大孔及涂敷硅球作基质的组氨酸拟亲和色谱纯化人免疫球蛋白G

研究用分子组氨酸和配体、大孔硅球为基质的拟亲和色谱分离纯化人免疫蛋白Ｇ（ＩｇＧ），认为键合组氨酸具有半抗原体质而与ＩｇＧ发生免疫亲和作用，以色谱组份重新进样验证了色谱柱对ＩｇＧ亲和专一性，并用包敷Ｄｅｘｔｒａｎ大孔硅球作基质的拟亲和色谱纯化人血清中的ＩｇＧ，减少了色谱峰拖尾，缩短了分离时间。     

ProteinA亲合膜色谱柱的性能及从人血浆中纯化免疫球蛋白的研究

以木纤维为基质,与甲基丙烯酸环氧丙酯共聚接枝合成了复合膜介质,用复合膜介质制备了ｐｒｏｔｅｉｎＡ亲合膜色谱柱,考察了ｐｒｏｔｅｉｎＡ亲合膜色谱柱液相流动特性和吸附性能。实验证明：流速与亲合膜色谱柱柱压呈线性关系,当流速为３ｍＬ／ｍｉｎ时,柱压为１６０ｋＰａ。免疫球蛋白（ＩｇＧ）浓度和上样速度是影响ｐｒｏｔｅｉｎＡ键合容量的重要因素,对其进行了优化研究。用动态吸附法确定了对人ＩｇＧ动态最大吸附能力可达２１．７ｍｇ／ｇ（干介质）。     

膜亲和色谱的现状、发展和应用

文章对膜亲和色谱的原理、特点、设备、过程和发展情况做了介绍，并对亲和膜在整个膜分离技术中的地位、所占的比重及市场预测做了述评，对膜亲和色谱与其它色谱分离技术的优缺点进行了比较。重点介绍了制备亲和膜的材料，活化方法，间隔臂和配基的种类、选择和共价键合方法，配基和配合物产生亲和作用的机理及解离过程和方法。并对膜亲和色谱在酶、蛋白质、核糖核酸等生物大分子纯化分离方面的应用情况做了述评。     

膜亲和色谱的现状、发展和应用

文章对膜亲和色谱的原理、特点、设备、过程和发展情况做了介绍，并对亲和膜在整个膜分离技术中的地位、所占的比重及市场预测做了述评，对膜亲和色谱与其它色谱分离技术的优缺点进行了比较。重点介绍了制备亲和膜的材料，活化方法，问隔臂和配基的种类、选择和共价键合方法，配基和配合物产生亲和作用的机理及解离过程和方法。并对膜亲和色谱在酶、蛋白质、核糖核酸等生物大分子纯化分离方面的应用情况做了述评。     

活性蓝F3GA固载的无孔单分散亲水性交联聚甲基丙烯酸环氧丙酯亲和色谱填料的制备与应用

以3.0 μm无孔单分散亲水性交联聚甲基丙烯酸环氧丙酯树脂为基质,与三嗪染料活性蓝F3GA(Cibacron Blue F3GA)反应,制备出 一种固定化染料聚合物高效亲和色谱填料。考察了应用该填料时流动相中的盐离子浓度、有机溶剂及流速等对牛血清白蛋白(BSA)和 溶菌酶(Lys)保留行为的影响。实验结果表明,该染料亲和填料具有良好的色谱性能。利用前沿色谱法测定了染料与溶菌酶之间的表观 解离常数为5.26×10-5 mol/L。使用该填料成功地从鸡蛋清和小牛血清中分别分离纯化了Lys和BSA,十二烷基硫酸钠-聚丙烯酰胺凝胶 电泳(SDS-PAGE)分析显示Lys和BSA的纯度分别为95%和92%。     

染料结合2μm无孔硅胶亲和填料的制备与应用

在２μｍ无孔硅胶表面键合３ 氨丙基 三乙氧基硅烷（ＡＰＳ）,并与三嗪染料活性蓝Ｆ３ＧＡ（ＣｉｂａｃｒｏｎＢｌｕｅＦ３ＧＡ,ＣＢ）反应,制得亲和色谱填料,并采用扫描电镜、元素分析、ｐＨ稳定性测试对此填料进行鉴定与表征。该填料具有良好的色谱性能,且对生物大分子有一定的亲和选择性,改变ｐＨ值及离子强度对溶菌酶的结合量有明显影响,可用于分离卵清蛋白（Ｏｖａｌ）和溶菌酶（Ｌｙｓ）,且对α ,β ,γ 球蛋白有不同的亲和作用,并可从鸡蛋清中制备少量溶菌酶。     

亲和膜色谱

亲和膜色谱又称亲和膜分离，其在蛋白质的分离纯化中作为一种综合性的技术出现在80年代末。亲和膜色谱主要优点是克服了颗粒状多孔载体扩散传质阻力大的缺点，代之以对流传质，这样就可以在较低的操作压和较高的流速下对目标蛋白进行快速的分离和纯化，从而缩短操作时间、提高纯化效率。本文将就近年来亲和膜色谱及其在蛋白质分离和纯化中的应用作一综述性介绍。     

单分散非多孔交联聚甲基丙烯酸环氧丙酯微球作为亲和色谱载体的研究

单分散、非多孔聚甲基丙烯酸环丙酯生球机械强度高,表面的环基易于修饰与键合,非常适宜于生物大分子的快速分离、纯化。对其表面环氧基浓度、非特异性地性能等进行了表征;并以胰蛋白酶抑制剂为配基,制备了胰蛋白酶抑制剂－交联聚甲基丙烯权环氧丙酯亲和色柱,考察了胰蛋白酶等蛋白南的亲和色谱行为,表明该基质适宜用作亲和色谱载体。提出以添加１％乙腈的方法,可有癣地消除此类载体的弱非特异性吸附,使人血清白蛋白的回收率     

磺胺甲基异噁唑作配基的高效亲和色谱分离胰凝乳蛋白酶和胰蛋白酶

用磺胺甲基异噁唑作配基、大孔硅胶为基质的高效亲和色谱分离纯化胰凝乳蛋白酶及胰蛋白酶。20多种蛋白质和酶在该柱上无特异性吸附。磺胺甲基异噁唑在硅胶上的键合量为4．3mg／g；该亲和填料对胰凝乳蛋白酶吸附量为9．6mg／g；两者之间的亲和解离常数K1／M为1×103mol／L。     

疏水膜色谱法对生物大分子的快速纯化

首次采用自制的分别级合了辛基、丁基、苯基及聚乙二醇-4000的4种常用疏水基团的纤维素疏水膜色谱柱,以键合了辛基、苯基的SepharoseCL－4B凝胶柱为对照,考察了疏水膜色谱柱对牛血清白蛋白（BSA）的动态吸附容量及流速对吸附容量的影响。疏水膜色谱柱对蛋白及酶具有较好的疏水吸附及纯化作用,但吸附容量比相应的琼脂糖凝胶柱低得多。增大流速及降低蛋白溶液质量浓度对疏水膜色谱柱的吸附容量影响较小,这些性能使膜色谱柱非常适合于大体积低质量浓度蛋白溶液（如基团工程培养液）的分离纯化。     

Solid-phase extraction for the simultaneous preconcentration of organic (selenocystine) and inorganic [Se(IV), Se(VI)] selenium in natural waters

The recombinantly produced different forms of protein G, namely monofunctional immunoglobulin G (IgG) binding, monofunctional serum albumin (SA) binding and bifunctional IgG/SA binding proteins G, are compared with respect to their specific affinities to blood IgG and SA. The affinity mode of the recently developed high-performance monolithic disk chromatography has been used for fast quantitative investigations. Using single affinity disks as well as two discs stacked into one separation unit, one order of magnitude in adsorption capacities for IgG and SA were found both for monofunctional and bifunctional protein G forms used as specific affinity ligands. However, despite the adsorption difference observed, the measured dissociation constants of the affinity complexes seemed to be very close. The analytical procedure developed can be realized within a couple of minutes. Up-scaling of the developed technology was carried out using another type of monolithic materials, i.e. CIM affinity tubes.     

Monitoring of mouse immunoglobulin G by flow-injection analytical affinity chromatography

A flow-injection analytical affinity chromatographic (FIAAC) system was developed for the on-line monitoring of mouse immunoglobulin G (IgG). Protein A or anti-mouse IgG antibodies immobilized on oxirane beads were filled in a miniature column. The IgG-containing samples and standards were passed through the column and detected fluorimetrically after elution with citrate buffer (pH 3 or 2.5). The on-line monitoring of mouse IgG 2a during a 7-day cultivation of hybridoma cells in a perfusion reactor by FIAAC is presented. A chemical barrier was used to prevent contamination of the reactor from the FIAAC.     

Isolation of human serum immunoglobulins with a new salt-promoted adsorbent

In this work a highly acetylated-ethylenediamine-Novarose (HA-EDA-Novarose) gel was synthesized and used as a new agarose-based salt-promoted adsorption chromatography (SPAC) matrix to effectively isolate serum immunoglobulins without the need of denaturing conditions. Samples of human serum in 0.5 M Na2SO4, 10 mM 3-(N-morpholino)-propane-sulfonic acid (MOPS), pH 7.6 were applied to a chromatographic column packed with the SPAC gel. Immunoglobulins (Igs) with affinity for the HA-EDA ligands were specifically adsorbed to the matrix, non-bound serum proteins were readily removed by washing the column with the same feed solution buffer. Bound Igs were effectively and very gently eluted by simply removing the salt from the feed solution buffer. The elution buffer consisted thus of only 10 mM MOPS, at pH 7.6 and no salt. The salt-dependent adsorption capacity of this system was estimated to be 7.3 mg/ml with protein recovery of about 93%. Sodium dodecyl sulfate-polyacrylamide gel (SDS-PAGE) electrophoresis analysis, radial immunodiffusion and enzyme-linked immunosorbent assays showed that immunoglobulins G, M and A (IgG, IgM and IgA) were the main components present in the elution fraction. The new SPAC adsorbent was used to purify Igs from human serum and IgG and IgA from non-pure commercially available Igs preparations in a very gentle single step.     

蛋白A连续床亲和毛细管色谱柱的制备及性能考察

人免疫球蛋白 G(HIg G)是一种重要的生物大分子 ,是人血浆中的主要成分之一 ,通常采用免疫学的方法测定 .蛋白 A(Protein A)与免疫球蛋白 (HIg G)的 Fc区之间具有很强的特异性亲和作用 ,因而固载蛋白 A的亲和介质可用于免疫球蛋白及单克隆抗体的分离、纯化和分析测定[1～ 3 ] .根据固定相存在形式的不同 ,毛细管色谱柱主要有开管、填充和连续床柱 3种方式 .连续床具有相比高、易制备 (一步合成 )、孔径易控制、不需烧塞子和易改性等优点 .连续床与其它常用的亲和介质 (如球型凝胶颗粒、灌流色谱基质 [4、 5] 、膜介质 [6,7] 等 )相比具…     

重组蛋白A亲和填料的制备及其性能评价

为了获得一种优良的抗体纯化介质,制备了重组金黄色葡萄球菌蛋白A(rProtein A)亲和填料,并考察了所制备的亲和填料的纯化性能。利用自行构建的rProtein A工程菌,经诱导表达、纯化获得rProtein A纯品,将其偶联到经环氧氯丙烷活化的Sepharose 4 Fast Flow凝胶上,得到rProtein A亲和填料,并使用兔抗尿酸氧化酶抗体对该填料的性能进行验证。结果显示,在自制的rProtein A亲和填料上rProtein A浓度为1.5×10~4 mol/L。采用Scatchard模型分析,得到其解离常数和最大表观吸附量分别为2.28×10~7 mol/L和20.697 g/L,说明制得的rProtein A亲和填料对抗体有很好的结合能力。将该填料于0.1 mol/L NaOH溶液中浸泡1 h,其色谱性能未见变化。将该填料用于纯化兔抗体,湿胶结合抗体量可达19 mg/mL;一步柱色谱即可得到电泳纯度的抗体样品,回收率高于96%。本研究为rProtein A亲和填料的国产化奠定了基础。     

Mechanism and kinetics of protein transport in chromatographic media studied by confocal laser scanning microscopy. Part II. Impact on chromatographic separations

The impact of different transport mechanism on chromatographic performance was studied by confocal laser scanning microscopy (CLSM) for solutions containing bovine serum albumin (BSA) and monoclonal IgG 2a under different solid- and fluid-phase conditions. During this investigation, a clear influence of the uptake mechanism on the affinity of the respective proteins for the different adsorbents and thus separation performance of the chromatographic process could be observed. For the system SP Sepharose Fast Flow at pH 4.5 pore diffusion could be ascribed to be the dominant transport mechanism for both proteins and the adsorption profiles resembled a pattern similar to that described by the 'shrinking core' model. Under these conditions a significantly higher affinity towards the adsorbent was found for BSA when compared to IgG 2a. With changing fluid- and solid-phase conditions, however, a change of the transport mode for IgG 2a could be detected. While the exact mechanism is still unresolved it could be concluded that both occurrence and magnitude of the now governing transport mechanism depended on protein properties and interaction with the adsorbent surface. For the system SP Sepharose XL at pH 5.0 both parameters leading to the change in IgG 2a uptake were combined resulting in a clear change of the system affinity towards the IgG 2a molecule, while BSA adsorption was restricted to the most outer shell of the sorbent.     

免疫吸附治疗用ProteinA切流膜色谱柱的研究

切流膜色谱柱是免疫吸附治疗中实现全血灌流的一种新的模式。实验研究表明,切流膜色谱柱的结构和血液流动形式对血细胞的损害很小。分别考察了水、血浆、血液等不同流体流速与切流膜色谱柱柱压降之间的关系,柱压降随着流体流速和粘度的升高而增高,血液流速为120mL／min时,柱压降达到93kPa;考察了ProteinA切流膜色谱柱对人血浆中免疫球蛋白IgG的吸附能力,切流膜色谱柱ProteinA健合量为139mg（6mgProteinA／g干介质）,血浆在柱中循环1h可吸附IgG553mg（23．8mgIgG／g平介质）,而血液在柱中循环1h,可吸附IgG499.4mm（21.5msIgG／g卡介质）。     

The effect of NaCl on the adsorption of human IgG onto CM-Asp–PEVA hollow fiber membrane-immobilized nickel and cobalt metal ions

Over the past decade, immobilized metal-affinity adsorbents have attracted increasing interest for purification of natural and recombinant immunoglobulin G (IgG). In this work, nickel and cobalt metal ions complexed with CM-Asp (carboxymethylaspartate) immobilized on poly(ethylenevinyl alcohol) (PEVA) hollow fiber membranes were evaluated for purification of human IgG from serum. The buffer system and NaCl had important effects on human serum protein adsorption in both adsorbents. Efficient purification of IgG was accomplished in sodium phosphate buffer without NaCl at pH 7.0. Under this condition, the electrostatic interactions are important for adsorption. The Ni(II)-CM-Asp–PEVA had a protein adsorption capacity of 17.5 mg of IgG mL^?1 fiber when human serum diluted was loaded in crossflow filtration mode and the eluted IgG had a purity of 82.6 % (based on total protein and IgG, IgM, HSA, and Trf nephelometric analysis). Fitting the experimental IgG adsorption data to the Langmuir and Langmuir–Freundlich models showed that Ni(II)-CM-Asp and Co(II)-CM-Asp had Langmuirean and non-Langmuirean behavior, respectively, with positive cooperativity for IgG-Co(II)-CM-Asp binding, probably due to multipoint interactions (n = 2.12 ± 0.31). Thus, these membranes can be considered as alternative adsorbents for the purification or depletion of IgG from human serum.