双功能硅烷化修饰MCM-41固载Cosalen催化环己烷氧化

采用双功能硅烷化试剂γ-氨丙基甲基二乙氧基硅烷(AMS),对(MCM-41)全硅介孔分子筛一步进行氨基官能团化和甲基疏水性修饰,然后将双水杨醛缩乙二胺合钴(Cosalen)通过氨基的轴向配位固载在修饰后的载体MCM-41上。X射线衍射和N2物理吸附/脱附的结果表明:经过AMS双功能硅烷化修饰以及固载Cosalen后载体的孔道结构保持良好。考察了硅烷试剂用量对硅烷化效率的影响,结果表明:当AMS的加入量为4.00mmol/g时,甲基修饰量达到1.95mmol/g;水和环己烷的静态吸附结果表明硅烷化修饰后,催化剂载体的疏水性明显增强。制得的催化剂应用于环己烷的分子氧氧化反应,130℃反应2h,环己烷转化率达到7.2%,环己醇和环己酮总选择性达到70.5%,较未经AMS修饰的催化剂Cosalen/MCM-41获得的醇酮总选择性提高了13%。     

环己烷催化氧化制环己酮的MCM-41催化剂研究

以十六烷基三甲基溴化铵为模板剂,正硅酸乙酯为硅源,采用水热合成法制备纯MCM-41分子筛和掺杂不同金属离子的MCM-41分子筛,并采用等体积浸渍法将一定量的金属离子负载在纯MCM-41分子筛内表面上,制备了负载型和掺杂型2类不同的MCM-41分子筛催化剂.分别考察了负载和掺杂的金属种类、金属Cr负载和掺杂量等对环己烷氧化制环己酮中的催化活性和选择性的影响.研究表明:采用掺杂制备的MCM-41分子筛催化剂活性明显高于负载型MCM-41分子筛催化剂;Cr掺杂量增加,虽然环己烷氧化转化率增加,但产物选择性下降;掺杂Cr的MCM-41分子筛催化剂,用于环己烷氧化制环己酮,在Si与Cr摩尔比为50以下、反应温度75℃、H2O2与环己烷摩尔比为1.2的条件下,环己烷的转化率可达60%左右,环己酮和环己醇的总选择性可达94%以上.     

分子氧氧化环己烯制备环己烯酮

针对分子氧氧化环己烯制备环己烯酮的催化反应体系,以Co(Ⅱ)为活性中心,3,5-二氯水杨醛与邻苯二胺为配体,胺化的MCM-41型介孔分子筛为载体,用化学键联法制备出一种固载型希夫碱催化剂。进而考察了该催化剂对分子氧氧化环己烯制备环己烯酮的工艺条件,结果表明,在常压、催化剂用量0.15 g(2 mL环己烯)、乙腈20 mL、氧气流量5 mL/min、反应温度60℃、反应时间8 h、叔丁基过氧化氢(TBHP)0.04 mL的条件下,环己烯酮的单程收率达54.87%,催化剂容易分离回收,可重复使用。     

杂原子MCM-41分子筛对过氧化氢液相氧化环己烷的研究

分别考察了反应温度、过氧化氢用量及加入方式等因素对Cr、Fe和Ce改性后的杂原子MCM-41分子筛催化剂液相催化氧化环己烷制取环己酮反应的影响。研究结果表明，Cr-MCM-41〖JP〗催化剂具有较好的催化活性。选择适当的反应温度、过氧化氢用量和加入方式可以有效提高环己烷转化率和过氧化氢利用率。在70 ℃和n(C₆ H₁₂)∶n(H₂O₂)=1∶2条件下，采用两次加入过氧化氢的方式，环己烷转化率为33.7％，酮醇总选择性97.2％，n(环己酮)∶n(环己醇）＝1.99，过氧化氢利用率37.1%。     

MCM-41介孔分子筛催化剂的制备及催化性能的研究

文章采用碱性水热晶化法制备MCM-41介孔分子筛为载体,用浸渍法将非贵金属Ni和12-硅钨杂多酸(HSi W)固载于分子筛上,制备得Ni-HSi W/MCM-41金属-酸双功能催化剂作为新型的长链烷烃异构化催化剂。研究了Ni-HSi W/MCM-41双功能催化剂在常压固定床反应器上,以正庚烷异构化反应为探针反应,催化剂在不同制备条件下的催化性能。结果表明催化剂在一定还原条件和反应条件下当Ni固载量为4 wt.%、HSi W固载量为30%,催化剂的焙烧温度为400℃时是最佳制备条件。     

MCM-48分子筛负载磷钨钼杂多酸催化合成环己酮1,2-丙二醇缩酮

以MCM-48分子筛负载磷钨钼杂多酸为多相催化剂,通过环己酮和1,2-丙二醇反应合成环己酮1,2-丙二醇缩酮.采用正交实验法探讨了MCM-48分子筛负载磷钨钼杂多酸对缩酮反应的催化活性,较系统地研究了原料用量、催化剂用量、带水剂用量、反应时间等因素对收率的影响.结果表明MCM-48分子筛负载磷钨钼杂多酸是合成环己酮1,2丙二醇缩酮的良好催化剂,在n(环己酮)n(1,2丙二醇)=11.6,催化剂用量为反应物料总质量的0.2%,环己烷为带水剂,反应时间1.0 h的条件下,环己酮1,2-丙二醇缩酮的收率可达90.7%.     

分子筛MCM-48负载磷钨酸催化合成丁酮乙二醇缩酮

报道了以分子筛MCM-48负载磷钨酸H3PW12O40/MCM48为催化剂,通过丁酮和乙二醇反应合成了标题化合物,探讨了 H3PW12O40/MCM-48对缩酮反应的催化活性,较系统地研究了酮醇物质的量比、催化剂用量、反应时问诸因素对产品收率的影响.实验表明:H3PW12O4z/MCM-48是合成丁酮乙二醇缩酮的良好催化剂,在n(丁酮):n(乙二醇):1:1.6,催化剂用量为反应物料总质量的1.5%,环己烷为带水剂,反应时间2 h的优化条件下,丁酮乙二醇缩酮的收率可达68.1%.     

MCM-41负载Lewis酸催化合成2-甲基吲哚

以苯肼和丙酮为原料,在负载有各种Lewis酸的MCM-41分子筛催化下采用Fischer吲哚合成法合成2-甲基吲哚,在比较了AlCl3/MCM-41、ZnCl2/MCM-41和FeCl3/MCM-41对反应的选择性和收率后发现,负载量为4mmol/g的ZnCl2/MCM-41具有对反应较好的选择性,目标产物收率达到了76.2%。     

分子筛MCM-48负载硅钨酸催化合成丁酮-1,2-丙二醇缩酮

报道了以分子筛MCM-48负载硅钨酸H4SiW12O40/MCM-48为催化剂,通过丁酮和1,2-丙二醇反应合成了丁酮-1,2-丙二醇缩酮。探讨了H4SiW12O40/MCM-48对缩酮反应的催化活性,较系统地研究了酮醇物质的量比、催化剂用量、反应时间诸因素对产品收率的影响。实验表明:H4SiW12O40/MCM-48是合成丁酮-1,2-丙二醇缩酮的良好催化剂,在n(丁酮)∶n(1,2-丙二醇)=1∶1.6,催化剂用量为反应物料总质量的0.6%,环己烷为带水剂,反应时间45 min的优化条件下,丁酮-1,2-丙二醇缩酮的收率可达91.9%。     

NiY/MCM-41催化剂的制备及催化氧化脱硫研究

采用后合成法制备复合分子筛Y/MCM-41,并以其为载体,用活性组分硝酸镍对其改性,制备Ni-Y/MCM-41催化剂,并利用XRD、BET、N2吸附-脱附对其进行表征。结果表明,复合分子筛同时具有微孔分子筛Y沸石和介孔材料MCM-41分子筛的特征。以硫质量分数为300μg/g的模拟油进行催化氧化脱硫实验,考察了Ni离子的负载量、反应温度、反应时间、催化剂用量、氧化剂用量等工艺条件对脱硫率的影响。结果表明:硝酸镍的负载量为10%,模拟油用量为20 m L,反应温度为70℃,反应时间为80 min,剂油比(催化剂与模拟油的质量比)为1∶70,V(H2O2)/V(油)=0.03时,脱硫率可达86.53%。     

Synthesis, Characterization of Ag/MCM-41 and the Catalytic Performance for Liquid-phase Oxidation of Cyclohexane

Nano-scale silver supported mesoporous molecular sieve Ag/MCM-41 was directly prepared by one-pot synthesis method. The prepared sample was characterized by XRD, TEM, and N₂ sorption. The results showed that the sample of Ag/MCM-41 had no appreciable incorporation of silver into the mesoporous matrix of MCM-41 with good crystallinity, and silver nanoparticles were dispersed inside or outside of the channels in the mesoporous host. The catalytic performance of the sample for the cyclohexane liquid-phase oxidation into cyclohexanone and cyclohexanol by oxygen in the absence of solvents without inducing agents was investigated. The 83.4% selectivity to cyclohexanol and cyclohexanone at 10.7% conversion of cyclohexane was obtained over Ag/MCM-41 catalyst at 428 K for 3 h. The turn over numbers (TONs) of Ag/MCM-41 was up to 2946. The catalytic activity of Ag/MCM-41 was also compared with Ag/TS-1 as well as Ag/Al₂O₃. The results indicated that Ag/MCM-41 showed superior activity to both Ag/TS-1 and Ag/Al₂O₃. A calcined Ag/MCM-41 was found to be an efficient catalyst for the cyclohexane oxidation into cyclohexanol and cyclohexanone using oxygen as oxidant.     

A Highly Efficient Catalyst Au/MCM-41 for Selective Oxidation Cyclohexane Using Oxygen

The liquid-phase highly efficient selective oxidation cyclohexane to cyclohexanol and cyclohexanone over Au/MCM-41 catalyst was carried out in a solvent-free system, which oxygen as the only oxidant and the reaction conditions are very moderate. The Au/MCM-41 was characterized by XRD, N₂adsorption/desorption, UV-Vis, XPS, and ICP-AES.     

Solvent-free partial oxidation of cyclohexane to KA oil over hydrotalcite-derived Cu-MgAlO mixed metal oxides

A highly efficient and stable hydrotalcite-derived Cu-MgAlO catalyst was developed for the partial oxidation of cyclohexane with molecular oxygen. The physical-chemical properties of Cu-MgAlO catalysts were studied, and the results indicated that the copper component had been successfully introduced into the hydrotalcite unit layer structure. The catalytic reaction results showed that copper as the active species could activate C-H bond and effectively promote the decomposition of cyclohexyl hydroperoxide (CHHP) to the mixture of cyclohexanol and cyclohexanone (KA oil). 8.3% of cyclohexane conversion and 82.9% of selectivity for KA oil were obtained over 9%Cu-MgAlO catalyst at 150℃ with 0.6 MPa of oxygen pressure for 2 h. Especially, its catalytic performance was still stable after five runs.     

纳米金复合催化剂制备及其低温选择催化环己烷氧化性能

采用光催化直接还原法将Au(0)负载在TiO2修饰的中孔分子筛MCM-41的孔道内外,采用XRD, N2吸附-脱附,FT-IR, TEM和EDS等手段对所制催化剂进行了表征,并考察了其在温和条件下对环己烷选择性氧化反应的催化性能. 结果表明,所制纳米金催化剂的分子筛载体仍具有较高的结晶度,金颗粒粒径在10 nm左右. 在环己烷氧化反应中,纳米金与TiO2光催化共同作用,使复合催化剂具有低温高催化活性. 在温度100℃、压力1.0 MPa及250 W紫外灯光照8 h的条件下,环己烷转化率高达3.9%,目的产物的总选择性为90.2%.     

Fe-MCM-41合成及催化氧化环己烷制备环己酮

采用浸渍法合成出的Fe-MCM-41分子筛作为催化剂,应用于环己烷催化氧化制备环己酮.以氧气为氧源,在反应压力为2.5 Mpa时,通过对温度、空气流量和空速等因素进行考察,得出在反应温度为160℃,空气流量为25 mL/min,空速条件为1.0 h-1的条件下,环己烷转化率为29.56%,环己醇的产率为9.63%,环己...     

Liquid-phase oxidation of cyclohexane using Co-P-MCM-41 catalyst

Co-P-MCM-41 catalyst was prepared by introduction of cobalt nitrate and phosphoric acid during gel-preparation for the synthesis of MCM-41. The catalyst, which was found to have very high surface area (995 m²/g), was tested for the one step liquid oxidation of cyclohexane to adipic acid using a semi-batch autoclave reactor (without addition of any promoter and solvent) at 115°C and in a flow of 5 bar of oxygen. The effect of the amount of catalyst on the induction time, catalytic conversion of cyclohexane, and selectivity to adipic acid was investigated. Depending on the amount of catalysts used in the reaction (from 0.1 to 3.0 g), an induction period from about 100 min to less than 10 min, cyclohexane conversion from 30 to 99%, and a selectivity to adipic acid from 15 to 40 %, could be achieved using Co-P-MCM-41 as the catalyst.     

氯取代基对四苯基卟啉Co~(2+)/M_n~(2+)/Cu~(2+)催化氧化环己烷反应的影响

以四苯基金属络合物(Mn2+/Co2+/Cu2+)为对比催化剂,以环己烷转化率、醇酮的选择性为指标,考察研究氯取代基对四苯基卟啉金属络合物(Mn2+/Co2+/Cu2+)催化氧化环己烷反应的影响,实验采用反应压力为1.0MPa、催化剂浓度不变,空气流量控制在0.10~0.12/(m3·h-1)之间,重点考查了反应时间、反应温度、金属卟啉种类等因素对催化氧化环己烷反应的影响。实验结果表明:(1)取代基(单氯)对四苯基金属卟啉催化氧化环己烷反应活性影响较小;取代基(单氯)对四苯基金属卟啉催化氧化环己烷反应时,目标产物--环己醇和环己酮选择性影响也较小;(2)络合三种金属中,催化活性的大小为Co2+Cu2+Mn2+,目标产物-环己醇和环己酮选择性顺序:Cu2+Mn2+Co2+,当以TCPPCu、TPPMn为催化剂时,醇酮的选择性达90%以上,当以TPPCo、TCPPCo、TPPCu、TCPPMn为催化剂时,醇酮的选择性达85%以上;(3)在所考察的6种催化剂中,较佳催化剂有TPPCo和TCPPCo,其相应的反应条件为:1TPPCo作催化剂时,反应温度150~155℃,反应时间50~60min,转化率达到8%以上,选择性达到86%以上;2TCPPCo作催化剂时,反应温度155℃,反应时间60min,转化率达9%以上,选择性为86%以上。     

Preparation of MCM-41 Supported Salen Vanadium Complex and its Catalysis for the Oxidation of Cyclohexane with H<Subscript>2</Subscript>O<Subscript>2</Subscript> as an Oxidant

A secondary amino group modified MCM-41 (mobile crystalline material number 41) was synthesized and used as a support for the immobilization of a salen oxovanadium complex via a multi-grafting method. The immobilized complex was characterized by UV–Vis spectroscopy, X-ray diffraction (XRD), N₂ adsorption and ICP analysis techniques. The immobilized complex was found to be an effective catalyst for oxidation of cyclohexane using H₂O₂ as an oxidant under mild conditions. A conversion of 45.5% of cyclohexane was obtained with a selectivity of 100% of the cyclohexanone/cyclohexanol mixture when the reaction was run at 60 °C for 12 h in acetonitrile. Decomposition of the complex, which leads to the deactivation of the catalyst, is observed and a decomposition mechanism is discussed.     

杂原子MCM-41分子筛的合成及对环己烷氧化的研究

用十六烷基三甲基溴化铵为模板剂,水玻璃为硅源,在合成过程分别加入Cr3+、Co2+、Fe3+杂原子,在150℃晶化48h,水热合成了Cr-MCM-41、Co-MCM-41、Fe-MCM-41等杂原子分子筛。考察了时间、温度、催化剂用量、过氧化氢用量及催化剂再生等因素对环己烷氧化反应的影响。最佳反应条件为:温度100℃;环己烷30mmol,Cr-MCM-41为催化剂,用量0 12g;n(H2O2)/n(C6H12)=1;反应时间16h,环己烷的转化率可达28 6%,产物的酮醇摩尔比为1 89。