响应面法优化重组工程菌的发酵工艺条件

目的：对基因改造运动发酵单胞菌的发酵工艺条件进行优化,提高重组菌发酵乙醇产量。方法：使用分子克隆实验操作技术构建重组运动发酵单胞菌,以单因素实验为基础,利用Box-Behnken中心组合实验和响应面分析法,确定了影响重组菌高产乙醇的三个重要因素。结果：成功构建含有YfdZ、MetB基因和Hsp基因的重组菌Zymomonas mobilis HYM,发酵主要影响因素的最佳条件分别为温度28℃,葡萄糖浓度24%（W/V）,pH7.4。在此优化条件下,Zymomonas mobilis HYM的乙醇产量可高达105.0735g/l,比原始菌株乙醇产量提高16.4%。结论：用中心组合设计和响应面分析法优化重组运动发酵单胞菌的发酵工艺条件,显著提高乙醇产量。     

响应面法优化酿酒酵母产油脂条件

运用响应面法对酿酒酵母(Saccharomyces cerevisiae)产油脂以及发酵条件优化进行了研究。首先根据单因素实验结果,利用Plackett-Burman设计对影响其产油脂相关因素进行评估并筛选出具有显著效应的3个因素:柠檬酸,CaCl2和初始pH值。接着用最陡爬坡试验逼近以上3个因子的最大响应区域后,采用Box-Behnken设计以及响应面分析法,确定其优化后发酵条件为(w/v):葡萄糖15%,蛋白胨0.2%,酵母浸粉0.4%,柠檬酸0.471%,MgSO4·7H2O0.1%,ZnSO4·7H2O0.2%,CaCl20.025%,FeSO4·7H2O0.005%,初始pH值为6.74,180r/min,30°C培养96h。优化后的油脂产率(干重)达到14.55%,比在种子培养基中油脂产率4.76%提高了2倍左右。     

产纤维素酶菌株的筛选、鉴定及产酶条件的优化

采集新疆吐鲁番地区土样,从中分离筛选1株产纤维素酶菌株C-8;经形态观察、生理生化及16S rRNA序列分析,初步鉴定为芽孢杆菌属(Bacillus sp.)。该菌株所产纤维素酶的最适合作用pH和温度分别为9.0、40℃,且具有良好的pH稳定性和温度稳定性。为了提高C-8菌株产纤维素酶能力,利用响应面法对其发酵产酶条件进行优化。采用Plackett-Burman设计筛选出影响其产酶条件的3个主效应因素,最陡爬坡试验逼近最大响应值区域,利用Box-Behnken响应面分析法优化发酵产酶条件。结果表明,起始pH、CMC-Na%和培养温度为主要影响因素。通过三因素三水平的响应面分析得到最优条件为起始pH8.0、CMCNa%2.5%、培养温度28℃。在此条件下纤维素酶活可达193.89 U/mL,与优化前相比,酶活提高2.35倍。     

响应面法优化L-谷氨酰胺发酵培养基的研究

目的:采用响应面法对L-谷氨酰胺发酵培养基成分进行优化,以提高L-谷氨酰胺发酵产量。方法:首先利用Plackett-Burman试验设计筛选出影响L-谷氨酰胺产量的主要因素葡萄糖、玉米浆和(NH4)2SO4,在此基础上采用最陡爬坡实验逼近最大响应区域,并利用中心组合设计及响应面分析法进行回归分析。结果:通过求解回归方程得到L-谷氨酰胺发酵培养基最佳浓度为葡萄糖100 g/L、玉米浆4.5 ml/L、(NH4)2SO437.2 g/L,L-谷氨酰胺产量理论最大值达41.0 g/L。结论:经模型验证,预测值与验证试验平均值接近,在优化条件下谷氨酰胺产量提高了37.6%。     

爱尔兰帚霉产低温纤维素酶的酶学性质和发酵工艺

本文旨在对爱尔兰帚霉E71702M菌株产低温纤维素酶的酶学性质进行初步研究,并获得其最优发酵条件,为低温纤维素酶开发利用提供参考。通过单因素试验确定温度、pH及金属离子对纤维素酶活力的影响;以Plackett-Burman试验设计从8个培养条件中筛选出影响产酶的3个主要因素,即麸皮含量、装瓶量和起始pH;运用Box-Behnken试验设计及响应面分析法确定这3个主要因素的最优发酵条件。对酶学性质的初步研究表明,该酶最适pH为3.0,最适反应温度为30℃,在0℃时残余酶活力为最适反应温度时的56.3%。响应面分析得到最优发酵条件为:麸皮含量8.79g/L、装瓶量40.93m L、初始pH 4.01。通过优化,纤维素酶活力由0.6338IU/m L提高到1.7386IU/m L,提高了174%。     

响应面法优化松茸发酵产多糖的培养条件

运用响应面法对松茸产多糖的发酵培养条件进行优化研究。首先根据C、N源实验结果,利用Plackett-Bur-man设计,对影响多糖产量的相关因素进行评估,筛选出具有显著效应的3个因素:玉米粉、豆粕和KH2PO4。在此基础上,利用最陡爬坡试验逼近以上3个因素的最大响应区域,采用Box-Behnken设计法对各因素的水平组合进行优化,获得松茸产多糖优化发酵的培养条件:玉米粉质量分数4.54%,豆粕质量分数4.96%,KH2PO4质量分数0.15%,MgSO4.7H2O质量分数0.05%,VB1质量分数0.001%,初始pH5.5,摇床转速180 r/min,发酵时间10 d。在此优化培养条件下松茸总多糖产量可达5.97 g/L。     

响应面法优化α-蒎烯发酵培养基

利用响应面法对α-蒎烯发酵培养基进行优化。先利用单因素实验法筛选出MD牛肉粉为最有利于发酵产α-蒎烯的N源。此后用Plackett-Burman(P-B)实验方法对相关影响因素效应进行评估,筛选出有显著效应的3个因素:柠檬酸用量、牛肉粉用量以及培养基初始pH。然后用最陡爬坡实验逼近以上3因素最优水平。最后由中心组和实验设计法及响应曲面分析法确定主要因素的最佳条件。在优化后的培养条件下,发现α-蒎烯产量从1.710mg/L提升到7.053 mg/L,发现产量提高了3倍左右。     

响应面法优化灵芪菌质多糖固态发酵条件

采用单因素试验和响应面分析法优化灵芪菌质多糖固态发酵条件.优化后发酵条件为:采用药性固体发酵培养基,初始pH6.5,接种量10.16ml/100g,发酵温度30.65℃,相对湿度59.54％,发酵周期28d.利用此优化条件进行灵芪菌质多糖发酵,灵芪菌质多糖含量可达9.12±0.09mg/g,较优化前8.06±0.07 ...     

响应面法优化海洋微生物发酵产生纤溶化合物的培养条件

采用响应面法对海洋微生物长孢葡萄穗霉菌FG216发酵产生纤溶化合物FGFC1 (Fungi fibrinolyticcompound 1)培养条件进行优化.在单因素试验结果的基础上通过Design-Expert软件对培养时间、诱导物添加量、培养温度进行3因素响应面试验设计,以FGFC1产出量为响应值优化菌株FG216的培养条件,并验证响应面预测值与实测值的一致性.结果表明,在培养时间为9d、诱导物添加量为0.5％、培养温度为28℃的最优培养条件下FGFC1产量可达1 978.33 mg/L,实测值与响应面预测值拟合良好,说明通过响应面试验设计对FG216培养条件的优化是有效的.     

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。     

Efficient lipid production with Trichosporon fermentans and its use for biodiesel preparation

Effects of medium components and culture conditions on biomass and lipid production of Trichosporon fermentans were studied. The optimal nitrogen source, carbon source and C/N molar ratio were peptone, glucose and 163, respectively. The favorable initial pH of the medium and temperature were 6.5 and 25 degrees C. Under the optimized conditions, a biomass of 28.1 g/l and a lipid content of 62.4% could be achieved after culture for 7 days, which were much higher than the original values (19.4 g/l and 50.8%) and the results reported by other groups. T. fermentans could grow well in pretreated waste molasses and a lipid yield of 12.8 g/l could be achieved with waste molasses of 15% total sugar concentration (w/v) at pH 6.0, representing the best result with oleaginous microorganisms on agro-industrial residues. Addition of various sugars to the pretreated molasses could efficiently enhance the accumulation of lipid and the lipid content reached as high as above 50%. Similar to vegetable oils, the lipid mainly contains palmitic acid, stearic acid, oleic acid and linoleic acid and the unsaturated fatty acids amount to about 64% of the total fatty acids. The microbial oil with an acid value of 5.6 mg KOH/g was transesterified to biodiesel by base catalysis after removal of free fatty acids and a high methyl ester yield of 92% was obtained.     

Improving lipid production from bagasse hydrolysate with Trichosporon fermentans by response surface methodology

Oleaginous yeast Trichosporon fermentans was proved to be able to use sulphuric acid-treated sugar cane bagasse hydrolysate as substrate to grow and accumulate lipid. Activated charcoal was shown as effective as the more expensive resin Amberlite XAD-4 for removing the inhibitors from the hydrolysate. To further improve the lipid production, response surface methodology (RSM) was used and a 3-level 4-factor Box-Behnken design was adopted to evaluate the effects of C/N ratio, inoculum concentration, initial pH and fermentation time on the cell growth and lipid accumulation of T. fermentans. Under the optimum conditions (C/N ratio 165, inoculum concentration 11%, initial pH 7.6 and fermentation time 9 days), a lipid concentration of 15.8g/L, which is quite close to the predicted value of 15.6g/L, could be achieved after cultivation of T. fermentans at 25°C on the pretreated bagasse hydrolysate and the corresponding lipid coefficient (lipid yield per mass of sugar, %) was 14.2. These represent a 32.8% improvement in the lipid concentration and a 21.4% increase in the lipid coefficient compared with the original values before optimization (11.9g/L and 11.7). This work further demonstrates that T. fermentans is a promising strain for lipid production and thus biodiesel preparation from abundant and inexpensive lignocellulosic materials.     

发酵性丝孢酵母HWZ004利用水稻秸秆水解液发酵产油脂

为高效利用水稻秸秆中的纤维素和半纤维素产油脂,采用稀酸预处理和酶水解两步法对水稻秸秆进行水解,然后以水解液为碳源,培养发酵性丝孢酵母Trichosporon fermentans HWZ004产微生物油脂。结果表明,经简单overliming法脱毒后水稻秸秆水解液中乙酸、糠醛和5-羟甲基糠醛的浓度分别为0.4 g/L、0.1 g/L和0.05 g/L。只需添加少量氮源和微量CuSO4?5H2O,该水解液即可满足T. fermentans HWZ004发酵产油脂的要求。发酵最适接种量、初始pH和温度分别是5.0％、7.0和25 ℃。T. fermentans HWZ004在优化条件下培养7 d的生物量、油脂含量和油脂产量分别是26.4 g/L,52.2％和13.8 g/L;油脂得率系数为17.0,大大高于驯化前菌株T. fermentans CICC 1368在脱毒水稻秸秆半纤维素水解液中的对应值 (11.9)。所产油脂的脂肪酸组成与植物油相似,不饱和脂肪酸含量达70％以上,宜作为生物柴油的生产原料。     

响应面法优化自养小球藻产生物柴油油脂

利用响应面法对小球藻(Chlorella vulgaris)在2L气升式生物反应器中对自养产生物柴油油脂的培养条件进行了优化。首先用Plackett-Burman方法对10个相关影响因素的效应进行评价并筛选出对产油有显著影响的3个因素:KNO3浓度、温度和CO2浓度;再用最陡爬坡实验逼近最大产油区域;最后由中心组合实验及响应面分析确定了影响产油主要因素的最佳条件为:KNO3浓度0.31g/L,温度26.5℃,CO2浓度6.80%,最高产油量达到0.42g/L,比优化前提高了近2倍。优化后,在10L气升式生物反应器中进行了扩大培养。     

皮状丝孢酵母B3利用木薯淀粉发酵生产微生物油脂

对皮状丝孢酵母B3以木薯淀粉水解液为碳源发酵生产微生物油脂培养条件进行了优化,并在2 L发酵罐中对菌体生长和油脂积累进行了考察。摇瓶实验表明,木薯淀粉水解液的浓度高于90 g/L时不利于菌体的生长和油脂积累,皮状丝孢酵母B3发酵生产微生物油脂的最适氮源及其浓度、最适C/N比和pH分别为酵母提取物3.0 g/L、116、6.0,在此条件下培养144 h菌体生物量、油脂产量和油脂含量分别达到15.2 g/L、6.22 g/L和40.9％;在2 L发酵罐中分批发酵44 h后菌体生物量、油脂产量和油脂含量分别达28.7 g/L、12.27 g/L和42.8％。以皮状丝孢酵母B3所产油脂制备生物柴油,其主要组成包括棕榈酸甲酯、硬脂酸甲酯、油酸甲酯、亚油酸甲酯等,且理化特性符合相关国家标准,可作为一种有潜力的化石燃料替代品。     

双液相体系强化氧传递促进微生物油脂生产

文中通过添加氧载体正十二烷进行双液相发酵来提高发酵性丝孢酵母利用木薯淀粉水解液生产微生物油脂的产量。结果表明,在摇瓶发酵液中添加氧载体,能明显缓解发酵过程中的氧限制程度。在2 L发酵罐中添加1%正十二烷进行双液相高密度发酵,其发酵生物量和油脂产量分别达到101.2 g/L和50.28 g/L。气相色谱分析表明,添加了氧载体发酵的微生物油脂中含有更高的饱和脂肪酸含量。     

利用转座标签mTn-lacZ/leu2插入突变发酵性丝孢酵母2.1368-Leu?筛选高效产油突变株

为提高微生物油脂产率,降低其生产成本,以转座标签mTn-lacZ/leu2插入突变发酵性丝孢酵母2.1368-Leu?筛选高效产油突变株。利用LacZ显色反应、脂肪酸合成酶抑制剂Cerulenin和磷酸香草醛反应,最终在玉米秸秆糖化液中筛选出一株高效产油突变株2.1368-Leu?-7。结果表明其油脂含量为38.30％,比对照的29.33％高了8.97％,而其产油率为8.35％,比对照的6.92％提高了20.63％;在玉米秸秆糖化液中的糖利用率为77％,每100 g玉米秸秆可转化油脂8.32 g。可为未来生物柴油产业提供了廉价原料。     

In vivo detoxification of furfural during lipid production by the oleaginous yeast Trichosporon fermentans

In vivo detoxification of furfural by the oleaginous yeast, Trichosporon fermentans, under lipid-producing (i.e., nitrogen-limited) conditions was evaluated for the first time. During the initial fermentation phase, furfural was rapidly reduced to furfuryl alcohol, which is more toxic to T. fermentans than furfural. Furfuryl alcohol was subsequently oxidized to furoic acid which has low toxicity to T. fermentans and is the end product of the in vivo detoxification of furfural in this organism. These observations explain how T. fermentans can grow and accumulate lipids in medium containing furfural. They also indicate that strategies to minimize the transient production of furfuryl alcohol could further improve the capacity of the strain to produce lipids from furfural-containing lignocellulosic hydrolysates.     

Optimization of alkaline protease production by <Emphasis Type="Italic">Aspergillus clavatus</Emphasis> ES1 in <Emphasis Type="Italic">Mirabilis jalapa</Emphasis> tuber powder using statistical experimental design

Medium composition and culture conditions for the bleaching stable alkaline protease production by Aspergillus clavatus ES1 were optimized. Two statistical methods were used. Plackett-Burman design was applied to find the key ingredients and conditions for the best yield. Response surface methodology (RSM) including full factorial design was used to determine the optimal concentrations and conditions. Results indicated that Mirabilis jalapa tubers powder (MJTP), culture temperature, and initial medium pH had significant effects on the production. Under the proposed optimized conditions, the protease experimental yield (770.66 U/ml) closely matched the yield predicted by the statistical model (749.94 U/ml) with R (2)=0.98. The optimum operating conditions obtained from the RSM were MJTP concentration of 10 g/l, pH 8.0, and temperature of 30 degrees C, Sardinella heads and viscera flour (SHVF) and other salts were used at low level. The medium optimization contributed an about 14.0-fold higher yield than that of the unoptimized medium (starch 5 g/l, yeast extract 2 g/l, temperature 30 degrees C, and pH 6.0; 56 U/ml). More interestingly, the optimization was carried out with the by-product sources, which may result in cost-effective production of alkaline protease by the strain.     

Process optimization for the production of diosgenin with Trichoderma reesei

Based on the response surface methodology, an effective microbial system for diosgenin production from enzymatic pretreated Dioscorea zingiberensis tubers with Trichoderma reesei was studied. The fermentation medium was optimized with central composite design (3⁵) depended on Plackett–Burmann design which identified significant impacts of peptone, K₂HPO₄ and Tween 80 on diosgenin yield. The effects of different fermentation conditions on diosgenin production were also studied. Four parameters, i.e. incubation period, temperature, initial pH and substrate concentration were optimized using 4⁵ central composite design. The highest diosgenin yield of 90.57% was achieved with 2.67% (w/v) of peptone, 0.29% (w/v) of K₂HPO₄, 0.73% (w/v) of Tween 80 and 9.77% (w/v) of substrate, under the condition of pH 5.8, temperature 30 °C. The idealized incubation time was 6.5 days. After optimization, the product yield increased by 33.70% as compared to 67.74 ± 1.54% of diosgenin yield in not optimized condition. Scale-up fermentation was carried out in a 5.0 l bioreactor, maximum diosgenin yield of 90.17 ± 3.12% was obtained at an aeration of 0.80 vvm and an agitation rate of 300 rpm. The proposed microbial system is clean and effective for diosgenin production and thus more environmentally acceptable than the traditional acid hydrolysis.