洗涤剂用沸石的钙离子交换性能的研究

作为洗涤剂助剂,沸石的主要作用是通过离子交换降低水中的钙镁离子浓度、软化洗涤用水以提高洗涤剂中的表面活性剂的洗涤效率。因此,沸石对钙镁离子交换容量的大小和交换速率的快慢是评价洗涤用沸石的重要质量指标［１,２］。目前,使用最多的沸石类助剂为ＮａＡ沸石。为了弥补ＮａＡ型沸石镁离子交换能力的不足,先后又出现了Ａ、Ｘ型沸石混合使用［３］、高铝Ｘ型沸石(ＭＡＸ)［４～５］和高铝Ｐ型沸石(ＭＡＰ)等技术［１,２］。ＭＡＸ型和ＭＡＰ型沸石与ＮａＡ型沸石一样具有最小的硅铝比(ＳｉＯ２／Ａｌ２Ｏ３＝２)。因此,这三种沸石的…     

离子选择电极法测定洗涤剂用沸石的钙离子交换性能

1 引言采用EDTA滴定、ICP和AA法测定洗涤剂用沸石的钙离子交换量时.需要将溶液与沸石分离后进行,因而不易测定交换过程中沸石的钙离子交换速率.而采用ISE法,可以在沸石与钙离子交换时,实时测定溶液中钙离子浓度随交换时间的变化,求得钙离子交换速率.本文采用ISE法测定洗涤剂用沸石的钙离子交换速率及交换量.2 实验部分2.1 仪器与试剂 pXS-215型离子活度计(上海雷磁仪器厂);钙离子选择电极(ISE)和甘汞电极(上海雷磁仪器厂);记录仪(上海大华仪器厂).洗涤剂用4A沸石(山东铝厂),0.1mol/L标准CaCl_2溶液,0.5mol/L NaOH溶液.     

高铝MAP沸石的非自发结晶动力学研究

在强碱性水溶液体系中,以水玻璃为硅源,以铝酸钠为铝源,在类质同晶高硅P沸石晶种导向作用下,反应物中自发生成的A型沸石可转晶为纯相高铝MAP沸石。升高反应温度有利于提高产物的结晶度。由不同温度下的晶化曲线计算出MAP沸石表观生长活化能为59.6kJ.mol^-^1。不用晶种时,同一反应物体系结晶产物为单一的A型沸石。在该反应物体系中,A型沸石的成核活化能与生长活化能分别为40.3和50.7kJ.mol^-^1。MAP高的生长活化能以及A型沸石相对低的成核与生长活化能揭示合成MAP沸石时使用晶种的原因。     

高硅无铝Mo-Beta沸石的合成与结构表征

用水热晶化法合成了无铝Mo-Beta沸石,讨论了合成条件对无铝Mo-Beta沸石晶化的影响,通过化学分析、XRD、IR、DTA/TGA、TEM、NMR、ICP和UV-Vis紫外漫反射光谱测定了样品的n(SiO₂)/n(MoO₃)比,并对其结构进行了表征,结果表明,所合成的Mo-Beta沸石晶粒均匀,Mo存在于沸石骨架中,由于Mo的掺入,引起Beta沸石红外光谱、差热分析曲线及晶胞参数, ²⁹SiMASNMR谱等发生变化。     

Y型沸石和高岭土原位晶化产品的Tb／Tb同位素交换及NaTb,Tb／…

本文在前文＾［１］Ｙ型沸石和高岭土原位晶化产品上的Ｎａ／Ｔｂ离了交换平衡研究的基础上，进一步了这两种离了交换剂上Ｔｂ／Ｔｂ同位素交换及Ｎａ／Ｔｂ，Ｔｂ／Ｎａ正逆离子交换动力学，确定了反应机理，测得了铽的自扩散系数以及正逆交换的积分粒内互扩散系数。对这两种离交换剂所得结果进行了对比和讨论。     

新型洗涤剂用沸石MAP的合成及其性能表征

在ＳｉＯ_２－Ａｌ_２Ｏ_３－Ｎａ_２Ｏ－Ｈ_２Ｏ体系中,采用加入晶种的方法水热合成出新型洗涤剂用沸石－ＭＡＰ。其硅铝比（Ｓｉ／Ａｌ）在 １．０７－１．１３之间,平均晶粒直径小于０．４μｍ,钙离子交换容量为２９０～３１３ ｍｇＣａＣＯ_３／ｇ（干沸石）,非离子表面活性剂的吸附量在 ８３～ １００ｇ ｏｉｌ／１００ｇ（沸石）之间。本文着重考察了影响合成 ＭＡＰ沸石的因素,确定了ＭＡＰ沸石会成的最佳范围,并对其物理化学性质进行了表征。     

阳离子交换膜催化合成乙酸丁酯动力学研究

研究了以阳离子交换膜为催化剂合成乙酸丁酯的动力学,回归得出催化剂的影响函数f(w),动力学方程中指前因子k0=2284024.48L/mol·min,活化能Ea=52102.95J/mol,建立动力学模型,得到实验范围内的动力学方程并对动力学方程的正确性进行了验证。     

钠改型天然斜发沸石对铵离子的交换性能

对分别来自国内三个产地和澳大利亚的沸石样品进行了铵离子交换性能的研究。在25℃下了样品的交换速率曲线。利用Verrmeulen's模型处理动力学数据，计算得到扩散系数，与文献报道的结果相一致，并发现不同样品的扩散系数与其致密程度相关。将粒度200mesh的沸石分别用三种不同方法聚集为颗粒，并测定了表观的扩散系数，均高于原颗粒的扩散系数，其中凝胶颗粒提高了一个数量级。     

类固相法快速合成高钙镁离子交换性能的P型分子筛

以硅铝干凝胶为硅源和铝源,氢氧化钠为碱源,采用类固相法快速合成了P型分子筛,并通过X射线衍射（XRD）、扫描电镜（SEM）等手段对产品进行了表征分析。结果表明,硅铝干凝胶的组成n_SiO2/n_Al2O3=5,晶化时间和晶化温度分别为3 h、140℃,原料的组成n_Na2O/n_SiO2、n_H2O/n_SiO2=18.51时,可制备形貌均一、结晶良好的P型分子筛产品。与传统水热法相比,该方法极大地减少了合成过程的用水量,缩短了晶化时间,提高了产品的钙镁离子交换性能,从整体上优化了P型分子筛的合成工艺。     

Determination of Chelating Properties of Detergent Builders with the Calcium Selective Ion Electrode

Abstract

A liquid membrane calcium selective ion electrode was used to measure the free calcium content in equilibrium with calcium chelates. The chelating value, chelating curves, formation constants and equivalent weights of several detergent builders were calculated from these measurements.     

Kinetics Characterization of Ion Release under Dynamic and Batch Conditions. I. Weak Acid and Weak Base Ion Exchange Resins

The aim of the present work is concerned with a study of the kinetics of release of both Ca²⁺ and F⁻ from the corresponding loaded ion-exchange resins (weak acid and weak base character for Ca²⁺ for F⁻, respectively), using both dynamic and batch experimental conditions with an artificial saliva solution as the ion-exchange media at 293 and 310 K. The influence of resin particle size and the temperature were evaluated by the kinetics parameters for the effective rate of release (B) and diffusion coefficient (D). The rate of ion release increases with temperature and decreases with particle size. The experimental data were well fitted by models based on intraparticle diffusion-controlled processes. In dynamic studies, the linear dependence of −log ₁₀(B) with the diameter of the resin particles can be applied for the estimation of B values when resins of low particle size are considered. In batch processes, although resins of low particle size can be studied, a linear relationship was only attained for the case of slow ion-exchange kinetic systems.     

带电胶体离子扩散与交换动力学的比较

Taking soil colloid and hydrated silica (quartz sand) as the experimental material, the comparative study has been made on the kinetics of ion diffusion and ion exchange in charged colloid and charged coarse disperse systems. The results showed that ion exchange kinetics in the two systems conform to the kinetic law of ion diffusion. Besides, through this comparative study on the kinetics of ion exchange and ion diffusion, a method has been advanced theoretically to estimate the quantity of adsorbed ion that is located in the inner of the Helmholtz layer. As far as hydrated silica is concerned , there were about 33 per cent of the total adsorbed quantity of Mg2+that were located in the inner of the Helmholtz layer under the given experimental conditions, bu tfor soil colloid the percentage was only 7.5.     

在阴离子交换树脂催化剂上合成二丙酮醇的动力学研究

动力学研究表明,在碱性树脂催化剂上丙酮缩合制二丙酮醇是一个1-1级可逆反应,本文对此多相催化的反应机理进行了探讨。     

儿茶素在离子交换纤维上的吸附动力学

儿茶素在离子交换纤维上的吸附动力学;离子交换纤维; 儿茶素; 吸附动力学; 反应级数; 反应速率常数     

Experimental and Modeling Study of Ion Exchange Between Aqueous Solutions and the Zeolite Mineral Clinoptilolite

Ion-exchange experiments were conducted at 25°C between the zeolite mineral clinoptilolite and aqueous solutions of Na⁺/Sr²⁺ (0.005, 0.05, and 0.5 N), K⁺/Sr²⁺ (0.05N), and K⁺/Ca²⁺ (0.05 N). The isotherm data were used to derive equilibrium constants and Gibbs energies for the ion-exchange reactions and Margules parameters for the zeolite solid solution. The Margules model, in combination with the Pitzer equations for activity coefficients of aqueous ions, was used to predict isotherms for ion exchange involving clinoptilolite and aqueous solutions of Na⁺/Sr²⁺, K⁺/Sr²⁺, and K⁺/Ca²⁺ over wide ranges of solution composition and concentration. The ion-exchange isotherms are strongly dependent on the total solution concentration. For Na⁺/Sr²⁺ ion exchange, isotherm values at 0.005 and 0.5 N predicted using thermodynamic parameters derived from the 0.05 N data showed excellent agreement with measured values. The model was also applied to calculations of aqueous composition based on the chemistry of coexisting zeolite phases. The results show that the aqueous composition can be predicted well from the composition of the zeolite, at least for systems that involved binary (two-cation) exchange. Because the thermodynamic model can be easily extended to ternary and more complicated mixtures, it may be useful for modeling ion-exchange equilibria in multicomponent systems.     

过渡金属离子在焦磷锑酸锡上的离子交换反应动力学研究

应用Nernst-Planck方程研究了过渡金属离子CO~(2+)、Cu(2+)、Zn(2+)和Cd(2+)在焦磷锑酸锡上的离子交换反应动力学.当金属离子浓度大于或等于0.050 mol/L时.其交换反应速率基本上不受金属离子浓度的影响,离子交换受粒间扩散过程控制.通过求解Nernst-Planck方程得出了自扩散系数、活化能和活化熵,这些动力学参数的获得有助于揭示其离子交换机理。     

NaA沸石离子交换过程的介电弛豫谱研究

在40 Hz~110 MHz频率段对不同Ca²⁺交换度的NaA沸石堆积体系进行了介电测量, 并利用Cole-Cole公式及Hanai方法对介电参数和相参数进行拟合与解析. 结果表明, 随着Ca²⁺交换度的不断增高, 堆积体系的介电增量、弛豫频率、弛豫分布系数以及粒子的电导率均有不同程度的降低, 而粒子的介电常数保持不变. 通过综合分析弛豫变化规律与离子交换度的内在联系发现, 离子交换后Ca²⁺选择六元环占位, 同时六元环和八元环位置的相邻2个Na⁺被置换; 占据六元环的Ca²⁺与八元环位置的Na⁺对沸石粒子的极化贡献等价; Ca²⁺的进入导致沸石孔道内微观电场多样化.