烟草磷酸吡哆醛水解酶的分离纯化与表征

采用硫酸铵沉淀、DEAE-Sepharose Fast Flow阴离子交换、Sephadex G-100凝胶过滤和SP Sephadex C-25阳离子交换柱层析等步骤,对烟草磷酸吡哆醛水解酶进行了分离纯化。结果表明:该酶被纯化了119.6倍,得率为28.49%,经凝胶过滤和SDS-PAGE测得该酶的全分子量为49.6kDa,亚基分子量约为25kDa;该酶最适温度为50℃,最适反应pH为5.5;Mg2+、Ca2+、Mn2+等对该酶有激活作用,金属离子螯合剂EDTA对酶有抑制作用,加入Mg2+后抑制作用得到解除;在最适反应条件下,测得反应底物磷酸吡哆醛(PLP)和磷酸吡哆胺(PMP)的Km值分别为0.23mmol/L和0.56mmol/L。     

烟草吡哆胺 丙酮酸转氨酶的部分纯化与表征

通过冷冻干燥、DEAE Sepharose Fast Flow阴离子交换柱层析、Sephadex G 100凝胶过滤柱层析,SP葡聚糖凝胶C 25阳离子交换柱层析等分离纯化技术,对烟草吡哆胺 丙酮酸转氨酶进行分离纯化。采用苯肼衍生化方法检测活性,并对其基本酶学性质进行分析。结果显示：该酶被纯化了92.34倍;最适温度为70 ℃,最适pH为9.0。在pH7.0～9.0内稳定且热稳定性较好,80 ℃保温3 h仍有51.55%的酶活力;在最适反应条件下,测得反应底物吡哆胺和丙酮酸的Km值分别为6.337 mmol?L 1和0.867 mmol?L 1。该结果为进一步研究烟草体内VB6代谢机制奠定了基础。     

金属螯合亲和层析法纯化抗乙肝核心抗原单克隆抗体

采用金属螯合亲和层析法,纯化了小鼠腹水来源的抗乙肝核心抗原单克隆抗体,对上样缓冲液的pH和离子强度、洗脱液种类和洗脱方式进行优化。结果表明,采用降低pH分步洗脱时,最佳上样缓冲液为pH8.0,20mmol/LPB+0.5mol/LNaCl,抗体在pH5.0被洗脱下来,抗体回收率80%,纯度85%。采用咪唑浓度梯度洗脱时,最佳的上样缓冲液为pH8.0,20mmol/LPB+5mmol/L咪唑,抗体纯度大于95%,回收率65%;在上样缓冲液中不添加NaCl而添加少量的咪唑,更有利于抗体分离。以上洗脱方式都能较好地保持mAb的生物学活性,为该抗体的应用提供了必要的实验基础。     

猪圆环病毒2型病毒样颗粒的高效组装技术研究*

目的:探索猪圆环病毒2型(PCV2)病毒样颗粒(VLPs)的高效组装技术,提高VLPs的稳定性。方法:利用大肠杆菌表达PCV2 Cap蛋白自组装为VLPs,分析不同离子强度下VLPs的稳定性。利用切向流技术添加尿素,降低pH,可使VLPs解组装,利用硫酸铵分级沉淀、阴离子交换层析纯化获得Cap蛋白,去除尿素,提高离子强度和pH,实现VLPs的高效再组装。结果:PCV2 Cap蛋白自组装VLPs在150mmol/L NaCl下稳定性较差,而在500mmol/L NaCl下可提高VLPs的稳定性,但仍较易发生聚集,核酸含量均较高。在150mmol/L NaCl、300mmol/L尿素和pH 5.5的缓冲体系条件下,能够使VLPs解组装。经25%~50%饱和硫酸铵(V/V)分级沉淀粗纯,阴离子交换层析500mmol/L NaCl下洗脱获得精纯Cap蛋白,蛋白质纯度≥95%,并能够有效去除核酸。通过切向流技术去除体系中的尿素,并将NaCl浓度提高至1mol/L、pH提高至8.0,改变蛋白质表面静电荷分布,实现VLPs的高效、均一再组装,组装效率≥99%,回收率为65.85%,并明显提高VLPs的稳定性,能够稳定保存6个月以上。结论:利用硫酸铵分级沉淀、阴离子交换层析纯化获得Cap蛋白,去除尿素,提高离子强度和pH,实现VLPs的高效再组装。     

鲍曼不动杆菌烈性噬菌体的分离与纯化

利用柱层析方法,纯化鲍曼不动杆菌（Acinetobacter baumannii）烈性噬菌体AB1。首先采用聚乙二醇6000沉淀方法,初步分离裂解液中的噬菌体,噬菌体纯度由6.1×1010 pfu/mg提高到37×1010 pfu/mg,噬菌体回收率为58.8%,蛋白质去除率为90.6%;噬菌体粗提样品经Sepharose 4B凝胶过滤层析柱进一步纯化,纯度提高到73×1010 pfu/mg,噬菌体回收率为95.7%,蛋白质去除率为48.1%;收集的噬菌体样品最后经DEAE-52阴离子交换层析柱处理,噬菌体纯度为40×1010 pfu/mg,回收率为50.8%,蛋白去除率15.6%。内毒素分析结果显示,Sepharose 4B凝胶过滤层析纯化的噬菌体样品中,内毒素含量为443.8 EU/mg,而DEAE-52阴离子交换层析纯化的噬菌体样品中,内毒素含量为544.4 EU/mg。实验结果显示,PEG沉淀方法与Sepharose 4B凝胶过滤方法能够有效地提高噬菌体纯度,而DEAE-52阴离子交换层析则不能提高噬菌体的纯度,也无法有效地去除样品中的内毒素。     

阴离子交换色谱纯化甲型肝炎病毒(YN5株)的研究

对阴离子交换色谱纯化HAV的合适条件进行了探索。先使用“试管法”研究DEAE Sepharose Fast Flow凝胶结合HAV及病毒解离的条件,然后分别使用线性阶段洗脱和阶段梯度洗脱在柱色谱上进行了HAV的纯化。结果表明经过阴离子交换色谱纯化得到的病毒保持有抗原性和免疫原性,HAV抗原回收率大于85％,杂蛋白去除率大于80％,纯化的病毒样品中的内毒素与宿主DNA的含量也大大降低,证明阴离子交换色谱可用于HAV疫苗的纯化。     

离子交换树脂纯化还原型谷胱甘肽(GSH)的研究

研究005×7阳离子交换树脂分离纯化谷胱甘肽(GSH)的工艺条件。考察了005×7阳离子交换树脂对GSH的静态吸附量,洗脱时铵离子浓度、洗脱流速等对分离纯化产品GSH的影响。根据试验结果确定最佳工艺条件为:最适上柱pH为3.0,洗脱流速为:2.4ml/min,洗脱液为0.5mol/L的NH4Cl溶液;收集洗脱液,浓缩,乙醇沉淀,真空冷冻干燥,用高效液相色谱检测产品GSH,所得GSH纯度为60.8%,GSH的平均收得率为61.3%。说明此分离纯化GSH工艺可行。     

重组E．coli胆固醇氧化酶的分离纯化及其酶学性质研究

对重组E.coli产生的胆固醇氧化酶采用70%硫酸铵盐析、CM Sepharose FF离子层析、Phenyl Sepharose 6 Fast疏水层析、Sephadex G-75凝胶过滤,得到的胆固醇氧化酶在SDS-PAGE上呈单一蛋白质条带,酶的纯化倍数为93,收率为21%.部分酶学性质表明:酶的最适反应温度为37℃,最适反应pH7.5,热稳定范围在40℃以下,酶的pH稳定范围为6～9,分子量分别为50 kD和52 kD.酶动力学参数Km值及Vmax分别为8.2×10-5 mol/L和0.21 mmol/(L.min).     

肝素纯化工艺中离子交换树脂的选择与应用研究

研究比较了5种树脂对肝素的吸附能力,从中选出S5428阴离子交换树脂来纯化肝素。通过对各因素的研究,确定了树脂对肝素的静态、动态吸附以及解吸的最佳条件。结果表明:静态吸附的温度45℃,pH 8.0的条件下吸附2 h,肝素的吸附率为90.5%;层析柱的动态吸附温度45℃,肝素溶液进样浓度1.0 mg/mL,进样速度1.5 mL/min,树脂柱能处理1.5 BV肝素液而不发生泄露,吸附量为3.05 mg/mL,达到饱和吸附时可处理4BV的料液,吸附量为9.18 mg/mL;采用2.0 mol/L NaCl洗脱,洗脱流速1.5 mL/min,肝素解吸率可达95.8%,肝素效价可达150 U/mg,效价回收率98%。     

河豚毒素中和性单抗的制备、鉴定及TTX检测方法的建立

目的研制河豚毒素中和性单抗,建立基于河豚毒素单抗的河豚毒素检测方法。方法用TTX-KLH免疫Balb/c小鼠,用TTX-BSA间接ELISA筛选,建立杂交瘤细胞系,腹腔接种Balb/c小鼠诱生腹水,Protein A Sepharose CL4B亲和柱纯化,SDS-PAGE、间接ELISA鉴定;用常规法确定TTX对昆明小鼠的LD50;将单抗和TTX混合物注入小鼠腹腔,检测单抗对TTX的中和能力;建立检测TTX的竞争ELISA法。结果获得了2株TTX中和性单抗,腹水用Protein A Sepharose CL 4B纯化后抗体纯度大于95%;常规间接ELISA检测,显示单抗5E7的结合能力高于5E4。单抗对2 LD50 TTX攻击昆明小鼠的保护率为50%,建立了基于中和性单抗的TTX检测方法,TTX的最小检出浓度为1.56μg/mL。结论获得了TTX中和性单抗,对致死剂量TTX攻击昆明小鼠的保护率为50%,建立了基于中和性单抗的TTX检测方法,TTX的最小检出浓度为1.56μg/mL。     

以聚乙二醇为层析伴侣同时制备SOD、过氧化氢酶和血红蛋白

发展了一条从红细胞裂解液中同时制备超氧化物歧化酶(SOD)、过氧化氢酶和血红蛋白的新工艺。采用0 75 %的聚乙二醇600作为层析伴侣,使血红蛋白直接流过阴离子交换层析柱,同时吸附SOD和过氧化氢酶。经过梯度洗脱获得SOD和过氧化氢酶组分,再经过疏水性相互作用层析与凝胶过滤层析相串联,使SOD和过氧化氢酶得到纯化。纯化后的SOD和过氧化氢酶的比活力分别达到15932u/mg和65918u/mg ,血红蛋白的纯度达到99.9%以上。总回收率为:SOD ,47.4% ;过氧化氢酶,29.6% ;血红蛋白,88.7%。     

Isolation and purification of lactoferrin and immunoglobulin G from bovine colostrum with serial cation-anion exchange chromatography

High-value dairy proteins such as lactoferrin (LF) and immunoglobulin (IgG) were separated from bovine colostrum. The whey was initially adjusted to pH 6.8 with 1 mol/L NaOH and then went through centrifugation, precipitation, and filtration to eliminate the fat and caseins in bovine colostrum. The treated whey was further ultra-filtrated to partially remove both other proteins and carbohydrates under 50 kD molecular weight. Then the ultra-filtrated whey was passed through cation and anion exchange columns in series. The LF and IgG were adsorbed on cation and anion exchanger, respectively, due to their different pI. Both the cation and anion exchange columns were washed with de-ionized water followed by successive elution with sodium chloride solutions of increasing molarities (0.27 and 0.85 mol/L; 17 and 51 mmol/L) in a stepwise manner, respectively. After desalted, the elution was freeze-dried. Finally, the LF and IgG with respective purities of 95.0% and 96.6% were obtained.     

Systematic interpolation method predicts protein chromatographic elution with salt gradients,pH gradients and combined salt/pH gradients

A methodology is presented to predict protein elution behavior from an ion exchange column using both individual or combined pH and salt gradients based on high‐throughput batch isotherm data. The buffer compositions are first optimized to generate linear pH gradients from pH 5.5 to 7 with defined concentrations of sodium chloride. Next, high‐throughput batch isotherm data are collected for a monoclonal antibody on the cation exchange resin POROS XS over a range of protein concentrations, salt concentrations, and solution pH. Finally, a previously developed empirical interpolation (EI) method is extended to describe protein binding as a function of the protein and salt concentration and solution pH without using an explicit isotherm model. The interpolated isotherm data are then used with a lumped kinetic model to predict the protein elution behavior. Experimental results obtained for laboratory scale columns show excellent agreement with the predicted elution curves for both individual or combined pH and salt gradients at protein loads up to 45 mg/mL of column. Numerical studies show that the model predictions are robust as long as the isotherm data cover the range of mobile phase compositions where the protein actually elutes from the column.     

发菜藻蓝蛋白分离纯化的研究

以发菜为材料,比较了提取液类型和饱和硫酸铵浓度对藻蓝蛋白提取的影响,并对藻蓝蛋白的提取程序和部分特性进行了研究。结果表明:50 mmol/L KP缓冲液(pH值7.2)是合适的提取液,体积分数为40%~50%饱和硫酸铵盐析效果优于其它浓度。经过DEAE-Toyopeal 650 S离子交换层析和SuperdexTM200凝胶过滤层析后,藻蓝蛋白纯度达6.2,最大吸收峰位于615 nm,荧光发射峰位于649 nm,由α和β2个亚基组成,其分子质量分别为18 051.17和19 142.27 Da。因此,发菜藻蓝蛋白分离纯化较为理想的程序为:藻粉→50 mmol/L KP缓冲液(pH值7.2)浸泡→French pressure(1 500 kg/cm2)破碎细胞→40%~50%饱和硫酸铵盐析→DEAE-Toyopeal 650 S离子交换层析→SuperdexTM200凝胶过滤层析→较纯的藻蓝蛋白。     

一种安全高效的血红蛋白纯化方法

目的:建立一种适用于大量制备的,安全、高效的血红蛋白纯化方法。方法: 将压积红细胞装入透析袋,以含有还原剂的Tris缓冲液透析破碎,破碎的上清经两级硫酸铵沉淀后透析至上样缓冲体系,离心后取上清即得血红蛋白提取液;红细胞提取液通过阴离子交换柱层析进一步分离,计算回收率。纯化产物浓缩后以SDS-PAGE及HPLC鉴定纯度,进行紫外-可见光谱扫描并以ABL800血气分析仪分析血气指标,以鲎试剂测定内毒素含量,以磷测定法测定脂质含量。结果: 血红蛋白提取液中脂质去除率98%,容易通过0.45μm滤膜;经阴离子交换层析纯化的血红蛋白经SDS-PAGE(银染法)及WB分析没有杂蛋白条带,HPLC分析纯度>99%、总回收率>85%;内毒素含量<2 EU,高铁血红蛋白含量<5%。结论: 该血红蛋白纯化方法安全高效、成本低廉、易于放大生产,具有较好的应用前景。     

兔感觉神经特异蛋白的纯化及稳定性观察

以兔脊神经节及背根纤维为材料,通过制备匀浆,DEAE-Sephacel阴离子交换层析,高压液相凝胶过滤层析分离纯化了感觉神经特异蛋白29 ku,并进行了该蛋白的稳定性观察.     

Analytical grade C-phycocyanin obtained by a single-step purification process

C-phycocyanin (C-PC) is a phycobiliprotein that can be used as a natural blue dye in the food and cosmetic industries, as a biomarker or as an agent in medical treatments, depending on its purity grade. Here we described for the first time a single-step purification process of C-PC extracted from the wet biomass of Spirulina (Arthrospira) platensis LEB-52 using ion exchange chromatography with pH gradient elution. Different conditions varying the elution buffers and volumes, the loading pH and the addition of salt in the elution buffer were studied. The chromatographic condition that resulted in high recovery and purity consisted in equilibration and washing with 0.025 mol/L Tris-HCl buffer pH 6.5 and elution combining a step with 0.08 mol/L NaCl in 0.025 mol/L Tris-HCl buffer pH 6.5 and a pH gradient elution with 0.05 mol/L citrate buffer pH 6.2–3.0. This process resulted in C-PC with purities of 4.2 and 3.5 with recoveries of 32.6 and 49.5 %, respectively, in one purification step.     

Strategy for a protein purification design using C-phycocyanin extract

A variety of techniques have been developed for the separation and recovery of proteins. The cost of purifying the product is frequently determined by the desired quality of the final product, which is evaluated by measuring the purity. In this work the design of a protein purification process for C-phycocyanin, a phycobiliprotein that can be used in the food and medical industries, was established. The study evaluated the use of ammonium sulfate precipitation, ion exchange chromatography and gel filtration to purify C-phycocyanin in a variety of sequences. The final design included the C-phycocyanin extraction step, precipitation with ammonium sulfate and ion exchange chromatography. When the elution step was studied, the kind of elution and pH were considered in order to obtain a product with a final purity of 4.0 with a purification factor of 6.35, so that, at the end of the strategy, C-phycocyanin of analytical grade would be obtained.