乙二胺基和2,4-戊二酮官能化介孔分子筛固载钼(VI):新型的环己烯环氧化催化剂

通过对介孔分子筛HMS和MCM 41表面修饰 ,将乙二胺基和 2 ,4 戊二酮引入到介孔分子筛孔道内 ,制备出乙二胺基和戊二酮官能化介孔分子筛 .首次将烯烃环氧化均相催化剂MoO2 (acac) 2 固载到乙二胺基和戊二酮官能化介孔分子筛孔道内 ,制备出新型的、易回收、可重复使用的烯烃环氧化多相催化剂 .环己烯催化环氧化表明 ,该催化剂的催化活性与均相催化剂MoO2 (acac) 2 相当 ,选择性大于 80 %.     

乙二胺基和2，4-戊二酮官能化介孔分子筛固载钼（Ⅵ）：新型的环己烯环氧化催化剂

通过对介孔分子筛HMS和MCM-41表面修饰，将乙二胺基和2，4-戊二酮引入到介 孔分子筛孔道内，制备出乙二胺基和戊二酮官能化介孔分子筛。首次将烯烃环氧化 均相催化剂MoO_2(acac)_2固载到乙二胺基和戊二酮官能化介孔分子筛孔道内，制 备出新型的、易回收、可重复使用的烯烃环氧化多相催化剂。环已烯催化环氧化表 明，该催化剂的催化活性与均相催化剂MoO_2(acac)_2相当，选择性大于80%。     

甲基三氧化铼与双氮席夫碱原位配位及催化烯烃环氧化

以2-吡啶甲醛与苯胺及其衍生物缩合制备了3个双氮席夫碱配体,对其结构进行了表征.研究了席夫碱配体与甲基三氧化铼(MTO)在催化反应体系中的原位配位作用对MTO催化30%H2O2环氧化烯烃反应的影响.结果表明,含吸电子基羧基的双氮席夫碱配体(I)由于具有适宜的配位能力和酸性,在较低温度下与MTO配位可显著提高烯烃环氧化反应选择性,而反应速率没有明显降低.例如,以30%H2O2为氧化剂环氧化环己烯,当I与MTO的摩尔比为2,反应温度10℃时反应4 h,环己烯的转化率达到94.6%,环氧化物选择性高达99.0%.不具羧基的双氮席夫碱配体与MTO配位,尽管可以提高环氧化物的选择性,但同时却降低了MTO的催化活性.     

纳米SnO2高效催化烯烃与H2O2环氧化反应研究

构建了用于催化烯烃与过氧化氢环氧化反应的高效、 绿色催化反应体系. 首先, 通过水热合成法制备了纳米SnO₂, 并在320 ℃下煅烧. 随后, 对所有催化剂进行X射线衍射(XRD)、 紫外-可见漫反射光谱(UV-Vis)、 傅里叶变换红外光谱(FTIR)、 扫描电子显微镜(SEM)和透射电子显微镜(TEM)表征. 进一步将催化剂用于以H₂O₂水溶液为氧化剂环氧化各种官能化烯烃(包括环烯烃, 苯乙烯和直链烯烃)的反应, 以高转化率和高选择性得到了环氧化物. 在相似的反应条件下, 发现合成的纳米SnO₂-170催化剂在催化1-甲基环己烯与H₂O₂的环氧化反应中的活性最佳, 在2 h内1-甲基环己烯的转化率达到100%, 环氧化物选择性达到100%.     

双核烷基咪唑过氧磷钨酸盐相转移催化剂合成及催化烯烃环氧化性能

合成并表征了一类双核长链烷基咪唑阳离子修饰的过氧磷钨杂多酸盐催化剂[Dnmin]1.5PW4O24,考察了催化剂在过氧化氢为氧源的烯烃环氧化反应中的催化活性.研究表明,这类催化剂在反应过程中表现出相转移催化现象,并具有较高的催化活性和选择性.其中,双核十二烷基咪唑杂多酸盐催化剂[D12min]1.5PW4O24的活性最佳,其环己烯转化率和环氧环己烷选择性分别达到97.7%和96.3%.催化剂在经过简单离心分离后可重复使用,重复使用4次后环己烯转化率和环氧环己烷选择性仍可分别达到72.4%和97.2%.催化剂[D12min]1.5PW4O24在其它几种烯烃的环氧化反应中均表现出相转移催化特性,且具有较高的催化活性.     

氨基酸辅助合成高活性六配位钛物种的TS-1分子筛

TS-1分子筛是以TO4(T=Si,Ti)四面体为基本单元,通过氧桥连接而形成的具有MFI拓扑结构的微孔晶体材料,其在催化烯烃环氧化、酮类氨肟化、氧化脱硫及芳香烃羟基化等氧化反应中表现出较好的催化活性.目前,提高TS-1分子筛催化性能的方法主要包括:(1)制备纳米和多级孔TS-1分子筛,以提高其扩散传质性能;(2)提高TS-1分子筛的钛含量并抑制锐钛矿相的产生,以增加其催化活性位点.最新研究表明,相比于传统四配位钛物种(TiO4)作为催化活性中心,六配位(TiO6)钛物种在烯烃环氧化反应中具有更高的催化活性,可进一步降低反应活化能,最终实现高效催化转化.然而,TiO6物种结构中的Ti-OH组分,易导致开环反应发生,从而降低环氧化产物的选择性.因此,构筑高活性TiO6物种及调变TiO4/TiO6比例,对提高烯烃转化率及环氧产物选择性具有重要意义.当前,高活性钛物种的结构表征及其构筑已成为研究热点且仍面临挑战.本文协同采用氨基酸辅助合成策略和两步晶化方法,成功地制备出具有TiO4和TiO6物种且无锐钛矿相的多级孔TS-1分子筛.在该协同策略中,两步晶化过程有利于抑制锐钛矿相的形成,而氨基酸的引入对高活性TiO6物种的构筑具有重要作用.氨基酸分子可与钛原料形成螯合物,为TS-1分子筛晶化提供"养料",并有效平衡晶体成核与生长速率及稳定TiO6物种,最终实现制备富含TiO6物种的多级孔TS-1分子筛.相比于传统TiO4物种作为催化活性中心(1-己烯的转化率<25％,环氧化产物选择性>95％),本文所制备的TS-1分子筛(Si/Ti=36.9)因其兼具TiO4和TiO6物种,在1-己烯环氧化反应中表现出更好的催化性能(1-己烯的转化率33％,环氧化产物选择性95％).这是由于TiO4物种不会导致开环反应的发生,因此可以保证较高的环氧产物选择性,而TiO6物种经H2O2活化后,可形成具有更高活性及更小位阻效应的催化中心,极大提高了1-己烯转化率.综上,本文合成策略为构筑具有高活性钛物种及多级孔结构的钛硅分子筛提供了指导作用,为调控硅铝酸盐及硅取代磷酸铝分子筛材料活性位点的含量和分布提供了新思路.     

丙氨酸-水杨醛席夫碱锰(Ⅲ)配合物的制备及其对烯烃环氧化的催化性能

 丙氨酸与水杨醛反应生成含羧基席夫碱, 利用羧基与氨丙基三乙氧基硅烷中的氨基生成酰胺键得到三乙氧基硅官能团化的配体. 该配体与乙酸锰配位生成的配合物与正硅酸乙酯通过溶胶-凝胶方法共聚制得锚链固定的多相化催化剂. 利用FT-IR,XPS和N2吸附法对该多相化催化剂进行了表征. 与均相催化剂相比,该催化剂对环己烯环氧化反应的催化活性及选择性较高. 在环己烯为25 mmol,异丁醛为50 mmol,催化剂用量为0.01 mmol,反应温度为35 ℃,反应时间为6 h的条件下,环己烯转化率可达99.6%,环氧环己烷选择性可达88.2%. 循环使用6次后催化剂性能没有明显改变.     

后处理工艺制备多级孔Ti-BEA沸石及其环氧化催化性能

基于脱铝多级孔BEA沸石与二氯二茂钛的固相反应,开展了钛掺杂量可调的多级孔Ti-beta后处理工艺制备研究.对制备的多级孔Ti-beta样品的理化性质进行了表征,包括X射线衍射、氮气吸附脱附测试、扫描电镜、透射电镜、紫外可见吸收光谱和紫外拉曼光谱等.结果表明,多级孔BEA沸石具有较好的化学稳定性,脱铝-钛化的后处理过程未对样品多级孔结构产生明显影响. 以环己烯和十二烯的烯烃环氧化为探针反应表征了合成多级孔Ti-beta与纯相微孔Ti-beta沸石的催化性能.结果表明,在小分子环己烯的环氧化反应中,多级孔Ti-beta沸石的催化活性(转化率59.4%)与微孔Ti-beta相当(转化率57.9%);但是在较大分子十二烯的催化反应中,多级孔结构Ti-beta材料的催化性能(转化率11.1%)明显优于纯相微孔材料(转化率6.8%),且产物中环氧化物选择性更高(分别为60.3%和37.8%).     

后处理工艺制备多级孔Ti-BEA沸石及其环氧化催化性能（英文）

基于脱铝多级孔BEA沸石与二氯二茂钛的固相反应,开展了钛掺杂量可调的多级孔Ti-beta后处理工艺制备研究.对制备的多级孔Ti-beta样品的理化性质进行了表征,包括X射线衍射、氮气吸附脱附测试、扫描电镜、透射电镜、紫外可见吸收光谱和紫外拉曼光谱等.结果表明,多级孔BEA沸石具有较好的化学稳定性,脱铝-钛化的后处理过程未对样品多级孔结构产生明显影响.以环己烯和十二烯的烯烃环氧化为探针反应表征了合成多级孔Ti-beta与纯相微孔Ti-beta沸石的催化性能.结果表明,在小分子环己烯的环氧化反应中,多级孔Ti-beta沸石的催化活性(转化率59.4%)与微孔Ti-beta相当(转化率57.9%);但是在较大分子十二烯的催化反应中,多级孔结构Ti-beta材料的催化性能(转化率11.1%)明显优于纯相微孔材料(转化率6.8%),且产物中环氧化物选择性更高(分别为60.3%和37.8%).     

Ti掺杂苯基与乙基桥连的有序介孔有机硅的制备及其催化环己烯氧化反应

分别采用1,4-(双乙氧基硅烷)苯(1,4-BTEB)和1,2-三乙氧基硅基乙烷(1,2-BTESE)作为有机硅源,正硅酸乙酯(TEOS)为无机硅源,钛酸四丁酯(TBOT)为钛源,以Pluronic EO20PO70EO20(P123)为模板剂在酸性环境下水热合成制备了Ti掺杂的有机-无机有序介孔有机硅材料Ti-SBA-15-ben和Ti-SBA-15-et.同时,在合成过程中加入H2O2作为配合剂调节钛源水解速度,制备得到Ti-SBA-15-ben-H和Ti-SBA-15-et-H.采用FT-IR、DR UV-Vis、N2物理吸附、XRD、TG-DSC、TEM等方法对制备的样品进行了表征.结果表明:合成过程中加入H2O2制备的苯基桥连有机硅杂化材料具有较好的疏水性能,其骨架中活性4价位钛含量高,结构有序性最好.在以叔丁基过氧化氢(TBHP)为氧源的环己烯氧化反应中对制备的催化材料进行了对比评价,结果表明:Ti-SBA-15-ben-H表现出最高的催化活性,其催化的反应以环氧化产物为主,环己烯的转化率为26.9%,环氧选择性为32.8%,T i-SBA-15-et催化的反应以烯丙位氧化产物2-环己烯-1-酮为主,环己烯的转化率为8.5%,2-环己烯-1-酮选择性为41.2%.     

双氮席夫碱配体对甲基三氧化铼催化烯烃环氧化反应的影响

 利用 2-吡啶甲醛、6-甲基-2-吡啶甲醛或 6-异丙基-2-吡啶甲醛与对甲基苯胺缩合制得双氮席夫碱配体, 考察了席夫碱配体以及溶剂和温度对甲基三氧化铼 (MTO) 催化不同结构烯烃环氧化反应的影响. 结果表明, 这些席夫碱配体与 MTO 构成的催化剂体系在甲醇溶剂中的催化性能最好, 双氮配体能显著提高环氧化反应的选择性. 当以甲醇为溶剂, 环己烯为底物, 在 –10 oC 反应 12 h 时, 环己烯转化率和环氧化物选择性均可达 100%. 席夫碱的配位能力越强, 越有利于提高环氧化物选择性, 而其配位能力取决于吡啶环中 6-位取代基的电子和立体结构. 给电子能力较强和空间位阻较小的烷基对应的配体的配位能力较强.     

Preparation,characterization, and catalytic performance of Ta-HMS mesoporous molecular sieve

Various Ta-HMS (hexagonal mesoporous silica) samples with different Ta content were hydrothermally prepared and characterized by XRD, N₂-adsorption, ICP-AES, FTIR, and UV–Vis spectroscopy. The catalytic performance of the samples was also evaluated in the epoxidation of cyclohexene with cumene hydroperoxide as oxidant. The regularity of mesoporous structure decreases while more extraframe Ta ions are formed with increasing the Ta content. Ta-HMS with Ta/Si ratio of 0.015 shows the highest conversion and selectivity in the studied epoxidation reaction. The catalyst can be used for three times without significant activity loss.     

Preparation, characterization, and catalytic performance of a novel methyl-rich Ti-HMS mesoporous molecular sieve with high hydrophobicity

A novel methyl-rich Ti-containing hexagonal mesoporous silica (Ti-HMS) molecular sieve with high hydrophobicity has been prepared by a two-step method involving co-condensation followed by vapor-phase methyl grafting. The sample was characterized by XRD, N₂ adsorption, FTIR, UV-visible and ²⁹Si NMR spectroscopies, TG, ICP-AES, and hydrophilicity measurements, and its catalytic performance was evaluated using the epoxidation of cyclohexene as a probe reaction. The Ti-HMS material retains a typical mesoporous structure and compared with a co-condensed Ti-HMS prepared in a one-step method possesses more methyl groups and higher hydrophobicity, and also exhibits better catalytic activity and selectivity.     

Cis-dioxo-Mo(VI) salophen complex supported on Fe<Subscript>3</Subscript>O<Subscript>4</Subscript>@SiO<Subscript>2</Subscript> nanoparticles as an efficient magnetically separable and reusable nanocatalyst for selective epoxidation of olefins

In this work, paramagnetic Fe₃O₄/SiO₂ nanoparticles were synthesized, characterized and functionalized with dioxo-Mo(VI) tetradentate Schiff base complex and characterized using IR spectroscopy, X-ray powder diffraction spectroscopy, scanning electron microscopy, transmission electron microscopy, vibrating sample magnetometry, diffuse reflectance spectroscopy and atomic absorption spectroscopy. Catalyst was used for the selective epoxidation of cyclooctene, cyclohexene, styrene, indene, α-pinene, 1-hepten, 1-octene, 1-dodecen and trans-stilbene using tert-butyl hydroperoxide as oxidant in 1,2-dichloroethane. This catalyst is efficient for oxidation of cyclooctene with a 100% selectivity for epoxidation with 100% conversion in 1 h. After the reaction, the magnetic nanocatalyst was easily separated by simply applying an external magnetic field and was used at least five successive times without significant decrease in conversion.

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Catalytic Performance of Amorphous Ti/SiO2 in the Gas-Phase Epoxidation of Propylene with H2O2

The epoxidation of propylene with dilute H₂O₂ aqueous solution over titanium silicalite-1 (TS-1) zeolite catalyst is a green chemical reaction for propylene oxide (PO) production. Carrying out the reaction in gas-phase can get rid of problems caused by using methanol solvent. This paper reports an attempt of using non-zeolite catalyst for the gas-phase epoxidation. Amorphous Ti/SiO₂, obtained by grafting amorphous SiO₂ with TCl₄ in ethanol solvent in a chemical liquid-phase deposition (CLD) process, has been used as the catalyst. Results show that the CLD Ti/SiO₂ with appropriate Si/Ti molar ratio is an active catalyst for gas-phase epoxidation, achieving 9.8 % propylene conversion and 66.9 % PO selectivity with 40.3 % H₂O₂ utilization, which indicates that this amorphous Ti/SiO₂ catalyst deserves extensive studies in the future.     

Catalytic activities of polymer‐supported metal complexes in oxidation of phenol and epoxidation of cyclohexene

The metal complexes of N, N′‐bis (o‐hydroxy acetophenone) propylene diamine (HPPn) Schiff base were supported on cross‐linked polystyrene beads. The complexation of iron(III), copper(II), and zinc(II) ions on polymer‐anchored HPPn Schiff base was 83.4, 85.7, and 84.5 wt%, respectively, whereas the complexation of these metal ions on unsupported HPPn Schiff base was 82.3, 84.5, and 83.9 wt%. The iron(III) complexes of HPPn Schiff base were octahedral in geometry, whereas copper(II) and zinc(II) ions complexes were square planar and tetrahedral. Complexation of metal ions increased the thermal stability of HPPn Schiff base. Catalytic activity of metal complexes was tested by studying the oxidation of phenol and epoxidation of cyclohexene in the presence of hydrogen peroxide. The polymer‐supported HPPn Schiff base complexes of iron(III) ions showed 73.0 wt% conversion of phenol and 90.6 wt% conversion of cyclohexene at a molar ratio of 1:1:1 of substrate to catalyst and hydrogen peroxide, but unsupported complexes of iron(III) ions showed 63.8 wt% conversion for phenol and 83.2 wt% conversion for cyclohexene. The product selectivity for catechol (CTL) and epoxy cyclohexane (ECH) was 93.1 and 98.3 wt%, respectively with supported HPPn Schiff base complexes of iron(III) ions but was lower with HPPn Schiff base complexes of copper(II) and zinc(II) ions. Activation energy for the epoxidation of cyclohexene and phenol conversion with unsupported HPPn Schiff base complexes of iron(III) ions was 16.6 kJ mol^?1 and 21.2 kJ mol^?1, respectively, but was lower with supported complexes of iron(III) ions. Copyright © 2007 John Wiley & Sons, Ltd.     

Synthesis of ceria nanoparticles for the catalytic activity of cyclohexene epoxidation and selective detection of nitrite

Based on a few noteworthy features, cerium oxide nanoparticles have gained significance in nanotechnology. The effective microwave combustion method (MCM) and the conventional sol–gel (CRSGM) technologies are used in this study to successfully generate the crystalline CeO₂ nanoparticles (NPs). Additionally, using a variety of spectroscopic and analytical methods, the synthesized CeO₂ NPs are examined to assess to understand their structure and morphology. The XRD patterns of CeO₂ NPs show that the structure exhibits a face-centered cubic lattice. Then, with demonstrated good conversion and selectivity, the impact of the epoxidation reaction of cyclohexene was examined. Finally, it can be said that using CeO₂ nanoparticles is an efficient strategy to increase the catalytic activity toward the epoxidation reaction of cyclohexene. In the presence of acetonitrile as a solvent and H₂O₂ as an oxidant, the catalyst samples utilized in the cyclohexene epoxidation reaction were examined. In this study, the CeO₂ catalyst outperformed all other catalysts in terms of cyclohexene maximal conversion and selectivity. After six prolonged cycles, the conversion of cyclohexene oxidation using CeO₂ NPs shows reasonable recyclability and conversion efficiency, making it the best catalyst for an industrial production application.Additionally, the upgraded CeO₂ nanoparticle electrode for nitrite detection has a linear concentration range (0.02–1200 M), a low detection limit (0.22 M), and a higher sensitivity (1.735 A M⁻¹ cm⁻²). CeO₂ NPs, on the other hand, have a quick response time, excellent sensitivity, and high selectivity. Additionally, the manufactured electrode is used to find nitrite in various water samples. Finally, it can be said that using CeO₂ NPs is an efficient strategy to increase the catalytic activity toward cyclohexene oxidation and nitrite.     

Heterogeneous Green Catalyst for Oxidation of Cyclohexene and Cyclooctene with Hydrogen Peroxide in the Presence of Host (Nanocavity of Y‐zeolite)/Guest (N4‐Cu(II) Schiff Base Complex) Nanocomposite Material

Copper(II) complex of a Schiff base ligand derived from pyrrolcarbaldehyde and o‐phenylenediamine (H₂L) has been synthesized and encapsulated in Y‐zeolite matrix. The hybrid material has been characterized by elemental analysis, IR and UV‐Vis spectroscopic studies as well as X‐ray diffraction (XRD) pattern. The encapsulated copper(II) catalyst is an active catalyst for the oxidation of cyclooctene and cyclohexene using H₂O₂ as oxidant. Under the optimized reaction conditions 81% conversion of cyclohexene with 65% selectivity for 2‐cyclohexenone formation and 87% conversion of cyclooctene with 46% selectivity for epoxide formation were obtained.