金针菇产漆酶发酵条件的优化

采用液体摇瓶培养方法,探讨了碳源、氮源、pH值、培养时间等各种因素对金针菇分泌漆酶能力的影响,并采用正交试验对主要的影响因素进行了优化.优化培养条件为:pH在5.0-6.0范围内有利于金针菇漆酶的分泌,且以pH5.5为最佳;以葡萄糖为最佳碳源,尿素为最佳氮源,Cu2+浓度为60μmol/L有利于漆酶的分泌.正交试验表明,葡萄糖20g/L、尿素2g/L、250mL容量瓶中装液量50mL、pH5.5,以邻联甲苯胺作底物,经7d培养,金针菇漆酶酶活达最高峰,峰值酶活为328U/mL.     

一株新型饲料用酶菌株的筛选及发酵条件研究

从土壤中筛选出20余株产中性植酸酶活性的菌株,对一株产中性植酸酶活性较高的绿脓假单胞菌(Phy10)进行了发酵条件优化.该菌株在pH值6.0、温度30℃、装液量100.0mL、接种量7.0mL、碳源为可溶性淀粉和氮源为NaNO2条件下产酶活性最大,优化后酶活可达到231.2U/mL,比未优化前提高了2.16倍.     

产菊粉酶芽孢杆菌发酵条件优化

采用液体摇瓶培养方法,探讨了碳源、氮源、pH值、培养温度等各种因素对巨大芽孢杆菌(Bacillus megaterium)分泌菊粉酶能力的影响.通过正交试验对主要影响因素进行优化,结果表明,最适产酶发酵条件为:菊粉30.0g/L、酵母膏7.0g/L、NaCl 5.0g/L、K2HPO4·3H2O 3.0g/L,初始pH 6.0,250mL发酵三角瓶装液量为50mL,30℃,160r/min振荡培养2d,酶活力达到最高,为2.354U/mL,比优化前提高了1.43倍.     

毛木耳产漆酶发酵条件的研究

以毛木耳为产酶菌，以CMC为唯一碳源，探讨了不同培养条件对毛木耳产漆酶的影响。结果表明，在最适温度为27℃、pH值为6．0、接种量为10％、装液量为90mL／250mL、摇床转速为180rpm、培养天数为6d时，产酶活力最大。以各个因子的最佳梯度做优化培养，发酵液中的漆酶活力高达70．76IU／mL。     

不同碳氮源对双孢蘑菇2796深层发酵的影响

碳源和氮源是食用菌生长发育过程中不可缺少的营养物质.通过单因子试验研究了液体培养中4种碳源和4种氮源对双孢菇菌丝体生物量、胞内多糖、胞外蛋白、酶活性的影响.结果表明,对菌丝生物量而言,可溶性淀粉是最适的碳源,玉米粉是最适的氮源;对产胞外蛋白而言,葡萄糖是最适的碳源,蛋白胨是最适的氮源;对产过氧化物酶、淀粉酶和多酚氧化酶而言,蔗糖是最适的碳源,酵母粉是最适的氮源.该试验为进一步研究双孢蘑菇的营养生理奠定了基础,为生产上选择优良的母种培养基及开发利用双孢蘑菇深层培养生产代谢产物资源提供了科学依据.     

一株纤维素分解菌利用枳实废渣产酶条件的研究

以枳实废渣为碳源,对产纤维素酶G2菌进行固体发酵,通过测定FPA、CMC、C1酶活的大小,对其产酶条件进行优化研究.结果表明产酶最适条件为:枳实在发酵前需进行酸处理;氮源为硫酸铵;含水率为70%;初始pH为5～6;发酵周期为6天.在以上最适条件下,G2菌酶活力为FPA:31.8 IU/ml,CMC:11.86 IU/ml,C1:15.79 IU/ml.     

一株纤维素分解茵利用枳实废渣产酶条件的研究

以枳实废渣为碳源，对产纤维素酶G2茵进行固体发酵，通过测定FPA、CMC、C1酶活的大小，对其产酶条件进行优化研究。结果表明产酶最适条件为：枳实在发酵前需进行酸处理；氮源为硫酸铵；含水率为70％；初始pH为5～6；发酵周期为6天。在以上最适条件下，G2菌酶活力为FPA：31．8IU／ml，CMC：11．86IU／ml，C1：15．79IU／ml。     

青霉菌X5对活性艳蓝KN-R脱色研究

采用梯度平板筛选法，从染布厂废水池污泥中分离到一株对蒽醌染料KN－R有较强脱色能力的青霉菌X5（Penicillium sp.)，并考察该菌在不同温度，pH，培养时间，染料浓度，菌量及不同碳源氮源条件下对活性艳蓝KN－R的脱色情况，结果表明,在20－40℃温度范围内该菌对活性艳蓝KN－R的脱色率均在95％以上，其最佳脱色温度为25℃，pH为4．0，培养时间为48h，染料浓度，菌量对染料脱色有一定影响，该菌对碳源、氮源具有较宽适应范围，在最佳条件下，该菌对染料的脱色率达99．3％。     

无花果曲霉菌丝球对活性艳蓝KN-R的脱色研究

生物吸附法是染料废水处理中很有前途的一种方法。本文将培养的无花果曲霉菌丝球用于蒽醌染料活性艳蓝KN-R的脱色，研究了培养时间、温度、转速、pH值及盐浓度、不同碳源、不同氮源对菌丝球脱色的影响；比较了活菌与死菌的脱色效果；探讨了菌丝球重复利用对脱色率的影响。结果表明：培养时间为72h，温度为33℃，转速为150rpm，pH值为6．0，盐浓度为0.5％，以乳糖为碳源、硝酸钠为氮源时，菌丝球对活性艳蓝KN-R的脱色效果最好：活菌对染料的吸附性能比死菌好；菌丝球在重复利用了四次后，脱色率仍达85．7％。     

高效纤维素分解菌复合系的构建及其环境适应性研究

以纤维素培养基和纤维素刚果红培养基为初筛和复筛培养基，从采集的样品中分离得到具有纤维素分解能力的菌株20株。选择其中具有较高纤维素酶活力的12个菌株与2株自生固氮菌和EM菌进行正交实验，得到3个组合表现出协同降解纤维素的作用，对滤纸降解效果为组合12〉组合8〉组合5。选用组合12进行了一系列的环境适应性研究，结果表明，碳源为微晶纤维素＋CMC-Na时CMC酶活最高，最适氮源为蛋白胨＋酵母膏，最适pH6．5，最适培养温度为30℃。培养第6天CMC酶活最高。     

4株苯磺隆降解菌的分离鉴定及其生长特性

从长期受农药苯磺隆污染的土壤中通过采用富集培养分离技术得到4株以苯磺隆为唯一碳源生长的细菌,分别将其命名为B1、B2、B3和B4。通过观察这4种菌株的形态学特征,研究其生理生化特性以及分析其16S rDNA序列,初步鉴定菌株B1为铜绿假单胞菌（Pseudomonas aeruginosa）,B2为戴尔福特菌（Delftia sp.）,B3为微杆菌（Microbacterium sp.）,B4为产碱杆菌（Alcaligenes sp.）。并通过研究温度、初始pH值、接种量、苯磺隆初始浓度、培养基体积、氮源、碳源、Mg^2＋浓度等因素对4种菌株生长情况的影响,确定了菌株的最佳生长条件。结果显示,B1菌株的最适温度为35℃,其他3株菌株均为30℃。菌株B3最适pH为8.0,其余3株菌株均为pH7.0。B1和B3菌株最适接种量为15%,B2和B4最适接种量为10%。菌株B3最适苯磺隆初始浓度为100mg·L^-1,其余菌株最适苯磺隆初始浓度均为200mg·L^-1。4株菌株最适培养基体积均为75mL,最适氮源均为硝酸铵,最适碳源均为葡萄糖。B2菌株最适Mg^2＋浓度为100mg·L^-1,其余3株菌株均为200mg·L^-1。B1和B4菌株最适NaCl浓度为20g·L^-1,B2菌株NaCl浓度为5-30g·L^-1,B3菌株最适NaCl浓度为50g·L^-1。该结果为利用微生物对农药苯磺隆污染的土壤进行原位生物修复提供理论依据。     

紫贻贝消化腺淀粉酶的提取及部分性质研究

以紫贻贝为原料,从其消化腺中提取淀粉酶,确定其最佳提取条件,并探讨其部分酶学性质。采用缓冲液提取法,通过单因素试验考察提取温度、提取溶剂的pH和提取时间三个因素对紫贻贝消化腺中淀粉酶活性的影响。用平行对照试验来研究该酶的最适催化温度以及各种离子对其活性的影响。结果表明,该酶的最佳提取条件为温度20℃、pH值3.0-4.0、提取时间45min;最适反应温度为35℃,EDTA、Mg2+、Zn2+对该酶有抑制作用,而Ca2+、Mn2+对该酶有促进作用。     

Use of an activated carbon from antibiotic waste for the removal of Hg(II) from aqueous solution

Porous carbon has been prepared from waste antibiotic material by a chemical activation method using K(2)CO(3) as an activating reagent. Carbon was studied systematically by the adsorption of nitrogen and iodine. It was found that the process parameters such as activation temperature and activation time are crucial for preparing high-quality activated carbon. The proper choice of the preparation conditions allows to produce microporous activated carbon with a micropore volume up to 0.492 cm(3)/g and a BET surface area of 1260 m(2)/g. Adsorption of mercury(II) from an aqueous solution on antibiotic carbon was investigated under the varying conditions of agitation time, metal ion concentration and pH. The adsorption capacity of the carbon is 129 mg/g.     

Utilization of anaerobically treated distillery spent wash for production of cellulases under solid-state fermentation

Pollution caused by distillery spent wash on one hand has stimulated the need to develop new technologies to treat the waste and on the other, forced us to reevaluate the efficient utilization of its nutritive potential for production of various high value compounds. In this study, anaerobically treated distillery spent wash was used for the production of cellulases by Aspergillus ellipticus under solid-state fermentation using wheat straw as a substrate. The interactions between distillery effluent concentration, initial pH, moisture content and inoculum size were investigated and modeled using response surface methodology (RSM) involving Box–Behnken design (BBD). Under optimized conditions, filter paper activity, β-glucosidase and endo-β-1,4-glucanase activities were found to be 13.38, 26.68 and 130.92 U/g of substrate respectively. Characterization of endo-β-1,4-glucanase and β-glucosidase was done after partial purification by ammonium sulfate fractionation followed by desalting. The partially purified endo-β-1,4-glucanase and β-glucosidase showed maximum activity at 60 °C. Saccharification studies performed with different lignocellulosic substrates showed that wheat bran was most susceptible to enzymatic hydrolysis. The study suggests that anaerobically treated distillery spent wash can be used as a viable nutrient source for cellulase production under solid-state fermentation by A. ellipticus.     

Magnetic composite prepared from palm shell-based carbon and application for recovery of residual oil from POME

Magnetic separation combined with adsorption by activated carbon has been found to be a useful method for removing pollutants. In this paper, the use of palm shell as a source of activated carbon for the removal and recovery of oil from palm oil mill effluent (POME) is studied. In the first part of the study, the properties of samples of activated carbon prepared from palm shell under a variety of different conditions were characterized for their hydrophobicity, surface areas and pore size distribution. The most effective of the activated carbon samples was prepared by impregnation with ZnCl(2) followed by combined physical/chemical activation under carbon dioxide flow at 800 °C. Four grams of these samples adsorbed 90% of the oil from 50 mL POME. In the second part, the palm shell-based carbon samples were given magnetic properties by the technique of iron oxide deposition. Ninety-four percent of the activated carbon/iron oxide composite containing the adsorbed oil could be extracted from the POME by a magnetic bar of 0.15 T. Four grams of the composite can remove 85% of oil from 50 mL POME and a total of 67% of the initial oil can then be recovered by hexane extraction. Powder X-ray diffractometry showed the presence of magnetite and maghemite in the activated carbon/iron oxide composite.     

Direct utilization of kitchen waste for bioethanol production by separate hydrolysis and fermentation (SHF) using locally isolated yeast

Kitchen wastes containing high amounts of carbohydrates have potential as low-cost substrates for fermentable sugar production. In this study, enzymatic saccharification of kitchen waste was carried out. Response surface methodology (RSM) was applied to optimize the enzymatic saccharification conditions of kitchen waste. This paper presents analysis of RSM in a predictive model of the combined effects of independent variables (pH, temperature, glucoamylase activity, kitchen waste loading, and hydrolysis time) as the most significant parameters for fermentable sugar production and degree of saccharification. A 100 mL of kitchen waste was hydrolyzed in 250 mL of shake flasks. Quadratic RSM predicted maximum fermentable sugar production of 62.79 g/L and degree of saccharification (59.90%) at the following optimal conditions: pH 5, temperature 60°C, glucoamylase activity of 85 U/mL, and utilized 60 g/L of kitchen waste as a substrate at 10 h hydrolysis time. The verification experiments successfully produced 62.71 ± 0.7 g/L of fermentable sugar with 54.93 ± 0.4% degree of saccharification within 10 h of incubation, indicating that the developed model was successfully used to predict fermentable sugar production at more than 90% accuracy. The sugars produced after hydrolysis of kitchen waste were mainly attributed to monosaccharide: glucose (80%) and fructose (20%). The fermentable sugars obtained were subsequently used as carbon source for bioethanol production by locally isolated yeasts: Saccharomyces cerevisiae, Candida parasilosis, and Lanchancea fermentati. The yeasts were successfully consumed as sugars hydrolysate, and produced the highest ethanol yield ranging from 0.45 to 0.5 g/g and productivity between 0.44 g L^–1 h^–1 and 0.47 g L^–1 h^–1 after 24-h incubation, which was equivalent to 82.06–98.19% of conversion based on theoretical yield.     

Growth factors, kinetics and biodegradation mechanism associated with Pseudomonas nitroreducens TX1 grown on octylphenol polyethoxylates

The growth properties and biodegradation mechanism of a Gram-negative bacterium, Pseudomonas nitroreducens TX1 that was able to grow on branched octylphenol polyethoxylates (OPEO(n), average n=9.5) as the sole carbon source over a wide concentration range (1-100,000 mgl(-1)) were studied. Analysis of growth factors indicated the highest specific growth rate (micro) of 0.53 h(-1) was obtained at an initial concentration of 5,000 mgl(-1) OPEO(n). An optimal C/N ratio of 12 was obtained for (NH(4))(2)SO(4) as the nitrogen source in a cultivated medium at pH 7. The kinetic analysis demonstrated that bacterial growth and OPEO(n) degradation followed the Monod equation and were based on a substrate concentration inhibition model and pseudo-first-order reaction, respectively. The substrate inhibition coefficient was over 18,000 mgl(-1) and this indicates that the strain has an ability to sustain growth at high concentrations of OPEO(n) and use it as the sole carbon source under such a stress condition. Furthermore, LC-MS analysis showed that the biodegradation mechanism of dodecyl octaethoxylate (AEO8) by P. nitroreducens TX1 was the sequential cleavage of the ethoxylate chain.     

The Effects of Gas Flow Rate and the Interval Time of Water Supplement on Ethanol Production of Rice Straw by Simultaneous Saccharification and Fermentation

In the present work, characteristics of ethanol production from a single particle composing of pretreated rice straw, cellulase, and β-glucosidase were invesitgated by simultaneous saccharification and fermentation (SSF). The experiment experienced a start-up stage for S. cerevisiae biofilm formation, which was operated at an initial pH value of 4.8 for yeast solution, culture temperature of 30°C, flow rate of 0.8 mL/min for yeast solution, and stably operating stage for ethanol production at a culture temperature of 30°C. Investigations found that the maximal ethanol yield of 9.7 mg/g and the biofilm thickness of 0.37 mm were obtained at 30 mL/min of carrier gas flow rate. Also, the optimal interval time of water supplement was 4 h for SSF. The results show that the appropriate gas flow rate and the interval time of water supplement can keep the high activities of biofilm and enzymes during SSF and result in a high ethanol yield.