超声波合成磁性4A沸石分子筛

为了解决微细粉末状沸石产品应用中与所处理溶液难以分离的问题, 在传统水热合成法合成4A沸石的晶化原料液中, 加入磁性Fe3O4微粒, 经过70 ℃, 功率为100 W的超声波晶化6 h, 合成了一系列Fe3O4含量不同的磁性4A沸石,并对其进行了XRD、SEM、IR、TG/DTA、EDX、磁化率及吸附性能等表征测试. 结果表明, 磁性4A沸石具有良好的磁稳定性, 其磁化率随Fe3O4含量的增加而增大; 磁性4A沸石对水中氟离子和六价铬的吸附与纯4A沸石性能相同, 其吸附速率可以用拟二级动力学方程来描述.     

小孔沸石微结构的CO_2吸附表征

以3种已知结构的小孔沸石3A、4A和5A为研究对象,以N2和CO2为吸附质,通过吸附数据测定,研究了小孔沸石微孔结构的吸附表征方法.结果表明,N2吸附无法检测4A沸石的孔,而CO2吸附可以检测.对于4A和5A沸石,在35s内CO2吸附就可以达到平衡.HK(Horvath-Kawazoe)柱状模型不能表征4A和5A沸石的孔结构,但是HK球形模型可以,基于最大吸附量、D-A(Dubinin-Astakhov)方程和Langmuir-Freundlich模型计算了4A和5A沸石的微孔孔容,其中根据最大吸附容量和D-A方程计算的微孔孔容与文献值最接近.     

磁性4A沸石制备及其对水中氯乙酸吸附

以工业级水玻璃、NaAlO2、NaOH和去离子水为原料,采用水热法先合成4A分子筛,然后在二价和三价铁离子混合溶液中用氨水调节负载铁的氧化物及真空干燥等步骤,制得了一系列磁化率不同的磁性分子筛,并对其进行了XRD、SEM、IR及TG等表征分析.结果表明,合成磁性4A沸石晶形完整,表面负载的四氧化三铁分布均匀,磁化率随所负载四氧化三铁量的增加而增大,粒度比纯4A沸石大.磁性4A沸石对钙、镁、铅和氯乙酸的吸附性能与纯4A沸石相当,利用磁性4A沸石可以方便地用磁场分离的特性,其粉末状产品不用成型就可以直接在溶剂或溶液中使用.     

高岭土合成4A沸石晶化历程

4A沸石是广泛用于催化、污水处理、洗涤剂助剂等领域的一种人工合成沸石分子筛[1,2].采用化学合成法,沸石分子筛是在无定形凝胶和水溶液共存的体系中生成[3].以高岭土为原料,在低温水热条件下进行4A沸石的合成时,由于高岭土并不完全溶解于碱性溶液中,因而这一固液两相体系的反应过程,可能是在偏高岭土无定形的表面上完成.本文通过对合成过程液相成分的变化和固相特征分析,探索了该条件下4A沸石晶核生成及其成长历程.81999-04-19收稿,1999-06-25修回内蒙古自然科学基金资助课题（971302-2）合成原料为n（StQ）：n（AI。O。）一2.06：1的…     

微波法煅烧高岭土及合成洗涤助剂4A沸石

本文用微波法煅烧高岭土并合成4A沸石.与传统高温热处理法相比,微波法煅烧的高岭土其活化深度好,增白程度高,粒度细,能耗大为降低,显示了明显的优越性.本文还采用煅烧后的活性高岭土为原料,在微波辐射下进行4A沸石的合成,并用XRD、DTA、SEM、白度计、钙离子交换度等进行表征.与传统水热处理法相比,微波法所得样品在结晶度、白度和钙离子交换能力方面均显优势,且大大地加快了沸石晶化反应速率.经动力学处理,发现微波法合成4A沸石的晶核形成及晶体成长的表观活化能均有所下降,说明微波辐射能促进新相的形成,加快整个晶化反应速率.     

偏高岭土水热合成4A沸石晶化行为的研究

以偏高岭土为原料合成4A沸石,由于其合成过程工艺简单,成本低而一直受到普遍的关注,对于该法晶化过程的行为研究,近年来陆续出现报道,Rocha等^[1]研究认为偏高岭土在碱液中缓慢溶解,形成含SiO3^2-,SiOH基团和Al(OH)4^-的溶液,逐步缩合为硅铝酸钠凝胶,再进一步形成4A沸石晶粒并通过结构重排而转变为4A沸石,王建等^[2]研究提出偏高岭土在NaOH溶液中部分溶解,且迅速转变为偏高岭土,并伴有硅铝酸钠凝胶产生,同时偏高岭土也不断在碱液的作用下凝胶化,生成的凝胶再进一步转变为4A沸石,因而合成的4A沸石产品与化学合成法存在着较大的差异。对偏高岭土合成4A沸石的晶化历程,作者曾进行过研究^[3],发现偏高岭土在碱液中溶解很小,由偏高岭土转为4A沸石晶型,主要是在偏高岭土固相的基础上进行的。本文似从合成过程的机理方面,探讨偏高岭土合成4A沸石的晶化过程行为及其与化学法合成产品差异的关键所在。     

用高效NaY沸石导向剂快速合成A型沸石

提出了应用高效NaY沸石导向剂快速合成A型沸石的新方法. 在合成过程中, NaY沸石导向剂提供了全部硅源(无需另加硅源). 与用水玻璃提供硅源的合成方法相比, 该法晶化速度快, 合成温度低, 并可在低碱度条件下合成超细A型沸石. 29Si NMR表征和UV Raman研究表明, 高效NaY沸石导向剂中含有大量的六元环等低分子量硅铝酸根前驱体, 它们有利于A型沸石成核与晶体生长.     

铝离子在beta沸石晶化过程中对多形体A富集的影响（英文）

以四乙基氢氧化铵为有机结构导向剂,采用超浓水热方法,从氟离子体系合成出手性多形体A(简称A形体)富集的全硅beta沸石.在同样的初始混合物中引入铝源后,所合成的beta沸石中A形体含量明显降低,产物为普通的硅铝beta沸石.用粉末X射线衍射、元素分析、热重-差热分析、氮气吸附、扫描电子显微镜和固体魔角自旋核磁共振等表征手段对全硅beta沸石和硅铝beta沸石进行了详细的表征,并研究了其晶化过程.结果表明,铝源的引入可以加速beta沸石的晶化,得到的硅铝beta沸石晶体粒径明显减小.在硅铝beta沸石的晶化过程中生成了五配位铝物种,五配位铝物种可能是导致产物中A形体含量降低的原因.     

偏高岭土合成4A沸石机理的研究

用XRD、FT IR、ICP、SEM、化学分析等方法研究了偏高岭土合成4A沸石的晶化反应机理。偏高岭土在NaOH溶液中部分溶解 ,且结构迅速转变为偏高岭土 * ,并伴有硅铝酸钠凝胶形成。偏高岭土 *也不断在碱液的作用下凝胶化 ,生成的凝胶进一步再转变为4A沸石 ,这两个过程在大部分反应时间里是同时进行的 ,直到晶化结束。液相参与凝胶、4A沸石前驱及晶核等的形成和4A沸石的成长。偏高岭土 *的凝胶化速度是整个晶化过程的决定步骤 ,该晶化过程极易形成大量聚晶。     

Y沸石的酸性

用^29Si MAS NMR(MAS为Magie Angle Spinning), 统计计算,NH3-TPD 等方法对(NH4)2·SiF6去铝补硅得到的高硅Y型沸石的酸位分布情况进行了研究, 并与典型酸催化反应数据相关联, 证实了Y型沸石的酸位强度取决于A1原子的周围环境, 即与次邻位A1原子数目n-NNN(NNN为Next Nearst Neighbor)有关, 沸石的强酸性来自次邻位无A1原子的AIO^-4四面体。 NH3-TPD法测量的沸石酸量和酸强度数据与^29Si MAS NMR 实验结果和统计计算得到的不同n-NNN A1位的分布是一致的。 随着A1含量减少, Y型沸石表面的总酸量是单调下降的。但强酸量却是先增加后下降, 在A1/(A1+Si)为0.15左右出现极大值。不同硅铝比的Y型沸石对典型的强酸性和弱酸性催化反应的活性变化规律亦与酸性相吻合。     

5A沸石在水溶液中对氯化十四烷基吡啶的吸附

表面活性剂在固液界面上的吸附作用是十分重要的课题,为此我们开展了这方面的研究^[1-3]。沸石结构规则,孔大小均匀,具有特殊的吸附性质。近年来由于作为合成洗涤剂助剂的三聚磷酸钠可使水质富营养化,故国内外都在研究洗涤剂的低磷化措施。     

苯与丙烯在β分子筛上吸附行为的蒙特卡罗研究

采用巨正则统计系综蒙特卡罗模拟方法研究了β分子筛上苯与丙烯分子的吸附行为. 由分子筛内吸附质粒子云分布可知, 在100 kPa时, 丙烯在分子筛上的吸附量要远远大于苯的吸附量. 由吸附相互作用能分布来看, 苯与分子筛之间相互作用能比丙烯与分子筛之间的相互作用能更负, 这就使苯分子的吸附相对于丙烯分子稳定. 相对而言, 温度变化对丙烯吸附影响远大于对苯吸附的影响, 如100 kPa时, 温度由298 K升高至443 K导致丙烯分子吸附量明显减少, 由每8个晶胞吸附98个丙烯分子减少到80个; 而对苯分子吸附却没有显著的影响. β分子筛上存在着苯和丙烯的竞争吸附, 并且吸附分子之间存在相互作用使两者与分子筛之间的相互作用能分布改变. 在压力范围1×10－3～5.0 kPa, 不同温度下苯与丙烯在分子筛内吸附等温线的模拟结果表明, 在较高温度、较低压力下丙烯的吸附量要小于苯的吸附量.     

载镧偕胺肟基纤维除氟性能研究

本文将稀土元素镧(Ⅲ)负载于偕胺肟基纤维上制备成载镧偕胺肟基纤维吸附剂,探讨该纤维吸附剂对水溶液中氟离子的吸附性能。研究结果表明,吸附最佳pH范围为5～7,在较宽的范围4～10之间也能显示出较高的除氟率;其吸附等温线符合Langmuir方程,最大吸附容量为40.1mg/g;吸附动力学可用准二级速率方程描述。     

On the applicability of the theory of ideal adsorption solutions to equilibria in the N2-O2-zeolite NaX system

Experimental data on the joint adsorption of a nitrogen-oxygen gas mixture on zeolite NaX were analyzed using the theory of ideal adsorption solutions. Acceptable accuracy was obtained in calculations of binary isotherms from the adsorption isotherms of the pure gas mixture components. The calculated binary isotherms can be used to determine the parameters of the mathematical models of binary adsorption, for instance, competitive adsorption models.     

Preparation of Tetraethylenepentamine-Functionalized 4A Zeolite for effective removal of phosphate in water

Recently, the high-concentration phosphorus-containing wastewater has been caused lots of negative influences on aquatic environment and thus driven people to develop some effective methods to remove excess of phosphate in water. In order to solve these environmental problem, in this work, a tetraethylenepentamine (TEPA) modified 4A zeolite has been prepared and used for removing phosphate. Removal of phosphate by precipitation of 4A zeolite and electrostatic action of TEPA with phosphate were determined by scanning electron microscopy, X-ray powder diffraction and Fourier infrared spectrum, and morphology and characteristic peak of TEPA-4A zeolite before and after adsorption changed significantly. In addition, the results of batch adsorption studies showed that the pH of the solution have a significant influence on the adsorption of TEPA-4A and the biggest adsorption capacity was 23 mg/g at pH = 2.3 ± 0.2. Adsorption isotherms results showed that the process was consistent with Langmuir model and the maximum adsorption capacity could reach to 28 mg/g at 25 °C. TEPA-4A adsorption processes were spontaneous endothermic reaction, and elevated temperatures were conducive to the adsorption process through kinetics and thermodynamics results. The research of TEPA modified 4A zeolite and raw 4A zeolite provides technical support for the development of 4A zeolite instead of sodium tripolyphosphate as a new type of detergent ingredient.     

High-resolution physical adsorption on supported borosilicate MFI zeolite membranes: comparison with powdered samples

We have performed physical adsorption measurements to analyze the structure of intact MFI membranes with a nominal Si:B ratio of 12.5:1. Argon adsorption isotherms of membranes at 77 K are nearly identical to isotherms of corresponding zeolite powders throughout most of the domain of relative pressures, the exception being the micropore-filling region (between 10⁻⁵ and 10⁻⁴ relative pressure). The isotherm in the micropore-filling region is steeper by a factor of 4–5 for the borosilicate membranes than it is for a powder made under the same conditions, while the saturation loadings are found to be similar. This implies a difference in how the zeolite pores fill with argon – either thermodynamic or kinetic in origin – and that fluxes for argon permeation through such powder and membrane samples may differ. Our membrane adsorption measurements reveal no hysteresis and hence no mesoporsity in the zeolite membranes. This finding, from adsorption measurements, stands in contrast to recent alkane permeation measurements on these membranes, which suggest the presence of mesopores. We reaffirm the conclusion, found in previous work, that zeolite membranes can be approximated as a zeolite powder plus a support for the purposes of adsorption characterization.     

Adsorption isotherms and ideal selectivities of hydrogen sulfide and carbon dioxide over methane for the Si-CHA zeolite: comparison of carbon dioxide and methane adsorption with the all-silica DD3R zeolite

Adsorption isotherms of H₂S, CO₂, and CH₄ on the Si-CHA zeolite were measured over pressure range of 0–190 kPa and temperatures of 298, 323, and 348 K. Acid gases adsorption isotherms on this type of zeolite are reported for the first time. The isotherms follow a typical Type-I shape according to the Brunauer classification. Both Langmuir and Toth isotherms describe well the adsorption isotherms of methane and acid gases over the experimental conditions tested. At room temperature and pressure of 100 kPa, the amount of CO₂ adsorption for Si-CHA zeolite is 29 % greater than that reported elsewhere (van den Bergh et al. J Mem Sci 316:35–45 (2008); Surf Sci Catal 170:1021–1027 (2007)) for the pure silica DD3R zeolite while the amounts of CH₄ adsorption are reasonably the same. Si-CHA zeolite showed high ideal selectivities for acid gases over methane at 100 kPa (6.15 for H₂S and 4.06 for CO₂ at 298 K). Furthermore, H₂S adsorption mechanism was found to be physical, and hence, Si-CHA can be utilized in pressure swing adsorption processes. Due to higher amount of carbon dioxide adsorbed and lower heats of adsorption as well as three dimensional channels of Si-CHA pore structure, this zeolite can remove acid gases from methane in a kinetic based process such as zeolite membrane.     

A single-site model for divalent transition and heavy metal adsorption over a range of metal concentrations

Metal adsorption data over a range of surface coverages typically are characterized by curvilinear metal adsorption isotherms. These isotherms generally have a slope of 1 at low surface coverage and a shallower slope at higher surface coverages. The curvature of metal adsorption isotherms with increasing surface coverage is frequently interpreted in terms of sequential adsorption onto different types of surface sites, multinuclear surface complexation, or nonideality of metal adsorption. We demonstrate that the curvature of metal adsorption isotherms can also be attributed to changes in surface charge and potential that depend on the predominant type of metal surface complex. A single-site extended triple-layer model is used to reinterpret previously studied metal adsorption isotherms and pH edges for a wide variety of metals (Cd2+, Co2+, Cu2+, Pb2+, and Zn2+) and solids (goethite, hydrous ferric oxide, corundum, and magnetite) in different electrolyte solutions (NaNO3 and NaClO4). Only metal adsorption on ferrihydrite at very low surface coverages is not consistent with the single-site triple-layer model. This discrepancy might be explained if ferrihydrite is in fact not a single phase but a mixture of two or more phases. Metal surface coverages ranging from 10(-4) to 10.2 mmol/m2 on the other minerals can be accounted for with a single-site extended triple-layer model if appropriate metal adsorption reactions are chosen. In addition, several examples suggest that, within the context of the model, surface complexation schemes can be established that describe metal adsorption over both a wide range of surface coverage and a wide range of ionic strength.     

Chromium (VI) ion adsorption features of chitosan film and its chitosan/zeolite conjugate 13X film

This research evaluated the importance of the adsorption properties of chitosan a chitosan/zeolite conjugate film for the removal of Cr(VI) ions from solutions in the 5-260 mg/L concentration range, when the pH was adjusted to 4.0 and 6.0. The uptake capacities of the films formed by chitosan and by the chitosan/zeolite conjugate were calculated by mass balance. The equilibrium isotherms were fitted to the Langmuir, Freundlich and Redlich-Peterson models. The chitosan film seems to be a good sorbent for Cr(VI) at pH 4, but its physical instability suggests the need for a more resilient support. Due to this fact zeolite was added to the chitosan matrix in solution and a chitosan/zeolite (CS/Zeo) film was thus formed. The solubility of the film and the characterization of the different matrices by FTIR, TGA and X-Ray showed that a cross-linked structure was formed between the chitosan and zeolite and the solubility of the film increased. In this study, the low manufacturing cost of the CS/Zeo matrix, the good uptake of Cr(VI) at acidic pH (17.28 mg/g) and the non desorption of Cr(VI) from the film in water suggests this combination should be tested in industrial environment.     

Th(IV) adsorption on alumina: effects of contact time, pH, ionic strength and phosphate

Adsorption of Th(IV) (total concentration, 10(-5)-10(-4) mol/L) was studied by a batch technique. The effects of pH, ionic strength, contact time, and phosphate on the adsorption of Th(IV) onto alumina were investigated. Adsorption isotherms of Th(IV) on alumina at approximately constant pH and three ionic strengths (0.05, 0.1, 0.5 mol/L KNO3) were determined. It was found that the pH values of aqueous solutions of both the Th(IV)-alumina and phosphate-alumina adsorption systems increase with increasing contact time, respectively. Adsorption of Th(IV) on alumina steeply increases with increasing pH from 1 to 4.5 and the adsorption edge consists of three regions. The phosphate added clearly enhances Th(IV) adsorption in the pH range 1-4. From the adsorption isotherms at approximately constant pH and three different ionic strengths, a reduced ionic strength effect was observed and is contradictory to the insensitive effect obtained from the adsorption edges on three oxides of Fe, Al, and Si at different ionic strengths. Compared with the adsorption edges at different ionic strengths, the adsorption isotherms at approximately constant pH and different ionic strengths are more advantageous in the investigation of ionic strength effect. The significantly positive effect of phosphate on Th(IV) adsorption onto alumina was attributed to strong surface binding of phosphate on alumina and the subsequent formation of ternary surface complexes involving Th(IV) and phosphate.