic, and butyric acids via anaerobic fermentations. In this study, corn meal, containing 75% (w/w) starch, 20% (w/w) fibers, and 1.5% (w/w) protein, was first hydrolyzed using amylases at 60 degrees C. The hydrolysis yielded approximately 100% recovery of starch converted to glucose and 17.9% recovery of protein. The resulting corn meal hydrolyzate was then used, after sterilization, for fermentation studies. A co-culture of Lactococcus lactis and Clostridium formicoaceticum was used to produce acetic acid from glucose. Propionibacterium acidipropionici was used for propionic acid fermentation, and Clostridium tyrobutylicum was used for butyric acid production. These cells were immobilized on a spirally wound fibrous matrix packed in a fibrous-bed bioreactor (FBB) developed for multi-phase biological reactions or fermentation. The bioreactor was connected to a stirred-tank fermentor that provided pH and temperature controls via medium circulation. The fermentation system was operated at the recycle batch mode. Temperature and pH were controlled at 37 degrees C and 7.6, respectively, for acetic acid fermentation, 32 degrees C and 6.0, respectively, for propionic acid fermentation, and 37 degrees C and 6.0, respectively, for butyric acid production. The fermentation demonstrated a yield of approximately 100% and a volumetric productivity of approximately 1 g/(1 h) for acetic acid production. The propionic acid fermentation achieved an approximately 60% yield and a productivity of 2.12 g/(1 h), whereas the butyric acid fermentation obtained an approximately 50% yield and a productivity of 6.78 g/(1 h). These results were comparable to, or better than those fermentations using chemically defined media containing glucose as the substrate, suggesting that these carboxylic acids can be efficiently produced from direct fermentation of corn meal hydrolyzate. The corn fiber present as suspended solids in the corn meal hydrolyzate did not cause operating problem to the immobilized cell bioreactor as is usually encountered by conventional immobilized cell bioreactor systems. It is concluded that the FBB technology is suitable for producing value-added biochemicals directly from agricultural residues or commodities such as corn meal.     

Factors influencing the production of a novel compound, 7,10-dihydroxy-8(E)-octadecenoic acid, by Pseudomonas aeruginosa PR3 (NRRL B-18602) in batch cultures

Pseudomonas aeruginosa PR3 (NRRL B-18602) converts oleic acid to a novel compound, 7,10-dihydroxy-8(E)-octadecenoic acid (DOD). Parameters that included medium volume, cell growth time, gyration speed, pH, substrate concentration, and dissolved oxygen concentration were evaluated for a scale-up production of DOD in batch cultures using Fernbach flasks and a bench-top bioreactor. Maximum production of about 2 g DOD (38% yield) was attained in Fernbach flasks containing 500 ml medium when cells were grown at 28 degrees C and 300 rpm for 16-20 h and the culture was adjusted to pH 7 prior to substrate addition. Increases of medium volume and substrate concentration failed to enhance yield. When batch cultures were initially conducted in a reactor, excessive foaming occurred that made the bioconversion process inoperable. This was overcome by a new aeration mechanism that provided adequate dissolved oxygen to the fermentation culture. Under the optimal conditions of 650 rpm, 28 degrees C, and 40-60% dissolved oxygen concentration, DOD production reached about 40 g (40% yield) in 4.5 L culture medium using a 7-L reactor vessel. This is the first report on a successful scale-up production of DOD.     

根霉12号固体发酵产生纤溶酶工艺条件的研究*

研究了根霉12号固体发酵产生纤溶酶的工艺条件。采用单因素试验、均匀设计方法对固体发酵培养基的碳源、氮源、碳氮比、初始pH、加水量、无机盐加量进行了优化;采用正交试验对发酵时间、接种量进行了研究。结果表明,实验范围内根霉12固体发酵产纤溶酶的适宜培养基组成为:麸皮∶豆粕=1∶2,初始pH5.0,加水量0.75ml/g物料, MnSO4H2O和 (NH4)2SO4加量分别为0.25%和 1.42%(对物料)。适宜培养条件为接种量107个孢子/g物料,培养时间72h。优化条件下的纤溶酶产量平均达791.81u/g物料。     

尖孢镰刀菌生产蒽醌色素的液体发酵条件研究

优化了尖孢镰刀菌液体发酵生产蒽醌类红色素的发酵条件。通过单因素实验和正交优化实验,确定最佳产色素发酵培养基为：可溶性淀粉30％,(NH4)2SO4 3％,MgSO4 0.3％,KH2PO4 4％,pH 6.0。产色素最适培养条件为：初始pH6.0,装液量20％,接种量10％,吐温-80添加量1％,温度28℃,摇床转速200r/min,发酵周期120h。此条件下,色素效价即可达到8.184U/ml,比优化前提高了1.8倍。国内首次对尖孢镰刀菌所产蒽醌色素进行研究,为其进一步应用奠定基础。