四甲基锡在MCM-41分子筛表面的接枝反应及产物性能

研究了真空条件下SnMe4在MCM-41分子筛表面的接枝反应，并用元素分析、ICP、GC-MS、XRD、FTIR、DRS、13C及119Sn MAS NMR、XPS、BET、TPD、TPR等方法对产物的组成、结构和性质进行了表征.结果表明, 两者可以定量地进行化学反应，将确定数目的甲基锡基团接枝在分子筛表面, 形成SnMe3/MCM-41物种；接枝反应发生在分子筛表面上, 不破坏MCM-41分子筛骨架结构；改性分子筛的BET比表面积有所降低，孔体积变小, 表面性质发生变化.四甲基锡在MCM-41上接枝反应的温度为343 K,比它与HY沸石的反应温度(193 K)高得多，并且产物SnMe3/MCM-41的热稳定性也高于SnMe3/HY.     

表面金属有机化学:SnMe4在HY沸石超笼表面的接枝反应

研究了高真空条件下SnMe4在HY沸石超笼的接枝反应,并用元素分析,ICP, GC, XRD, FTIR, DTG, DTA, UV-vis, DRS, N2吸附等方法对产物的组成、结构和性质进行了详细表征.研究结果表明,两者可以定量地、有选择性地进行化学反应,将确定数目的三甲基锡基团接枝在沸石的超笼中.反应可以在非常低的温度下快速进行,表观活化能为10.4 kJ·mol-1.经SnMe4改性后的HY沸石分子筛BET比表面积降低,孔体积变小,对不同尺寸的烃分子表现出明显的吸附择形性.     

烷基锡化合物在HY沸石超笼表面的接枝反应研究

在高真空系统中研究了HY沸石分子筛与SnMe₄、SnEt₄、SnPr₄和SnBu₄的反应，用元素分析、ICP、GC、XRD、FTIR、TG、DRS、TPR、BET及烷烃和芳烃的脉冲吸附等方法表征了产物的组成、结构和性质。结果表明，HY沸石分子筛超笼羟基与SnMe₄、SnEt₄、SnPr₄和SnBu₄的反应温度分别为：183K、243K、273K和333K，生成组成为(≡Si-O)SnR₃的表面单接枝物种。表面接枝烷基锡碎片后，HY沸石的孔口尺寸变小，吸附行为发生显著变化。     

HY沸石超笼“半三明治”环戊二烯铁物种的接枝

在真空条件下研究了Cp₂Fe在HY沸石表面的接枝反应，并用原位FTIR、ICP、XRD、TPD-MS和UV-Vis DRS等方法对接枝产物的组成、结构及性质进行了表征。结果表明，在低于423 K的温度下，Cp₂Fe可以强吸附在沸石的超笼内，并被氧化为Cp₂Fe⁺阳离子；当在423 K长时间加热时，Cp₂Fe⁺可与超笼表面的酸性中心发生化学反应，脱除一个环戊二烯基团，在沸石超笼形成“半三明治”环戊二烯铁CpHFe(OZ≡)₃(Z为沸石骨架Si或Al原子)表面物种。一个超笼中可接枝3个CpHFe基团，该物种在真空、惰性气体气氛和473 K以下能够在表面稳定存在。接枝反应不破坏HY的骨架结构，修饰后HY沸石的BET比表面积和微孔体积大约降低一半。     

沸石催化的2,4,4-三甲基-1-戊烯的酰化反应

通过HY沸石与某些传统催化剂的比较，发现HY在2，4，4-三甲基-1-戊烯与乙酸酐的酰化反应中比那些传统催化剂更有效．用HY沸石作催化剂，室温下通过2，4，4-三甲基-1-戊烯与乙酸酐的酰化反应，合成了三种异构体，即4-（2，2-二甲基丙基）-4-戊烯-2-酮、（E）-4，6，6-三甲基-4-庚烯-2-酮和（Z）-4，6，6-三甲基-4-庚烯-2-酮．考察了HY沸石的用量对该酰化反应的影响．当2，4，4-三甲基-1-戊烯／乙酸酐／HY沸石=1mmol／10mmol／0．250g，反应温度25℃、反应时间2h时，生成的三种异构体产率之和为72％，HY沸石对于该反应具有极好的选择性和优良的活性稳定性，不同阳离子交换的Y沸石也用于催化2，4，4-三甲基-1-戊烯的酰化反应。     

用新方法催化合成6-乙酰基-1-甲基环己烯

室温下用HY沸石取代传统催化剂通过1-甲基环己烯与乙酐的酰基化反应合成了6-乙酰基-1-甲基环己烯，考察了HY沸石的SiO2／Al2O2摩尔比、用量和活化时间以及反应时间对该酰化反应的影响．当1-甲基环己烯／乙酐／HY沸石(SiO2／Al2O3摩尔比=29)=1mmol／10mmol／0．200g、反应温度25℃、反应时间3h时，所得酰化产品的产率为60％，HY沸石能够回收和重新使用，显示出与新鲜催化剂几乎相同的催化活性．     

原位FTIR及探针反应法研究Pt与L沸石的相互作用

本文报道了一种适合催化研究的金属原位IR池,Pt分散在NH~4L沸石上呈缺电子性,在异丙醇分解反应中不显示脱氢活性,但通过加氢抗结炭作用保护着沸石上的酸位,从而增强了NH~4L沸石的酸性催化作用,负载在碱性KL沸石上的Pt呈富电子性,在反应中极易被噻吩中毒(Pt/KL+NH~4L)混合样品在预处理和反应的过程中Pt从KL 向NH~4L沸石上迁移,导致其催化性能相似于Pt/NH~4L,实验证明:Pt与L 沸石载体之间存在着明显的相互作用,由于Pt易给出电子而不易接受电子,因此与酸位的相互作用强于与碱位的相互作用.     

沸石分子筛催化剂上萘的择形异丙基化反应性能

 研究了HY,Hβ,HM和HZSM－5沸石分子筛对萘择形异丙基化反应的催化性能．结果发现,这些沸石分子筛的活性顺序为HY＞Hβ＞HM＞HZSM－5,对2,6－二异丙基萘的选择性顺序为HM＞Hβ＞HY．除沸石分子筛的酸量与酸分布外,其孔道结构与大小是影响萘异丙基化反应的主要因素．脱铝能选择性地降低沸石外表面的酸性,且对沸石的催化性能有较大影响．常压水蒸气脱铝结合强酸再处理有利于催化剂催化性能的提高．提高反应温度有利于萘的转化,但温度过高会引发许多副反应,适宜的反应温度约为523K．反应时间对产物分布的影响不明显．异丙醇／萘摩尔比应小于2．     

沸石表面有机金属化学ZSM-5外表面上——Ge(n-C4H9)x基团的接枝及其性质研究

用气体分析及IR,NMR和元素分析等方法研究了真空系统中230℃和280℃下四丁基锗在ZSM-5沸石表面上的接枝反应,并对所得沸石的热稳定性和吸附性质进行了表征,与作者曾报道的硅胶及丝光沸石上的反应类似,四丁基锗也能与ZSM-5沸石表面上的硅羟基发生缩合反应,在其外表面或孔口生成组成为(=Si-O)xGe(n-C4H9)4-x(x=2~3)的表面有机锗化合物,在２３０℃接枝丁基锗基团不影响沸石的结构和表面积,仅改变它的孔口大小,在改性后的沸石上,Ｎ２的吸附性质没有改变,而不同分子尺寸的烃,加正已烷,２-甲基戊烷,２,３-二甲基丁烷却呈现出完全不同于起始ＺＳＭ-５沸石的择形吸附效应.     

沸石表面有机金属化学ZSM-5外表面上

用气体分析及IR,NMR和元素分析等方法研究了真空系统中230和280℃下四丁基锗在ZSM-5沸石表面上的接枝反应,并对所得沸石的热稳定性和吸附性质进行了表征.与作者曾报道的在硅胶及丝光沸石上的反应类似,四丁基锗也能与ZSM-5沸石表面上的硅羟基发生缩合反应,在其外表面或孔口生成组成为(≡Si—O)     

红外光谱法研究表面溢出效应

采用红外光谱法, 利用重氢交换反应证明在Pt-NaY/HY体系有氢溢出(spillover)效应发生, 测量了100 ℃和50 ℃时的交换速率。发现在50 ℃时高频羟基的交换速率大于低频羟基。并对溢出机构进行了初步的讨论。     

Selective methane chlorination to methyl chloride by zeolite Y-based catalysts

The CH₄ chlorination over Y zeolites was investigated to produce CH₃Cl in a high yield. Three different catalytic systems based on Y zeolite were tested for enhancement of CH₄ conversion and CH₃Cl selectivity: (i) HY zeolites in H⁺-form having various Si/Al ratios, (ii) Pt/HY zeolites supporting Pt metal nanoparticles, (iii) Pt/NaY zeolites in Na⁺-form supporting Pt metal nanoparticles. The reaction was carried out using the gas mixture of CH₄ and Cl₂ with the respective flow rates of 15 and 10 mL min⁻¹ at 300–350 °C using a fixed-bed reactor under a continuous gas flow condition (gas hourly space velocity = 3000 mL g⁻¹ h⁻¹). Above the reaction temperature of 300 °C, the CH₄ chlorination is spontaneous even in the absence of catalyst, achieving 23.6% of CH₄ conversion with 73.4% of CH₃Cl selectivity. Under sufficient supplement of thermal energy, Cl₂ molecules can be dissociated to two chlorine radicals, which triggered the C-H bond activation of CH₄ molecule and thereby various chlorinated methane products (i.e., CH₃Cl, CH₂Cl₂, CHCl₃, CCl₄) could be produced. When the catalysts were used under the same reaction condition, enhancement in the CH₄ conversion was observed. The Pt-free HY zeolite series with varied Si/Al ratios gave around 27% of CH₄ conversion, but there was a slight decrease in CH₃Cl selectivity with about 64%. Despite the difference in acidity of HY zeolites having different Si/Al ratios, no prominent effect of the Si/Al ratios on the catalytic performance was observed. This suggests that the catalytic contribution of HY zeolites under the present reaction condition is not strong enough to overcome the spontaneous CH₄ chlorination. When the Pt/HY zeolite catalysts were used, the CH₄ conversion reached further up to 30% but the CH₃Cl selectivity decreased to 60%. Such an enhancement of CH₄ conversion could be attributed to the strong catalytic activity of HY and Pt/HY zeolite catalysts. However, both catalysts induced the radical cleavage of Cl₂ more favorably, which ultimately decreased the CH₃Cl selectivity. Such trade-off relationship between CH₄ conversion and CH₃Cl selectivity can be slightly broken by using Pt/NaY zeolite catalyst that is known to possess Frustrated Lewis Pairs (FLP) that are very useful for ionic cleavage of H₂ to H⁺ and H⁻. Similarly, in the present work, Pt/NaY(FLP) catalysts enhanced the CH₄ conversion while keeping the CH₃Cl selectivity as compared to the Pt/HY zeolite catalysts.     

Reactivities of tetraalkyltin complexes toward Pt/HY zeolite

Tetraalkyltin complexes, SnR₄ (R = Me, Et, Pr, Bu) could react with Pt/HY at 193, 243, 273 and 333 K, respectively. The reactions occurred on the surface of the zeolite and the organotin grafted zeolites were characterized in detail. The framework and the microporous structure of the grafted Pt/HY zeolites were retained. However, the modified zeolites showed better size selectivity in the absorption of hydrocarbons.     

分子筛体系的氢溢出效应

分子筛体系的氢溢出效应李晓燕，盛太成，杨孔章（山东大学化学院，济南２５０１００）关键词铂／分子筛催化剂，氢溢出，程序升温脱附负载型金属催化剂的表面氢溢出效应近年来引起了人们的重视．人们采用不同的实验方法对此进行了广泛的研究，但对以分子筛为担体的负载型...     

AROMATIZATION OF C_6 PARAFFIN OVER Pt/ML(M=K,Rb)AND Pt/AlPO_4-5 CATALYSTS AT DIFFERENT TEMPERATURE

The reaction product distributions from the reactions of n-C6 and MCP over different Pt-catalysts at different temperatures were studied. It is shown that the product distributions depended on the reaction temperatures The influences of the zeolite channel functioned only at high temperature. The activity and selectivity of aromatization of n-C6 over Pt/AIPO4-5 were lower than those over Pt/L zeolite catalysts. A1PO4-5 is a non-basic support and its product distribution and reaction mechanism were different from that of basic-support catalysts such as Pt/KL and Pt/RbL.     

Synthesis of 3-(1-Cyclohexenyl)-2-butanone via Environmentally Friendly Catalysts

Introduction3- ( 1 - Cyclohexenyl) - 2 - butanone( CHB) is oneofthe importantchemicals and has a potential valuein perfume industry.Beak et al.[1] reported thatthe acylation of ethylidenecyclohexane( EDC) withzinc chloride as a catalystgave3- ( 1 - cyclohexenyl) -2 - butanone in a good yield,butthey have notmadea more detailed investigation.The use of such aconventional catalyst as zinc chloride leads to anumber of problems such as corrosion,unclean re-action products and the disposal of pot…     

苯甲醚在复合催化剂上的催化酰化

复合催化剂首次用于催化苯甲醚与酰化剂乙酰氯的酰化反应.发现不同沸石的单独使用仅给出很低产率的对-甲氧基苯乙酮.但是由HY沸石(硅铝比=40)或USY(超稳Y沸石)和SnO组成的复合催化剂的催化活性比单独使用沸石时高得多.增加由USY沸石和不同量的SnO组成的复合催化剂中的SnO的量,导致对-甲氧基苯乙酮产率的提高.由H型沸石(HY和H-ZSM-5沸石)和SnO组成的复合催化剂在苯甲醚与乙酰氯的酰化反应中的催化活性主要取决于所用沸石的硅铝比.     

Catalytic Acylation of Anisole over Some Zeolites

Introduction　　 Friedel- Crafts acylation is one of the most important methods for synthesizing aromaticketones[1 ].Lewis acids or other catalysts are used in order to allow the reaction of anisole toproceed ata convenientrate.Forexample,the reaction of anisole with aceticanhydride in thepresence of aluminium chloride(Al Cl3/ anisole molar ratio=2 .2 / 1 ) gives4- methoxyace-tophenone in a good yield[2 ].Polyphosphoric acid(PPA/ anisole molarratio=1 3.6 / 1 ) hasalsobeen used for the react…