化学转化法制备磁性阳离子交换树脂的研究

本文通过化学转化法即化学共沉淀法，分别研究了强酸性和弱酸性阳离子交换树脂的磁转化对相应所得树脂的磁性的影响，制得了磁性毫米级和微米级粒径的强酸性，弱酸性阳离子交换树脂。所得磁性树脂有磁性强，磁性物质分布均匀而且稳定，并保持树脂的原有特性。     

磁性阳离子交换树脂的结构与性能分析

利用古埃磁天平法、扫描电镜、粉末Ｘ射线衍射以及分光光度法等检测了化学转化法制备的磁性阳离子交换树脂。结果表明,所制备的树脂内部磁性物质为Ｆｅ３Ｏ４,且在 树脂内部的孔道及表面分布均匀,均被封锁在树脂内部,因而,这类磁性树脂在碱性和中性盐溶液中具有较高的稳定性。此外,树脂的磁化过程并不影响其交换容量。     

聚苯乙烯磁性树脂的合成及性能

用悬浮聚合法,将γ—Fe_2O_3加入苯乙烯和二乙烯苯(DVB)中可制得聚苯乙烯磁性树脂。本文详细研究了各种因素对合成的影响。实验制得一批典型树脂的磁粉含量为12.8％,粒度为80目。磺化后得到磺酸型阳离子交换树脂,其交换容量为3.22mmol/g—R。实验表明,该种磁性树脂有一定的磁化性能,且耐碱性较好。     

用D_2EHPA从离子交换树脂上解吸金的硫脲络合物

用阳离子交换树脂从硫脲溶液中吸附金是容易的,但是金的解吸很困难。本文提出了用D_2EHPA从阳离于交换树脂上解吸金,树脂和解吸剂都可以返回使用。这是用阳离子交换树脂从硫脲溶液中回收金的经济的工艺。     

阳离子交换树脂分离-分光光度法测定水中痕量铜

采用静态法研究了HD-8阳离子交换树脂对铜的吸附速率、吸附温度和吸附量等性能。试验结果表明:在0.1～0.5mol·L~(-1)盐酸溶液介质中铜的吸附率在95%以上,用3mol·L~(-1)盐酸溶液3mL可将吸附于柱上的铜(Ⅱ)完全洗脱下来。在优化的试验条件下,该HD-8阳离子交换树脂微柱对铜的富集限为2μg/200mL,富集倍数为67倍。在此基础上提出了一种阳离子交换树脂分离分光光度法测定水样中痕量铜的方法。该方法用于测定鄱阳湖水中痕量铜,测得平均回收率为101.5%之间,相对标准偏差(n=5)为1.82%。     

有机胺对阳离子交换树脂性能的影响

采用浸泡方法分别研究了氨、乙醇胺、吗啉对阳离子交换树脂性能的影响。利用光学显微镜观察浸泡前后阳离子交换树脂的形貌。55℃下,分别在pH值为9.3的氨、乙醇胺及吗啉的溶液中浸泡不同时间后离子交换树脂的总交换容量、含水率、湿视密度、湿真密度变化均不明显。以3种不同浓度(0.9mol/L、1.4mol/L、1.9mol/L)的氨、乙醇胺及吗啉的溶液分别浸泡离子交换树脂,浸泡后总交换容量、含水率、湿视密度、湿真密度的变化也不大。在恒定pH值与不同浓度碱化溶液中浸泡后,黑琥珀色半透明离子交换树脂的颜色均变浅。实验结果表明有机胺对凝胶型阳离子交换树脂的性能和形貌影响不大。     

离线预富集电感耦合等离子体质谱法测定天然水体中溶解态硅

以Mg(OH)2共沉淀和阳离子交换树脂作为离线预富集方法,建立了天然水体中溶解态硅电感耦合等离子体质谱(ICP-MS)测定方法。实验采用NaOH作为Mg(OH)2沉淀引发剂,以共沉淀方式将溶解态硅元素从天然水体中分离富集,再利用阳离子交换树脂将基体Mg2 清除,并对洗脱液流速、共沉淀碱度等条件进行优化选择。结果显示:Mg(OH)2共沉淀步骤可定量回收溶解态硅,控制溶液通过阳离子交换树脂的速率可将硅元素与基体Mg2 完全分离而不会造成损失。不同基体的水样的加标回收率为99%~105%,方法检出限为4.5μg/L(3S,n=8),方法精密度RSD小于3%。     

自然光照下PEG/PAA 凝胶在Fe3+/CA溶液中的 凝胶-溶胶转化行为的研究

本文将PEG/PAA凝胶浸入铁/柠檬酸（Fe3+/CA）溶液中,在自然光照一定的时间可实现凝胶-溶胶的相互转化,而且转化行为受溶液的组成及其pH值的影响。只有当溶液中[Fe3 ]0: [CA]0≤1:2,且溶液的pH在1-6之间,该转化才会发生,通过改变溶液中[Fe3 ]0: [CA]0的值或溶液的pH可以有效地控制其转化速率。此外,实验结果表明,当凝胶转化为溶胶后,在其中加入高价金属阳离子,例如Fe3 、 Al3 、Ce4 、Cu2 等,溶胶又会再次转化为凝胶。由于这种新颖的特性,该凝胶有望应用于药物释放、细胞培养等领域。     

铀和铀同位素的离子交换过程研究

在浓缩铀同位索的阳离子交换法中,UC_2~(2+)在离子交换树脂中的传质问题具有特别重要的意义.但迄今未见有详细的报道.本文对阳离子交换树脂—HCl溶液体系中的UO_2~(2+)—H~+正、逆交换,特别对~(235)UO_2~(2+)—~(238)UO_2~(2+)交换动力学及机制作了研究和探讨.     

离子交换法处理曝气后氯化亚铜的废水研究

通过预曝气的方法,氯化亚铜废水溶液中Cu(Ⅰ)被氧化为Cu(Ⅱ),并能简化氯化亚铜废水溶液的粒子结构,分别采用201×7 OH-型强碱性阴离子树脂和732 Na型强酸性阳离子树脂处理曝气后的氯化亚铜废水,进行了曝气时间、pH值和温度等因素对废水处理效果的研究,得到最佳的处理废水条件。曝气180 min后,在温度60 ℃,V溶液/V树脂=2/1,阳离子交换反应15 min时,可使废水溶液中铜粒子浓度达到国家废水一级排放标准。     

球形纤维素磁性阴离子交换树脂的化学转化制备及特性研究

自制了大孔球形纤维素基阴离子交换树脂(PSC-AN),并利用化学转化法成功制备了大孔球形纤维素基磁性阴离子交换树脂(PSC-MAN)。对影响树脂质量磁化率的几个主要因素进行了探讨,实验确定最佳制备条件为:铁盐的配比为1∶10,EDTA的浓度为0.005 mol/L。对树脂的结构和性能进行了研究,表明化学转化法制备大孔球形纤维素基阴离子交换树脂(PSC-MAN)磁性强,在碱液中相当稳定,树脂磁化前后交换容量分别为Q前=1.33 meq/g、Q后=1.16 meq/g,即树脂基的交换容量基本不受磁化过程的影响。     

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。     

Pressure effect on bulk weak ferromagnets: (BDH-TTP)[M(isoq)2(NCS)4] (M = Cr(III), Fe(III); isoq = Isoquinoline)

The pressure dependence of the magnetic properties of weak ferromagnets (BDH-TTP)[M(isoq)2(NCS)4] [BDH-TTP = 2,5-bis(1',3'-dithiolan-2'-ylidene)-1,3,4,6-tetrathiapentalene; M = Cr, Fe; isoq = isoquinoline] is discussed. These salts form two-dimensional magnetic sheets, where ferrimagnetic chains of donor cation radical (S = 1/2) and anion [S = 3/2 (Cr), 5/2 (Fe)] are antiferromagnetically connected by weak donor-donor and anion-anion interchain S...S contacts. Under ambient pressure, both the Cr and Fe salts undergo a weak ferromagnetic transition at Tc = 7.6 K, below which a spontaneous magnetization emerges along the direction perpendicular to the sheets. The application of the pressure elevates the transition temperatures up to 16.6 and 11.6 K at 9 kbar for M = Cr and Fe, respectively. As the pressure increases, the remanent magnetization M(r) decreases, whose pressure dependence for the Cr salt is larger than that for the Fe salt. This difference indicates that the spin-canting angle of the Cr salt is reduced because of the increase of antiferromagnetic interaction by applied pressure, in contrast to the Fe salt, where single-ion anisotropy contributes less. The quantitative analysis of the magnetization curves of the Cr salt using the mean-field approximation reveals that the intermolecular exchange interaction increases as the pressure increases, among which the interchain anion-anion interaction has the highest pressure sensitivity. This result is consistent with the temperature dependence of the crystal structure showing that the thermal contraction in the distances of interchain anion-anion S...S contacts is the most remarkable in intrachain S...S contacts. The large pressure dependence of the transition temperature of these salts is therefore explained as a result of the fact that the interchain interactions, the anion-anion interaction in particular, are strengthened by applied pressure.     

合成乳酸正丁酯的主要催化剂述评

综述聚氯乙烯—三氯化铁树脂、强酸性阳离子交换树脂、氨基磺酸、甲基磺酸、维生素C、稀土化合物、硅胶固载硫酸钛、硫酸铁铵、硫酸氢钠、磁性固体超强酸、酸改性高岭土、杂多酸(盐)等数种不同催化剂催化合成乳酸正丁酯的实验结果.结果表明,强酸型阳离子交换树脂、硫酸氢钠、磁性固体超强酸、硅胶固载硫酸钛、活性炭固载杂多酸五种催化剂催化合成乳酸正丁酯的酯收率较高,具有实际使用价值.     

Activity of metal chromate and phosphate supported on ion‐exchange resins toward hydrogen peroxide decomposition

The mixed resins, Dowex MR‐3 and MR‐12, in the H⁺/Cl⁻ form, and the cation resin, Dowex‐50W, in the H⁺ form, were used as a support for some metal chromate and phosphate salts. Similarly, anionic resin, Amberlite IRA‐400, in the Cl⁻ form, was used as a support for some metal chromate salts. The activity of these metal salt‐supported on four different resins toward hydrogen peroxide decomposition was investigated. The decomposition of H₂O₂, with these catalysts, was found to follow first‐order kinetics with respect to [H₂O₂]. Factors that affected the rate of reaction, such as mesh size of the support, amount of supported salt, and the electrostatic interactions, were investigated. With Ag(I)‐chromate supported on mixed resin MR‐3 in the Ag⁺/NO₃⁻ form, the rate of reaction was greater than that with the mixed resin MR‐12 in the same form. Moreover, the rate with Ag(I) chromate supported on the anion resin IRA‐400 in the R‐NO₃⁻ form was greater than mixed resins. Also, the rate with Fe(III) chromate supported on Amberlite IRA‐400 in the R‐CrO₄²⁻ form was greater than other counter‐anionic forms as well as Dowex‐50W resin in the metal ion form. However, Fe(III)‐chromate supported on cation resin R‐Fe³⁺ showed greater activity than other cationic forms. On the other hand, the rate with MR‐3 resin in the Na⁺/PO₄³⁻ form was greater than that in the presence of supported Fe(III) phosphate. However, the rate of reaction increased when Fe(III) was replaced by Ba(II). Iron(III) phosphate supported on Dowex‐50W resin in the Na⁺ form showed greater activity compared to MR‐3 resin in the Na⁺/PO₄³⁻ form. In the case of Fe(III) phosphate supported on mixed resin MR‐12, the rate was much greater than that with unsupported resin. However, when Ba(II) phosphate was incorporated instead of Fe(III) phosphate, the rate of reaction increased considerably. The activity of Fe(III) chromate is greater than that of Fe(III) phosphate supported on the same cation resin. Activation parameters were evaluated and a probable reaction mechanism was proposed. © 2000 John Wiley & Sons, Inc. Int J Chem Kinet 32: 667–675, 2000     

The separation of beryllium from iron,aluminium and titanium by ion exchange,and its application to the analysis of beryl

A now ion exchange method is proposed for the separation of Befrom Al, Fe, Ti, Ca and phosphate, by prefercntially adsorbing it on cation exchange resin AmberliteIR-120, after complexing the other ions with EDTA and H₂0₂ The successful application of the method to the analysis of beryls is demonstrated     

蛇笼树脂交换量的测定

本文介绍了蛇笼树脂的结构及其离子阻滞作用机理,提出了离子阻滞交换量的概念.研究了残余阴离子交换量、残余阳离子交换量、全阴离子交换量、离子阻滞交换量和全阳离子交换量的测定及计算方法,测定了美国的Retardion 11A-8及本文合成的9种蛇笼树脂的交换量.     

Ion exchange removal of calcium carbonate and gypsum from mineral material prior to determination of cation exchange capacity using89Sr++

Summary The aim of the present work was to show that ion exchange resins can be used to remove sparingly and slightly soluble salts from calcareous and gypseous soils, which may otherwise cause serious errors in the determination of cation exchange capacity. It was shown that CaCO₃ and CaSO₄-2H₂O can be removed from a mixture with montmorillonite(Ca++) by a mixed bed resin. After resin treatment of the mixture its C.E.C. as retained Sr⁺⁺ corresponds approximately to the C.E.C. for pure montmorillonite within certain limits. Use of an anion exchange resin alone for removing these salts, however, gave an Sr⁺⁺ retention well below the C.E.C. for the mineral. It was assumed that this results from the blocking of exchange sites by resin particles.

---

Zusammenfassung In kalkhaltigen und gipshaltigen B?den st?ren CaCO₃ und CaSO₄-2H₂O die Bestimmung des Kationenaustauschverm?gens. In der vorliegenden Arbeit wird gezeigt, da? Salze wie CaCO₃ und CaSO₄-2H₂O aus Mischungen mit Ca-Montmorillonit durch Ionenaustauscher herausgel?st werden k?nnen. Als Ionenaustauscher müssen jedoch Mischbettaustauscher verwendet werden; Anionenaustauscher allein liefern bei einer anschlie?enden Bestimmung des Kationenaustausches mit Sr⁺⁺ falsche Werte. Die angegebene Methode erscheint vor allem für die Untersuchung von B?den wichtig zu sein.

     

Determination of U,Th and other impurities in molybdenum by radiochemical neutron activation analysis

A radiochemical separation method has been applied for determining uranium, thorium and other impurities in molybdenum metallic powder. The impurities of Na, K, Sm, Cr, Zr, Cs, Rb, Zn, Fe, Co and La were separated with a cation exchange resin, and uranium and thorium were, then, separated with an anion exchange resin. The content of impurities were determined by a single comparator method using two monitors, gold and cobalt.     

Neutron activation analysis of rare earth impurities in metallic uranium

A method with a sensitivity of 2·10⁻⁷ to 1·10⁻¹⁰% has been developed for determining Yb, Ho, Dy, Gd, Eu, Sm and La impurities in metallic uranium by means of neutron activation. The method is based on a preliminary chromatographic separation of the total amount of rare earth elements from uranium by passing the solution in sulphuric acid through KU-2 cation exchange resin and eluting the traces of uranium retained by the resin with a solution of ascorbic acid. The rare earth impurities are then eluted from the resin with 4–5N HCl, evaporated, and irradiated for 20 hours with a neutron flux of 1.2·10¹³ n·cm⁻²·sec⁻¹. Subsequently the traces of the rare earth elements are co-precipitated with Fe(OH)₃, dissolved in concentrated HCl and separated from the iron and other impurities by passing the solution through Dowex 1X8 anion exchange resin in the chloride form. The individual rare earth elements are then separated from each other using KU-2 cation exchange resin and a solution of ammonium α-hydroxyisobutyrate as the eluant.