共聚物接枝蛋白离子交换色谱介质制备及性能

高容量蛋白质色谱介质是色谱过程高效化的材料基础和重要前提。采用原子转移自由基聚合（ATRP）技术,以甲基丙烯酸3-磺酸丙酯钾和甲基丙烯酸甲酯（MMA）为单体化合物合成了多种无规共聚物接枝离子交换色谱介质,并对其蛋白质吸附性能进行研究。单体总浓度一定情况下共聚物接枝色谱介质孔道半径（r_pore）随MMA浓度升高而增大,反映出接枝共聚物链渐趋塌陷的特征。蛋白质吸附结果表明,溶菌酶吸附容量取决于介质的离子交换容量;而抗体吸附容量则与rpore及相应的聚合物层厚度变化密切相关。随着聚合物层厚度的增大,聚合物层对抗体的空间排阻作用增强,抗体吸附容量下降。此外,引入MMA优化共聚物分子链可显著提高蛋白质吸附量,在SEP-gS30/M30介质中抗体和溶菌酶的饱和吸附量分别达到237 mg·g^-1和380 mg·g^-1。无规共聚物接枝离子交换色谱介质孔道内聚合物层厚度和蛋白质吸附也受无机盐浓度调控。     

共聚物接枝蛋白离子交换色谱介质制备及性能

高容量蛋白质色谱介质是色谱过程高效化的材料基础和重要前提。采用原子转移自由基聚合(ATRP)技术,以甲基丙烯酸3-磺酸丙酯钾和甲基丙烯酸甲酯(MMA)为单体化合物合成了多种无规共聚物接枝离子交换色谱介质,并对其蛋白质吸附性能进行研究。单体总浓度一定情况下共聚物接枝色谱介质孔道半径(r_(pore))随MMA浓度升高而增大,反映出接枝共聚物链渐趋塌陷的特征。蛋白质吸附结果表明,溶菌酶吸附容量取决于介质的离子交换容量;而抗体吸附容量则与r_(pore)及相应的聚合物层厚度变化密切相关。随着聚合物层厚度的增大,聚合物层对抗体的空间排阻作用增强,抗体吸附容量下降。此外,引入MMA优化共聚物分子链可显著提高蛋白质吸附量,在SEP-g S30/M30介质中抗体和溶菌酶的饱和吸附量分别达到237 mg·g~(-1)和380 mg·g~(-1)。无规共聚物接枝离子交换色谱介质孔道内聚合物层厚度和蛋白质吸附也受无机盐浓度调控。     

接枝聚合物配基的蛋白质吸附层析

以离子交换、亲和结合和疏水性吸附为主的蛋白质吸附层析是药用蛋白质生产过程的核心技术,开发新技术和提高蛋白质吸附层析操作的分离效率(如选择性和动态吸附容量等)是该领域的主要研究目标。近年来聚合物配基接枝的层析介质由于同时具有较高的吸附容量和传质速率,得到产学界的广泛关注。本文针对聚合物配基接枝修饰的蛋白质吸附层析介质的配基化学特征、吸附和传质特性、层析分离应用和设计等方面进行评述。首先介绍不同种类的聚合物接枝介质,然后系统阐述聚合物配基化学特性对介质吸附和传质性能的影响机制,并分析上述性质对聚合物配基接枝层析介质分离特性的影响机理和应用,最后讨论和展望了高效聚合物配基接枝介质设计、开发和应用的前景。     

反离子对牛血清白蛋白在荷电葡聚糖接枝介质中色谱行为的影响

从前期开发的具有极高的吸附容量及传质速率的二乙氨乙基葡聚糖接枝离子交换介质中选取FF-D50-DexD100和FF-DexD100为典型代表,利用Cl^-、SCN^-、SO₄^2-、HPO₄^2-为模型反离子,以牛血清白蛋白（BSA）为模型蛋白,以商品化介质（Q Sepharose FF、Q Sepharose XL、DEAE Sepharose FF）为对照,在离子强度为0.06mol/L下,系统研究反离子对二乙氨乙基葡聚糖接枝介质的蛋白质吸附与洗脱行为的影响。结果表明,二乙氨乙基葡聚糖接枝介质对不同反离子的偏好性存在差异,且该偏好性差异与基团所处位置（接枝链配基或表面配基）无关。同时,介质偏好性弱的反离子会通过促进二乙氨乙基葡聚糖接枝介质的“链传递”效应加快蛋白质的传质速率,从而提高动态吸附容量。因此,在使用二乙氨乙基葡聚糖接枝介质进行蛋白质色谱柱分离过程中,可在吸附操作中使用HPO₄^2-,在洗脱操作中使用SCN^-来优化分离效果。     

反离子对部分电荷中和的聚乙烯亚胺接枝介质的蛋白质色谱行为的影响

前期研究表明部分电荷中和的聚乙烯亚胺接枝琼脂糖介质FF-PEI-R440具有较高静态吸附容量和快速传质速率。本文选取硫氰酸根离子、氯离子、磷酸氢根离子以及硫酸根离子这4种反离子,在离子强度为0.03、0.06 mol·L^-1下,研究其对FF-PEI-R440吸附与洗脱行为的影响。结果表明：在两种离子强度下,饱和吸附容量的增加顺序均为SCN^- < SO₄^2- < HPO₄^2- < Cl^-;在低离子强度下,除SCN^-外,反离子种类对传质速率和动态结合容量没有显著影响;在高离子强度下,传质速率的增加顺序为SCN^- < SO₄^2- ≈ Cl^- < HPO₄^2-,而动态结合容量的增加顺序与饱和吸附容量序列一致;两种离子强度下Cl^-均保持最高的动态结合容量;反离子种类对蛋白质洗脱行为没有显著影响。上述结果说明反离子主要影响FF-PEI-R440的吸附性能,而不影响洗脱,且流动相中选择Cl^-为反离子最利于FF-PEI-R440的实际柱色谱操作。     

反离子对部分电荷中和的聚乙烯亚胺接枝介质的蛋白质色谱行为的影响

前期研究表明部分电荷中和的聚乙烯亚胺接枝琼脂糖介质FF-PEI-R440具有较高静态吸附容量和快速传质速率。本文选取硫氰酸根离子、氯离子、磷酸氢根离子以及硫酸根离子这4种反离子,在离子强度为0.03、0.06mol·L~(-1)下,研究其对FF-PEI-R440吸附与洗脱行为的影响。结果表明:在两种离子强度下,饱和吸附容量的增加顺序均为SCN-SO_4~(2-)HPO42-Cl~-;在低离子强度下,除SCN-外,反离子种类对传质速率和动态结合容量没有显著影响;在高离子强度下,传质速率的增加顺序为SCN-SO_4~(2-)≈Cl~-HPO42-,而动态结合容量的增加顺序与饱和吸附容量序列一致;两种离子强度下Cl~-均保持最高的动态结合容量;反离子种类对蛋白质洗脱行为没有显著影响。上述结果说明反离子主要影响FF-PEI-R440的吸附性能,而不影响洗脱,且流动相中选择Cl~-为反离子最利于FF-PEI-R440的实际柱色谱操作。     

载体材料表面化学组成对蛋白质吸附行为的影响研究进展

蛋白质在载体表面的吸附行为,如其吸附速率、吸附量以及取向和构象的变化,在很大程度上依赖于载体材料的表面化学组成。调控载体材料的表面化学组成已成为控制蛋白质吸附行为的重要手段。本文主要对载体材料表面不同组成对蛋白质吸附行为的影响进行了归纳。介绍了材料表面的功能基团包括疏水基团（甲基和含氟基团）和亲水基团（羟基、氨基和羧基）对蛋白质吸附行为的影响。另外,在载体材料表面接枝聚合物链是一种常用的有效调控表面化学组成的方法。重点介绍了材料表面接枝不同聚合物链时,聚合物链的种类、长度、密度和链的结构对蛋白质吸附行为的影响。     

蛋白质在离子交换介质中的动态吸附性能

研究了离子交换介质CM－Sepharose FF对几种不同的蛋白质－溶菌酶，木瓜蛋白酶，牛血清蛋白的动态吸附性能，考察了PH值，溶液粘度，初始蛋白浓度及吸附剂量等因素的影响，结果表明，这些参数会对吸附动态吸附性能产生不同程度的影响，而这些蛋白质也都显示了相似的规律，采用两相阻力模型描述了蛋白质在离子交换介质的动态吸附性能，计算得到了蛋白质在吸附剂颗粒中的扩散系数，有助于进一步研究蛋白质吸附过程的传质现象。     

阳离子交换型连续床用超大孔晶胶的制备

采用原位接枝法,将3-烯丙氧基-2-羟基-1-丙磺酸钠(AHPSA)接枝到聚丙烯酰胺基晶胶基质孔隙内表面,制备得到了阳离子交换型连续床用的带磺酸基超大孔晶胶介质.通过脉冲示踪法测量停留时间分布(RTD),得到了晶胶介质的理论等板高度(HETP).通过测量一定压差下流经晶胶床柱的液量,得到晶胶介质的渗透率.用溶菌酶作为模型蛋白测量晶胶介质的吸附容量.考察了单体浓度、接枝反应时间等反应条件对晶胶介质的HETP、渗透率、蛋白质吸附容量等性能的影响.结果表明:接枝AHPSA的阳离子交换晶胶介质的HETP基本不受接枝反应时间和单体浓度的影响,其渗透率随接枝反应时间增大略有减小,其对溶菌酶的吸附容量与接枝单体的浓度成正比,受接枝反应时间的影响较小.     

琼脂糖-DEAE离子交换介质的配基密度和孔径对BSA吸附的影响

离子交换色谱是蛋白质分离纯化的有效方法之一,配基密度和介质孔径是影响蛋白质吸附的关键因素。采用3种不同琼脂糖浓度的凝胶为基质,具有不同的平均孔径,分别偶联上阴离子交换配基DEAE,通过调控反应条件,包括反应温度、反应时间、碱浓度和DEAE浓度,得到了不同配基密度和介质孔径的系列DEAE离子交换介质。考察了牛血清白蛋白（BSA）的静态和动态吸附性能,发现随配基密度增加或介质孔径减小,BSA饱和吸附容量有所增大;对于吸附动力学,介质孔径显著影响有效扩散系数。结果表明,配基密度和介质孔径共同决定了蛋白质的吸附性能,介质孔径主导蛋白质的孔内扩散,而配基密度则影响配基-蛋白质间的相互作用。     

Fabrication of high-capacity cation-exchangers for protein adsorption: Comparison of grafting-from and grafting-to approaches

In this work, we have synthesized two polymer-grafted cation exchangers: one via the grafting-from approach, in which sulfopropyl methacrylate (SPM) is grafted through atom transfer radical polymerization onto Sepharose FF (the thus resulting exchanger is referred as Sep-g-SPM), and another via the grafting-to approach, in which the polymer of SPM is directly coupled onto Sepharose FF (the thus resulting exchanger is called as Sep-pSPM). Protein adsorption on these two cation exchangers have been also investigated. At the same ligand density, Sep-g-SPM has a larger accessible pore radius and a smaller depth of polymer layer than Sep-pSPM, due to the controllable introduction of polymer chains with the regular distribution of the ligand. Therefore, high-capacity adsorption of lysozyme and γ-globulin could be achieved simultaneously in Sep-g-SPM with an ionic capacity (IC) of 308 mmol·L^-1. However, Sep-pSPM has an irregular chain distribution and different architecture of polymer layer, which lead to more serious repulsive interaction to proteins, and thus Sep-pSPM has a lower adsorption capacity for γ-globulin than Sep-g-SPM with the similar IC. Moreover, the results from protein uptake experiments indicate that the facilitated transport of adsorbed γ-globulin occurs only in Sep-pSPM and depends on the architecture of polymer layers. Our research provides a clear clue for the development of high-performance protein chromatography.     

Implications from γ-globulin adsorption onto cation exchangers fabricated by sequential alginate grafting and sulfonation

Our previous work proved that high adsorption capacity and uptake rate of lysozyme were achieved on alginate(Alg)-grafted re sin with an ionic capacity(IC) of 240 mmol·L~(-1)(Alg-FF-240).Moreover,the salt-tolerant feature of Alg-FF-230 was improved by using sequential alginate grafting and sulfonation strategy.Inspired by the enhanced adsorption performance of lysozyme,we have herein proposed to investigate the static and dynamic adsorption behaviors of γ-globulin on a series of Alg-grafted resins with different grafting densities and sulfonation degrees.The adsorption ca pacity of γ-globulin decreased with increa sing alginate-grafting density(IC) from 160 to 230 mmol·L~(-1) at 0 mmol·L~(-1) NaCl because of the steric hindrance caused by the alginate-grafting layer.Effects of ionic strength(IS) indicated that the adsorption capacities of the resins with the IC value of 230-370 mmol·L~(-1) were much higher than CM Sepharose FF at 50-100 mmol·L~(-1) NaCl,and the uptake rate of Alg-FF-230 was about twice as much as that of CM Sepharose FF.This work demonstrated the important effects of alginate-grafting layer and IS in γ-globulin adsorption behavior,which would be helpful in the design of Alggrafted resins and the selection of proper IS condition for protein purification.     

Adsorption Performance of Proteins to CM Sepharose FF and DEAE Sepharose FF Adsorbents

Adsorption equilibrium and kinetics were studied for the binding of proteins to CM Sepharose FF and DEAE Sepharose FF. The influence of temperature, pH, viscosity, initial concentration and the volume of adsorbents on the adsorption characteristics was investigated in detail. The results showed that the isotherms of lysozyme to CM Sepharose FF were well described by a Langmuir-type correlation. The two phase resistance model describing the dynamic adsorption process of lysozyme, papain, BSA to CM Sepharose FF was presented, and the pore diffusion coefficients were determined by using this model and the dynamic adsorption data.     

Protein retention in dextran-grafted cation exchange chromatography: The influence of pHs,counterions and polymer structure

Polymer-grafted ion exchange adsorbents were of great interest for the development of high-performance protein chromatography in biopharmaceutical and related fields. In this work, protein retention was systematically investigated in ion exchange chromatography packed respectively with dextran-grafted cation exchange adsorbents containing sulphopropyl(SP) ligand, SP Sepharose XL and Capto S, and non-grafted cation exchange adsorbent, SP Sepharose FF, using five proteins. With an increase of buffer p Hs, retention factors of proteins decreased among all the adsorbents, demonstrating the dominant role of electrostatic interaction for protein binding on cation exchange adsorbents. The evidences further revealed that the scattered positive charges on the surface of protein molecules, rather than net charge of protein molecule, determined protein retention on cation exchange adsorbent. Likely, counterions including NH~(4+), K~+, Na~+ and Mg~(2+) exhibited distinct influence on protein retention. It was well ascribed to solvent-mediated indirect ion–macromolecule interactions and direct ion–macromolecule interactions. Compared with SP Sepharose FF, polymer structure in dextran-grafted cation exchange adsorbents ultimately brought about different ligand distributions and smaller pore sizes, thereby regulating protein retention in cation exchange chromatography. By comparing the retention of myoglobin and β-lactoglobulin B in SP Sepharose XL and Capto S, we reasonably speculated that the enhancement of nonelectrostatic interaction caused by reducing the space arm length was a major reason for an increasing retention factor of myoglobin in Capto S. The results in this research help us understand adsorption mechanism of protein in polymer-grafted adsorbents and give scientific guidance for the development of chromatographic materials.     

α/γ-氧化铝对合成镁铝水滑石结构性能的影响

为了解α-氧化铝和γ-氧化铝合成镁铝水滑石（LDH）结构性能的差异,以α-氧化铝和γ-氧化铝为原料采用水热法合成了镁铝水滑石α-LDH-2.0和γ-LDH-2.0。通过扫描电镜（SEM）、红外光谱（FT-IR）、拉曼光谱（Raman）、X射线光电子能谱（XPS）、X射线衍射（XRD）、热重分析（TG-DTG）等对α-LDH-2.0和γ-LDH-2.0进行了检测,并将α-LDH-2.0和γ-LDH-2.0用于吸附刚果红的实验。结果表明：γ-氧化铝合成的γ-LDH-2.0板层更无序、结晶度较高,吸附实验中γ-LDH-2.0对刚果红的吸附效果强于α-LDH-2.0,并且适应更广的溶液pH范围,说明使用不同晶型的氧化铝可以调控镁铝水滑石的形貌结构使其高效吸附刚果红。当刚果红质量浓度为100 mg/L、镁铝水滑石添加量为20 mg时,α-LDH-2.0和γ-LDH-2.0对刚果红的吸附量较大,酸性条件更有利于α-LDH-2.0和γ-LDH-2.0对刚果红的吸附,α-LDH-2.0和γ-LDH-2.0去除刚果红的吸附动力学更符合拟二级动力学方程,等温吸附过程符合Langmuir模型。     

Surface DEAE groups facilitate protein transport on polymer chains in DEAE‐modified‐and‐DEAE‐dextran‐grafted resins

Sepharose FF was modified with diethylaminoethyl‐dextran (DEAE‐dextran, DexD) and/or DEAE (D) to fabricate three types of ion exchangers FF‐DexD (grafting‐ligand resin), FF‐D (surface‐ligand resin), and FF‐D‐DexD (mixed‐ligand resin), for protein adsorption equilibria and kinetics study. It was found that both adsorption capacity and uptake rate (effective diffusivity, D_e) were significantly enhanced by grafting DEAE‐dextran. Notably, the D_e values on FF‐DexD and FF‐D‐DexD (D_e/D₀ > 1.4) were six times greater than those on FF‐D (D_e/D₀ < 0.3). More importantly, the increase of surface‐ligand density greatly enhanced uptake kinetics on FF‐D‐DexD. The results indicate that the surface ligands assisted the transport of bound proteins on polymer chains in the mixed‐ligand resins. That is, surface ligands worked as “transfer stations” between two neighboring chains, resulting in enhanced transport of bound proteins on chains. The research thus disclosed the unique role of surface ligands in facilitating protein uptake kinetics onto polymer‐grafted ion‐exchangers. © 2016 American Institute of Chemical Engineers AIChE J, 62: 3812–3819, 2016     

纳米γ-氧化铁的制备及其吸附性能研究

以硝酸铁和十二烷基三甲基溴化铵为原料,采用固相法制备了γ-氧化铁纳米粒子。通过X射线衍射、氮气吸附-脱附、磁性测试等手段对γ-氧化铁样品进行了表征。研究了γ-氧化铁对有机染料直接耐酸大红4BS的吸附性能。结果表明,制备的γ-氧化铁样品为γ-氧化铁纳米粒子,平均晶粒尺寸为18.5 nm;γ-氧化铁的比表面积为83.2 m ²/g,孔容为0.25 cm ³/g,最可几孔径为3.8 nm,属于介孔范围;γ-氧化铁的最大饱和磁化强度为63.7 A·m ²/kg;介孔γ-氧化铁对直接耐酸大红4BS的吸附过程符合准二级吸附动力学模型;γ-氧化铁对直接耐酸大红4BS的吸附符合Langmuir吸附等温式,极限吸附量为113.3 mg/g;将γ-氧化铁脱附处理后可重复使用。