碱金属离子X型沸石的固相离子交换及其催化性能的研究

本文考察了水合13X沸石与碱金属盐类间的固相离子交换反应,并对交换样品的比表面、孔容和异丙醇分解反应活性进行了测定.结果表明,这种类型的固相离子交换在室温下即可发生.体积较大的Cs~+比K~+难于交换,高温焙烧有利于提高Cs~+的交换度.固相交换样品的比表面、孔容变化和异丙醇分解反应活性都与液相交换样品相同,只是交换度的函数,与交换方法无关.与K~+交换样品相比,Cs~+交换样品中Cs~+离子更多地占据超笼,导致更高的超笼局部碱性和脱氢反应活性.     

水合NaX沸石与碱金属盐类间的固相离子交换

通过XRD和吡啶吸附的IR技术考察了水合13X沸石与碱金属盐类间的固相离子交换反应,结果表明,此类固相离子交换在室温下即可发生。一次交换的程度有限,通过重复交换可提高交换度,体积较大的Cs⁺比K⁺难于交换,高温焙烧有利于提高Cs⁺的交换度。     

引入SiO2对SO4^2—／ZrO2超强酸体系的影响

用共沉淀法和负载法制备了一系列SO4^2-/ZrO2催化剂,详细研究了添加SiO2对SO4^2-/ZrO2超强酸样品的晶化、比表面、硫含量、超强酸性和异丙苯裂解及异丙醇脱水反应的影响。引入SiO2会延迟ZrO2的晶化和晶相转变,减弱SO4^2-/ZrO2体系的超强酸性,但对提高样品的异丙苯裂解和异丙醇脱水反应活性有利。     

电喷雾质谱法中K^+加合离子受Cs^+影响及在牛膝多糖分子 量分布测定中的应用

以测定牛膝多糖的分子量分布为例,研究了在Cs^+存在情况下,电喷雾(ESI)/飞行时间质谱法(TOF-MS)中出现加合离子(adductions)的规律。实验中发现,牛膝多糖样品中加入适量的Cs^+,可影响其与Na^+,K^+加合离子的相对丰度,使K^+加合离子成为几乎唯一的加合离子形式,并获得了满意结果。另外讨论了Cs^+浓度、喷管电压(nozzlepotential)对这一现象的影响。     

引入SiO2对SO2-4/ZrO2超强酸体系的影响

用共沉淀法和负载法制备了一系列SO2-4/ZrO2-SiO2催化剂, 详细研究了添加SiO2对SO2-4/ZrO2超强酸样品的晶化、比表面、硫含量、超强酸性和异丙苯裂解及异丙醇脱水反应的影响. 引入SiO2会延迟ZrO2的晶化和晶相转变, 减弱SO2-4/ZrO2体系的超强酸性, 但对提高样品的异丙苯裂解和异丙醇脱水反应活性有利.     

CuCl_2和HY分子筛的表面反应及Cu/Y分子筛的制备及其催化甲醇氧化羰基化（英文）

以CuCl2为前驱物与HY分子筛进行固相离子交换制备了Cu/Y催化剂,采用热重方法研究了CuCl2与HY分子筛的表面固相离子交换反应,结合活性测试表明催化剂中高度分散的CuCl和离子交换形式的Cu+物种是甲醇氧化羰基化合成碳酸二甲酯的催化活性中心.X射线光电子能谱表征和元素分析结果表明,活性金属Cu主要以CuCl形式存在于分子筛外表面,而在分子筛笼内则以交换的Cu+和少量吸附的CuCl形式存在.与以CuCl为交换铜源所制催化剂相比,以CuCl2为铜源制备的催化剂Cu含量低,催化活性更高.     

不同方法制备的Cu/HZSM-5催化剂上NO的催化分解反应

采用离子交换法、固相分散法和微波固相法等不同方法制备了Cu/HZSM-5催化剂,以BET、XRD和XPS等手段对催化剂样品进行了表征。结果表明,不同方法制备的Cu/HZSM-5催化剂上Cu物种的落位分布状态不同,离子交换法制备的催化剂Cu物种更多地落位于分子筛孔道内,微波固相法和固相分散法制备的催化剂Cu物种较多地落位分布在分子筛外表面。固相分散法制备的样品未能使铜物种完全分散于分子筛表面,在13.1°、16.8°、35.5°和38.0°等处仍存在CuO的晶相衍射峰。催化分解NO反应的活性考察结果表明,用微波固相法制备的催化剂催化分解NO的活性及稳定性明显超过另两种方法所制备的催化剂,在无氧条件下NO最初转化率高达89.2%,经反应25h后,转化率仍维持在70%以上;在富氧气氛下催化分解NO活性降低速率低于由离子交换法制备的催化剂。结合表征结果可以得出,落位于分子筛外表面以离子交换态形式存在的Cu物种对催化分解NO反应更为有利,而且催化稳定性更好。     

高活性甲醇氧化羰基化CuY催化剂的结构及催化活性中心

采用硝酸铜溶液和NaY分子筛溶液离子交换制备了CuY催化剂,通过加入氨水提高交换溶液的pH值以及高温焙烧活化,显著提高了甲醇氧化羰基化合成碳酸二甲酯的催化活性,与固相离子交换、沉积和浸渍法制备的催化剂相比,虽负载的铜量较低,但催化活性较高. 通过元素分析、XRD、H2-TPR、XPS和AES等对CuY催化剂微观结构的表征表明,在Cu(NO3)2离子交换溶液中加入氨水,促进了Cu2+离子交换的进行,提高了CuY催化剂的Cu交换量,并且交换的Cu2+主要落位于分子筛的超笼中. 在惰性气氛中焙烧活化CuY催化剂,Cu2+自还原为Cu+,氨促进了自还原过程的进行,显著提高了催化剂的活性. 焙烧活化温度越高,越有利于超笼中Cu2+→Cu+的自还原过程,使超笼中Cu+的含量增加, CuY催化活性增加. 进一步研究表明Y分子筛超笼中的Cu+是主要的催化活性中心.     

冠醚配合物热力学性质的研究VI. 几种冠醚配合物的CNDO/2计算

本文用CNDO/2方法从理论上探讨了碱金属离子Na^+,K^+和Cs^+与2,3-苯并-8,11,15-三甲基-18-冠-6(简称BC3-18C6)在溶液中发生的配位反应,计算了配位反应中CNDO总能量的变化,再现了量热法所得出的碱金属离子Na^+,K^+和Cs^+与BC3-18C6在溶液中生成配合物的稳定性次序:K^+>Na^+>Cs^+。所计算的配位能和配合物的水化能表明,在水溶液中碱金属水合离子与冠醚配位,形成稳定的二水配位的碱金属离子冠醚配合物[M(BC3-18GC6)(H~2O)~2]^+。碱金属离子与冠醚中的氧形成的金属-氧键不如其水合物中的金属-氧键强,碱金属离子能与冠醚配位形成稳定的配合物主要是由于配体的大环效应和配合物的溶剂化作用。     

CuCl2和HY分子筛的表面反应及Cu/Y分子筛的制备及其催化甲醇氧化羰基化

以CuCl₂为前驱物与HY分子筛进行固相离子交换制备了Cu/Y催化剂,采用热重方法研究了CuCl₂与HY分子筛的表面固相离子交换反应,结合活性测试表明催化剂中高度分散的CuCl和离子交换形式的Cu⁺物种是甲醇氧化羰基化合成碳酸二甲酯的催化活性中心。X射线光电子能谱表征和元素分析结果表明,活性金属Cu主要以CuCl形式存在于分子筛外表面,而在分子筛笼内则以交换的Cu⁺和少量吸附的CuCl形式存在。与以CuCl为交换铜源所制催化剂相比,以CuCl₂为铜源制备的催化剂Cu含量低,催化活性更高。     

MECHANISM OF CESIUM EXCHANGE WITH POTASSIUM TITANIUM HEXACYANOFERRATE

The mechanism of cesium exchange on potassium titanium hexacyanoferrate (KTiFC) is described in this paper.The dependence of the exchange rate on temperature,particle granule size,and shaking frequency is studied.The results show that ion exchange process is controlled by liquid film diffusion in granule particle.An exchange reaction occurs mainly between K^+ in the exchanger and Cs^+ in the solution.     

Combined Water and the Ion Exchange Characteristics of Manganese Dioxide Produced by Ozonation

The change in ion exchange properties of manganese dioxide produced by ozonation (OMD) was studied with respect to its preheated temperature. This was performed by heating samples to different temperatures and later, saturating a part of them in aqueous cadmium sulfate solutions. Analyses were practiced on both the cadmium ion exchanged and un-ion exchanged samples. Results showed that the ion exchange reaction followed a stoichiometric relation between the hydrogen and cadmium ions, promoted by the combined water. The molar ratio of combined water to exchanged cadmium was found to be five. X rays and photographs taken in the scanning electron microscope showed that the structure and morphology of the OMD were not modified by the insertion of the cadmium during ion exchange. From the X rays, the structure of the OMD was determined to be of the gamma type. When the samples were heated to 400 and 500 degrees C, the crystal structure changed to beta and finally to Mn2O3, respectively. However, the changes in structure alone apparently did not affect the ion exchange. The surface area, measured by the BET technique, diminished linearly with the preheat temperature. The ion exchanged cadmium and the surface area showed a nonlinear relationship. However, the surface area and the quantity of combined water in the OMD were both linearly affected by preheating and are directly related to the ion exchange capacity. Copyright 1999 Academic Press.     

Effects of exchanged surfactant cations on the pore structure and adsorption characteristics of montmorillonite

Ca-montmorillonite (Ca-Mont) was exchanged with two quaternary amines, tetramethylammonium (TMA) chloride and hexadecyltrimethylammonium (HDTMA) bromide, to study the surfactant ion exchange effect on the pore structure, surface characteristics, and adsorption properties of montmorillonite. The revolution of both the surface area and pore structure of montmorillonite was characterized based on classical and fractal analyses of the nitrogen isotherms as well as the XRD patterns. The change of surface characteristics was identified from FTIR patterns and zeta-potential plots. The adsorption isotherms of acid dye, Amido Naphthol Red G (AR1), were then measured to identify the effects of the ion-exchange process on the adsorption properties of montmorillonite. It was found that the exchange processes might induce an increase or decrease in the surface area, pore size, pore volume, and surface fractal dimension D of montmorillonite, depending on the size, the molecular arrangement, and the degree of hydration of the exchanged ion in the clay. On the other hand, it was also found that the hydrophobic bonding by conglomeration of large C(16) alkyl groups associated with HDTMA could cause positive charge development on the surface of montmorillonite, which was not observed for TMA-modified montmorillonite (TMM). The effects of the alteration of the surface characteristics of montmorillonites on their adsorption selectivity for acid dye were discussed.     

XRD测定NaY型分子筛的钾离子交换度

对K离子交换的NaY分子筛进行火焰光度分析和XRD测试,研究XRD特征峰的面积和强度变化与离子交换度之间的关系。结果表明,衍射角2θ=20.3何恢蒙戏迩慷取⒎迕婊谌淄挤段诘陌俜直扔隟+离子交换度之间均存在很好的线性关系,由此得到的交换度计算值与采用火焰光度分析方法得到的实验值之间的相对误差分别小于2.0%和5.5%,可以用于离子交换度的定量测定。     

分子筛表面酸性对微波固相法制备ZnCl2/Y催化剂的影响

 采用XRD和原子吸收光谱法研究了微波作用下分子筛表面酸性对ZnCl2与Y分子筛固态相互作用的影响．结果表明，微波辐射可显著促进ZnCl2在分子筛表面分散，其分散阈值与分子筛表面酸性有关．随着分子筛表面酸量和酸强度增加，ZnCl2在分子筛表面的最大分散量减少，分散的ZnCl2与Y分子筛的固态离子交换量也减少；NaY型分子筛比HY分子筛更容易发生固态离子交换反应．考察了微波固相法制备的ZnCl2／HY催化剂在苯甲醚与乙酰氯酰化反应中的催化性能．结果表明，在分子筛表面分散的ZnCl2具有更高的催化活性及对甲氧基苯乙酮选择性．     

Decationization and dealumination of clinoptilolite tuff and ammonium exchange on acid-modified tuff

The paper presents results of investigation of exchange of the clinoptilolite tuff cations with hydrogen ions from HCl solution of concentration 0.1 mmol cm(-3) and ammonium ions solutions of concentrations 0.0071 to 2.6 mmol cm(-3). Molal concentrations, x (mmol g(-1)) of cations exchanged in acid solution and in ammonium ions solutions were compared with molal concentrations of cations obtained by determination of the cation-exchange capacity of clinoptilolite tuff. The obtained results show that at ammonium ion concentrations lower than 0.1 mmol cm(-3), with regard to exchange capacity for particular ions, best exchanged are Na+ ions, followed by Mg2+ and Ca2+ ions, while exchange of K+ ions is the poorest (Na+ > Mg2+ > Ca2+ > K+). At ammonium concentrations from 0.2 to 1 mmol cm(-3) the order is Na+ > Ca2+ > Mg2+ > K+. At concentrations higher than 1 mmol cm(-3) the order is Na+ > Ca2+ > K+ > Mg2+. The results are a consequence of the uptake of hydrogen ions by zeolite samples in ammonium ions solutions at concentrations lower than 1 mmol cm(-3) and indicate the importance of Mg2+ (besides Na+ ions) for the exchange between clinoptilolite cations and H+ ions, in contrast to K+ ions, whose participation in the reaction with H+ ions is the lowest. During decationization of the clinoptilolite in acid solution, best exchanged are Na+, Mg2+, and Ca2+ ions, while exchange of K+ ions is the poorest. Due to poor exchange of K+ and H+ ions and good exchange of Na+, Mg2+, and Ca2+ ions, it is to be assumed that preservation of stability of the clinoptilolite structure is caused by K+ ions present in the channel C. Clinoptilolite is dissolved in the clinoptilolite A and B channels where Na+, Mg2+, and Ca2+ ions are present. On the acid-modified clinoptilolite samples, exchange of ammonium ions is poorer than on natural zeolite. The longer the contact time of the zeolite and acid solution, the worse ammonium ions exchange. It can be assumed that H+ ions exchanged with zeolite cations are consumed for solution of aluminum in the clinoptilolite structure; therefore the concentration of H+ ions as exchangeable cations decreases. In the ammonium ion solution at a concentration of 0.0065 mmol cm(-3), from the acid-modified zeolite samples, Al3+ ions are exchanged best, followed by Na+, Mg2+, Ca2+, and K+ ions. Further to the results, it is to be assumed that exchangeable Al3+ ions available from clinoptilolite dissolution are best exchanged with H+ ions in acid solution.     

Na型斜发沸石上Na+-Cu2+离子交换过程动力学

用静态离子交换法研究了Ｎａ型斜发沸石上２Ｎａ＝Ｃｕ＾２＋离子交换动力学，分别测定了液膜扩散常数Ｒ，粒内扩散系数Ｄ和滞留时间Ｔｄ，实验发现，离子交换起始为液膜扩散控制，随后在交换的大部分时间内为粒内扩散控制，并就温度、浓度对离子交换过程速率，Ｃｕ＾２＋平衡交换数量以及滞留时间的影响进行了讨论。     

Adsorption equilibrium modeling and solution chemistry dependence of fluoride removal from water by trivalent-cation-exchanged zeolite F-9

Fluoride in drinking water above permissible levels is responsible for human dental and skeletal fluorosis. In this study, therefore, the large internal surface area of zeolite was utilized to create active sites for fluoride sorption by exchanging Na+-bound zeolite with Al3+ or La3+ ions. Fluoride removal from water using Al3+- and La3+-exchanged zeolite F-9 particles was subsequently investigated to evaluate the fluoride sorption characteristics of the sorbents. Equilibrium isotherms such as the two-site Langmuir (L), Freundlich (F), Langmuir-Freundlich (LF), Redlich-Peterson (RP), Toth (T), and Dubinin-Radushkevitch (DR) were successfully used to model the experimental data. Modeling results showed that the isotherm parameters weakly depended on the solution temperature. From the DR isotherm parameters, it was considered that the uptake of fluoride by Al3+-exchanged zeolite proceeded by an ion-exchange mechanism (E = 11.32-12.13 kJ/mol), while fluoride-La3+-exchanged zeolite interaction proceeded by physical adsorption (E = 7.41-7.72 kJ/mol). Factors from the solution chemistry that affected fluoride removal from water were the solution pH and bicarbonate content. The latter factor buffered the system pH at higher values and thus diminished the affinity of the active sites for fluoride. Natural groundwater samples from two Kenyan tube wells were tested and results are discussed in relation to solution chemistry. In overall, Al3+-exchanged zeolite was found to be superior to La3+-exchanged zeolite in fluoride uptake within the tested concentration range.