碱处理对X沸石孔结构影响的研究

研究了X型沸石经碱溶液处理后介孔的形成,考察了碱溶液浓度、碱处理温度和时间对形成介孔的影响.并采用ICP、N2吸附-脱附、SEM、XRD等进行表征.结果表明:碱处理抽提沸石骨架上的硅使处理后样品硅铝比发生变化,从而改变了X型沸石的性能;浓度为0.05 mol·L-1的NaOH溶液70℃下处理30 min是形成介孔的最佳条件,在此条件下形成介孔孔容为0.24 cm3·g-1,孔径分布为2.3～8 nm的介孔,比表面积从处理前的352.69 m2·g-1升高到443.11 m2·g-1.而碱处理温度低于70 ℃,沸石骨架上硅不易抽提;碱溶液浓度高于0.05 mol·L-1或碱处理时间长于30 min,X型沸石则易形成大孔.样品经亚甲基蓝吸附测试,证实X型沸石碱处理后确实形成了一定量的介孔.     

碱改性介-微孔HZSM-5分子筛催化乙醇脱水制乙烯性能

对两种不同硅铝比的HZSM-5分子筛进行碱处理,制备介-微孔复合HZSM-5分子筛,研究乙醇脱水制乙烯的催化性能,并考察碱溶液浓度和处理温度对HZSM-5分子筛孔结构和表面酸性的影响。结果表明,适宜的碱处理条件有利于分子筛发生骨架脱硅和脱铝,从而形成介孔。碱处理对硅铝比低的HZSM-5分子筛酸性质影响明显,而硅铝比高的HZSM-5分子筛在碱处理过程中酸性质变化不明显,更易发生脱硅和脱铝而形成更多介孔。碱改性介-微孔HZSM-5分子筛催化剂使乙醇脱水制乙烯催化性能得到改善,尤其低温催化活性提高,这主要归功于碱处理中介孔的形成和表面酸性的调变。     

丝光沸石骨架脱硅与介孔改性研究

采用碱溶和酸洗过程对合成的MOR沸石进行骨架脱硅与介孔改性。结果表明,碱溶-酸洗联合处理促进 MOR 骨架选择性脱硅和晶内介孔的形成;脱硅沸石的相对结晶度和产率随介孔率的增加呈下降趋势。辅以酸洗可调整碱处理沸石的硅铝比,改进其酸强度分布和介孔率。     

丝光沸石硅铝比对骨架脱硅衍生介孔结构的影响

用水热合成和铵交换法制备系列氢型丝光沸石(H-MOR),通过水热碱蚀与碱溶滤联合处理对H-MOR样品进行选择性脱硅和介孔改性.研究H-MOR骨架Si/Al比对改性沸石的介孔结构、酸性和水热稳定性的影响.N2吸附结果表明,碱处理沸石的介孔率随H-MOR硅铝比减少而增加;典型样品(n(Si) /n(Al) 9.43)具有附加介孔结构,介孔体积可达0.082 cm3/g,最可几孔径为4.6 nm;SEM观察显示,改性沸石的介孔结构源于脱硅产生的结构缺陷,晶内介孔呈无序分布;ICP和EDX分析证实,联合碱处理促进H-MOR晶体选择性脱硅(脱硅率均大于93.1％);水热稳定性和NH3-TPD数据表明,介孔改性丝光沸石较好地保持了前体的结晶性和水热稳定性,其酸性与对应H-MOR沸石相匹配.骨架硅铝比影响改性MOR沸石的介孔率,但与沸石脱硅率无相关性.     

镁碱沸石分子筛改性研究进展

镁碱沸石分子筛独特的孔道结构使其在催化领域得到广泛应用,如作为吸附剂或用于合成气制二甲醚、正丁烯骨架异构、己烯骨架异构和丁烯聚合等反应。近年来,由于异丁烯供不应求,用于正丁烯骨架异构制异丁烯的镁碱沸石分子筛的研究受到关注。分子筛的孔道结构、酸性以及比表面积等物化性能是决定催化性能的重要因素,这些物化性质可通过改性方法调控,从而达到优化催化性能的目的。从离子交换改性、脱铝改性、碱处理改性以及表面修饰改性综述国内外镁碱沸石分子筛改性的研究进展,分别论述各种改性方法,总结改性后镁碱沸石分子筛在正丁烯骨架异构、N₂O分解、二甲苯异构及二丁醇脱水等反应中的催化性能,并对改性机理进行综述,对镁碱沸石分子筛未来发展方向进行展望。     

L型沸石的离子交换与脱铝改性研究

为了改善L型沸石的催化性能,优化其在FCC中的应用,对L沸石进行离子交换和脱铝的改性研究。考察离子交换时间和离子交换方式对降低L沸石中氧化钾含量的影响及水热焙烧和化学脱铝对提高L沸石硅铝物质的量比的影响。结果表明,L型沸石离子交换时间不易过长,较适宜的时间为3 h。离子交换和水蒸汽处理相结合对降低L型沸石的钾含量更有效,离子交换和水蒸汽处理交替进行3次的样品氧化钾质量分数可降至0.82%。水热焙烧和化学脱铝能使L型沸石显著脱铝,其中,经过700 ℃水蒸汽处理1 h,再进行盐酸处理而制得改性L型沸石样品的硅铝物质的量比可达21.91,相对结晶度高于80％。     

水热碱蚀与碱溶滤联合处理制备介孔丝光沸石

以硅酸钠溶胶和铝酸钠为硅、铝源,采用水热合成和离子交换法制备了质子型丝光沸石(H-MOR)。研究水热碱蚀与碱溶滤联合处理对H-MOR改性样品的介孔结构、晶体形貌、组成及酸性质的影响。结果表明:用初始浸渍液对H-MOR进行水热碱蚀,H-MOR骨架脱硅选择性高,晶体含有均一的筛状介孔;水热碱蚀与一次碱溶滤处理的样品具有尺度分布较窄的槽形介孔,沸石骨架硅铝比降低而介孔率增加;再度进行碱溶滤处理,沸石的最可几介孔尺寸和累计介孔体积进一步增大,而残留抽出物(无定形SiO2–Al2O3)的硅铝比为生成介孔丝光沸石晶相的5倍以上。联合碱处理的丝光沸石样品具有骨架脱硅选择性和介孔率高、介孔分布(4.4~5.7nm)可控的特性,其结晶度、固有微孔结构和酸性质退化程度较低。     

纳米β沸石的改性

采用水热处理和酸处理等方法对纳米β沸石进行改性,考察纳米β沸石的性质变化。结果表明,Na2O含量越低,水热处理后结晶度越高,热稳定性就越好;酸处理在低浓度时以酸洗掉非骨架铝为主,而高浓度酸时不仅脱除非骨架铝,而且还脱除骨架铝;纳米β沸石较难提高硅铝比,达到相同硅铝比时比小晶粒β沸石所需条件要苛刻,其耐酸性能好于小晶粒β沸石。     

丙酸异戊酯合成用催化剂

介绍了各种无机盐、离子交换树脂、杂多酸及沸石分子筛等不同催化剂催化合成丙酸异戊酯的研究结果。催化活性较高的为离子交换树脂、杂多酸及沸石分子筛,有一定的应用前景。同时作者以改性β沸石为催化剂合成丙酸异戊酯。将β沸石经水蒸气处理、酸处理,及负载金属Fe改性,将不同处理条件及不同硅铝比的沸石进行酯化比较,结果表明,β沸石的硅铝比越高,酯化率越高;酸量越高,酯化率越高。β沸石作为催化剂,产品质量好、选择性好,对设备无腐蚀,可重复使用。     

粉煤灰分步溶出硅铝制备纯沸石分子筛的研究

研究了一种由粉煤灰合成纯沸石分子筛的新工艺,粉煤灰与碳酸钠混合焙烧生成硅酸钠和硅铝酸钠,用少量水浸取其中的硅酸钠,含硅铝酸钠的残余物用碱液浸取.实验发现,在碱溶过程中溶液中的硅铝存在过饱和现象,在过饱和期内实现固液分离,可提取粉煤灰中的硅铝用于合成X型、A型、P型纯沸石产品.1 kg粉煤灰合成310～560 g纯沸石.晶化导向剂和晶种对沸石晶型和晶化时间有很大影响.经仪器和化学分析方法对沸石产品从矿物组成和阳离子交换容量进行表征,制得产品的阳离子交换容量可达3.2～ 4.7meq/g,纯度较高.     

MAS NMR studies of ZSM-5 zeolites: Correlation to para selectivity and SEM observations

²⁷Al and²⁹Si MAS NMR studies of various ZSM-5 zeolites of different Si/Al ratio, crystal size synthesized with and without alkali metal salt addition by the hydrothermal technique were carried out. The NMR observations clearly showed that the technique can be employed to differentiate Si/Al ratio, framework tetrahedral content and the crystal size. The last observation has been confirmed by SEM and catalytic activity test for para ethylation of ethylbenzene. A good correlation was found between the catalytic activity and the data from NMR and SEM.     

Composition and microstructure of alkali activated fly ash binder: Effect of the activator

The alkali activation of fly ashes is a chemical process by which the glassy component of these powdered materials is transformed into very well-compacted cement. In the present work the relationship between the mineralogical and microstructural characteristics of alkaline activated fly ash mortars (activated with NaOH, Na₂CO₃ and waterglass solutions) and its mechanical properties has been established. The results of the investigation show that in all cases (whatever the activator used) the main reaction product formed is an alkaline aluminosilicate gel, with low-ordered crystalline structure. This product is responsible for the excellent mechanical-cementitious properties of the activated fly ash. However the microstructure as well as the Si/Al and Na/Al ratios of the aluminosilicate gel change as a function of the activator type used in the system. As a secondary reaction product some zeolites are formed. The nature and composition of these zeolites also depend on the type of activator used.     

Creating Mesopores in ZSM-5 Zeolite by Alkali Treatment: A New Way to Enhance the Catalytic Performance of Methane Dehydroaromatization on Mo/HZSM-5 Catalysts

Well-controlled treatment with alkali solution causes the etching of HZSM-5 framework, which results in the formation of the new porosity and channel structure with the coexistence of micropores and mesopores, as evidenced by nitrogen adsorption experiments. The dissolution of the zeolite framework, as revealed by the investigation of solid-state NMR, begins from the crystalline site with Si–O–Si linkages. The inertness of the alkali treatment toward Si–O–Al bond in the framework preserves the specific Brønsted acid site that is defined to be the bridging OH species over Si–O–Al units in zeolite. The Mo-modified catalysts derived from the alkali treatments showed a very high catalytic performance in the conversion of methane to aromatics (MDA) when compared with the conventional Mo/HZSM-5 catalyst. The unique selectivity to aromatics and stability of the catalysts derived from the alkali-treated ZSM-5 are attributed to the coexistence of mesopores and inherent micropores in the zeolites, which optimizes an environment for catalytic reaction and mass transfers. The channel with mainly 3–5?nm in diameters in the zeolites serves as the “aisle” to enhance the diffusion of molecules, especially the aromatics molecules, while the micropores have been identified to be the active cavities for the aromatics formation.     

Fractal Extra-Framework Species in De-aluminated LaY Zeolites and Their Catalytic Activity

Lanthanum-containing Y (LaY) zeolites were prepared by ionic exchange from NaY parent zeolite. The LaY zeolites were de-aluminated by steaming. De-aluminated zeolites presented different Si/Al ratio. The physicochemical properties of these catalysts were characterized by X-ray diffraction, pyridine and xenon adsorption, infrared spectroscopy and ²⁹Si, ²⁷Al, ¹²⁹Xe, ¹³⁹La solid-state nuclear magnetic resonance spectroscopy. Furthermore, a fractal geometry approach was adopted to describe the evolution in the texture as a consequence of de-alumination. The catalytic properties of materials were evaluated in the n-hexane cracking reaction. The catalyst with the highest catalytic activity was the zeolite highest de-aluminated (Si/Al ratio of 3.7). Such performance was attributed on the one hand, to active extra-framework aluminum species hosted in the large cavities of zeolites and, on the other hand to redistribution of lanthanum species into the zeolite as a consequence of de-alumination.     

FT-IR spectroscopic and catalytic study of de-aluminated H-mordenites as environmental friendly catalysts in the hydroxymethylation of 2-methoxyphenol with formaldehyde in aqueous medium

Several de-aluminated H-mordenites, prepared by treating a commercial H-mordenite (HM-16, Engelhard) with aqueous HCl solutions, were characterized and tested as catalysts in the liquid-phase hydroxymethylation of guaiacol with aqueous solutions of formalin, for the production of p-vanillic alcohol (3-methoxy-4-hydroxybenzyl alcohol), the intermediate in vanillin synthesis.

Samples were obtained with Si/Al atomic ratios from 10 to 36; their acidic and hydrophilic properties have been characterized by means of FT-IR spectroscopy of adsorbed probe molecules, namely CO at nominal 77 K, NH₃ and H₂O at room temperature, and ammonia TPD.

De-alumination led to the development of a mesoporous structure, and to a partial structure degradation with the most de-aluminated sample (Si/Al = 36).

As to the acidic properties, both Brønsted species in the main channels and in side-pockets were removed, and less acidic hydroxyls formed.

The catalytic performance was affected mainly by samples hydrophilicity that considerably decreased upon de-alumination. In the Si/Al ratio range investigated, a decrease in the number of acidic sites led to a complex catalytic behaviour, with a maximum activity for intermediate Si/Al ratio (=25). A higher concentration of aromatic compounds in the pores of more hydrophobic zeolites (higher Si/Al ratios) also led to a higher selectivity towards heavy, di-arylic by-products. A comparison with commercial H-mordenites having similar Si/Al ratio evidenced that the occurrence of mesoporosity, in strongly de-aluminated samples, also affected the catalytic performance, favouring the formation of bulky di-aryl compounds and leading to lower guaiacol conversion.     

碱处理制备介孔-微孔沸石分子筛的影响因素及其应用研究进展

综述了碱处理制备介孔-微孔沸石分子筛的影响因素,包括碱处理条件、沸石分子筛硅铝比和模板剂对碱处理脱硅形成介孔的影响。评述了碱处理所制备介孔-微孔沸石分子筛在应用方面所取得的进展,重点介绍了它们在烷基化、异构化、裂化和醇烃化等催化反应中的应用。通过碱处理引入介孔可极大地缩短分子在沸石微孔道中的扩散距离,从而增强表观催化反应活性及提高催化剂的稳定性。提出了今后研究的重点为：阐明碱处理引入介孔的形成机理和碱处理对分子筛骨架结构、酸性的影响,拓展碱处理制备介孔-微孔沸石分子筛的应用 范围。     

气相低浓度甲苯在超稳Y分子筛的吸附-脱附性能

为提高Y分子筛对可挥发性有机废气的选择性吸附能力,采用高温水热处理技术对NaY分子筛进行骨架脱铝制备超稳Y分子筛(USY),并在固定床反应器中考察了USY在水汽存在下动态吸附低浓度甲苯的性能。结果表明,随着USY分子筛骨架Si/Al比的增加,虽然其微孔孔体积和比表面积发生了下降,但形成了较多的中孔结构。并且骨架硅含量增加后,USY对非极性的甲苯分子选择性吸附能力明显增加,当Si/Al为22左右,在相对湿度50%下,单位面积甲苯吸附量要比水吸附量大5.6倍。热重脱附研究表明,经过改性后,甲苯脱附温度可从NaY的300℃下降到超稳Y分子筛的160℃,具有优良的热再生性能。     

TUN, IMF and -SVR Zeolites; Synthesis, Properties and Acidity

The effect of synthesis conditions on the preparation and properties of three novel zeolites TUN, IMF, and -SVR was investigated and compared with MFI. X-ray powder diffraction, infrared spectroscopy, chemical analysis, sorption measurements, and scanning electron microscopy were employed to characterize the textural and chemical properties of these zeolites. FTIR spectroscopy in combination with pyridine as probe molecule was used to describe the type, concentration and acid strength of these zeolites. Zeolite -SVR was synthesized with Si/Al ratios higher than 100 in contrast with TUN and IMF having Si/Al ratios about 20–30, respectively. TUN, MFI and IMF zeolites exhibit similar concentrations of Brønsted and Lewis acid sites and also similar acid strength of Brønsted sites. In contrast, the presence of one vacancy/unit cell in the case of -SVR zeolite substantially changes its acidic properties. Generally, zeolites TUN and IMF exhibit similar acidic properties in terms of acid strength and Brønsted to Lewis acid site ratio like MFI and due to their slightly larger pores higher activities in catalytic reactions are expected.     

沸石的碱处理溶解

晶体的溶解与晶体的生长存在着密切的联系，详细研究沸石晶体的溶解行为将有助于更好的理解沸石晶体的生长机理。鉴于目前对沸石晶体的碱处理溶解行为的研究尚处于初始阶段，所以从沸石碱溶解的几点关键内容出发，如沸石的硅铝比对沸石碱处理的影响，焙烧“活化”后沸石的碱处理溶解行为的变化，沸石与其无定形前驱物的溶解性差异以及沸石的溶解机理和溶解动力学方程方面，综述了有关沸石碱处理溶解研究方面的最新动态。