超大孔离子交换制备色谱分离纯化高活性凝血因子VIII

建立了一条从人血浆中分离高活性凝血因子VIII(FVIII)的纯化工艺。基于FVIII和介质孔径的尺度比及其对蛋白质活性影响的分析,设计了以超大孔离子交换制备色谱为核心步骤的新型分离纯化工艺。分别进行超大孔离子交换色谱与传统离子交换色谱的条件优化,并对优化工艺所得产品进行了活性检测(底物显色法)和纯度检测(高效凝胶过滤和凝胶电泳)。结果表明,超大孔介质结构不但可以有效地保护蛋白质大分子结构,而且能够大幅度地提高制备色谱的传质速率,从而得到具有高凝血活性的FVIII产品。FVIII在超大孔制备色谱过程中的回收率(85%)比传统离子交换制备色谱高4～5倍,产品比活高达154 IU/mg。此外,还研究了超大孔介质的再生程序,采用5个柱体积的1 mol/L NaOH低流速清洗色谱柱,保证了色谱工艺的稳定性。本纯化工艺步骤简单,重现性好,易于放大生产。     

膜径向离子交换色谱分离凝血酶原复合物

 利用径向离子交换色谱法分离纯化了Nitschmann组分Ⅲ中的凝血酶原复合物 ( prothrombincomplexconcentrate ,PCC) ,流动相为pH 7.5的Tris HCl缓冲液 ,色谱柱为XK 1 6DEAEfastflowSepharose ( 0 .8cmi.d .× 5cm)及膜DEAE径向色谱柱 ( 3.0cmi.d .× 5.8cm)。通过改变不同上样流速及洗脱流速 ,研究了流速对所分离的凝血酶原复合物的蛋白质量浓度及凝固活性的影响 ,为今后在血浆蛋白分离纯化中进一步推广使用径向色谱技术和放大实验提供了依据。     

径向离子交换色谱柱在生物工程产品下游纯化中的应用

 ]本文利用我们自行研制的径向离子交换色谱柱，对人血浆成分、登革病毒单克隆抗体及基因工程产物A蛋白及人白介素-2进行了分离纯化结果表明，以上目标产品均可得到有效的分离，它在流速、处理量方面均优于传统的色谱方法。由于其体积小，易于放大，不失为一种理想的生物工程产品中试至生产规模的初级分离纯化方法。     

重组灵芝免疫调节蛋白的纯化及其性质

采用超滤浓缩、强阴离子交换、疏水作用和凝胶色谱等方法, 对毕赤酵母表达的rGlip进行分离和纯化, 对离子交换色谱中rGlip与固相结合的最佳pH值进行了考察, 并对纯化产物的活性进行了鉴定. rGlip在215 nm处有强的紫外吸收, 经激光解析电离时间飞行质谱鉴定其相对分子量为12722, 经反相液相色谱鉴定纯度≥97%. 设计rGlip的疏水作用色谱, 有效地去除色素. 凝血实验结果表明, rGlip可以凝集绵羊血红细胞, 但对人血A, B, AB和O型等红细胞无凝集作用, 有类似凝集素的生物学活性.     

蛋白质制备色谱的研究

研究了蛋白质纯化制备的二种运行模式,其一,在色谱柱超载下纯化制备蛋白质模式,并成功地用离子交换色谱纯化制备了大豆中的胰蛋白酶,用反相液相色谱纯化了细胞色素Ｃ;其二,用溶质－溶质顶替色谱纯化制备了核糖核酸酶－Ａ,并对顶替色谱过程中诸参数进行了讨论和选择。     

重组人干扰素-γ的制备与鉴定

用聚乙二醇200疏水相互作用色谱固定相(PEG200-STHIC)分别在色谱柱和色谱饼上完成了一步复性并同时纯化来源于大肠杆菌(E.coli)表达的重组人干扰素-γ(rhIFN-γ)。为了能使色谱分离方法用于不同来源的rhIFN-γ的纯化,对rhIFN-γ在反相色谱、离子交换色谱、固定化镍离子亲和色谱上的保留行为也进行了研究。色谱柱纯化的rhIFN-γ收集液经排阻色谱除盐和冷冻干燥得到rhIFN-γ干粉。用基质辅助激光解吸电离飞行时间质谱对rhIFN-γ干粉进行了测定,rhIFN-γ单体的相对分子质量为17184.0,二聚体的相对分子质量为34204.4。用细胞病变抑制法(CPEI)测定rhIFN-γ干粉的比活性为9.5×108 IU/mg。用十二烷基硫酸钠-聚丙烯酰胺凝胶电泳（SDS-PAGE）测定rhIFN-γ干粉的纯度高于95%。用色谱柱复性并同时纯化rhIFN-γ的质量回收率达到93.7%,纯度高于95%,比活性为4.3×107 IU/mg。结果表明,采用PEG200-STHIC色谱柱复性并同时纯化rhIFN-γ是一种十分高效的方法。     

猪肝中单胺氧化酶B的分离纯化

依据单胺氧化酶B(monoamine oxidase B, MAOB)的疏水特性,建立了一种从猪肝中分离纯化MAOB的新方法。用含有1% Triton X-100的膜蛋白裂解液制备粗酶,以饱和度为20%～50%的硫酸铵反抽提进行粗提,再利用自制的配基密度为75.7 μmol/mL的苯基疏水色谱及Sepharose Q High Performance离子交换色谱进一步分离纯化,得到纯化倍数为18.2、酶比活为135 U/mg的MAOB。十二烷基硫酸钠-聚丙烯酰胺凝胶电泳(SDS-PAGE)分析显示为相对分子质量约60 000的单一蛋白质带。采用高效液相色谱-电喷雾串联质谱对该酶进行鉴定,证实为MAOB。本研究所用分离纯化方法可以有效纯化MAOB, 为MAOB的深入研究提供技术支撑。     

强阴离子交换色谱结合分子排阻色谱纯化血清中免疫球蛋白和白蛋白

动物血清中免疫球蛋白和白蛋白的等电点分别约为7.8和4.8,根据它们等电点的较大差别,利用Q SepharoseTM-XL强阴离子交换色谱结合分子排阻色谱同时分离纯化这2种蛋白。以0.02 mol/L pH 8.0的Tris-HCl缓冲液平衡离子交换色谱柱并将已稀释10倍的高免疫的兔血清上样,采用pH分段洗脱。在pH 6.0时以0.3 mL/min低流速洗脱得到高纯度的免疫球蛋白,继续在pH 4.0时洗脱,再辅以Sephadex G-75分子排阻色谱可获得纯度大于95%的白蛋白。对纯化后的蛋白进行活性检测,证明所纯化的免疫球蛋白和白蛋白都保持正常的生物活性。蛋白质含量测定说明免疫球蛋白的纯化回收率达到95%以上,而白蛋白的纯化回收率大于90%。该法简便快速,可同时从动物血清中纯化出保持生物活性的免疫球蛋白和白蛋白,纯化效率高。     

从猪血中分离纯化高纯度的猪血红蛋白

为了从猪血中分离纯化高纯度的猪血红蛋白,建立了通过超滤、DEAE-Sepharose Fast Flow离子交换色谱和Sephadex G-75凝胶 排阻色谱三步法制备高纯度猪血红蛋白的方法,并通过十二烷基磺酸钠-聚丙烯酰胺凝胶电泳(SDS-PAGE)、高效凝胶排阻色谱和反相高 效液相色谱方法,对纯化后的猪血红蛋白进行了鉴定。经三步分离纯化后,猪血红蛋白的纯度大于99%,含量为1.328 g/L。     

凝胶层析和离子交换层析结合法纯化高盐发酵液中谷氨酰胺转胺酶

采用凝胶层析和离子交换层析相结合的方法分离纯化高盐培养基中的谷氨酰胺转胺酶,优化的凝胶层析的条件,上样量6mL,流速为0.25 mL/min;离子交换层析的上样量50 mL,流速为3 mL/min.酶被纯化了4.22倍,比活力达17.33 U/mg蛋白,回收率为77.5％.液相色谱-串联质谱鉴定、蛋白质数据库比对结果表明,纯酶与AAN01353是同种蛋白质.     

高效阳离子交换法分离纯化蛋清中的溶菌酶

 建立了用高效阳离子交换分离纯化蛋清中溶菌酶的新方法 ,讨论了纯化的工艺条件。蛋清样品匀浆后 ,用氯化钠初步纯化 ,然后用弱阳离子交换柱XIDACE WCX分离。结果表明 ,被纯化的溶菌酶和杂蛋白得到很好分离。经活性检测 ,溶菌酶过柱后的活性回收率为 10 7% ,蛋白的比活为 15 4 6 7U/mg ,纯化倍数提高了 5 6倍。用尺寸排阻 (SEC)鉴定 ,得到的溶菌酶呈均一性。该法较传统软基质低压离子交换分离速度快 ,纯化效率高。     

Purification of L-Lysine in Simulated Moving Bed and Fixed-Bed Chromatography

 L-Lysine was produced by a microbial process utilizing a Corynebacterium glutamicum (ATCC 21799) strain. L-Lysine was purified from the cultivated medium by fixed-bed and simulated moving bed （SMB） chromatography. The separation conditions including pH, eluent concentration and Lys+ and Lys2+ adsorption isotherms were studied in batch adsorption. The column capacity, eluent flow rate and eluent concentration have been studied in fixed-bed chromatography. Maximum purification rate of lysine was obtained as 0.066 g/(g·h) (per gram resin and per hour) at an eluent flow rate of 10 mL/min in fixed-bed chromatography. The results obtained from SMB were 0.11 g/(g·h) for L-lysine purification rate and 96% for L-lysine recovery.     

Renaturation with simultaneous purification of rhG-CSF from Escherichia coli by ion exchange chromatography

Protein refolding is a key step for the production of recombinant proteins, especially at large scales, and usually their yields are very low. Application of liquid chromatography to protein refolding is an exciting step forward for this field. In this work, recombinant human granulocyte colony-stimulating factor (rhG-CSF) expressed in Escherichia coli was renatured with simultaneous purification by ion exchange chromatography (IEC) with a Q Sepharose FF column. Several chromatographic parameters affecting the refolding yield of the denatured/reduced rhG-CSF, such as the urea concentration, pH value, concentration and ratio of reduced/oxidized glutathione in the mobile phase, as well as the flow rate of the mobile phase, were investigated in detail and indicated that the urea concentration and the pH value were of great importance. At the optimal conditions, the renatured and purified rhG-CSF was found to have a specific bioactivity of 3.0 x 10(8) IU/mg, a purity of 96%, and a mass recovery of 49%. Compared with the usual dilution method, the IEC method developed here is more effective for rhG-CSF refolding in terms of specific bioactivity and mass recovery.     

Purification of rat liver soluble catechol-O-methyltransferase by high performance liquid chromatography

The soluble form of catechol-O-methyltransferase (EC 2.1.1.6) from rat liver was purified to homogeneity by high-performance anion-exchange chromatography and high-performance gel-filtration chromatography. The specific activity of the final pool was 270 U/mg protein. The purification was 1180-fold and recovery of the enzyme activity was 15%. During this rapid and gentle purification there were no problems with loss of activity, and the estimated half of the final purified enzyme pool was 5.5 days at +4 degrees C. The only additive used was phenylmethylsulfonylfluoride in the homogenizing buffer.     

Purification of low-abundance lysozyme in egg white via free-flow electrophoresis with gel-filtration chromatography

As an effective separation tool, free-flow electrophoresis has not been used for purification of low-abundance protein in complex sample matrix. Herein, lysozyme in complex egg white matrix was chosen as the model protein for demonstrating the purification of low-content peptide via an FFE coupled with gel fitration chromatography (GFC). The crude lysozyme in egg while was first separated via free-flow zone electrophoresis (FFZE). After that, the fractions with lysozyme activity were condensed via lyophilization. Thereafter, the condensed fractions were further purified via a GFC of Sephadex G50. In all of the experiments, a special poly(acrylamide- co-acrylic acid) (P(AM-co-AA)) gel electrophoresis and a mass spectrometry were used for identification of lysozyme. The conditions of FFZE were optimized as follows: 130 μL/min sample flow rate, 4.9 mL/min background buffer of 20 mM pH 5.5 Tris-Acetic acid, 350 V, and 14 °C as well as 2 mg/mL protein content of crude sample. It was found that the purified lysozyme had the purity of 80% and high activity as compared with its crude sample with only 1.4% content and undetectable activity. The recoveries in the first and second separative steps were 65% and 82%, respectively, and the total recovery was about 53.3%. The reasons of low recovery might be induced by diffusion of lysozyme out off P(AM-co-AA) gel and co-removing of high-abundance egg ovalbumin. All these results indicated FFE could be used as alternative tool for purification of target solute with low abundance.     

Preparation of a monolithic column for weak cation exchange chromatography and its application in the separation of biopolymers

A procedure for the preparation of a monolithic column for weak cation exchange chromatography was presented. The structure of the monolithic column was evaluated by mercury intrusion. The hydrodynamic and chromatographic properties of the monolithic column--such as back pressures at different flow rates, effects of pH on protein retention, dynamic loading capacity, recovery, and stability--were determined under conditions typical for ion-exchange chromatography. The prepared monolithic column might be used in a relatively broad pH range from 4.0 to 12.0 and exhibited an excellent separation to five proteins at the flow rates of both 1.0 and 8.0 mL/min, respectively. In addition, the prepared column was first used in the purification and simultaneous renaturation of recombinant human interferon gamma (rhIFN-gamma) in the extract solution with 7.0 mol/L guanidine hydrochloride. The purity and specific bioactivity of the purified rhIFN-gamma in only one chromatographic step were obtained to be 93% and 7.8 x 10(7) IU/mg, respectively.     

Urease purification from the seeds ofCajanus Cajan and its application in a biosensor construction

Urease has been purified from the seeds of Cajanus Cajan. The purification process involves three solvent extraction steps followed by DEAE-cellulose column chromatography. The specific activity of the purified enzyme is found to be 1920 U/mg with the recovery of 8%. The application of the purified enzyme in a biosensor construction is discussed.     

采用不同疏水相互作用色谱柱从包涵体中快速制备重组人干细胞因子

为了提高重组人干细胞因子(rhSCF)的复性效率,改进了高效疏水相互作用色谱(HPHIC)纯化和复性rhSCF的方法。首先将目标蛋白溶解于8.0 mol/L脲中,然后将rhSCF包涵体的提取液直接进样到不同规格的HPHIC柱进行纯化和复性。优化了固定相配基结构和流动相组成等实验条件,结果表明,本方法可以快速地获得高质量回收率和高生物活性的rhSCF,rhSCF在40 min内即可完成复性与纯化,目标蛋白的纯度在95.5%以上,质量回收率高于49.6%。通过体积排阻色谱和基质辅助激光解吸离子化飞行时间质谱(MALDI-TOF-MS)的分析,确认rhSCF以单体存在。结果进一步证明HPHIC法是同时复性和纯化重组蛋白的有效工具。