碱性氨基酸离子交换平衡特性的研究

研究了碱性氨基酸与001×7阳离子交换树脂的离子交换平衡特性。测定了001×7树脂对碱性氨基酸两种价态离子的选择性吸附系数,并考察了pH和碱性氨基酸的浓度对平衡吸附量的影响,确定了离子交换的最佳pH 和碱性氨基酸的浓度。     

肌苷的离子交换法提取工艺研究

研究了肌苷发酵液不同pH值、树脂预平衡条件、饱和树脂的洗菌、淋洗条件对肌苷离子交换提取和解吸工艺影响情况，并对其离子交换吸附机理进行了详细探讨，旨在确定最佳提取工艺条件。     

离子交换法提取谷氨酸的研究

本文就离子交换法提取谷氨酸树脂的筛选，不同树脂对发酵液中谷氨酸静态吸附性能及其影响因素进行了系统地研究．旨在探索离子交换法提取谷氨酸的最佳工艺条件和开发新的离子交换树脂．     

有机羧酸在强碱性阴离子交换树脂上的超当量吸附

本文测定了甲酸、乙酸、丙酸和苯甲酸在强碱性阴离子交换树脂上的吸附等温线,观测到了甲酸、乙酸和丙酸的超当量吸附。通过对吸附了上述四种有机羧酸的离子交换树脂的红外光谱的研究,探讨了造成超当量吸附的原因,结果表明其原因是有机羧酸以多聚体形式占据交换位置。用Bull方程求算了甲酸和苯甲酸在强碱性阴离子交换树脂上的标准吸附自由能。     

氨基酸的提纯方法

本发明提供一种从氨基酸的碱金属盐的水溶液中提纯氨基酸的方法，所述方法包括下列步骤：（1）阳离子交换步骤，其中，用包含阳离子交换树脂的移动床式连续离子交换装置对氨基酸的碱金属盐的水溶液进行脱盐提纯处理，以得到粗氨基酸的水溶液；（2）阴离子交换步骤，其中，用弱碱性阴离子交换树脂从所得的粗氨基酸的水溶液中吸附除去作为共存的副产物的亚氨基二羧酸，并且甚至在对所述亚氨基二羧酸的吸附达到所述弱碱性阴离子交换树脂的突破点之后，仍使所述粗氨基酸的水溶液流过。     

氨基酸的离子交换“过滤色谱”分离

离子交换色谱作为一种有效的分离手段已有系统而深入的研究和悠久的应用历史。我们在长期利用离子交换色谱于氨基酸分离的工作实践中,总结出一种利用离子交换树脂从混合氨基酸中分离某些单组分氨基酸的有效力法。色谱分离过程相似于过滤过程,混合氨基酸通过色谱柱后,要分离的氨基酸以单组分的形式在树脂柱上交换,其它氨基酸从柱中流出,我们把这一色谱分离手段称为离子交换“过滤色谱”。     

用离子交换树脂脱除氨基酸与盐混合液中的盐

在用蛋白质酸性水解备氨基酸时,因中和残留的酸会使水解液中带入大量的盐。在进一步用离子交换色谱法分离混合氨基酸时,首先需脱掉其中的盐。本文用苯乙烯系强酸性阳离子交换树脂的盐型柱,根据氨基酸与苯乙烯系强酸性阳离子交换树脂之间既存在离子间的静电作用,又存在疏水作用,且二者之间存在协同作用,而盐在盐型苯乙烯系强酸性阳离子交换树脂柱上不保留的原理,用水作为洗脱剂,使盐和氨基酸（配制的盐和氨基酸混合液及含盐的毛发水解液）得到分离,本方法脱除氨基酸中的盐简单易行,用水作为洗脱剂即廉价由不造成污染,盐型树脂不用再生即可用于下次运行,研究了各种条件对分离性能的影响。     

CL-TBP萃淋树脂吸附分离镓(Ga)研究

本文研究了 Cl- TBP萃淋树脂从酸性溶液中吸附分离镓的性能 ,结果表明 ,在 6mol· L-1HCl介质中 ,树脂对镓有良好的吸附性能。可有效地从含镓溶液中分离富集镓。被吸附的镓可用 NH4 Cl溶液定量洗脱 ,对吸附过程机理进行了初步研究 ,证实吸附为离子交换过程。     

具有精细结构的吸附与离子交换树脂

本文论述了某些具有精细化学，物理结构的离子交换树脂和吸附树脂的特性与应用。     

氨基酸与离子交换树脂相互作用的研究(Ⅱ)——高浓度下离子交换树脂超当量吸附氨基酸的机理

近年来,对氨基酸离子交换平衡虽有不少研究^[1～4],但涉及超当量吸附的研究并不多见,且解释亦各有不同^[6～7].本文拟对超当量吸附机理作深入研究.     

INTERACTION OF AMINO ACID WITH ION EXCHANGE RESIN Ⅲ.FURTHER INVESTIGA TION OF SUPEREQUIVALENT ADSORPTION MECHANISM OF AMINO ACID ON ION EXCHANGE RESIN

The adsorption isotherms of glycine,alanine and oxidized glutathion on strong acid cation and strong base anion exchange resins from aqueous solutions were measured and the superequivalent adsorptions of glycine and alanine observed.The infrared spectra of glycine adsorbed on the cation and the anion exchange resins,001×7 and 201×7,were measured.From these results,it is concluded that the amino acid adsorption on the ion exchange resin proceeds not only through ion exchange and proton transfer mechanisms,but also through aminecarboxylate interaction between the adsorbed amino acid molecules,and the formation of second layer of amino acid molecules is the mechanism of superequivalent adsorption of amino acid,the carboxylate or amine groups of the first layer of amino acid molecules on the ion exchange resin act as the exchange sites for the second layer of amino acid molecules.     

模拟磷矿脱镁废水中镁离子的交换动力学研究

用动边界模型积分方程描述模拟磷矿脱镁废水中Mg2＋在001×7×7型树脂上的有限浴交换动力学,得到了动力学总方程.Mg2＋的交换过程属颗粒扩散控制,表观活化能为23.45 kJ•mol－1,Mg2＋的表观反应级数为0.68.     

稀土离子在多孔阳离子交换剂内的扩散动力学

研究了稀土离子在Amberlyst15、D001、XN1010多孔树脂内的自扩散。结果表明,扩散过程遵循二级分散扩散机制。用粒内扩散方程求算了有效粒内扩散系数e,将e分解为树脂孔道扩散系数p及树脂固相扩散系数s,p与该离子在外部溶液中的自扩散系数相近,而s接近于与实验用的多孔树脂交联度相同的凝胶树脂内的自扩散系数值。     

批量离子交换层析和凝胶过滤层析在类人胶原蛋白I纯化中的应用

研究了利用批量离子交换层析与凝胶过滤层析相结合的方法纯化类人胶原蛋白I的最佳条件。分别考察了不同离子交换树脂、缓冲溶液pH、离子强度、进料蛋白浓度对批量离子交换的影响,以及不同凝胶过滤介质对凝胶过滤层析的影响。结果表明,采用阴离子交换树脂DEAE52吸附杂蛋白,缓冲液pH为7.0,NaCl浓度为0.2mol/L,进料蛋白浓度为40mg/mL,并采用凝胶过滤介质SephadexG-100进一步纯化后,类人胶原蛋白I的纯度可达到98.2%,总纯化倍数为3.1,总回收率为80.6%。SDS-PAGE分子量分析和N末端氨基酸序列分析均表明纯化后的类人胶原蛋白I与基因设计一致。     

离子交换树脂的选择及柠檬酸溶液循环使用研究

用离子交换树脂法吸附柠檬酸溶液中的金属离子,苯乙烯系阳离子交换树脂的吸附性能较好,它对镍、铝离子的吸附容量均较大,且吸附前后柠檬酸溶液的浓度变化较小.静态条件下树脂对镍的吸附容量为16.83mg Ni/g干树脂,对铝为21.36mg Al/g干树脂;动态条件下树脂对镍的吸附容量为6.78mg Ni/g干树脂,对铝为31.8mgAl/g干树脂,吸附液流速为1m/h～3m/h.吸附后的柠檬酸溶液可循环使用.当用1mol/L硫酸解吸时,树脂对镍铝的解吸率可达90%以上.当硫酸中Ni2 为1.70mmol/L,Al3 为7.40mmol/L时,树脂的解吸率仍可达80%以上.     

牛磺酸和甘氨酸在D290树脂上的离子交换平衡

研究了牛磺酸与甘氨酸在阴离子树脂D290上的离子交换平衡.采用静态法分别进行牛磺酸/氢氧根/D290树脂和甘氨酸/氢氧根/D290树脂体系的离子交换平衡实验并测定等温线;在不同的离子强度下进行了牛磺酸/甘氨酸/氢氧根/D290阴离子交换树脂体系的离子交换平衡实验,测定牛磺酸和甘氨酸在碱性条件下的竞争交换平衡等温线.实验结果表明,牛磺酸在D290阴离子交换树脂上的交换量大于甘氨酸的交换量,阴离子交换树脂对牛磺酸和甘氨酸的选择性系数分别为STau-,OH-=2.55,SGly-,OH-=1.65.在牛磺酸/甘氨酸/氢氧根/D290树脂体系中,D290树脂对牛磺酸/甘氨酸/氢氧根3种离子的选择性从高到底顺序是:牛磺酸＞甘氨酸＞氢氧根.树脂对牛磺酸的选择性要大于对甘氨酸的选择性.随着溶液中离子强度的增大,树脂对牛磺酸与甘氨酸之间的选择性下降.     

Phenol removal from aqueous solution by adsorption and ion exchange mechanisms onto polymeric resins

The removal of phenol from aqueous solution was evaluated by using a nonfunctionalized hyper-cross-linked polymer Macronet MN200 and two ion exchange resins, Dowex XZ (strong anion exchange resin) and AuRIX 100 (weak anion exchange). Equilibrium experimental data were fitted to the Langmuir and Freundlich isotherms at different pHs. The Langmuir model describes successfully the phenol removal onto the three resins. The extent of the phenol adsorption was affected by the pH of the solution; thus, the nonfunctionalized resin reported the maximum loading adsorption under acidic conditions, where the molecular phenol form predominates. In contrast both ion exchange resins reported the maximum removal under alkaline conditions where the phenolate may be removed by a combined effect of both adsorption and ion exchange mechanisms. A theoretical model proposed in the literature was used to fit the experimental data and a double contribution was observed from the parameters obtained by the model. Kinetic experiments under different initial phenol concentrations and under the best pH conditions observed in the equilibrium experiments were performed. Two different models were used to define the controlling mechanism of the overall adsorption process: the homogeneous particle diffusion model and the shell progressive model fit the kinetic experimental data and determined the resin phase mechanism as the rate-limiting diffusion for the phenol removal. Resins charged after the kinetic experiments were further eluted by different methods. Desorption of nonfunctionalized resin was achieved by using the solution (50% v/v) of methanol/water with a recovery close to 90%. In the case of the ion exchange resins the desorption process was performed at different pHs and considering the effect of the competitive ion Cl⁻. The desorption processes were controlled by the ion exchange mechanism for Dowex XZ and AuRIX 100 resins; thus, no significant effect for the addition of Cl⁻ under acidic conditions was observed, while under alkaline conditions the total recovery increased, specially for Dowex XZ resin.     

FACTORS AFFECT THE RELEASE OF PSEUDOEPHDRINE HYDROCHLORIDE FROM THE UNCOATED CATION EXCHANGE RESIN—BASED DRUG DELIVERY SYSTEM IN VITRO

In this paper,it was investigated that the effect of parameters such as the ionic strength,pH.counter-ion type of release medium,particle size.and cross linkage of cation exchange resin on the release of model drug pseudoephedrine hydrochloride(PE) from uncoated drug-resin complex.The drug-resin complex was pepared by the reaction of PE with strongly acidic cation exchange resin(001×4,001×7,001×14） .The result showed that the loading of PE increased with the increase of temperatures.The release of PE from drug-resin complex at 37℃ was monitored in vitro.From the experiments,it was found that the release rate of PE depends on the pH.comosition of the releasing media,increased at lower pH media or with increase of ionic strength of media.Moreover,the release rate of PE was inversely proportional to the cross-linkage and particle size of the cation exchange resin.