含氟聚醚砜阴离子交换膜的制备和性能研究

以双(4-氯苯基)砜和2,2-双(4-羟基苯基)六氟丙烷为单体通过缩聚反应、氯甲基化、季铵化和碱化,制备了不同季铵化的含氟聚醚砜阴离子交换膜。利用核磁共振氢谱(~1H-NMR)对聚醚砜(PES)、氯甲基化聚醚砜(CMPES)和季铵化聚醚砜(QPES)的结构进行了表征,并测试了膜的各项性能。结果表明,膜的离子交换容量(IEC)受氯甲基化反应条件的影响,最佳条件下制得QPES-A5膜性能最佳,IEC为1.739 meq·g~(-1),80℃下吸水率(WU)可达45.4%,溶胀率(SR)为20.6%,电导率为26.10 mS·cm~(-1),常温下拉伸强度为24 MPa。60℃时用3 mol/L NaOH溶液浸泡24 h后,电导率仍为21.90 mS·cm~(-1),良好的综合性能说明含氟聚醚砜阴离子交换膜在碱性阴离子交换膜燃料电池方面有很好的应用前景     

用中空纤维超滤膜浓缩酶

本文介绍了2709碱性蛋白酶及7658α-淀粉酶采用03型与05型中空纤维超滤膜进行中试规模的浓缩试验,所获得的有关浓缩倍数,酶的收率,Rf值及超滤流率等数据,对该超滤膜进行了评价;并对运行中压力,温度以及关于膜的清洗进行了讨论。     

用中空纤维超滤膜浓缩酶

本文介绍了2709碱性蛋白酶及7658α-淀粉酶采用03型与05型中空纤维超滤膜进行中试规模的浓缩试验,所获得的有关浓缩倍数,酶的收率,Rf值及超滤流率等数据,对该超滤膜进行了评价;并对运行中压力,温度以及关于膜的清洗进行了讨论。     

羊毛防毡缩用蛋白酶的化学修饰

为减少防毡缩整理中蛋白酶对羊毛纤维主体结构的破坏作用,分别研究了戊二醛、微生物谷氨酰胺转氨酶(MTG)和水溶性碳二亚胺(EDC)对蛋白酶Savinase 16L的化学修饰,以期达到增大蛋白酶分子量,从而将水解作用限制在纤维表面的目的。主要通过体积排阻色谱、SDS-PAGE谱图以及荧光光谱研究修饰酶的分子量和结构变化。结果表明,戊二醛不能对蛋白酶分子进行有效修饰;MTG会被蛋白酶水解,无法催化酶分子间发生共价交联;而碳二亚胺既可以使蛋白酶分子间发生交联,又能将含有伯胺基的大分子修饰剂偶联到酶分子上。     

大豆乳清中蛋白质和异黄酮的超滤分离技术

研究了用超滤技术分离大豆乳清中的蛋白质和异黄酮的工艺条件. 结果表明,大豆乳清在超滤之前要进行预处理以减轻膜污染;通过2因素3水平正交试验,确定了最佳的预处理工艺：按大豆乳清中固形物含量的5%,向其中加入CaCl₂,并在85 ℃下加热15 min,在此条件下,蛋白质的沉淀率为49.8%,异黄酮的保留率为90.4%;通过单因素试验,确定了比较合适的超滤条件：选择切割分子量（MWCO）为10000的聚醚砜膜,超滤压力选择51～68 kPa,超滤温度选择30 ℃～40 ℃.在此条件下,大豆乳清中蛋白质的截留率为83.9%,而异黄酮的截留率为7.6%.     

白喉毒素超滤浓缩后膜通透性恢复试验的研究

应用超滤浓缩技术对白喉毒素培养液进行澄清过滤和超滤浓缩,已经早已为生产厂家所使用.但是,超滤膜的通透性下降很快,使膜的使用期限大大缩短,生产成本较高.因此在试验过程中,注重摸索超滤过程的中间控制以及超滤结束后的清洗方法,特别是使用0.5 mol/LNaOH+200ppm次氯酸钠作为清洗剂,在超滤结束以后对滤膜进行彻底的恢复性清洗,可以使澄清和浓缩过滤速度分别达到平均77 L/M2·h和75 L/M2·h,回收率分别达到93.1%和92.8%,使滤膜的滤过性能(NWP)基本恢复到滤前水平.     

水体病毒浓缩方法的建立和优化研究

采用氯化钙(CaC l2)、聚乙二醇(PEG,pH7.0)、聚乙二醇(PEG,pH11.5)、三氯化铝(A lC l3)沉淀、Am icon Utcra超滤离心装置和硝酸纤维素吸附膜6种浓缩方法,浓缩人工添加于水体的1型脊髓灰质炎疫苗病毒(PV1),并对浓缩实验条件进行选择和优化。结果表明,CaC l2和聚乙二醇(pH7.0)沉淀法适用于浓缩大容量水体中的病毒,而超滤离心管浓缩法适用于小容量水体,这3种浓缩方法的病毒回收率均达到100%。     

Vero细胞狂犬病疫苗在凝胶柱层析工艺中样品浓度对纯化效果的影响

为研究浓缩Vero细胞狂犬病疫苗蛋白浓度对纯化效果的影响。用超滤浓缩法对狂犬病疫苗进行不同倍数的超滤浓缩,将浓缩后不同倍数的样品分别用凝胶柱层析法进行纯化,结果样品浓度在40mg/ml以下时,狂犬病毒收集液中杂蛋白去除率可达99%以上,小牛血清含量在25-37.5ng/ml之间;浓缩超过40mg/ml时,并随着样品浓度的增加,狂犬病毒收集液中杂蛋白去除率逐渐下降,且有病毒丢失,因此采用凝胶柱层析法纯化狂犬病疫苗,蛋白浓度应低于40mg/ml。     

赛多利斯推出用于浓缩生物大分子的离心超滤浓缩装置Vivaspin Turbo 15

赛多利斯近日推出了一款全新的用于浓缩生物大分子的离心超滤浓缩装置Vivaspin Turbo 15。该超滤浓缩装置有8种不同的截留分子量可供选择,可以更大面积的双排垂直膜使浓差极化和堵塞程度降至更低,确保更快的     

嗜热土芽孢杆菌GSEY01及其高温蛋白酶的初步研究

从云南腾冲热海热泉中分离出一株产高温蛋白酶的菌株GSEY01。该菌株最适生长温度为60℃,16S rRNA基因序列分析表明,该菌株为土芽孢杆菌属(Geobacillus)的耐热菌株。该菌株所产高温蛋白酶可以通过超滤浓缩,硫酸铵分级沉淀和强阴离子交换层析获得纯酶。此高温蛋白酶分子量约为42kD,最适催化温度为80℃,最适催化pH7.5,Mg2+能增强该酶活力,Fe3+,Cd2+和Ni2+对其活性则有抑制作用。PMSF对该酶影响较小,乙二胺四乙酸(EDTA)和十二烷基磺酸钠(SDS)则对其有强烈的抑制作用,此高温蛋白酶和其他土芽孢杆菌所产蛋白酶有较大差异,可以应用于相关的高温催化环境。     

卡拉胶固定粘质赛氏菌产碱性蛋白酶的研究

将粘质赛氏菌(Seratia marcescens)包埋于卡拉胶中,发现2．5％的卡拉胶适于固定该菌产碱性蛋白酶。固定化细胞在其较适宜产酶培养基中发酵,酶活力一般可达400u/ml,在卡拉胶中添加3％玉米粉和1%豆饼粉或2％砂子制备固定化细胞,其产酶能力分别提高了25%和23．9％;固定化细胞颗粒越小,其产酶能力越高。采用摇瓶半连续发酵。其产酶半衰期为14次(24小时为一个周期);而用环流器进行半连续发酵,其产酶半衰期为52次(12小时为一个周期),产酶效率分别比游离细胞摇瓶发酵的产酶效率高11．8％和45．07％,而环流器半连续发酵的产酶效率比摇瓶半连续发酵高29．7％。     

Separation of dilute aqueous butanol and acetone solutions by pervaporation through liquid membranes

A simultaneous extraction-stripping process is proposed for separating volatile products from fermentation broths, it is based on pervaporation through a liquid membrane supported with a hydrophobic porous membrane. The liquid membrane prepared with oleyl alcohol was selected as the most suitable for separating volatile products resulting from acetone-butanol fermentation. The separation performance and stability of the oleyl alcohol liquid membrane were investigated by using dilute aqueous butanol and acetone solutions. The oleyl alcohol liquid membrane was found to be superior by far in both selectivity and permeability of butanol to the better known silicone rubber membrane in its high selectivity for alcohols. Using the oleyl alcohol liquid membrane, the dilute aqueous butanol solutions of around 4 g/L obtained in acetone-butanol fermentation could be concentrated up to 100 times. The stability of this liquid membrane was also quite good as long as the surface tension of the feed solution was less than the critical surface tension of the support membrane. No change in the separation performance was found after the continuous usage in a long period of 100 h.     

致病疫霉拮抗菌株YR-7 的分离鉴定及其活性物质

【目的】从黄河边的农田土壤中分离筛选拮抗致病疫霉的粘细菌,鉴定目标菌株,分析其发酵上清液的稳定性及对马铃薯晚疫病菌的抑制效果,为活性物质分离鉴定及抗马铃薯晚疫病菌生物农药的研发奠定基础。【方法】采用兔粪诱导法分离菌株,通过平板对峙法筛选对马铃薯晚疫病菌有拮抗作用的粘细菌,通过形态特征、生理生化特征以及16S r RNA基因序列分析对菌株进行鉴定。采用称重法测定菌株生长曲线,通过平皿法测定菌株不同生长时期发酵上清液对致病疫霉的菌丝生长抑制率和浓缩发酵上清液的稳定性。通过马铃薯离体叶片涂布浓缩发酵上清液和接种病原菌孢子悬浮液法,测定该菌株对马铃薯晚疫病的防病作用。【结果】从土壤样品中共分离获得7株粘细菌,其中4株拮抗致病疫霉,拮抗效果最强的为YR-7菌株,菌丝的生长抑制率为96%,该菌株被鉴定为Myxococcus xanthus。培养7 d后,菌株发酵上清液对致病疫霉的抑制活性趋于稳定。浓缩发酵上清液经30-50°C处理后,对致病疫霉菌丝的生长抑制率可达50.90%,高于50°C时抑菌活性逐渐下降,90°C处理后菌丝的生长抑制率仍可达25.45%。浓缩发酵上清液在p H 4.0-9.0条件下比较稳定,保持40.21%以上菌丝的生长抑制率,当p H4.0或p H9.0时,抗菌活性显著降低。活性物质不能被蛋白酶降解,其抗菌活性不受紫外线、自然光照射的影响。对马铃薯离体叶片的生防效果检测表明,YR-7的浓缩发酵上清液处理组叶片相对病斑面积仅为0.35%,对照组的相对病斑面积高达68.19%。【结论】粘细菌菌株YR-7可以产生抗马铃薯晚疫病菌的次生代谢产物,抗菌活性物质具有较好的稳定性,可以有效抑制致病疫霉侵染马铃薯叶片,具有开发成抗马铃薯晚疫病生物农药的潜在价值。     

Production of Alkaline Protease from Acetic Acid

The use of acetic acid as a carbon source in alkaline protease fermentation was examined. Acetic acid was a good carbon source and yielded a great deal of alkaline protease.

Acetic acid has advantages over ordinary carbon sources such as starch and glucose in that it can be supplied to culturing liquid as much as needed to perform the fermentation efficiently, that it has a function to control the pH of culturing liquid at a constant level and that it was obtained at lower price.

The maximum proteolytic activity attained was 1.6 × 10⁴ units/ml (11.4 mg-enzyme/ml).     

微生物转谷氨酰胺酶的生产菌种诱变和发酵生产分析

对本研究室从土壤分离得到的使霉菌(Streptomyces sp.)WZFF．W-12菌株的斜面孢子预培养处于初萌发状态后,以亚硝基胍(NTG)进行诱变育种试验,并根据诱变处理后菌落的某些形态变化状况与产酶能力相结合的特征,初步判断产酶性能,挑选高酶活菌株,再经过初筛和复筛,获得一性能良好的产酶突变菌株WZFF.W-12.var MN-35,转谷氨酰酶活达0．53U／mL,比原始菌株提高了1．2倍。然后在摇瓶条件下,对其发酵过程中的主要培养基组成及各种培养条件对菌体生长和产酶的影响作用进行了研究,结果表明该菌株发酵生产转谷氨酰酶的适宜破源为可溶性淀粉 葡萄糖,氮源是多价胨外加少量的酵母膏,优化工艺条件为种龄时间24h、接种量10％、初始以值6．5、温度30℃和搅拌速度200r／min,产酶能力显著提高,用小型生化反应器可以稳定生产2.0U／mL以上的酶产品。     

Screening,selection and development of Bacillus subtilis apr-IBL04 for hyper production of macromolecule alkaline protease

Bacillus subtilis microbe is commonly found in soil and produces proteases on nitrogen and carbon-containing sources and increases the fertility rate by degrading nitrogenous organic materials. The present study was aimed to develop hyper producing mutant strain of B. subtilis for the production of proteases, to improve the process variables by the response surface methodology (RSM) under central composite design (CCD) and the production of protease by the particular mutant strain in a liquid state fermentation media. The mutation of the strain was carried out using ethidium bromide. Pure B. subtilis strain was collected and screened for hyper-production of protease. The production of protease by mutant B. subtilis strain was optimized by varying temperature, inoculum size, pH and incubation time under liquid state fermentation. The CCD model were found to be reliable with r² of 0.999. The maximum enzyme activity of B. subtilis IBL-04 mutant with 3 mL/100 mL inoculum size, 72 h fermentation time, pH 8, and 45 °C temperature was developed with enzyme activity 631.09 U/mL, indicates 1–7-fold increase in enzyme activity than the parent strain having 82.32 U/mL activity. These characteristics render its potential use in industries for pharmaceutical and dairy formulation.     

Fermentation of starch for enhanced alkaline protease production by constructing an alkalophilic Bacillus pumilus strain

A new engineering strain, Bacillus pumilus c172-14 (pBX 96), was obtained by introducing the pBX 96 plasmid, which carries the alpha-amylase amy gene, into the host strain of alkalophilic Bacillus pumilus c172 via transformation. The newly constructed strain was found to express the amy gene and could use starch instead of glucose or starch hydrolysate as carbon source for its fermentation of alkaline protease. The pBX 96 plasmid in the new host was found to be segregationally and structurally stable. The expression of amy gene did not affect the host strain's resistance to bacteriophages. Moreover, the level of alkaline protease was improved significantly compared with the parent strain. The constructed strain gave a maximum alkaline protease activity of 14,014 U/ml in shaking flask after 48 h cultivation when growing in a medium containing 6% corn meal, 4% soybean flour, 0.4% Na2HPO4, 0.03% KH2PO4, 0.02% MgCl2, 0.3% CaCl2, 0.25% Na2CO3, 0.1% glucose, and 20 microg/ml kanamycin (pH 7.0). The optimal pH value and temperature of the alkaline protease were 11.0 and 40 degrees C, respectively. This enzyme was stable over a pH range of 8-11. Its residual activity remained at 100% when treated under a temperature of less than 45 degrees C for 30 min. The corresponding residual activity reduced to 65% of its optimal value at 60 degrees C for 30 min. The alkaline protease was a kind of serine protease, which was demonstrated by the complete inactivation by PMSF (1 mM). This newly constructed strain will be useful in the alkaline protease industry.     

Optimization of medium and cultivation conditions for alkaline protease production by the marine yeast Aureobasidium pullulans

A yeast strain, Aureobasidium pullulans, which could produce the high yield of protease was isolated from sediment of saltern in Qingdao, China. Maximum production of enzyme (623.1 U/mg protein; 7.2 U/ml) was obtained in a medium containing 2.5 g soluble starch and 2.0 g NaNO(3), 100ml seawater, initial pH 6.0, after fermentation at 24.5 degrees C for 30 h. The protease had the highest activity at pH 9.0 and 45 degrees C.     

Preparation and Characterization of a pH-responsive Polymer that Interacts with Microbial Transglutaminase during Affinity Precipitation

Microbial transglutaminase (MTG) has been widely used in the food and pharmaceuticals industries. In this study, MTG was purified using affinity precipitation with an affinity polymer (P_MMDN-T), which was synthesized using a pH-responsive polymer (PMMDN) coupled with L-thyroxin as an affinity ligand. Interactions between MTG and P_MMDN-T were investigated using turbidimetric titration, zeta potential measurements, and low-field nuclear magnetic resonance (LF-NMR). We found different behaviors, architectures, and phase states of pH-dependent interactions between MTG and P_MMDN-T interactions. Binding energetics between MTG and P_MMDN-T were determined by isothermal titration calorimetry (ITC). The isoelectric point (pI) of the affinity polymer was 4.65 and was recovered with 96.7% efficiency after recycling the polymer three times. The optimal adsorption condition was 0.02 mol/L phosphate buffer (pH 6.0) with 1.0 mol/L NaCl at 30.0°C and a ligand density of 50.0 μmol/g. The maximum elution recoveries of total MTG were 98.44% (protein) with 92.19% (activity) using 0.02 mol/L pH 10.0 Gly-NaOH as the eluent.     

In vitro refolding process of urea-denatured microbial transglutaminase without pro-peptide sequence

Efficient refolding process of denatured mature microbial transglutaminase (MTG) without pro-peptide sequence was studied in the model system using urea-denatured pure MTG. Recombinant MTG, produced and purified to homogeneity according to the protocol previously reported, was denatured with 8M urea at neutral pH and rapidly diluted using various buffers. Rapid dilution with neutral pH buffers yielded low protein recovery. Reduction of protein concentration in the refolding solution did not improve protein recovery. Rapid dilution with alkaline buffers also yielded low protein recovery. However, dilution with mildly acidic buffers showed quantitative protein recovery with partial enzymatic activity, indicating that recovered protein was still arrested in the partially refolded state. Therefore, we further investigated the efficient refolding procedures of partially refolded MTG formed in the acidic buffers at low temperature (5 degrees C). Although enzymatic activity remained constant at pH 4, its hydrodynamic properties changed drastically during the 2h after the dilution. Titration of partially refolded MTG to pH 6 after 2h of incubation at pH 4.0 improved the enzymatic activity to a level comparable with that of the native enzyme. The same pH titration with incubation shorter than 2h yielded less enzymatic activity. Refolding trials performed at room temperature led to aggregation, with almost half of the activity yield obtained at 5 degrees C. We conclude that rapid dilution of urea denatured MTG under acidic pH at low temperature results in specific conformations that can then be converted to the native state by titration to physiological pH.