一种新型的琼脂糖疏水层析介质开发及其在重组乙肝表面抗原(CHO-HBsAg)分离纯化中的应用

以粒径均一的国产高交联度快速流琼脂糖为基质,采用活化、交联等步骤合成了针对分离纯化CHO-HBsAg的3C间臂的丁基琼脂糖疏水介质,通过控制丁基配基密度提高分离HBsAg的纯化倍数和回收率,获得了纯化倍数约20、HBsAg回收率约80%的介质。评估了合成介质的理化性质,流速为500cm/h时柱压力小于0.06MPa,表明介质具有较高的机械强度和良好的流动性能,介质经过酸、碱、变性剂等处理后化学性质稳定。将介质合成工艺进一步放大到2L介质/批,应用到HBsAg分离纯化的三步层析整和工艺中,结果表明,批量合成的疏水介质,HBsAg回收率与进口介质相当,HBsAg终产品纯度在95%以上,符合国家药典要求。最后考察了介质合成批次间的配基密度的可控性和单批次合成介质的重复使用性,结果表明,合成工艺和介质的重复性能满足产业化要求,这种成本低的介质有望替代目前工业生产广泛使用的进口疏水介质。     

一种新型的琼脂糖疏水层析介质开发及其在重组乙肝表面抗原（CHOHBsAg）分离纯化中的应用

以粒径均一的国产高交联度快速流琼脂糖为基质,采用活化、交联等步骤合成了针对分离纯化CHOHBsAg的3C间臂的丁基琼脂糖疏水介质,通过控制丁基配基密度提高分离HBsAg的纯化倍数和回收率,获得了纯化倍数约20、HBsAg回收率约80%的介质。评估了合成介质的理化性质,流速为500cm/h时柱压力小于0.06MPa,表明介质具有较高的机械强度和良好的流动性能,介质经过酸、碱、变性剂等处理后化学性质稳定。将介质合成工艺进一步放大到2L介质/批,应用到HBsAg分离纯化的三步层析整和工艺中,结果表明,批量合成的疏水介质,HBsAg回收率与进口介质相当, HBsAg终产品纯度在95%以上,符合国家药典要求。最后考察了介质合成批次间的配基密度的可控性和单批次合成介质的重复使用性,结果表明,合成工艺和介质的重复性能满足产业化要求,这种成本低的介质有望替代目前工业生产广泛使用的进口疏水介质。     

不同配基密度离子交换介质对CHO表达的乙肝抗原纯化的影响

中华仓鼠卵巢细胞(CHO)表达的重组乙肝病毒表面抗原(HBs Ag)为糖基化蛋白。本文主要采用多步层析法,在离子交换层析分别使用1批进口厂家A和2批国产厂家B(配基密度各不相同)的DEAE离子介质(均为交联琼脂糖含量6%,配基密度范围110-160μmol/ml)。通过对比发现,在范围内波动的不同配基密度,抗原最适洗脱盐浓度不同。配基密度越大,所需洗脱盐浓度越高。需要精确控制每种配基密度的洗脱盐浓度,在保证质量的情况下,提高抗原收率。     

乳腺生物反应器表达的重组人乳铁蛋白的分离纯化及生物活性鉴定

以国产高交联度的快流速琼脂糖为基质,合成了不同配基密度的SP(Sulfopropyl,磺酸基)离子交换介质,建立了乳腺生物反应器表达重组人乳铁蛋白(Recombinant Human Lactoferrin,rHLF)的纯化方法。以溶菌酶为模型蛋白考察了不同配基密度离子交换介质的静态和动态吸附行为,结果表明介质具有良好的吸附性能。不同配基密度离子交换介质均可纯化得到rHLF,其中,高配基密度(0.24mol/L)的离子交换介质每毫升可以处理50mL rHLF牛乳,rHLF收率为86.5%,纯度为98.5%。圆二色谱的测定结果表明纯化的rHLF二级结构与天然人乳铁蛋白一致。生物学功能实验结果表明,rHLF的铁结合与释放活性与天然人乳铁蛋白相似,浓度为5g/L的rHLF对大肠杆菌的生长具有明显的抑制作用。     

产HBsAg CHO细胞无血清培养研究

在分析CHO C2 8细胞对培养基中氨基酸利用的基础上 ,对DMEM培养基进行初步优化。再采用统计学正交分析方法 ,在初步优化的DMEM培养基中添加胰岛素、转铁蛋白等促细胞生长因子 ,建立了一种适于CHO C2 8细胞持续用无血清培养基———CHO C2 8 SFM。经转瓶维持实验 ,在CHO C2 8 SFM中维持培养的细胞 ,其乙型肝炎表面抗原 (HBsAg)表达水平达到用含 5 %FBS培养液维持的 70 %～ 80 % ,但纯化收率提高 1 0 %以上 ,可用于大规模生产。     

亲和介质及溶液条件对蛋白质溶液中内毒素去除的影响

生物制品中内毒素的去除是一项十分重要的工作。为了更好地去除各种生物制品中的内毒素,采用合成的多粘菌素B琼脂糖亲和介质,通过静态吸附的方法去除蛋白质溶液中的内毒素。重点考察了介质的间臂长度、配基密度以及各种溶液条件(pH值、盐种类和浓度、蛋白质种类和浓度、内毒素浓度、添加剂等)对内毒素去除率及蛋白质回收率的影响。分别采用动态浊度法和Lowry法检测内毒素含量和蛋白质浓度。结果表明该介质具有载量高、去除速度快、去除率高、可重复使用的特点。此外,配基密度、pH值、盐浓度和蛋白质特性(等电点和疏水性)对内毒素去除效果均有重要影响。在优化的条件下,血红蛋白、人血清白蛋白和溶菌酶的回收率分别达到87.2%、73.4%和97.3%,相应的内毒素去除率分别达到99.8%、97.9%和99.7%。阐明了各种因素对内毒素去除率和蛋白质回收率的影响规律,为生物制品中内毒素的高效去除提供了参考。     

疏水层析分离正确折叠与错误折叠的复合干扰素

采用疏水层析纯化重组复合干扰素,成功去除了复性过程中产生的错误折叠体、聚集体及杂蛋白,并考察了配基类型、盐浓度、pH值和流速对疏水层析纯化效果的影响,结果表明采用ButylSepharose 4FastFlow、硫酸铵初始浓度0.8mol/L、缓冲液pH值8.3、线流速为90cm h时疏水层析纯化效果最佳,最终目标蛋白反相高效液相色谱检测纯度达到99.6% ,还原及非还原型SDS PAGE电泳均呈单一条带,其比活为2.3×10⁹IU/mg,回收率为36.7%。     

金黄色葡萄球菌蛋白A (SpA) Z结构域串联体的克隆、表达和筛选

筛选一种高效重组金黄色葡萄球菌蛋白A(SpA)用于制备抗体纯化亲和介质。首先通过基因操作获得金黄色葡萄球菌蛋白A(SpA)的Z结构域单体、二串体、三串体、四串体和五串体基因,将目的基因分别克隆至pET-22b表达载体并转化至大肠杆菌BL21(DE3)感受态细胞,获得不同串联个数的Z结构域基因工程菌,经诱导表达和Ni2+亲和层析纯化得到Z结构域单体和二-五串体蛋白。纯化后的目的蛋白偶联至琼脂糖凝胶作为亲和层析介质,对人免疫球蛋白G(IgG)进行分离纯化。分析比较Z结构域串联体蛋白产量及其偶联的亲和介质对抗体吸附载量的差异。结果表明,构建的Z结构域单体、二串体、三串体、四串体和五串体基因工程菌能有效表达目的蛋白,制备的凝胶亲和介质可特异性吸附人IgG。增加Z结构域串联数,重组蛋白产量和单位摩尔数多聚体蛋白吸附载量获得提高,其中,重组四串体蛋白产量大(160 mg/10 g湿菌体),对抗体的吸附载量高(34.4 mg人IgG/mL胶),更适合作为配基用于亲和层析介质的制备。     

基于分子模拟的离子交换层析中静电相互作用研究

将分子模拟方法引入到蛋白质离子交换层析中的静电相互作用研究。选用蛋清溶菌酶和牛胰凝乳蛋白酶为模型蛋白质,阳离子交换吸附剂SP Sepharose FF等为模型层析介质。从蛋白质数据库(PDB)中获得蛋白质三维结构数据,分析了介质孔径和配基分布,以点电荷模拟离子交换层析介质的功能配基,构筑了蛋白质-介质配基模拟表面体系。采用MCCE、Delphi和GRASP等程序包进行了分子模拟计算,考察了作用方向、作用距离、盐浓度、pH等对蛋白质和模拟配基平面间静电相互作用的影响。结果表明,宏观的层析平衡常数与微观分子模拟计算的相互作用能量参数间存在良好的线性关系。     

乳腺生物反应器表达产物层析分离过程中介质的污染机理及其再生策略

考察了磺酸基离子交换层析介质 (SP Sepharose FF) 在分离表达人乳铁蛋白的重组牛乳过程中的污染机理及其再生策略。通过层析原料及流分中各组分含量的检测分析,发现牛乳中的脂类通过堵塞效应或疏水相互作用残留在层析柱上,造成层析运行压力升高;部分酪蛋白通过静电相互作用占据介质的配基位点,导致介质的交换容量降低;乳糖与介质之间无直接相互作用。连续层析运行次数的增加以及层析-再生时间间隔的延长,均能导致残留组分和介质之间的相互作用逐渐增强,最终影响介质的再生效率。使用NaOH进行及时清洗,可以有效地清除柱上残留的脂类和蛋白,恢复离子交换介质的层析性能和微观形态。     

A highly efficient hydrophobic interaction chromatographic absorbent improved the purification of hepatitis B surface antigen (HBsAg) derived from Hansenula polymorpha cell

To improve the purification efficiency of recombinant hepatitis B surface antigen derived from Hansenula polymorpha (Hans-HBsAg), a serial of absorbents for hydrophobic interaction chromatography with the controllable ligand density and spacer arm were synthesized, then developed and further applied to purify Hans-HBsAg. The absorbent, Butyl-S QZT with the ligand density of 25 μmol/(g wet gel) and spacer arm of 3C, was screened out and its physical and chemical properties were evaluated. High rigidity and low backpressure (<0.06 MPa) were obtained at the flow rate up to 20 ml/min. Moreover, it has the stable chemical characteristics of subjecting to high concentrations of acid, alkali and detergents. This HIC absorbent was further applied to purify Hans-HBsAg with the recovery 94% and purification-fold 9 under the optimized operation condition at pH 6.5 and concentration of ammonium sulfate 7.5%. Finally, the HIC adsorbent of Butyl-S QZT was applied in the integrated three-step chromatographic purification process to purify Hans-HBsAg. About 140 mg of purified Hans-HBsAg was obtained from 1 l cell disruption supernatant at the total recovery of 27% and the purification-fold of 151.8. Based on the assay of SDS-PAGE and SEC-HPLC, the purity of the purified HBsAg was over 99% to meet the requirement for the further inoculation use.     

Protein A immobilized affinity cartridge for immunoglobulin purification

Recombinant Protein A was immobilized on a cellulose and acrylic composite matrix through Schiff base formation. Various factors that could affect the binding of immunoglobulin by the Protein A molecules immobilized on the solid matrix were studied to achieve optimum affinity purification. The spacer arm length and ligand concentration of Protein A were verified as factors crucial to optimized IgG purification. Liquid-phase environmental conditions such as pH and salt concentration also play important roles in adsorption capacity by affecting the molecular interaction between IgG and the immobilized Protein A. The rate of interaction between Protein A and IgG is rather fast, with minimal differences observed at 10-fold increases in the cartridge loading rate. This paper describes a cellulose/acrylic composite matrix for immobilizing Protein A, at an optimized ligand concentration, installed on a spacer arm of adequate length, to purify immunoglobulins from animal plasma. The fast-flow property of the cartridge made from such a matrix and its simplicity in operation provide effective means for purifying immunoglobulins on a relatively large scale.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30-60 and 1,4-butanediol-diglycidyl ether: 16-36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a Mr of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and processcompatible alternative to other types of chromatography.     

Immobilized metal affinity chromatography of monoclonal immunoglobulin M against mutant amidase from Pseudomonas aeruginosa

The chromatographic behavior of monoclonal antibodies (MAbs) of immunoglobulin (Ig) M class against mutant (T103I) amidase from Pseudomonas aeruginosa was investigated on immobilized metal chelates. The effect of ligand concentration, the length of spacer arm, and the nature of metal ion were investigated in immobilized metal affinity chromatography (IMAC). The MAbs against mutant amidase adsorbed to Cu(II), Ni(II), Zn(II), Co(II), and Ca(II)-iminodiacetic acid (IDA) agarose columns. The increase in ligand concentration (epichlorohydrin: 30–60 and 1,4-butanediol-diglycidyl ether: 16–36) resulted in higher adsorption to IgM into immobilized metal chelates. The length of spacer arm was found to affect protein adsorption, as longer spacer arm (i.e., 1,4-butanediol-diglycidyl ether) increased protein adsorption of immobilized metal chelates. The adsorption of IgM onto immobilized metal chelates was pH dependent because an increase in the binding of IgM was observed as the pH varied from 6.0 to 8.0. The adsorption of IgM to immobilized metal chelates was the result of coordination of histidine residues to metal chelates that are available in the third constant domain of heavy chain (CH3) of immunoglobulins, as the presence of imidazole (5 mM) in the equilibration buffer abolished the adsorption of IgM to the column. The combination of tailor-made stationary phases for IMAC and a correct design of the adsorption parameters permitted to devise a one-step purification procedure for IgM. Culture supernatants containing IgM against mutant amidase (T103I) were purified either by IMAC on EPI-60-IDA-Co (II) column or by gel filtration chromatography on Sephacryl S-300HR. The specific content of IgM and final recovery of antibody activity exhibited similar values for both purification schemes. The purified preparations of IgM obtained by both schemes were apparently homogeneous on native polyacrylamide gel electrophoresis with a M _r of 851,000 Da. The results presented in this work strongly suggest that one-step purification of IgM by IMAC is a cost-effective and process-compatible alternative to other types of chromatography.     

Production of polygalacturonase from <Emphasis Type="Italic">Coriolus versicolor</Emphasis> grown on tomato pomace and its chromatographic behaviour on immobilized metal chelates

Tomato pomace and pectin were used as the sole carbon sources for the production of polygalacturonase from a strain of Coriolus versicolor in submerged culture. The culture of C. versicolor grown on tomato pomace exhibited a peak of polygalacturonase activity (1,427 U/l) on the third day of culture with a specific activity of 14.5 U/mg protein. The production of polygalacturonase by C. versicolor grown on pectin as a sole carbon source increased with the time of cultivation, reaching a maximum activity of 3,207 U/l of fermentation broth with a specific activity of 248 U/mg protein. The levels of different isoenzymes of polygalacturonase produced during the culture growth were analysed by native PAGE. Differential chromatographic behaviour of lignocellulosic enzymes produced by C. versicolor (i.e. polygalacturonase, xylanase and laccase) was studied on immobilized metal chelates. The effect of ligand concentration, pH, the length of spacer arm and the nature of metal ion were studied for enzyme adsorption on immobilized metal affinity chromatography (IMAC). The adsorption of these lignocellulosic enzymes onto immobilized metal chelates was pH-dependent since an increase in protein adsorption was observed as the pH was increased from 6.0 to 8.0. The adsorption of polygalacturonase as well as other enzymes to immobilized metal chelates was due to coordination of histidine residues which are available at the protein surface since the presence of imidazole in the equilibration buffer abolished the adsorption of the enzyme to immobilized metal chelates. A one-step purification of polygalacturonase from C. versicolor was devised by using a column of Sepharose 6B-EPI 30-IDA-Cu(II) and purified enzyme exhibited a specific activity of about 150 U/mg protein, final recovery of enzyme activity of 100% and a purification factor of about 10. The use of short spacer arm and the presence of imidazole in equilibration buffer exhibited a higher selectivity for purification of polygalacturonase on this column with a high purification factor. The purified enzyme preparation was analysed by SDS-PAGE as well as by "in situ" detection of enzyme activity.     

Purification of lactoperoxidase from creek-water buffalo milk and investigation of kinetic and antibacterial properties

Water buffalo lactoperoxidase (WBLP) was purified with Amberlite CG 50 H+ resin, CM Sephadex C-50 ion-exchange chromatography, and Sephadex G-100 gel filtration chromatography from skim milk. All purification steps of the WBLP were shown with SDS-PAGE and Rz (A412/A280) controlled the purification degree of the enzyme. Rz value for the purified WBLP was 0.8. To determine purification steps and kinetic properties, the activity of enzyme was measured by using 2,2-azino-bis-(3-ethylbenzthiazoline-6 sulfonic acid) diammonium salt (ABTS) as a choromogenic substrate at pH=6. Km, Vmax, optimum pH, and optimum temperature for the WBLP were found by means of graphics for ABTS as substrates. Optimum pH and optimum temperature of the WBLP were 6 and 60 degrees C, respectively. Km value at optimum pH and optimum temperature for the WBLP was 0.82 mM. Vmax value at optimum pH and optimum temperature was 13.7 micromol/mL x min. Km value at optimum pH and 25 degrees C for the WBLP was 0.77 mM. Vmax value at optimum pH and 25 degrees C was 4.83 micromol/mL x min. The purified WBLP was found to have high antibacterial activity in a thiocynate-H2O2 medium for some pathogenic bacteria, such as Escherichia coli, Klebsiella pneumoniae, Pseudomonas aeruginose, Shigella sonnei, Staphylococcus saphrophyticus, Staphylococcus epidermidis, and Shigella dysenteriae and compared with well known antibacterial substances such as tetracycline, penicillin, and netilmicine.     

Use of magnetic poly(glycidyl methacrylate) monosize beads for the purification of lysozyme in batch system

The hydrophobic affinity ligand L-tryptophan immobilized magnetic poly(glycidyl methacrylate) [m-poly(GMA)] beads in monosize form (1.6 microm in diameter) were used for the affinity purification of lysozyme from chicken egg white. The m-poly(GMA) beads were prepared by dispersion polymerization in the presence of Fe3O4 nano-powder. The epoxy groups of the m-poly(GMA) beads were converted into amino groups with 1,6 diaminohexane (i.e., spacer arm). l-tryptophan was then covalently immobilized on spacer arm attached m-poly(GMA) beads. Elemental analysis of immobilised L-tryptophan for nitrogen was estimated as 42.5 micromol/g polymer. Adsorption studies were performed under different conditions in a batch system (i.e., medium pH, protein concentration and temperature). Maximum lysozyme adsorption amount of m-poly(GMA) and m-poly(GMA)-L-tryptophan beads were 1.78 and 259.6 mg/g, respectively. The applicability of two kinetic models including pseudo-first order and pseudo-second order model was estimated on the basis of comparative analysis of the corresponding rate parameters, equilibrium adsorption capacity and correlation coefficients. Results suggest that chemisorption processes could be the rate-limiting step in the adsorption process. It was observed that after 10 adsorption-elution cycle, m-poly(GMA)-L-tryptophan beads can be used without significant loss in lysozyme adsorption capacity. Purification of lysozyme from egg white was also investigated. Purification of lysozyme was monitored by determining the lysozyme activity using Micrococcus lysodeikticus as substrate. It was found to be successful in achieving purification of lysozyme in a high yield of 76% with a purification fold of 71 in a single step. The specific activity of the eluted lysozyme (62,580 U/mg) was higher than that obtained with a commercially available pure lysozyme (Sigma (60,000 U/mg).     

Purification of hepatocyte growth factor using polyvinyldiene fluoride-based immobilized metal affinity membranes: equilibrium adsorption study

Polyvinyldiene fluoride (PVDF)-based affinity membranes with immobilized copper ions were developed in this study. The resulting membranes were tested for their adsorption properties using a model protein, lysozyme, in batch mode. First, different lengths of diamine were utilized as spacer arms to immobilize the metal ions onto the membranes. It was found that the application of 1,8-diaminooctane as the spacer arm led to the highest adsorption capacity. Moreover, the effects of pH and salt concentration were investigated to distinguish the proportion of specific and nonspecific interactions. A big fraction of lysozyme adsorption capacity for the immobilized metal affinity membranes was considered to come from nonspecific electrostatic interactions, which could be reduced by increasing salt concentration. Lastly, the purification of hepatocyte growth factor (HGF) from insect cell supernatant was performed using the immobilized metal affinity membranes in batch mode. HGF was found in the elution condition using EDTA, indicating the successful purification of HGF.