Direct Conversion of Syngas into Methyl Acetate,Ethanol, and Ethylene by Relay Catalysis via the Intermediate Dimethyl Ether

Selective conversion of syngas (CO/H₂) into C₂₊ oxygenates is a highly attractive but challenging target. Herein, we report the direct conversion of syngas into methyl acetate (MA) by relay catalysis. MA can be formed at a lower temperature (ca. 473 K) using Cu‐Zn‐Al oxide/H‐ZSM‐5 and zeolite mordenite (H‐MOR) catalysts separated by quartz wool (denoted as Cu‐Zn‐Al/H‐ZSM‐5|H‐MOR) and also at higher temperatures (603–643 K) without significant deactivation using spinel‐structured ZnAl₂O₄|H‐MOR. The selectivity of MA and acetic acid (AA) reaches 87 % at a CO conversion of 11 % at 643 K. Dimethyl ether (DME) is the key intermediate and the carbonylation of DME results in MA with high selectivity. We found that the relay catalysis using ZnAl₂O₄|H‐MOR|ZnAl₂O₄ gives ethanol as the major product, while ethylene is formed with a layer‐by‐layer ZnAl₂O₄|H‐MOR|ZnAl₂O₄|H‐MOR combination. Close proximity between ZnAl₂O₄ and H‐MOR increases ethylene selectivity to 65 %.     

Direct Conversion of Syngas into Methyl Acetate,Ethanol, and Ethylene by Relay Catalysis via the Intermediate Dimethyl Ether

Selective conversion of syngas (CO/H₂) into C₂₊ oxygenates is a highly attractive but challenging target. Herein, we report the direct conversion of syngas into methyl acetate (MA) by relay catalysis. MA can be formed at a lower temperature (ca. 473 K) using Cu‐Zn‐Al oxide/H‐ZSM‐5 and zeolite mordenite (H‐MOR) catalysts separated by quartz wool (denoted as Cu‐Zn‐Al/H‐ZSM‐5|H‐MOR) and also at higher temperatures (603–643 K) without significant deactivation using spinel‐structured ZnAl₂O₄|H‐MOR. The selectivity of MA and acetic acid (AA) reaches 87 % at a CO conversion of 11 % at 643 K. Dimethyl ether (DME) is the key intermediate and the carbonylation of DME results in MA with high selectivity. We found that the relay catalysis using ZnAl₂O₄|H‐MOR|ZnAl₂O₄ gives ethanol as the major product, while ethylene is formed with a layer‐by‐layer ZnAl₂O₄|H‐MOR|ZnAl₂O₄|H‐MOR combination. Close proximity between ZnAl₂O₄ and H‐MOR increases ethylene selectivity to 65 %.     

MOR/SBA-15复合分子筛的合成、表征及其催化性能评价

采用MOR纳米晶和正硅酸四乙酯为硅源,P123三嵌段共聚物为模板剂水热合成MOR/SBA-15复合分子筛催化剂。采用XRD、SEM、TEM和EDX等手段对催化剂进行了表征,在固定床反应器中评价二甲醚制乙醇催化性能。结果表明,通过控制合适的MOR纳米晶种及MOR纳米晶种在SBA-15水热合成体系中的添加量,可以成功地将MOR纳米晶作为SBA-15的结构单元嫁接到SBA-15的介孔骨架中,水热合成的MOR/SBA-15复合分子筛催化剂同时具有MOR和SBA-15的XRD特征衍射峰,相比于SBA-15,其比表面积和总孔体积由756 m2·g~(-1),1.07 cm3·g~(-1)降低至628 m2·g~(-1),0.85 cm3·g~(-1),平均孔径由8.1 nm提高到9.3nm,Cu修饰的MOR/SBA-15复合分子筛催化剂同时具有Cu MOR羰基化和Cu SBA-15加氢的双功能催化性能,其催化剂评价结果显示二甲醚转化率为43.6%左右,乙醇选择性为95.3%,Cu MOR/SBA-15复合分子筛催化剂实现了二甲醚到乙醇的一步转化。     

Modification of Zeolite Morphology via NH4F Etching for Catalytic Bioalcohol Conversion

Various commercial zeolites, including FER, MOR, ZSM-5, BEA, and FAU frameworks, were treated with NH₄F aqueous solutions to study the effects of fluoride etching on different zeolite frameworks. NH₄F-treated small-medium pore FER, MOR, and ZSM-5 samples showed much higher mesoporosities than the untreated ones without alteration of the structural compositions and acidic properties. On the other hand, the 12-membered ring zeolites BEA and FAU showed severe dissolution of the framework aluminosilicate structure after NH₄F etching due to the high accessibility of fluoride species into the framework structures. The effect of NH₄F concentration on the fluoride treatment of H-ZSM-5 zeolite was specifically studied. From the results, we observed that structural etching with 20 wt % NH₄F was optimal for fabricating open-pore H-ZSM-5 zeolite and resulted in a high mesoporosity with comparable relative crystallinity and acidity with respect to the untreated H-ZSM-5. The catalytic activities of the open-pore H-ZSM-5 were evaluated with acid-catalyzed methanol and bioethanol conversions. Remarkably, the hierarchical open-pore H-ZSM-5 zeolite fabricated via fluoride etching exhibited an enhanced catalytic performance in bioethanol conversion with >85 % conversion over 34 h TOS and a higher catalytic stability in methanol conversion than the parent H-ZSM-5 (~50 % of bioethanol conversion at 34 h TOS).     

Specificity of sites within eight-membered ring zeolite channels for carbonylation of methyls to acetyls

The acid-catalyzed formation of carbon-carbon bonds from C1 precursors via CO insertion into chemisorbed methyl groups occurs selectively within eight-membered ring (8-MR) zeolite channels. This elementary step controls catalytic carbonylation rates of dimethyl ether (DME) to methyl acetate. The number of O-H groups within 8-MR channels was measured by rigorous deconvolution of the infrared bands for O-H groups in cation-exchanged and acid forms of mordenite (M,H-MOR) and ferrierite (H-FER) after adsorption of basic probe molecules of varying size. DME carbonylation rates are proportional to the number of O-H groups within 8-MR channels. Na+ cations selectively replaced protons within 8-MR channels and led to a disproportionate decrease in carbonylation turnover rates (per total H+). These conclusions are consistent with the low or undetectable rates of carbonylation on zeolites without 8-MR channels (H-BEA, H-FAU, H-MFI). Such specificity of methyl reactivity upon confinement within small channels appears to be unprecedented in catalysis by microporous solids, which typically select reactions by size exclusion of bulkier transition states.     

Pervaporation Separation and Catalysis Activity of Novel Zirconium Silicalite-1 Zeolite Membrane

Novel zirconium silicalite‐1 zeolite membrane was hydrothermally prepared on the mullite porous support at 150–185°C for 40–72 h by an "in situ" method using tetraethyl orthosilicate (TEOS), zirconium butoxide (ZBOT) and tetrapropylammonium hydroxide (TPAOH) as silica source, zirconium source and organic structure directing agent, respectively. X‐ray diffraction (XRD) patterns, fourier transformed infrared (FT‐IR) spectra, and inductively coupled plasma‐atomic emission spectrometry (ICP) of the accompanying zeolite powder confirmed that the zirconium was isomorphously incorporated into the zeolite framework. The surface chemical compositions of the obtained membrane were measured with an energy‐dispersive X‐ray spectral analyzer (EDS), and the membrane morphologies were observed by a scanning electron microscope (SEM). The results showed that the zeolite crystals growing on the support were zirconium silicalite‐1 zeolites, and the dense membrane layer was composed of the well inter‐growing zeolite crystals. The zirconium silicalite‐1 zeolite membrane, which was derived from the synthesis solution having a molar ratio of 1.00SiO₂:0.01ZrO₂:0.17TPAOH:120H₂O, showed high ethanol permselectivity with a flux of 1.01 kg/(m²·h) accompanied with a separation factor of 73 for ethanol/water (5/95, w/w) system under a pervaporation condition at 60°C. Moreover, this membrane displayed pervaporation‐aided catalysis activity for iso‐propanol oxidation with hydrogen peroxide as oxidant, and the corresponding iso‐propanol conversion was 35%.     

无机体系合成纳米丝光沸石组装体及其优异的二甲醚羰基化催化性能

乙醇是一种重要的有机化工原料和燃料/燃料添加剂.二甲醚(DME)羰基化制乙酸甲酯(MAc)并进一步加氢制备乙醇提供了一条乙醇生产新途径.作为该路线的核心过程,DME羰基化制备MAc反应具有原子经济性高和反应条件温和等特点,近年来备受关注.在DME羰基化制备MAc的多相催化剂中,丝光沸石(MOR)是迄今为止最为高效的催化剂之一,表现出优异的羰基化反应活性和高MAc选择性.但传统的无机体系合成方法只能得到Si/Al比(SAR)介于5～7的MOR沸石,且晶体尺寸通常较大.本文设计了低碱度凝胶体系和晶种法相结合的合成策略,在无有机模板条件下绿色高效合成了SAR最高为9.4的MOR沸石纳米组装体.选取三个具有不同SAR(I-5.3,I-7.4和I-9.4)的样品进一步表征并与其催化性能相关联.实验发现,催化剂的酸强度随着SAR的提高而明显增强,但是三个样品的总酸量以及Br?nsted酸在主孔道和侧口袋的分布比例接近.利用傅里叶变换红外和钠核磁技术分别对H-MOR及其Na-MOR母体样品中的酸羟基和Na+的空间分布进行分析,发现质子在主孔道与侧口袋的分布比例与Na+的分布并不一致,表明质子和Na+可以落位于同一T位的不同氧位.通过对催化剂扩散性质以及酸性位的可接触性的表征,发现低硅样品I-5.3和I-7.4尽管晶粒尺寸较小,但由于孔道中骨架外铝的含量较高,严重阻碍内扩散,并且导致吡啶对12元环主孔道中酸中心的可接触性降低.相对于低硅样品,高硅样品I-9.4由于其相对较低的骨架铝密度和较低的脱铝程度,表现出最优的传质性能以及吡啶对12元环主孔道中酸中心的可接触性,催化剂主通道中的所有酸性位都能被吡啶所覆盖.相应地,样品I-9.4(吡啶修饰催化剂)在DME羰基化反应中表现出较高的催化活性与MAc选择性(接近100％),MAc产率高达6.8 mmol/g/h.综上,本文发展的无有机模板策略合成MOR沸石纳米组装体具有良好应用前景.     

FER分子筛中铝原子的受限落位

分子筛是一类具有规则孔道或笼状结构的多孔材料,因其独特的结构和可调的酸性而广泛用于石油化工、精细化学品合成、现代煤化工等诸多行业.2006年Iglesia等在具有8元环孔道结构/侧口袋的FER和MOR分子筛上实现了无卤素添加、无贵金属存在条件下,由二甲醚羰基化合成乙酸甲酯的反应.乙酸甲酯通过进一步加氢可实现煤基乙醇的绿色生产.MOR分子筛通常具有较高的催化活性,但失活迅速;FER分子筛表现出良好的催化稳定性,但活性较低.如何在保证FER分子筛稳定性的前提下,进一步提升其羰基化活性是目前研究的热点.前期理论和实验研究发现,二甲醚羰基化反应活性与分子筛8元环孔道中的Br?nsted酸位密度存在正相关.因此,通过优化合成条件,选择性调控铝原子分布在"ferrierite"笼中,可以提高FER分子筛的羰基化反应活性.尽管研究者已在调节FER分子筛铝分布方面进行了大量研究,但对于不同T位上Al原子的精准识别以及对应Br?nsted酸位的可接触性还缺少系统和深入的认识.本文选取了几种代表性模板剂,分别在碱性和含氟体系下制备了系列FER分子筛样品,利用Rietveld精修和模拟退火算法,在原子水平揭示了模板剂种类以及合成介质变化对Al原子在不同T位分布的影响,并结合二甲醚羰基化反应进行了结构和性能的关联.首先选取不同尺寸大小的环状胺(环己胺、哌啶、吡啶、吡咯烷)和链状胺(乙二胺)合成了具有相似形貌、孔结构、酸密度的系列FER分子筛样品.以CHA-Na-FER为例,PXRD精修结果显示,Na+(平衡35％的骨架负电荷)分布在10元环孔道中与O1形成氢键,质子化的环己胺分布在"ferrierite"笼中,并且环己胺上的N与O3形成氢键.这说明与O1相连的T3位以及与O3相连的T1位都有可能是Al富集的位置.为了进一步验证该结论,本文还精修了吸附探针分子吡啶的样品CHA-Na-FER-Py-60h.原粉以及吸附吡啶样品的精修结果表明,T1位和T3位是样品中铝富集的位置.随后,运用相同方法研究了Py-Na-FER,PI-Na-FER,En-Na-FER和Pyrr-HF-FER样品中的Al落位,发现T1/T3位均是样品中Al富集的位置.此外,理论计算结果表明T1/T3位上Al原子的取代能较低,说明Al优先取代T1/T3位上的Si,这与精修结果相一致.前期理论模拟结果表明,FER分子筛中T2-O5和T4-O7位点的CO插入反应能垒较低,是二甲醚羰基化反应的活性位.本文吡啶吸附实验、热重分析以及PXRD精修结果表明,FER分子筛中大部分Al富集在T1/T3位,与T2/T4位相关的Br?nsted酸约占18％～30％.最后,对各样品进行了二甲醚羰基化反应评价,结果显示PI-Na-FER,Py-Na-FER,En-Na-FER和CHA-Na-FER催化剂的乙酸甲酯生成速率相近,约为0.10 mol/(mol H+?h).Pyrr-HF-FER催化剂的乙酸甲酯生成速率最高,可达到0.16 mol/(mol H+?h),这可能是由于Pyrr-HF-FER催化剂具有更多T2/T4位相关的Br?nsted酸.虽然Pyrr-HF-FER催化剂的乙酸甲酯生成速率较其他四个催化剂有一定提升,但其仍远低于MOR分子筛上乙酸甲酯生成速率(0.40 mol/(mol H+·h)).综上,有机模板剂的选择与合成介质的改变对FER分子筛中Al分布的调控作用是有限的,即Al原子总是优先分布于T1/T3位.而与T1和T3位相关的Br?nsted酸位不是二甲醚羰基化反应的活性位点.因此与MOR相比,FER分子筛在二甲醚羰基化反应中表现出较低的催化活性.     

纳米晶自组装多级孔丝光沸石合成及其优异的催化性能

由于具有独特的孔道结构、高的热稳定性及适宜的酸性,丝光沸石(MOR)被广泛应用于正构烷烃异构化、二甲苯异构化、烷基化、甲苯歧化与烷基芳烃之间的烷基转移以及二甲醚羰基化反应中.但是其单一的微孔孔道结构在催化反应中带来严重的扩散限制,导致微孔内部活性位点利用率低和容易积碳失活等问题,同时也限制了MOR在大分子催化反应中的应用.在分子筛中引入介孔或减小晶粒尺寸是克服扩散限制的有效方法,也成为目前分子筛领域的研究热点.早期的研究中主要通过水蒸气处理、酸处理或碱处理等方法来制备多级孔MOR.但是,对于富铝的MOR,通常需要通过多步处理才能引入介孔.一步法直接制备多级孔MOR是目前的研究热点和难点.虽然文献报道可以采用自制的具有随机分子量分布的阳离子聚合物为模板剂和双亲有机硅表面活性剂OS-12制备多级孔MOR,但是合成的多级孔MOR为具有较窄a-b截面的纳米纤维或纳米棒状MOR,其12元环主孔道中的扩散限制没有得到有效改善.研究者采用N,N,N',N'-四乙基-外,外-二环[2.2.2]辛-7-烯-2,3：5,6-联四氢吡咯二碘铵盐和N,N,N,N',N',N'-六乙基-1,5-戊二胺阳离子为结构导向剂或者多季铵盐表面活性剂C18H37N+(Me)2C6H12N+(Me)2CH2C6H4CH2N+(Me)(C4H7CH2OH)为封端剂合成了具有三维纳米尺寸的MOR.然而这些纳米MOR的合成使用了结构复杂、价格昂贵的模板剂或表面活性剂.因此,开发简便、经济的MOR纳米晶合成路线仍是一个巨大挑战.本文通过在凝胶中添加少量四乙基氢氧化铵(TEAOH)和商业化表面活性剂,在低温下采用一步水热法成功制备了20–50 nm颗粒自组装的多级孔MOR (MOR-M),这是多级孔MOR合成中无c轴优势生长的首例报道.采用X射线衍射、X射线荧光光谱、扫描电镜、透射电镜、N2物理吸附、核磁共振、热重及NH3程序升温脱附等多种表征手段对合成样品的物理化学性质进行了研究.考察了合成参数对产物形貌和孔结构的影响,发现TEAOH的加入和较低的晶化温度是合成MOR-M的关键因素,而表面活性剂的作用则是进一步抑制晶粒的过度生长.仅添加双季铵盐表面活性剂C12-2-12时得到的为c轴优势生长的纳米片状多级孔MOR.与常规MOR相比, MOR-M具有较短的扩散路径、较大的外比表面积和丰富的介孔结构,在大分子苯和苯甲醇苄基化反应中表现出较常规MOR和具有更长c轴长度的纳米片状MOR更高的活性和目标产物选择性.在二甲醚羰基化制备乙酸甲酯的反应中, MOR-M亦表现出较高的活性及抗失活性能,积碳速率显著下降.     

Investigation and Modeling of the Hydrothermal Stability of Technically Relevant Zeolites

The dense-structured zeolites of types ZSM-5 (MFI) and mordenite (MOR) of different SiO₂/Al₂O₃ moduli are relatively stable under treatment by liquid water for 72 hours up to 513 K. The open-structured zeolites of types Y in dealuminated modification (FAU) and beta (BEA) undergo strong decomposition in the same range. For these two sample types a mathematical model for the decomposition of the zeolite framework is established that takes into account the influence of modulus as well as temperature. Here the kinetic of the solid phase reaction is a superposition of two different mechanisms described by the Monod equation. Dedicated to the late of Wolfgang Schirmer.     

Cu-Pd/MCM-22催化剂上二甲醚低温水解反应

 考察了分子筛的类型、硅铝比及Cu和Pd改性对分子筛催化剂上二甲醚低温水解活性的影响. 结果表明,酸性的MCM-22和HZSM-5分子筛催化剂具有较高的二甲醚水解活性,且其活性随着分子筛硅铝比的增加而降低. 这表明分子筛的类型及酸性对催化剂性能有重要影响,具有超笼结构的MCM-22分子筛上B酸中心的良好可接近性,使得该分子筛催化剂的水解活性较相同硅铝比的HZSM-5分子筛高. 与改性前相比, Cu和Pd改性后的MCM-22催化剂显示出更高的二甲醚水解活性.     

纳米薄层HZSM-5分子筛催化甲醇制丙烯

在合成系列硅铝比纳米薄层HZSM-5分子筛的基础上,研究了纳米薄层HZSM-5分子筛催化甲醇制丙烯(MTP)的反应性能.在固定床微反装置上详细考察了工艺条件对纳米薄层HZSM-5分子筛催化性能的影响,同时与纳米HZSM-5分子筛对MTP反应的催化性能进行了比较.结果表明,纳米薄层HZSM-5分子筛具有较高的目的产物选择性和较长的催化寿命.在适宜硅铝比(n(SiO2)/n(Al2O3)=213)和反应条件下(温度470°C,甲醇质量空速为3 h-1),丙烯的选择性达到46.7%,三烯(乙烯、丙烯和C4烯烃)选择性达到78.7%.其中,丙烯/乙烯的质量比可达到6.5,是纳米HZSM-5分子筛的2倍,而芳烃的选择性比纳米分子筛明显降低.这是因为纳米薄层HZSM-5分子筛比纳米HZSM-5分子筛具有较宽的(010)晶面、较大的外比表面积和介孔孔容.     

Catalytic activity of H-ZSM-5 and H-ZSM-5/AL-MCM-41 in the conversion of ethanol to gasoline fraction hydrocarbons

H-ZSM-5 (Si/Al = 10.6 and 20) efficiently catalyzes the transformation of ethanol into C₅-C₁₂ gasoline hydrocarbons in 27–33 mass % yield at 320°C and feed rate 20 mmol C₂H₅OH/(gcat·h). Only ethylene is produced on the mesoporous zeolite H-ZSM-5/Al-MCM-41 with 100% ethanol conversion. This discrepancy may be attributed to blockage of the ZSM-5 micropores in the mesoporous zeolite structure.     

Effect of Calcination Temperature on Catalytic Activity and Textual Property of Cu/HMOR Catalysts in Dimethyl Ether Carbonylation Reaction

The effect of calcination temperature on the catalytic activity for the dimethyl ether (DME) carbonylation into methyl acetate (MA) was investigated over mordenite supported copper (Cu/HMOR) prepared by ion-exchange process. The results showed that the catalytic activ-ity was obviously affected by the calcination temperature. The maximal DME conversion of 97.2% and the MA selectivity of 97.9% were obtained over the Cu/HMOR calcined at 430 oC under conditions of 210 oC, 1.5 MPa, and GSHV of 4883 h^-1. The obtained Cu/HMOR catalysts were characterized by powder X-ray diffraction, N₂ absorption, NH₃ temperature program desorption, CO temperature program desorption, and Raman techniques. Proper calcination temperature was effective to promote copper ions migration and diffusion, and led the support HMOR to possess more acid activity sites, which exhibited the complete decomposing of copper nitrate, large surface area and optimum micropore structure, more amount of CO adsorption site and proper amount of weak acid centers.     

ZSM-5／MOR复合分子筛催化剂对混合C4烃转化反应的催化性能

以ZSM-5/丝光沸石(MOR)复合分子筛为催化剂,对混合C4烃的催化转化反应进行了评价,并采用程序升温脱附和原位红外光谱技术对ZSM-5/MOR的酸性进行了表征. 结果表明,与ZSM-5相比, MOR具有很低的催化活性,但ZSM-5/MOR复合分子筛具有较高的催化活性,随着ZSM-5/MOR复合分子筛中ZSM-5含量的增加, C4烃转化率稍有升高;在C4烃转化率大致相同的情况下,乙烯和丙烯的总选择性比较接近,但苯和甲苯的总收率却快速升高. 随着ZSM-5/MOR复合分子筛中ZSM-5含量的增加,弱酸和中强酸的酸量逐渐减少,强酸的酸量有所增加. 由于ZSM-5/MOR复合分子筛中MOR对ZSM-5起到分散作用而产生更多的L酸中心,且此L酸中心处于分子筛的外表面而具有较高的能量,导致苯和甲苯的总收率升高.     

HZSM-5型分子筛硅铝比对一步法合成二甲醚的影响

以Cu/Zn/Al(摩尔比为6∶3∶1)甲醇合成催化剂与HZSM-5型分子筛混合,制备了一步法二甲醚合成催化剂。通过改用三种不同Si/Al摩尔比（摩尔比为25、38和50）的HZSM-5型分子筛,考察了催化剂中脱水组分（HZSM-5分子筛）的酸性对二甲醚合成的影响。结果表明,随着催化剂Si/Al摩尔比的降低,分子筛的酸性增强,使得CO单程转化率提高。当催化剂Si/Al＝38时,CO对二甲醚的选择性最高,可达到68.13％,其次是催化剂Si/Al＝50,选择性最差的是Si/Al＝25的催化剂。在553 K、 3 MPa和4 000 h－1的条件下,Si/Al＝25和Si/Al＝38的催化剂CO单程转化率和DME的选择性接近一致。在此条件下,两者的时空产率达到试验的最大值,分别为0.38 gDME/(gcat·h)和0.36 gDME/(gcat·h),在试验范围内,一步法合成二甲醚催化剂最佳的Si/Al摩尔比为25。     

清液体系中T型分子筛膜的高重复性合成与渗透汽化性能

以自制微米级分子筛为晶种,在清液体系中成功合成出高性能的T型分子筛膜,考察了硅铝比、水硅比、碱度及合成温度与时间等条件对膜的生长和渗透汽化性能的影响.结果表明,在摩尔组成为1SiO₂:0.015Al₂O₃:0.41(Na₂O+K₂O):30H₂O的清液体系中,于423K晶化6h的条件下可较快地形成一层厚度为5μm的连续致密纯相T型分子筛膜,较大缩短了膜合成时间且提高了膜致密性.在优化条件下所合成的膜具有优良的分离性能和高重复性.348K时,在10wt%水-90wt%异丙醇混合物体系中膜的渗透通量和分离因子分别高达4.20kg/(m²·h)和7800.     

Conjugate Conversion of Methanol and Lower Alkanes C3-C4 on Zeolite-Containing Catalysts

Simultaneous conversion of methanol and lower alkanes C₃-C₄ on high-silica zeolites of ZSM-5 type of various compositions (SiO₂/Al₂O₃ 30, 50, 90) was studied. The catalytic activity of zeolite catalysts and their physicochemical properties (acidity, sorption capacity, and pore structure) were evaluated.     

Catalytic Acylation of Ethylidenecyclohexane over Zeolite Catalysts

Beak et al[1 ] reported that the acylation of ethylidenecyclohexane( EDC) using zincchloride as a catalyst gave 3 -( 1 -cyclohexenyl) -2 -butanone( CHB) in good yield.However,it is pity that they provided only little information about reaction conditions,and no information on comparison of activities of various catalysts. Itis well known thatconventional Zn Cl2 catalyst leads to a great number of environmental pollution,whichcould be mainly overcome by use of the solid catalysts as we have …     

磷酸盐辅助一步合成介孔Beta分子筛

在合成纳米Beta分子筛的体系中添加磷酸二氢钠等无机盐,通过一步晶化制备介孔Beta分子筛.纳米分子筛组装形成的二次粒子克服了传统纳米粒子难以过滤分离的问题,同时所形成的粒间介孔改善了分子在催化剂内的扩散从而提高催化反应效率.采用X射线衍射、扫描电镜、氮吸附-脱附和氨程序升温脱附等表征方法对材料进行表征,结果表明磷酸二氢钠的用量对介孔体积有很大影响.当NaH2PO4/SiO2摩尔比为0.1时,合成的材料具有较好的孔结构和酸性,并在叔丁醇与苯酚的液相烷基化反应中表现出最好的催化活性.