超微NaY分子筛的合成(Ⅰ)──添加轻稀土离子的影响

导向剂的陈化时间和反应胶的晶化温度可以影响NaY分子筛的晶化行为.随导向剂陈化时间的增加,NaY分子筛的晶化速度加快,晶粒尺寸减小;随晶化温度的升高,NaY分子筛的晶化速度加快,但晶粒尺寸增加.而向合成体系中添加轻稀土离子(Ln³⁺)对NaY分子筛的晶化行为影响更为明显.与未添加稀土离子时相比较,在一定的稀土离子添加量范围内[n(Ln³⁺)/n(Al³⁺)<0.2],NaY分子筛的晶化速度明显加快而晶粒尺寸显著减小,同时所合成出的NaY分子筛的n(SiO₂)/n(Al₂O₃)比也有较大的提高.添加稀土离子使合成体系中形成异晶晶种的Ln(OH)₃微晶,从而进一步引发NaY分子筛的成核.     

高温合成NaY沸石

提出了应用NaY沸石导向剂提供全部硅源合成NaY沸石的新方法, 研究了高温条件下合成NaY沸石的规律和特点, 发现在高温条件下合成NaY沸石不仅晶化速度快, 而且可以在不加有机物的条件下合成较高硅铝比[n(SiO2)/n(Al2O3)=6]的NaY沸石.     

SAPO-11分子筛合成条件对其结晶度与催化性能的影响

在水热条件下改变合成条件合成一系列SAPO-11分子筛,采用XRD对样品进行结晶度表征,并考察了合成条件对SAPO-11分子筛催化性能的影响.结果表明,合成条件对SAPO-11分子筛的结晶度和催化性能有很大影响.以二正丙胺(DPA)为模板剂,n(DPA)/n(Al2O3)=1.5,n(SiO2)/n(Al2O3)=0.2,晶化时间为24 h和晶化温度为170℃时,合成出的SAPO-11分子筛催化剂最有利于萘和甲醇的甲基化反应.初步探究其在萘和甲醇的甲基化反应中的失活原因.结果表明,催化剂失活的主要原因是在萘和甲醇的甲基化反应过程中生成大量的水,经高温水脱铝导致分子筛结构坍塌,从而导致分子筛失活.     

超微NaY分子筛的合成(Ⅱ)——添加铝络合剂的影响

NaY分子筛合成体系中添加铝的络合剂(乙二胺四乙酸、柠檬酸和醋酸),可有效地减小分子筛的晶粒尺寸及增加分子筛的晶化速度和SiO2/Al2Oa物质的量比.在添加柠檬酸的合成体系中,考察了柠檬酸的添加量对NaY分子筛晶化行为的影响.发现存在着一个最佳的柠檬酸的添加量范围,即n(柠檬酸)：n(氧化铝)≤2：1,在此范围内,NaY的晶化速率和硅铝比较高,而晶粒尺寸较小.     

纳米NaY分子筛的合成及其催化柴油加氢改质性能

在系统考察添加阳离子表面活性剂、凝胶陈化以及晶化温度和晶化时间等因素对NaY分子筛细化影响的基础上,对纳米NaY分子筛的合成规律进行了研究;合成出了n(SiO2)/n(Al2O3)=4.5,BET比表面积为620m2/g,孔容为0.34 cm3/g,微孔集中分布在0.55 nm附近,粒度分布范围在100 nm以内的纳米NaY分子筛.并采用XRD、BET、IR、TTEM和NH3-TPD等手段系统表征了纳米NaY分子筛的微观结构.分别采用合成的纳米NaY分子筛和微米NaY分子筛为原料制备负载型Ni-Mo-P催化剂,并以FCC柴油为原料,考察了催化剂的加氢改质性能,结果表明,与微米NaY分子筛基负载型Ni-Mo-P催化剂相比,纳米NaY分子筛基负载型Ni-Mo-P催化剂,在加氢脱氮率、密度和十六烷值相当的情况下,其加氢脱硫率较高,柴油收率较高.     

超微NaY分子筛的合成（II）—添加铝络合剂的影响

NaY分子筛合成体系中添加铝的络合剂（乙二胺四乙酸、柠檬本矣醋酸）,可有效地减小分子筛的晶粒尺寸及增加分子筛的晶化速度和SiO2/Al2O3物质的量比,在添加柠檬酸的合成体系中,考察了柠檬酸的添加量对NaY分子的筛晶化的影响,发现存在着一个最佳的柠檬酸的添加量范围,即n（柠檬酸）：n（氧化铝）≤2：1,在此范围内,NaY的晶化速率和硅铝比较高,而晶粒尺寸较小。     

含硼杂原子Na-B-ZSM-5分子筛对甲醇脱氢制甲醛反应的催化性能

以白炭黑为硅源、硼酸为硼源、NaOH为碱源、四丙基溴化铵(TPABr)和1,6-己二胺(HMDA)混合模板剂,采用水热合成法制备含硼杂原子Na-B-ZSM-5分子筛,用XRD、SEM、FT-IR、UV-vis、11B MAS NMR、NH3-TPD等方法对其进行表征。在连续流动常压固定床反应器上评价Na-B-ZSM-5分子筛对甲醇脱氢制甲醛反应的催化性能,考察n(Si)/n(B)、n(Na2O)/n(SiO2)、晶化温度和晶化时间等制备参数以及反应温度和质量空速等工艺参数对催化性能的影响。结果表明,硼进入了分子筛的骨架结构中,存在与B酸中心有关的骨架四配位硼和与L酸中心有关的骨架三配位硼,Na-B-ZSM-5分子筛含有较多的弱酸位和少量的中强酸位。催化剂的最佳制备参数为n(Si)/n(B)比值为7.5、n(Na2O)/n(SiO2)比值为0.14、晶化温度170℃、晶化时间48 h。Na-B-ZSM-5(7.5)分子筛在反应温度550℃、质量空速1.85 h-1的反应条件下对甲醇的转化率为62.97%,甲醛的选择性为68.86%。     

高硅分子筛ZSM-23的合成及表征

采用静态水热晶化法以吡咯烷为模板剂,合成出结晶度良好的ZSM-23分子筛晶体.对合成条件的研究结果表明,合成的关键是避免ZSM-35分子筛的生成.当n(Si)/n(Al)=25～110,n(H20)/n(SiO2)=1.3～4.8,n(pyr.)/n(SiO2)=0.12～0.5时,均能稳定生成ZSM-23分子筛晶体.当n(Si)/n(Al)>110时,不能得到分子筛晶体;当n(Si)/n(Al)<25时,生成的是ZSM-35分子筛晶体.采用XRD,SEM,TG-DTA,FTIR等技术,对合成的ZSM-23分子筛晶体的形貌,以及影响分子筛合成的因素进行了详细的研究.     

利用粉煤灰合成低硅铝比NaP分子筛

以粉煤灰分级处理获得的硅铝组分Na2SiO3和NaAlO2为原料,通过水热反应制备了NaP型分子筛.考察了钠盐不同阴离子和有机空间位阻剂对NaP分子筛制备的影响,优化了水热合成NaP分子筛的工艺参数,采用X射线衍射(XRD)、扫描电子显微镜(SEM)和BET方程对NaP分子筛产品的晶型、形貌和孔容进行分析表征,对NaP分子筛吸附水溶液中Ni2+的性能进行了评价.结果表明,合成NaP分子筛的最佳原料摩尔比为n(Na2O)∶n(SiO2)∶n(Al2O3)∶n(H2O)=3.23∶1.95∶1∶226,反应温度为120℃,晶化时间为8h.当钠盐中阴离子为Br-时,可增大P型分子筛产率并提高其纯度.添加有机空间位阻剂三乙醇胺(TEA)[n(TEA)∶n(Al2O3)=1∶1]时,合成的P型分子筛粒径较小且具有较大的孔容,此时对应的Ni2+去除率较高,可达96.2%.     

凝胶硅铝比对合成MCM-22,UTM-1和Kenyaite的影响

 以白碳黑为硅源,偏铝酸钠为铝源,六亚甲基亚胺(HMI)为结构导向剂,采用动态水热法合成了MCM-22,UTM-1和kenyaite,并考察了硅铝比对产物晶相的影响. 结果表明, 配料硅铝比是影响产物晶相的重要因素. n(SiO2)/n(Al2O3)=30～50时,晶化产物为MCM-22; n(SiO2)/n(Al2O3)=71～190时,晶化产物为MCM-22与kenyaite的混合物,且随着硅铝比的增大,MCM-22的含量逐渐减少而kenyaite的含量逐渐增加; n(SiO2)/n(Al2O3)=228～609时,晶化产物为八元环结构的UTM-1; 不含铝源时,晶化产物为kenyaite. 就合成MCM-22和UTM-1而言,凝胶中的铝是必不可少的. 上述几种晶化产物均呈片状,可以通过扫描电镜加以区分.     

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.     

Synthesis of NaX and NaY Zeolites from Tunisian Kaolinite as Base Catalysts: An Investigation of Knoevenagel Condensation

The synthesis of Faujasite‐type zeolites with high purity has been successfully performed from Tunisian kaolinite and the effects of different crystallization parameters on the final products were widely investigated. The alkaline fusion of kaolinite followed by hydrothermal treatment lead to zeolite NaX synthesis whereas the classic hydrothermal transformation of metakaolinite produces NaY zeolite. The results show that an increase in the synthesis temperature and time has improved the crystallization process of the zeolite NaX whereas the SiO₂/Al₂O₃ and the Na₂O/SiO₂ molar ratios were the key parameters to obtain a pure zeolite NaY. The highest specific surface areas obtained with the optimal crystallization conditions were 554 m2 g^?1 and 592 m2 g^?1 for respectively NaX and NaY zeolites. The basic properties of NaX and NaY zeolites were explored in the Knoevenagel condensation of benzaldehyde with ethyl cyanoacetate at 140 °C as a test reaction in the absence of solvent. The influence of ion exchange with cesium cation on the catalytic activity of prepared catalysts was also investigated. It was found that the NaX provided higher activity than that of NaY catalyst due to its lower Si/Al ratio whereas a cesium exchange conferred higher basicity to the prepared Na‐faujasite.     

利用Taguchi法以高岭土为原料制备高硅NaY分子筛

采用Taguchi试验方法优化出了以高岭土为原料制备高硅NaY分子筛的最佳合成参数,考察了硅溶胶的加入量、反应体系的碱度、加水量以及晶化时间对NaY分子筛硅铝比和结晶度的影响。结果表明,高硅NaY分子筛的最佳合成条件是：反应体系各组分的物质的量比为7.5SiO₂∶1.0Al₂O₃∶2.2Na₂O∶120H₂O,晶化时间为16 h。同时发现,对合成样品性能的影响最为显著的因素是硅溶胶的加入量和碱度。采用X射线衍射、N₂静态容量吸附法和扫描电镜对利用最佳条件所合成样品的硅铝比、比表面积、孔分布以及表观形貌进行了表征。结果显示,以高岭土原料制备的NaY分子筛比参考样品拥有更高的硅铝比和更大的比表面积。     

Microwave synthesis of zeolites. 2. Effect of vessel size, precursor volume, and irradiation method

The enhancement of synthesis reactions under microwave heating is dependent on many complex factors. We investigated the importance of several reaction engineering parameters relevant to microwave synthesis. Of interest to this investigation were the reaction vessel size, volume of precursor reacted, microwave power delivery, and microwave cavity design. The syntheses of NaY zeolite and beta-zeolite were carried out under a number of varying conditions to determine the influence of these parameters on the nucleation rate, the crystallization rate, and the particle size and morphology. The rates of NaY and beta-zeolite nucleation and crystallization were more rapid in the multimode CEM MARS-5 oven compared to the more uniform field CEM Discover. The faster synthesis rate in the MARS-5 may be the result of the multimode microwave electric field distribution. Slower rates of NaY and beta-zeolite formation observed in the Discover and a circular waveguide may be the result of a more uniform microwave electric field distribution. Changes in reaction vessel size and precursor volume during the microwave synthesis of beta- and NaY zeolite were found to influence the rate of zeolite formation. These results indicate that reactor geometry needs to be considered in the design of systems used for microwave synthesis. Comparative synthesis reactions were carried out with conventional heating, and microwave heating was shown to be up to over an order of magnitude faster for most of these syntheses.     

微波诱导快速合成纳米NaY分子筛

报导了一种在常压回流微波加热条件下,可使合成的NaY分子筛晶粒尺寸减小至100 nm以下的方法.添加柠檬酸的晶化速率接近添加稀土离子的晶化速率,合成60 min后两者得到的NaY分子筛的晶粒度和硅铝比接近,约为40 nm和5.2,晶粒度小且硅铝比高于在相同条件下没有添加合成得到的NaY分子筛.微波合成的NaY分子筛的晶粒度明显小于常规相同配比所得样品的晶粒度且晶化时间明显缩短,充分证明了微波加热快速均匀且能够得到较小晶粒度的特点.     

In situ SAXS/WAXS of zeolite microwave synthesis: NaY, NaA, and beta zeolites.

A custom waveguide apparatus is constructed to study the microwave synthesis of zeolites by in situ small-angle X-ray scattering (SAXS) and wide-angle X-ray scattering (WAXS). The WR-284 waveguide is used to heat precursor solutions using microwaves at a frequency of 2.45 GHz. The reaction vessels are designed to include sections of thin-walled glass, which permit X-rays to pass through the precursor solutions with minimal attenuation. Slots were machined into the waveguide to provide windows for X-ray energy to enter and scatter from solutions during microwave heating. The synthesis of zeolites with conventional heating is also studied using X-ray scattering in the same reactor. SAXS studies show that the crystallization of beta zeolite and NaY zeolite is preceded by a reorganization of nanosized particles in their precursor solutions or gels. The evolution of these particles during the nucleation and crystallization stages of zeolite formation depends on the properties of the precursor solution. The synthesis of NaA and NaX zeolites and sodalite from a single zeolite precursor is studied by microwave and conventional heating. Microwave heating shifts the selectivity of this synthesis in favor of NaA and NaX over sodalite; conventional heating leads to the formation of sodalite for synthesis from the same precursor. The use of microwave heating also led to a more rapid onset of NaA zeolite product crystallization compared to conventional heating. Pulsed and continuous microwave heating are compared for zeolite synthesis. The resulting rates of formation of the zeolite products, and the relative amounts of the products determined from the WAXS spectra, are similar when either pulsed or continuous microwave heating is applied in the reactor while maintaining the same synthesis temperature. The consequences of these results in terms of zeolite synthesis are discussed.     

Synthesis of EMT/FAU-type zeolite nanocrystal aggregates in high yield and crystalline form

This work focuses on different ways to improve the yield and/or the crystalline quality of EMT/FAU-type zeolite nanocrystal aggregates obtained in the presence of organic additive triethanolamine (TEA). The increase of the amount of aluminum reagent enhances the synthesis yield by a factor of 2.5 without affecting the crystallization rate and the microporous volume. On the other hand, the increase of the thermal treatment time allows to increase the synthesis yield, the crystallization rate and the microporous volume. Furthermore, addition of EMT zeolite seeds into the starting reaction medium improves the crystallization rate and the microporous volume.