Determination of an economical medium for growth of Clostridium butyricum fermentum

本文重点在于提高酪酸梭状芽孢杆菌活菌数量,降低发酵培养基成本.通过对发酵培养基中不同碳源、氮源、生长因子等进行单因素研究,得到最佳培养基组成:可溶性淀粉10 g/L,豆粕(中性蛋白酶水解3 h)20 g/L,玉米浆3g/L.用此培养基在37℃培养24h,采用高层半固体琼脂试管法对酪酸梭状芽孢杆菌进行活菌计数,活菌数可达8.2×108 cfu/mL.培养基中添加K2HPO4 5g/L、MgSO4·7H2O 0.2 g/L、MnSO4·H2O 0.2 g/L培养32 h时,酪酸梭状芽孢杆菌芽孢转化率可达95％.     

纺锤芽孢杆菌CGMCC1347发酵生产异丁香酚单加氧酶的条件优化

对从土壤中筛选获得的纺锤芽孢杆菌CGMCCl347生产异丁香酚单加氧酶的发酵条件进行了单因素考察及正交实验优化,确定了最适的发酵摇瓶培养基组成和培养条件。在发酵培养基组成为尿素1g／L,玉米浆55g/L,K2HP042g／L,MgSO4·7H2O1g／L,初始pH7．5,发酵温度37℃,摇床转速180r／min的条件下培养16h获得的细胞,能转化2％的异丁香酚生成2．49g／L香兰素,异丁香酚单加氧酶酶活达3．79U／L。     

手性拆分环氧氯丙烷菌株的筛选、鉴定及产酶条件研究

从土壤中筛选到5株环氧化物水解酶生产菌,并通过ITS序列鉴定了其中的C375菌,结果为黑曲霉（Aspergillus nigerZJB-09103）。考察了培养基不同碳源、氮源、金属离子和pH等对产酶的影响,得到了较佳的培养基条件：淀粉16g／L,豆饼粉3g／L,蛋白胨3g／L,KH2PO4 0．4g／L,K2HPO4 0．8g／L,MgSO4 0．2g／L,ZnSO4 0．03g／L,pH6．5。采用优化后的培养基条件,酶活力达到156．1U／L,比优化前初始发酵培养条件下的酶活提高了252％,当环氧化物水解酶催化时间为10h时,（s）-环氧氯丙烷的对映体过量值（e．e．）可达99．0％。产率为18．6％。     

少根根霉菌株发酵生产纤溶酶条件的研究

发酵条件优化可提高少根根霉菌株8B所产纤溶酶的活性。使用单因素试验和正交试验确定该茵发酵产酶的最佳条件。试验确定最优化发酵条件,培养基：麸皮水5g／L,尿素5g／L,胰蛋白胨0．5g／L,K2HPO4·3H2O 0．3g／L,MgSO4·7H2O 0.15g／L,pH5.5,摇床转速160r／min,30℃发酵56h。在此优化条件下培养,8B产纤溶酶活力达到345．41U／mL,是初始培养基发酵产酶活力的7．52倍。     

一株芽孢杆菌在维生素C二步发酵中对小菌的促进作用

从土壤中分离到1株能更好促使小菌生长和产酸的芽孢杆菌B601,作为伴生菌与巨大芽孢杆菌相比,在生长过程中,发酵液中B601活菌数小于巨大芽孢杆菌,而其芽孢数则多于巨大芽孢杆菌。对B601组成菌系的发酵条件进行优化,得到如下结果：100g／L L-山梨糖、6g／L尿素、10g/L玉米浆、培养温度30℃和发酵周期44h。与巨大芽孢杆菌组成菌系相比其底物,L-山梨糖质量浓度提高了25％,尿素下降了50％．玉米浆质量浓度下降了33％,温度提高了2℃,发酵周期缩短了4h。结果表明：B601作为伴生菌,与巨大芽孢杆菌相比,该菌株明显提高了发酵效率。     

根瘤菌4012a菌株产细胞分裂素发酵条件的研究

用酶标免疫检测法研究了根瘤菌4012a菌株细胞分裂素发酵的适宜培养基和培养条件。结果表明,其最佳培养基为（g／L）：葡萄糖10.0,（NH4）2SO41.0,K2HPO4·3H2O0．6,MgSO4·7H2O0.1,CaCl2·2H2O0.4,FeCI3·6H2O0．04,Na2MoO4·2H2O0．1mg／L,泛酸钙100μg／L,腺漂吟200mg／L。该菌株在150r／min的旋转摇床上27℃振荡培养96h,发酵液中细胞分裂素产量可达908μg／L,生物活性（萝卜子叶扩大法）为1mg／L激动素当量。     

益生菌Lactobacillus casei Zhang固态发酵条件的优化

利用一株分离自传统发酵酸马奶中的益生干酪乳杆菌（Lactobacillus casei Zhang）进行固态发酵（Solid State Fermentation,SSF）。以发酵物中的活菌数为主要指标,采用九因素四水平（L32（4^9））的正交试验优化固态发酵培养基,并在优化的培养基基础上研究不同的初始含水量及培养时间对Lactobacillus casei Zhang活菌数的影响。实验结果表明,在固态发酵培养基组成为4g豆粕、5g麸皮、0．6g乳清粉、0．3g葡萄糖、0．3g碳酸钙、0．02g硫酸铵、0．01g硫酸镁,初始含水量为55％的优化条件下,37℃发酵60h,发酵物中Lactobacillus casei Zhang活菌数可达到4．08×10^10CFU／g。     

猪源屎肠球菌WEI-9的高密度培养

目的对分离自健康仔猪肠道的屎肠球菌(Enterococcus faecium)WEI-9的高密度发酵培养基进行响应面优化,为菌株WEI-9的工业化生产奠定基础。方法首先采用单因素试验确定最适高密度发酵培养基的碳源和氮源,随后采用Plackett-Burman设计筛选出影响菌株WEI-9发酵活菌数的显著因素,利用最陡爬坡试验得出显著因素逼近最大活菌数产量的响应区域,最后应用Box-Behnken设计和响应面分析法确定显著影响因子的最佳浓度。结果优化后的最适高密度发酵培养基成分和配比为:乳清粉21.34 g/L,蛋白胨21.94 g/L,Na AC·3H2O 5 g/L,柠檬酸铵2 g/L,K2HPO4·3H2O 2 g/L,Mg SO4·7H2O 0.2 g/L,Mn SO4·H2O 0.05 g/L,吐温-80 1 g/L,发酵液最高活菌数达到1.6×109CFU/m L,是相同条件下MRS培养基中活菌数的1.98倍。结论本研究实现了猪源屎肠球菌(Enterococcus faecium)WEI-9的高密度培养。     

Optimization of fermentation conditions for isoeugenol monooxygenase from Bacillus fusiformis CGMCC1347

对从土壤中筛选获得的纺锤芽孢杆菌CGMCC1347生产异丁香酚单加氧酶的发酵条件进行了单因素考察及正交实验优化,确定了最适的发酵摇瓶培养基组成和培养条件.在发酵培养基组成为尿素1 g/L,玉米浆55 g/L,K2HPO4 2g/L,MgSO4·7H2O 1 g/L,初始pH 7.5,发酵温度37℃,摇床转速180 r/min的条件下培养16h获得的细胞,能转化2％的异丁香酚生成2.49 g/L香兰素,异丁香酚单加氧酶酶活达3.79 U/L.     

红曲菌利用生物柴油废液生产红曲色素

对生物柴油废液作简单处理,利用红曲茵发酵生物柴油废液中副产物甘油生产红曲色素。通过响应面方法确定最佳发酵培养基为：甘油48．49g/L,蛋白胨3．12g／L,K2HPO4·3H202．01g/L,MgSO4 0．48g／L,ZnSO4·7H2O 0．04g／L,MnSO4·H2O 0．03g／L,玉米浆13mL／L,植物油10mL／L,起始pH为6。发酵结果表明：在接种量6％（v／v）,转速140r／min,35℃的条件下发酵培养6d,红曲色素最高产量到达204U／mL。说明用生物柴油废液中的粗甘油为原料生产红曲色素是基本可行的。可望为生物柴油废液的资源化提供一条环境友好型的途径。     

羊源丁酸梭菌HDRyYB1发酵工艺的优化

【目的】目前,国内外鲜有关于羊源丁酸梭菌的报道。本课题选用羊源丁酸梭菌HDRy YB1为研究对象,对其发酵工艺进行优化,为该菌株作为饲料添加剂应用于畜牧业生产奠定基础。【方法】采用Plackett-Burman(PB)试验设计法和响应面法分析并优化显著影响HDRy YB1菌株发酵液中芽胞数的培养基成分。【结果】发酵培养基中的面粉浓度、鱼粉浓度和米粉浓度显著影响发酵液中的芽胞数,优化后的发酵培养基组分(质量体积比)为:面粉3.72%、鱼粉0.90%、米粉3.96%、酵母粉0.60%、Na Cl 0.19%、Mg SO4·7H2O 0.19%、KH2PO4 0.01%、Na HCO3 0.01%、Ca CO3 0.48%;培养参数为:37°C,初始p H为7.2-7.4,瓶装量100/250,接种量3%。在此条件下,HDRy YB1菌株发酵完全(18 h)的芽胞数为1.478×108 CFU/m L,是优化前的2.7倍。【结论】HDRy YB1菌株发酵培养基得到了优化,优化后的培养基可用于后期的扩大发酵试验,验证其在实践生产中的应用价值。     

一株维氏气单胞菌发酵培养基优化及其制备疫苗免疫效力比较

采用单因素试验、响应面试验法对维氏气单胞菌（Aeromonas veronii）发酵培养基的氮源、碳源、无机盐和磷酸盐成分及用量进行优化组合,确定优化培养基组成：胰蛋白胨10.8 g/L,葡萄糖5.0 g/L,牛肉膏3.0 g/L,磷酸二氢钾2.0 g/L,硫酸镁0.4 g/L,NaCl 5.0 g/L。并与基础培养基的发酵活菌数、制备的灭活疫苗免疫效力进行比较,经过验证试验绘制维氏气单胞菌在优化培养基条件下的7 L发酵罐生长曲线。在优化发酵培养基条件下,维氏气单胞菌活菌数为5.94×10⁹ cfu/mL,比基础培养基增幅43.13%;制备的灭活疫苗相对保护率为77.78%,比基础培养基提高了14.81%。7 L发酵罐发酵培养10 h,活菌数达到最大8.85×10⁹ cfu/mL。通过对发酵培养基的优化,可以获得低成本、优质高效的维氏气单胞菌发酵菌液,为今后维氏气单胞菌灭活疫苗规模化发酵培养提供参考。     

Response surface methodology for optimizing the fermentation medium of Clostridium butyricum

AIMS: Strains of Clostridium butyricum have been increasingly used as probiotics for both animals and humans. The aim of this study was to develop a growth medium for cultivating C. butyricum ZJUCB using a statistical methodology. METHODS AND RESULTS: Response surface methodology (RSM) was used to evaluate the effects of variables, namely the concentrations of the glucose, pectin, soyabean cake extract, casein, corn steep flour, ammonium sulphate, sodium bicarbonate and the medium initial pH. A fractional factorial design was applied to study the main factors that affected the growth of a probiotic strain of C. butyricum currently preserved in our lab and the central composite experimental design was adopted to derive a statistical model for optimizing the composition of the fermentation medium. The experimental results showed that the optimum fermentation medium for the growth of C. butyricum was composed of 2% glucose (w/v), 0.5% pectin (w/v), 0.2% casein (w/v), 3.98% soyabean cake extract, 0.1% (NH4)2SO4 (w/v), 0.124% NaHCO3 (w/v), 0.37% corn steep flour (w/v), 0.02% MnSO4 H2O (w/v), 0.02% MgSO4 7H2O (w/v) and 0.002% CaCl2 (w/v) at pH 7.5. CONCLUSIONS: After incubating 24 h in the optimum fermentation medium, the populations of the viable organisms were estimated to be 10(9) CFU ml(-1). In the present study, we report the optimization of a growth medium that produced increased yields using statistical approach. SIGNIFICANCE AND IMPACT OF THE STUDY: The use of bacteria as a probiotic is showing increasing potential. The development of a growth medium that has a high yield is an obvious need, and the approach to optimizing a growth medium is innovative.     

甘蔗渣和糖蜜混合发酵制备燃料丁醇

以抗逆突变株Clostridium beijerinckii IB4为研究对象,葡萄糖为C源,对其进行补料分批发酵过程的优化,同时将该优化工艺应用于甘蔗渣和糖蜜混合发酵制备燃料丁醇。结果表明:在5 L发酵罐中,先加入作为还原糖的甘蔗渣酸解糖液10 g/L,16 h后补加甘蔗糖蜜30 g/L,于35℃、100 r/min发酵50 h,丁醇和总溶剂产量分别达到11.1和15.3 g/L,丁醇比例高达72.5%。     

优化益生菌Lactobacillus casei Zhang高密度培养条件

为实现L. casei Zhang的高密度培养,在之前优化增殖培养基的基础上进一步寻求适宜该菌的培养条件。研究了不同中和剂、缓冲盐浓度、葡萄糖浓度、pH值控制、通气条件和补料分批培养对菌体在恒pH条件下发酵的影响,根据不同条件下菌体的比生长速率、菌体密度和活菌数情况,确定L. casei Zhang较适宜的高密度培养条件为：培养基葡萄糖浓度为80 g/L~100 g/L,以氨水为中和剂使pH保持5.9,采用间歇通氮气的方法保持环境厌氧,分批培养方式下37°C保温发酵10 h~12 h后,L. casei Zhang细胞干重达到7 g/L,活菌数3.5×1010 CFU/mL,比优化前提高7倍以上,能够满足益生菌制品生产要求的高菌体密度。     

Dark hydrogen fermentation from hydrolyzed starch treated with recombinant amylase originating from Caldimonas taiwanensis On1

Starch is one of the most abundant resources on earth and is suited to serve as a cost-effective feedstock for biological hydrogen production. However, producing hydrogen from direct fermentation of starch is usually inefficient, as the starch hydrolysis is often the rate-limiting step. Therefore, in the present work, enzymatic starch hydrolysis was conducted to enhance the feasibility of using starch feedstock for H2 production. The amylase (with a molecular weight of ca. 112 kDa) used for starch hydrolysis was produced from a recombinant E. coli harboring an amylase gene originating from Caldimonas taiwanensis On1. Using statistical experimental design, the optimal pH and temperature for starch hydrolysis with the recombinant amylase was pH 6.86 and 52.4 degrees C, respectively, at an initial starch concentration of 7 g/L. The hydrolyzed products contained mainly glucose, maltotriose, and maltotetrose, while a tiny amount of maltose was also detected. The enzymatically hydrolyzed products of soluble starch and cassava starch were used as the substrate for dark hydrogen fermentation using Clostridium butyricum CGS2 and Clostridium pasteurianum CH4. The highest H2 production rate (vH2) and yield (YH2) of C. butyricum CGS2 was 124.0 mL/h/L and 6.32 mmol H2/g COD, respectively, both obtained with the hydrolysate of cassava starch. The best H2 production rate (63.0 mL/h/L) of C. pasteurianum CH4 occurred when using hydrolyzed cassava starch as the substrate, whereas the highest yield (9.95 mmol H2/g COD) was obtained with the hydrolyzed soluble starch.     

一株拜氏梭菌利用甘蔗废糖蜜发酵生产丙酮丁醇

以甘蔗废糖蜜作为原料,利用Clostridium beijerinckii DSM 6422菌株进行丙酮丁醇发酵的初步研究.结果表明:采用H2SO4预处理糖蜜,初糖质量浓度60 g/L,(NH4)2SO4 2g/L,CaCO3 10 g/L,温度30℃,pH 5.5～7.0,接种量6％(体积分数),在5L发酵罐中发酵培养96 h,总溶剂产量为16.17 g/L,其中丁醇质量浓度为10.07 g/L,总溶剂产率为30.2％,糖利用率为89.3％.     

以糙米为原料流加L-蛋氨酸的S-腺苷蛋氨酸发酵优化

研究了S-腺苷甲硫氨酸(SAM)高产菌啤酒酵母S-W55的廉价培养基及分批补料发酵过程优化.对啤酒酵母S-W55生长和SAM产量影响最为重要的糙米水解糖和酵母粉进行了响应面优化,得到了最优化的配方为糙米水解糖51.4g/L、酵母粉4.74g/L,此条件下啤酒酵母S-W55的SAM产量达2.61 g/L.不同分批补料发酵...     

铁改性沸石对Clostridium acetobutylicum XY16固定效率及发酵性能的影响

考察4种无机铁盐改性沸石对丁醇生产菌Clostridium acetobutylicum XY16的固定效率及其发酵产丁醇性能的影响。结果表明:铁改性沸石对菌体的固定效率均优于未改性沸石,而Fe3+改性效果优于Fe2+,经FeCl3改性的沸石对菌体具有良好的吸附作用,当Fe3+-zeolite用量为180 g/L时,细胞的固定效率达到87%。在此基础上,比较了沸石负载的铁离子量对丁醇发酵性能的影响,沸石负载的铁离子量为6.0 mg/g时可显著提高丁醇发酵性能,当葡萄糖质量浓度为60 g/L时进行发酵,丁醇产量为13.5 g/L,总溶剂可达20 g/L,总溶剂的生产速率为0.385g/(L.h),比游离细胞发酵分别提高了9.5%、10.3%和40%。     

丙酮丁醇梭菌发酵菊芋汁生产丁醇

对丙酮丁醇梭菌Clostridium acetobutylicum L7发酵菊芋汁酸水解液生产丁醇进行了初步研究。实验结果表明,以该水解液为底物生产丁醇,不需要添加氮源和生长因子。当水解液初始糖浓度为48.36 g/L时,其发酵性能与以果糖为碳源的对照组基本相同,发酵终点丁醇浓度为8.67 g/L,丁醇、丙酮和乙醇的比例为0.58∶0.36∶0.06,但与以葡萄糖为碳源的对照组相比,发酵时间明显延长,表明该菌株葡萄糖转运能力强于果糖。当水解液初始糖浓度提高到62.87 g/L时,发酵终点残糖浓度从3.09 g/L增加到3.26 g/L,但丁醇浓度却提高到11.21 g/L,丁醇、丙酮和乙醇的比例相应为0.64∶0.29∶0.05,表明适量糖过剩有助于C.acetobutylicum L7胞内代谢从丙酮合成向丁醇合成途径调节;继续提高水解液初始糖浓度,发酵终点残糖浓度迅速升高,丁醇生产的技术经济指标受到明显影响。