用聚乙二醇(PEG)／无机盐双水相体系从枯草杆菌发酵液中提取a-淀粉酶的研究

本文报道分别用聚乙二醇(PEG)／磷酸盐和PEG／(NH·)2SO4双水相体系从枯草轩菌发酵液中提取a-淀粉酶。研究了PEG的平均分子量、PEG浓度,成相的盐的浓度和Nacl的浓度对a-淀粉酶和蛋白质的分配系数以及相比的影响,确定了最佳的操作条件。实验表明在180%PEG 1500／10％磷酸盐／0．05M NaCl的体系中,a-淀粉酶的分配系数为6.62,蛋白质分配系数为1．14,相比为2．5,a-淀粉酶总收率为94．3％,在16％PEG 1500／12％(NH₄)₂SO₄／O．05M NaCl体系中,a-淀粉酶分配系数为82,蛋白质分配系数为5．2,相比为O．92,酶收率为99％,结果表明用PEG／无机盐双水相体系直接从含有菌体的发酵液中提取a-淀粉酶是可行的。     

双水相体系逆流色谱技术在蛋白质分离中的应用

双水相体系逆流色谱技术结合了逆流色谱的高效率、高制备量以及双水相体系适于蛋白质分离的特点,因此在蛋白质的分离方面具有独特的应用价值。本文综述了近年来基于正交轴逆流色谱仪器的双水相体系逆流色谱技术在多种蛋白质分离中的应用。并对一些新兴的蛋白质逆流色谱分离技术及新型逆流色谱柱分离系统进行了介绍。     

聚乙二醇沉淀联用双水相萃取法纯化蛋清溶菌酶的研究

研究以聚乙二醇(Polyethylene Glycol,PEG)沉淀法联用PEG-硫酸铵双水相萃取体系纯化蛋清溶菌酶的工艺。结果表明,向预处理的鸡蛋清液中加PEG 4000至质量分数为16%时,可选择性沉淀除去蛋清中98.1%的杂蛋白,随后向上清液中加硫酸铵溶液至其质量分数为4.32%,可以构建PEG-硫酸铵双水相体系,分离上相即得高纯度溶菌酶。该法所得产物中96.34%为溶菌酶,其余为PEG 4000,不含有其它杂蛋白,溶菌酶总回收率达70.2%,比活为25 000 U/mg。该法简便易行,易于放大,每毫克精制溶菌酶中仅残留36.6μg PEG 4000,生物安全性较高。     

螺旋槽圆盘柱高速逆流色谱及其在多肽和蛋白分离中的应用

本研究重点考察了实验室自行设计研制的J型螺旋槽圆盘柱逆流色谱系统对正丁醇-醋酸-水体系和聚乙二醇(PEG1000)-磷酸盐-水双水相体系的固定相保留能力,并研究了流动相流速(F)、柱转速(w)和温度(T)等因素对固定相保留率(Sf)的影响。结果表明,该新型分离柱可使两种溶剂体系在L-I-T、U-O-H和L-I-H三种洗脱模式下都可获得较高的Sf,即以下相为流动相,采用由螺旋槽内端(I)向外端(O)的流通方式,或以上相为流动相,采用由螺旋槽外端(O)向内端(I)的流通方式可以获得较高的固定相保留。其保留能力较传统的螺旋管逆流色谱柱有显著提高。Sf随着w的增加而升高,随着F的增加而降低,且Sf与F1/2/w线性相关。20oC～45oC之间温度对Sf影响不明显,但低于20oC不利于双水相体系的保留。应用研究表明,采用正丁醇-醋酸-水(4:1:5,V/V/V)和PEG1000-磷酸钾盐-水(12.5:12.5:75,W/W/W)(pH9.0)体系可以在较高的流动相流速和较高的固定相保留下分别实现对亮氨酸-酪氨酸(Leu-Tyr)和缬氨酸-酪氨酸(Val-Tyr)二肽混合物、细胞色素C与肌红蛋白混合物、肌红蛋白与溶菌酶...     

pH调控双水相萃取色素蛋白复合体及其分配行为研究

为发展色素蛋白复合体分离纯化新方法,探究pH调控PEG1000/柠檬酸钾双水相系统萃取分离纯化色素蛋白复合体。优化萃取条件,光谱法研究其分配行为,检测产物纯度和生物活性。结果表明,最佳萃取条件为调节pH9.0,相组成CPEG100019.0%/C柠檬酸钾20.0%,蛋白质加量3.42 mg/g,K和萃取率达到最大,分别为8.8及86.0%。响应面分析法揭示,PEG1000和柠檬酸钾质量浓度及pH对分配系数和萃取率影响显著。调节pH7.0,反萃取分配系数和反萃取率最小为0.15及86.6%。蛋白质总回收率为74.2%。pH对色素蛋白复合体分配行为具有调控作用,pH大于8.5体系,色素蛋白趋于分配上相,反之分配于下相,PEG1000/柠檬酸钾以及蛋白质加入量不影响色素蛋白复合体分配于上相。电泳表征发现,萃取(pH9.0)上相存在2个蛋白质组分,相对分子量(MW)为7.0 kD及14.0 kD。反萃取(pH7.0)使相对分子量7.0 kD蛋白质组分分配于下相,该组分为LH2β亚基,经萃取和反萃取产物生物活性稳定。pH可调控PEG1000/柠檬酸钾双水相系统萃取分离色素蛋白复合体,产物纯度高,生物活性稳定。     

应用液—液双水相抽提技术分离纯化甘油激酶、a-甘油磷酸脱氢酶及心肌黄酶

用液-液双水相抽提技术分别从嗜热脂肪芽胞杆菌(Bacillus stearothermophilus)菌体、兔肌及猪心肌匀浆液中分离甘油激酶、a-甘油磷酸脱氢酶及心肌黄酶,研究了pH,匀浆液的量、氯化钠浓度及丙酮等因素对分配系数、上下相体积之比,酶活性回收率及分离效果等参数的影响,并确定了抽提上述三种酶的最佳相组成系统。用本文的工艺抽提甘油激酶、a-甘油磷酸脱氢酶及心肌黄酶有下列优点： 1．酶活回收率较高,分别为90％、95％及70％2：分离效果较好,通常提纯三、四倍以上3．各酶均存留在下相,即磷酸钾盐富相中,故可省去聚乙二醇(PEG)的分离工序而直接与后继精制工艺衔接,简化了工艺,在实验室及工业生产中均有实用价值。     

应用双水相萃取技术提取香菇多糖的研究

利用聚乙二醇(PEG)-硫酸铵双水相体系提取香菇多糖,研究了不同PEG-硫酸铵组成的双水相体系对香菇多糖分配比和收率的影响。结果表明:PEG分子量在6000时对香菇多糖的提取效果较好;PEG6000浓度在24%时、硫酸铵浓度在30%时组成的双水相体系提取香菇多糖的效果最好,此时香菇多糖的分配系数(K)可达到1.90,收率(Y)可达到57.42%。     

离子液体双水相体系及其在生物分离中的应用

作为一种高效而温和的新型绿色分离体系,离子液体双水相体系结合了离子液体和双水相体系的优点。因此倍受国内外研究者的青睐。介绍了双水相萃取技术的原理和离子液体双水相体系;综述了离子液体双水相体系在生物分离中的研究进展,主要包括抗生素、蛋白质、和食用色素等的萃取分离;并展望了离子液体双水相体系在生物分离中的应用前景。     

双水相体系萃取人参根中人参皂苷的研究

建立稳定的聚乙二醇(PEG)与(NH4)2SO4双水相体系以分离人参根中人参皂苷。通过上下相体积比(R)、分配系数(K)和回收率(Y)分析双水相体系对人参皂苷的萃取效果,研究了PEG分子量、PEG/(NH4)2SO4质量分数、pH值和温度等因素对双水相成相及人参皂苷萃取的影响。结果表明:PEG分子量为3350、PEG3350的质量分数为12%、(NH4)2SO4质量分数为16%、溶液pH为7.0、温度为60℃时,双水相体系对人参皂苷有较高的萃取率,回收率可到达88.94%。     

非水体系中脂肪酶催化合成乳酸乙基糖苷酯的工艺研究

在非水体系中 ,通过固定化脂肪酶催化合成一种新型α 羟基酸衍生物 乳酸糖苷酯。考察了常压下有机溶剂、酰基供体、不同种固定化酶、乙基糖苷的浓度、酶量和反应温度对反应的影响。研究表明在无溶剂体系中以乳酸丁酯作为酰基供体可有效地合成乳酸糖苷酯 ,固定化酶Novozym435和来源于Candida sp .菌株的细胞固定化酶 ,化学修饰的干酶粉均是合适的催化剂。最佳反应条件为 :酶浓度 75g L ,乙基葡萄糖苷的浓度为 0.4mol L ,温度为 70℃ ,转速 200r min ,反应 50h ,转化率可达 71%。在真空度为 0.09MPa的压力下 ,反应温度 65℃ ,酶浓度 75g L ,乙基葡萄糖苷 0.35mol L时 ,反应初速率可达到 607(mmol·L^-1·h^-1 ) ,40h后转化率可达到 90%。反应产物经过萃取法和硅胶柱层析方法分离 ,纯度达到 95 % (W/W)。     

Aqueous two-phase systems extraction of alpha-toxin from Clostridium perfringens type A

Two sequential half-fraction designs were applied to studying the alpha-toxin partition produced by Clostridium perfringens type A in aqueous two phase systems (ATPS), as a function of four factors: PEG molar mass and concentration, phosphate concentration and pH. The highest purification factor, yield and partition coefficient results were obtained with PEG 8000 (15%, w/w), phosphate at 20% (w/w) and pH 8.0. This system allows, in a single step, an alpha-toxin purification of 4.6-fold with final activity yield of 230% and partition coefficient of 113.9 in the PEG rich phase.     

One-step purification of proteins from chicken egg white using counter-current chromatography

Proteins present in chicken egg white are separated by counter-current chromatography (CCC) in one step using a cross-axis coil planet centrifuge (X-axis CPC). The separation was performed with an aqueous polymer two-phase system composed of 16% (w/w) poly(ethylene glycol) 1000 and 12.5% (w/w) dibasic potassium phosphate by eluting the lower phase at a flow-rate of 1.0 ml/min. From about 20 g of the crude egg white solution, lysozyme, ovalbumin, and ovotransferrin were resolved within 5.5 h. Each component was identified by 12% SDS gel electrophoresis with Coomassie brilliant blue staining.     

Partial purification of α-amylase from culture supernatant of <Emphasis Type="Italic">Bacillus subtilis</Emphasis> in aqueous two-phase systems

A study was made of the partition and purification of -amylase from a culture supernatant of Bacillus subtilis in the polyethylene glycol (PEG)—citrate aqueous two-phase system (ATPS). Factors that influenced the partition of the protein in this system, including the molecular weight of the PEG, the tie line length of ATPS, the pH value and the sodium chloride concentration, were investigated. Purification of -amylase was attained with a purification factor (PF) of 1.8 and 90% yield at pH 6.0 in a PEG1000-citrate ATPS with short tie line length. By utilizing the salt-out effect of neutral salt, the purification of -amylase was further improved to 2.0 of PF and 80% yield in a PEG3350-citrate ATPS with 4% sodium chloride.     

Production of cyclodextrin homologues using aqueous two-phase system

Cyclodextrin homologues (CDs), produced by cyclodextrin glycosyltransferase (CGTase), were simultaneously partitioned in aqueous two-phase system (ATPS). Partition coefficients of CDs were measured in PEG/salt and PEG/dextran systems. Phosphate, citrate, sulfate were tested as salt. ATPS of PEG/salt and PEG/dextran had the partition coefficients of the CDs, larger than unity. However, PEG/dextran system was observed better than PEG/salt as CGTase activity decreased sharply with salt concentration. Enzymatic reaction occurred mainly in PEG-rich bottom phase because of the low partition coefficient of CGTase. The resulting CDs transferred to the PEG-rich top phase, obeying the diffusional partition. In the ATPS of 7% PEG (M.W. 20,000) and 9% dextran (M.W. 40,000), 7 mg/ml of CDs were obtained in top phase at 4.5 hours.     

Partial purification of penicillin acylase from Escherichia coli in poly(ethylene glycol)–sodium citrate aqueous two-phase systems

Studies on the partition and purification of penicillin acylase from Escherichia coli osmotic shock extract were performed in poly(ethylene glycol)–sodium citrate systems. Partition coefficient behavior of the enzyme and total protein are similar to those described in other reports, increasing with pH and tie line length and decreasing with PEG molecular weight. However, some selectivity could be attained with PEG 1000 systems and long tie line at pH 6.9. Under these conditions 2.6-fold purification with 83% yield were achieved. Influence of pH on partition shows that is the composition of the system and not the net charge of the enzyme that determines the behaviour in these conditions. Addition of NaCl to PEG 3350 systems significantly increases the partition of the enzyme. Although protein partition also increased, purification conditions were possible with 1.5 M NaCl where 5.7-fold purification and 85% yield was obtained. This was possible due to the higher hydrophobicity of the enzyme compared to that of most contaminants proteins.     

The inhibition of vegetative cell outgrowth and division from spores of Bacillus cereus T by hen egg albumen

Spores of Bacillus cereus T germinated and formed vegetative cells in Tryptone Soya broth (TSB), pH 9-0 and 7-4 at 30^oC. Spores germinated but did not form vegetative cells when suspended in hen egg white (pH 9-0) supplemented with L-alanine and inosine. Using a split image eyepiece, the volumes of germinating spores in egg white were seen to increase as a result of increases in both length and breadth. In TSB at the same pH, the major volume increase resulted from a progressive increase in cell length. Egg white supplemented with L-alanine and inosine (pH 7-6 30^oC) allowed limited outgrowth to occur but the vegetative cells differed in morphology to those in TSB. Fe(NH₄)₂(SO₄)2.6H₂O overcame the inhibition of outgrowth in egg white at pH 7–8 but not in egg white at pH 9-1. Solutions containing trace elements, growth factors and casamino acids could not replace iron in this respect. Sporulation occurred in egg white only when iron was present.     

Production and Partial Purification of Tannase from Aspergillus ficuum Gim 3.6

A novel fungal strain, Aspergillus ficuum Gim 3.6, was evaluated for its tannase-producing capability in a wheat bran-based solid-state fermentation. Thin-layer chromatography (TLC) analysis revealed that the strain was able to degrade tannic acid to gallic acid and pyrogallol during the fermentation process. Quantitation of enzyme activity demonstrated that this strain was capable of producing a relatively high yield of extracellular tannase. Single-factor optimization of process parameters resulted in high yield of tannase after 60 hr of incubation at a pH of 5.0 at 30°C, 1 mL of inoculum size, and 1:1 solid–liquid ratio in the presence of 2.0% (w/v) tannic acid as inducer. The potential of aqueous two-phase extraction (ATPE) for the purification of tannase was investigated. Influence of various parameters such as phase-forming salt, molecular weight of polyethylene glycol (PEG), pH, and stability ratio on tannase partition and purification was studied. In all the systems, the target enzyme was observed to preferentially partition to the PEG-rich top phase, and the best result of purification (2.74-fold) with an enzyme activity recovery of 77.17% was obtained in the system containing 17% (w/w) sodium citrate and 18.18% (w/w) PEG1000, at pH 7.0.     

牛血清白蛋白在聚乙二醇/葡聚糖双水相体系中分配特性的研究

采用考马斯亮蓝G250染色法测得室温下BSA在PEG/dextran双水相体系中的分配系数。以BSA在PEG/dextran体系的下相富集为目标,研究了PEG的分子量、浓度、dextran浓度以及所加入中性盐的种类与浓度、体系pH诸因素对其分配特性的影响。实验结果表明,在PEG4000/dextran体系中,采用PEG质量分数9%-dextran质量分数9%的浓度组成,同时在pH=7.0,NaC l浓度为0.2 mol.L-1或pH6.0,NaC l浓度为0.34 mol.L-1的工艺条件下萃取BSA均可达最小分配系数,其值为0.014。     

Purification of alcohol dehydrogenase from bovine liver crude extract by dye-ligand affinity counter-current chromatography

Alcohol dehydrogenase (ADH) was extracted from a crude bovine liver homogenate by dye-ligand affinity counter-current chromatography (CCC) using a cross-axis coil planet centrifuge (x-axis CPC). The purification was performed using two types of polymer phase systems composed of 4.4% polyethylene glycol (PEG) 8000-7.0% dextran T500-0.1 M potassium phosphate buffers and 16% PEG 1000-12.5% potassium phosphate buffers, both containing a procion red dye as an affinity ligand at various pH values. The best purification was achieved using the PEG 1000-potassium phosphate system at pH 7.3 containing 0.05% procion red as a ligand. The upper PEG-rich phase containing procion red was used as the stationary phase and a crude bovine liver homogenate was eluted with the potassium phosphate-rich lower phase at 0.5 ml/min. After elution of bovine liver proteins in the homogenate, ADH still retained in the stationary phase was collected from the column by eluting with the PEG 1000-rich upper phase. Collected fractions were analyzed by ADH enzymatic activity and by sodium dodecyl sulfate (SDS)-polyacrylamide gel electrophoresis (PAGE) to detect contaminant proteins in the ADH fractions. The ADH was purified directly from crude bovine liver extract within 6h with minimum loss of its enzymatic activity.