响应面分析优化产木聚糖酶毕赤酵母基因工程菌培养条件

研究不同碳源、氮源和无机盐对毕赤酵母AX181菌株产木聚糖酶的影响。实验表明,分别采用葡萄糖和玉米浆干粉为碳源和氮源可以明显提高木聚糖酶的产量。无机盐单因子优化实验显示添加适量的（NH4）2SO4、KH2PO4、MnSO4·H2O、FeSO4·7H2O也可以部分提高木聚糖酶产量。在此基础上利用响应面法优化毕赤酵母产木聚糖酶培养基,利用12次实验的Plackett—Burman设计实验筛选出影响产木聚糖酶的3个主要因素,即玉米浆干粉、MnSO4·H2O和FeSO4·7H20。并进一步通过最陡爬坡路径逼近最大响应区域,采用中心组合实验设计确定最佳条件。优化后的产木聚糖酶培养基组分为（g/L）：葡萄糖40．00,玉米浆干粉80．84,（NH4）2SO46．25,KH2PO41．25、MnSO4·H2O0．35,FeS04-7H2O1．31。培养基优化后,实际产酶2883．86u／mL,是优化前YPD培养基产酶的2．51倍。     

戴尔根霉发酵麸皮酶解液制备富马酸的研究

拟通过根霉菌发酵小麦麸皮纤维质实现其高效生物转化制备富马酸的目标。在单因素试验研究基础上,对发酵工艺进行响应曲面法优化,并开展代谢机理初步探索。通过单因素试验确定了酵母浸粉、硫酸镁及硫酸锰质量浓度为主要影响因素,响应曲面研究结果显示:当发酵水解液总糖浓度80.0g/L、硫酸铵2.00g/L、酵母浸粉0.29g/L、硫酸镁0.26g/L、硫酸锰0.07g/L、硫酸亚铁0.05g/L时,富马酸产量最高,其值为27.423g/L。对戴尔根霉Rhizopus delemar CICC41341的木糖代谢途径的初步分析结果表明木酮糖激酶为该菌株木糖代谢的关键限速酶。论文研究结果可为纤维质糖液工业发酵制备平台有机酸提供一定支持。     

嗜中高温嗜酸古菌Ferroplasma thermophilum的培养条件优化

在中高温和较低pH条件下, Ferrroplasma spp. 是进行硫化矿生物浸出的重要微生物。Ferroplasma spp.为古菌,无细胞壁, 对矿浆浓度、搅拌剪切力以及溶液中的重金属离子等敏感, 很难得到高密度的纯培养, 给大规模的工业应用带来了一定难度。研究了F. thermophilum摇瓶培养时的最佳生长条件, 单因素考察结果表明最适培条件为: 温度50oC, 初始pH 0.5, 250 mL的摇瓶装液量为50 mL, 无机氮源(NH4)2SO4。通过正交试验确定了FeSO4·7H2O、酵母粉和蛋白胨最适组合为FeSO4·7H2O 40 g/L, 酵母粉0.3 g/L, 蛋白胨0.2 g/L。优化培养后, F. thermophilum 浓度达到了6.3×107个/mL, 40 g/L的FeSO4·7H2O在72 h内全部氧化完全。该结果可为该类古菌的扩大培养以及工业应用提供参考。     

嗜中高温嗜酸古菌Ferroplasma thermophilum的培养条件优化

在中高温和较低pH条件下, Ferrroplasma spp. 是进行硫化矿生物浸出的重要微生物。Ferroplasma spp.为古菌,无细胞壁, 对矿浆浓度、搅拌剪切力以及溶液中的重金属离子等敏感, 很难得到高密度的纯培养, 给大规模的工业应用带来了一定难度。研究了F. thermophilum摇瓶培养时的最佳生长条件, 单因素考察结果表明最适培条件为: 温度50oC, 初始pH 0.5, 250 mL的摇瓶装液量为50 mL, 无机氮源(NH4)2SO4。通过正交试验确定了FeSO4·7H2O、酵母粉和蛋白胨最适组合为FeSO4·7H2O 40 g/L, 酵母粉0.3 g/L, 蛋白胨0.2 g/L。优化培养后, F. thermophilum 浓度达到了6.3×107个/mL, 40 g/L的FeSO4·7H2O在72 h内全部氧化完全。该结果可为该类古菌的扩大培养以及工业应用提供参考。     

阿拉伯胶酶产生菌株的筛选及其发酵培养基的优化

从土壤中筛选产阿拉伯胶酶的微生物菌株,并通过紫外诱变选育后得到高产突变菌株ZHB05F,依据菌落和孢子形态特征初步鉴定为镰刀茵(Fusarium sp.).通过单因素试验,优化了产酶培养基的主要组分的浓度和pH值,得到最佳的产酶发酵培养基组成为:阿拉伯胶30 g/L,(NH4)2SO4 8 g/L,K2HPO4 1g/...     

休哈塔假丝酵母HDYXHT-01利用木糖生产乙醇的发酵工艺优化

采用Plackett-Burman (PB) 方法和中心组合设计 (Ccentral composit design,CCD) 对休哈塔假丝酵母Candida shehataeHDYXHT-01利用木糖发酵生产乙醇的工艺进行优化。PB试验设计与分析结果表明：硫酸铵、磷酸二氢钾、酵母粉和接种量是影响木糖乙醇发酵的4个关键因素,以乙醇产量为响应目标,采用CCD和响应面分析法 (Response surface methodology,RSM),确定了木糖乙醇发酵的最佳工艺为：硫酸铵1.73 g/L、磷酸二氢钾3.56 g/L、酵母粉2.62 g/L和接种量5.66％,其他发酵条件为：木糖80 g/L,MgSO4·7H2O 0.1 g/L,pH 5.0,培养温度30 ℃,装液量100 mL/250 mL,摇床转速140 r/min,发酵时间48 h,在该条件下发酵液中乙醇产量可以达到26.18 g/L,比未优化前提高了1.15倍。     

Antibacterial and Anticancer activity of ε -poly-L-lysine (ε -PL) produced by a marine Bacillus subtilis sp

A marine Bacillus subtilis SDNS was isolated from sea water in Alexandria and identified using 16S rDNA sequence analysis. The bacterium produced a compound active against a number of gram negativeve bacteria. Moreover, the anticancer activity of this bacterium was tested against three different human cell lines (Hela S3, HepG2 and CaCo). The highest inhibition activity was recorded against Hela S3 cell line (77.2%), while almost no activity was recorded towards CaCo cell line. HPLC and TLC analyses supported evidence that Bacillus subtilis SDNS product is ?;-poly-L-lysine. To achieve maximum production, Plackett-Burman experimental design was applied. A 1.5 fold increase was observed when Bacillus subtilis SDNS was grown in optimized medium composed of g/l: (NH(4) )(2) SO(4) , 15; K(2) HPO(4) , 0.3; KH(2) PO(4) , 2; MgSO(4) · 7 H(2) O, 1; ZnSO(4) · 7 H(2) O, 0; FeSO(4) · 7 H(2) O, 0.03; glucose, 25; yeast extract, 1, pH 6.8. Under optimized culture condition, a product value of 76.3 mg/l could be obtained. According to available literature, this is the first announcement for the production of ?;-poly-L-lysine (?;-PL) by a member of genus Bacillus. (? 2012 WILEY-VCH Verlag GmbH & Co. KGaA, Weinheim).     

4-丁内酰胺水解酶法制备γ-氨基丁酸

以吡咯烷酮为唯一碳源,从采集的土样中分离、筛选得到具有4-丁内酰胺水解酶活性的菌株.采用响应面分析法对该菌株的产酶培养基组分进行了优化研究并对酶促转化反应条件也进行了研究.结果表明:编号为HHSW-16的菌株水解活性最高.优化后的培养基组成为:葡萄糖11.50 g·L-1,牛肉膏6.35 g·L-1,酵母粉5.58 g...     

Bioconversion of glycerol to 1,3-propanediol in thin stillage-based media by engineered Lactobacillus panis PM1

Thin stillage (TS) is a waste residue that remains after bioethanol production, and its disposal reflects the high costs of bioethanol production. Thus, the development of cost-effective ways to process TS is a pending issue in bioethanol plants. The aim of this study was to evaluate the utilization of TS for the production of the valuable chemical, 1,3-propanediol (1,3-PDO), by Lactobacillus panis PM1. Different fermentation parameters, including temperature, pH and strains [wild-type and a recombinant strain expressing a NADPH-dependent aldehyde reductase (YqhD) gene] were tested in batch and fed-batch cultivations. The highest 1,3-PDO concentration (12.85 g/L) and yield (0.84 g/g) were achieved by batch fermentation at pH-4.5/30 °C by the YqhD recombinant strain. Furthermore, pH-controlled batch fermentation reduced the total fermentation period, resulting in the maximal 1,3-PDO concentration of 16.23 g/L and yield of 0.72 g/g in TS without an expensive nutrient or nitrogen (e.g., yeast extract, beef extract, and peptone) supplementation. The addition of two trace elements, Mg²⁺ and Mn²⁺, in TS increased 1,3-PDO yield (0.74 g/g) without 3-hydroxypropionaldehyde production, the only intermediate of 1,3-PDO biosynthetic pathway in L. panis PM1. Our results suggest that L. panis PM1 can offer a cost-effective process that utilizes the TS to produce a value-added chemical, 1,3-PDO.     

产脂肪酶菌株C7828-5的筛选、鉴定以及产酶条件的优化

以花生油为唯一碳源,从海口市各地被油脂污染土样中分离筛选出1株中温碱性脂肪酶菌株C7828-5。形态学、生理生化特征和分子生物学鉴定结果表明,该菌株为铜绿假单胞菌(Pseudomonas aeruginosa)。该菌所产脂肪酶的最适温度为37℃,最适pH为8.0。优化了菌株的产酶条件,最适产酶培养基(g/L)为:蔗糖5、牛肉膏20、(NH_4)_2SO_41、MgSO_4·7H_2O 0.5、CaCl_20.5,聚乙烯醇花生油乳化液120 mL,发酵72 h,获得高达8.08 U/mL的脂肪酶表达量。     

底物种类和浓度对污泥重金属生物淋滤效果的影响

以生污泥为材料,研究单质硫(浓度分别为5、10、20 g/L)、FeSO4?7H2O (浓度分别为10、20 g/L）和硫代硫酸钠（浓度分别为10、20 g/L）三种底物的不同浓度对污泥中Zn、Cu、Pb、Cd、Cr和Ni六种重金属生物淋滤效果的影响。结果表明：单质硫的致酸性最好,第4天pH值就达到2.0左右,Zn、Cu、Pb、Cr和Ni的滤出量最大（原污泥Cd未检出）,并以底物投放浓度在10～20 g/L为佳。FeSO4?7H2O的致酸性和重金属滤出量较单质硫弱。硫代硫酸钠在浓度10 g/L时,致酸性和重金属的滤出量介于单质硫和FeSO4?7H2O之间,但浓度20 g/L时滤液呈碱性,重金属难于滤出甚至不滤出。     

圆红冬孢酵母菌发酵产油脂培养基及发酵条件的优化研究

采用均匀设计和单因子试验法,系统考察了圆红冬孢酵母菌(Rhodosporidiumtoruloides)在不同碳氮比条件下产油发酵情况以及添加无机盐对产油发酵的影响,通过均匀设计软件对二次多项回归方程求解及单因素分析得知在培养基组成分别为葡萄糖70g/L,硫酸铵0.1g/L,酵母粉0.75g/L,磷酸二氢钾0.4g/L,七水硫酸镁1.5g/L,初始pH6.0,在灭菌(121℃15min)后添加ZnSO41.91×10-6mmol/L、CaCl21.50mmol/L、MnCl21.22×10-4mmol/L、CuSO41.00×10-4mmol/L。发酵摇瓶装液量为250mL三角瓶装培养基50mL,接种量为10%(种龄28h)。在上述条件下,30℃振荡(200r/min)培养120h,所得菌体油脂含量高达76.1%,脂肪得率系数可达22.7。     

Butanol production from thin stillage using Clostridium pasteurianum

The production of butanol from thin stillage by Clostridium pasteurianum DSM 525 was evaluated in the paper. At initial pH values ranging from 5.0 to 7.0 C. pasteurianum DSM 525 produced 6.2-7.2 g/L of butanol utilizing glycerol in thin stillage as the main carbon source, with yields of 0.32-0.44 g butanol produced/g glycerol consumed, which are higher than previously reported yields (e.g., 0.14-0.31 g butanol/g glycerol, Biebl, 2001). Lactic acid in the thin stillage acted as a buffering agent, maintaining the pH of the medium within a range of 5.7-6.1. Lactic acid was also utilized along with glycerol, enhancing butanol production (6.5 g/L butanol vs. 8.7 g/L butanol with 0 and 16 g/L lactic acid, respectively). These results demonstrate the feasibility of cost-effective butanol production using thin stillage as a nutrient-containing medium with a pH buffering capacity.     

翅鳞伞深层发酵胞外多糖优化研究

采用PlackettBurman设计(PlackettBurman Design, PB)对影响翅鳞伞［ Pholiota squarrosa (Pers. Ex Fr.) Quel.］ AS 5245菌株发酵产糖的内在和外在相关因素进行了筛选,所选取的20个相关因素为葡萄糖、果糖、麦芽糖、酵母膏、胰蛋白胨、KH₂PO₄、K₂HPO₄、(NH₄)₂SO₄、NaNO₃、FeSO₄、MgSO₄、MnCl₂、ZnCl₂、FeCl₃、CuSO₄·5H₂O、维生素B1、起始pH、发酵温度、时间和装液量。在此基础上,再采用响应曲面法(Response Surface Methodology,RSM)对影响发酵产糖的内在关键影响因素酵母膏、果糖、MgSO₄、麦芽糖、ZnCl₂和发酵基质起始pH值的最佳水平范围作了进一步的研究与探讨,通过对二次多项回归方程求解得知,在上述自变量分别为6.0g/L、11.5g/L、0.5g/L、9.6g/L、38.6mg/L和5.3时,胞外多糖最大预测值为876.32μg/mL发酵醪,此预测可信度不仅被统计分析所验证,也实践所证实。     

产腈水解酶基因工程菌的产酶诱导条件及培养基优化

本文通过对产酶诱导条件及发酵培养基进行优化,成功提高了产腈水解酶基因工程菌E. coli BL21(DE3)-pETNYNit的产酶水平。研究结果显示,最佳发酵培养基为：葡萄糖0.2%、甘油0.7%(v/v)、蛋白胨1.2%、酵母膏0.8%、NaCl 0.3%、(NH4)2SO40.3%、NH4Cl 0.13%、Na2 HPO4·12H2 O 1.04%、KH2 PO40.39%、MgSO4·7H2 O 0.03%,pH 7.2。最佳产酶诱导条件为：发酵4 h时加入0.5 mmol/L IPTG,然后在28℃、240 r/min下诱导腈水解酶基因表达14 h~16 h。采用优化方案,重组菌产酶水平可提升至0.9~1×105 U,与野生菌株的产酶水平相比,提高幅度超过50%。同时重组菌培养仅需24 h,培养周期缩短超过50 h。     

响应面法优化普鲁兰多糖发酵培养基

以出芽短梗霉IFO 4464为实验菌种,采用响应面法(RSM)优化了出芽短梗霉IFO 4464产普鲁兰多糖的发酵培养基。通过实验得到出芽短梗霉最佳发酵培养基为蔗糖59.8g/L,硫酸铵0.7 g/L,硫酸镁0.3 g/L,磷酸二氢钾5.0g/L,氯化钾0.5g/L,氯化钠1.5g/L,酵母浸膏2.5 g/L,多糖产量可达21.92 g/L。     

A NEWLY ANTI-Streptococcus suis BACTERIOCIN PRODUCING STRAIN FROM UNWEANED PIGLETS FECAL MATTER: ISOLATION, PRELIMINARY IDENTIFICATION, AND OPTIMIZATION OF MEDIUM COMPOSITION FOR ENHANCED BACTERIOCIN PRODUCTION

A newly isolated anti-Streptococcus suis bacteriocin-producing strain LPL1-5 was obtained from healthy unweaned piglets' fecal matter, and was designated as Lactobacillus pentosus LPL1-5 based on morphology, biochemical properties, and 16S rDNA sequencing analysis. The medium composition for enhanced bacteriocin production by L. pentosus LPL1-5 was optimized by statistical methodology. Yeast extract, K(2)HPO(4)?·?3H(2)O, and MnSO(4)?·?H(2)O were identified as significant components influencing pentocin LPL1-5 production using the Plackett-Burman method. Response surface methodology was applied for further optimization. The concentrations of medium components for enhanced pentocin LPL1-5 production were as follows (g/L): lactose 20.00, tryptone 10.00, beef extract 10.00, yeast extract 14.00, MnSO(4)?·?H(2)O 0.84, K(2)HPO(4)?·?3H(2)O 4.92, triammonium citrate 2.00, Na-acetate 5.00, MgSO(4)?·?7H(2)O 0.58, Tween 80 1.00. Under the optimized condition, a value of 3154.65?±?27.93 IU/mL bacteriocin activity was achieved, which was 4.2-fold that of the original medium.     

沼泽生红冬孢酵母生长及产类胡萝卜素培养条件的研究

通过单因素实验和正交实验对沼泽生红冬孢酵母生长和产类胡萝卜素的培养条件进行研究,最适培养条件为葡萄糖40 g/L,牛肉膏10 g/L,酵母膏10 g/L,NaCl 10 g/L,MgSO4.7H2O 0.1 g/L,K2HPO4 2 g/L,KH2PO4 2 g/L,初始pH 6.3,装液量为50 mL/250 mL,摇床转速170 r/min,培养温度为28℃,接种量为10%。在此发酵条件下,培养72 h后,沼泽生红冬孢酵母生物量和类胡萝卜素产量分别达到11.72 g/L和3.55 mg/L。     

Medium optimization of antifungal activity production by Bacillus amyloliquefaciens using statistical experimental design

In order to overproduce biofungicides agents by Bacillus amyloliquefaciens BLB371, a suitable culture medium was optimized using response surface methodology. Plackett-Burman design and central composite design were employed for experimental design and analysis of the results. Peptone, sucrose, and yeast extract were found to significantly influence antifungal activity production and their optimal concentrations were, respectively, 20 g/L, 25 g/L, and 4.5 g/L. The corresponding biofungicide production was 250 AU/mL, corresponding to 56% improvement in antifungal components production over a previously used medium (160 AU/mL). Moreover, our results indicated that a deficiency of the minerals CuSO(4), FeCl(3) · 6H(2)O, Na(2)MoO(4), KI, ZnSO(4) · 7H(2)O, H(3)BO(3), and C(6)H(8)O(7) in the optimized culture medium was not crucial for biofungicides production by Bacillus amyloliquefaciens BLB371, which is interesting from a practical point of view, particularly for low-cost production and use of the biofungicide for the control of agricultural fungal pests.     

Optimization of bio-hydrogen production from biodiesel wastes by Klebsiella pneumoniae

Biodiesel wastes containing glycerol were utilized by Klebsiella pneumoniae DSM 2026 to produce hydrogen. The optimization of medium components was performed using both Plackett-Burman and uniform design methods. Using the Plackett-Burman design, glycerol, yeast extract, NH(4)Cl, KCl and CaCl2 were found to be the most important components, which were further investigated by uniform design and second-order polynomial stepwise regression analysis. The optimized medium containing 20.4 g.L(-1) glycerol, 5.7 g.L(-1) KCl, 13.8 g.L(-1) NH(4)Cl, 1.5 g.L(-1) CaCl(2) and 3.0 g.L(-1) yeast extract resulted in 5.0-fold increased level of hydrogen (57.6 mL/50 mL medium) production compared to initial level (11.6 mL/50 mL medium) after 24 h of fermentation The optimization of fermentation condition (pH, temperature and inoculum) was also conducted. When the strain grew in the optimized medium under optimal fermentation condition in a 5-L stirred tank bioreactor for batch production, hydrogen yield and production reached 0.53 mol/mol and 117.8 mmol/L, respectively. The maximum hydrogen evolution rate was 17.8 mmol/(L.h). Furthermore, 1,3-propanediol (6.7 g.L(-1)) was also obtained from the liquid medium as a by-product.