基于多金属氧酸盐的介孔离子催化剂催化苯一步氧化制苯酚（英文）

苯酚是一种重要的有机化工原料,工业上主要采用合成路线长、原子利用率低、能耗高、环境污染严重的异丙苯法生产.当前,随着绿色化学的普及,H_2O_2催化苯一步氧化制苯酚受到越来越多的关注.在研究的众多催化剂中,钒取代杂多酸被认为是该反应最有效的催化剂之一.然而,纯杂多酸易溶于H_2O_2催化的苯羟基化反应体系,导致污染严重、后处理和分离困难.为了获得可回收的固体杂多酸催化剂,通常将其负载于多孔载体上,但这种方法常伴随着活性组分易溶脱,反应速率慢等缺点.因此,在H_2O_2催化苯一步氧化制苯酚体系中获得高效、可重复使用的杂多酸基固体催化剂仍然是一个挑战.采用有机单元修饰杂多酸是制备杂多酸基固体催化剂的有效方法.研究表明,有机基团的引入可以有效调控杂多酸的溶解性和氧化还原性.另一方面,催化剂中的疏水微环境也能有效促进非极性底物与催化活性中心的相互作用,提高反应速率,改善催化活性.因此,我们通过离子交换法将对二甲苯型双核咪唑离子液体阳离子与含钒杂多阴离子结合,研究制备了一种具有疏水微环境的介孔杂多酸基离子固体催化剂.采用傅里叶变换红外光谱、X射线衍射、扫描电镜、N2吸附-脱附和CHN元素分析等表征手段对催化剂进行全面分析.结果表明,该催化剂是一种具有较高比表面积的半无定形疏水有机杂多酸盐.在H_2O_2催化的苯一步氧化制苯酚反应中引导了液-固两相催化体系,在反应时间1 h,反应温度70 oC,苯酚产率可达到28.9%,与均相纯杂多酸的催化活性基本相当,且催化剂重复使用性能良好.催化剂构效关系和反应动力学研究表明,高比表面积和疏水微环境的构建加快了苯与催化活性中心的相互作用,提高了催化反应速率和产物选择性.同时,咪唑基离子液体阳离子通过分子内的电子相互作用改善了杂多阴离子的氧化还原能力,也赋予固体催化剂更高的催化活性.该研究为H_2O_2催化苯一步氧化制苯酚反应提供了一种制备简单,经济高效,可重复使用的杂多酸基固体催化剂.     

疏水性杂化分子筛的控制合成及催化应用

以乙基三乙氧基硅烷和甲基三乙氧基硅烷为有机硅源, 分别通过转动和静态干胶转化法一步合成出乙基和甲基功能化杂化分子筛并对其进行了表征. 通过对合成路线、 有机基团碳链长度、 凝胶配比等的调变, 实现了对杂化分子筛疏水性的有效调控, 合成出水接触角为124°的疏水性杂化分子筛. 以疏水性杂化分子筛为载体制备的Ru负载催化剂在催化苯酚加氢反应中表现出优异的催化性能, 这归因于疏水/亲油的催化剂表面有利于苯酚分子在催化剂表面的富集进而促进反应的进行.     

硅钼钒和硅钨钒杂多酸的制备及其在苯直接羟基化制苯酚中的活性研究

本文采用分步反应、分步酸化法制备了硅钼钒和硅钨钒杂多酸,用等离子原子发射光谱、热重分析、红外、紫外、粉末X射线对制备的化合物进行了表征。结果表明,制备所得化合物为Keggin结构的杂多酸。同时,本文还用该杂多酸作催化剂,研究了其对由苯直接氧化羟基化合成苯酚的催化活性,结果显示,在本文条件下,用所合成的杂多酸作催化剂,可获得17.2%苯酚收率和高于90%的苯酚选择性。     

锚定在杂多酸上的席夫碱锰配合物催化磷酸与等摩尔月桂醇绿色酯化反应

 将席夫碱锰配合物与硅钨酸结合制备出一种新颖的无机-有机杂化固体催化剂, 通过红外光谱和热重表征数据推测出这种催化剂的组成和结构, 并将其用于磷酸与等摩尔月桂醇酯化制备长链单烷基磷酸酯 (MAP). 结果表明, 采用 L1-Mn-SiW (L1: 双水杨醛缩-1,6-己二胺) 催化剂, 在优化的反应条件下, 酯化反应可获得 93% 的 MAP 收率和高达 98% 的 MAP 选择性. 催化剂的重复使用测试表明, 液-固多相酯化体系中该固体催化剂可方便地回收, 且具有优异的稳定性, 重复使用 6 次后催化剂活性未见下降, 结构没有变化, 是高效绿色催化剂. 该催化剂作用下的磷酸酯化是固体碱催化过程.     

杂多酸/离子液体杂化材料催化苯的高选择性羟基化

制备了V取代的磷钼酸H_3+xPMo_12-xV_xO₄₀（x=0,1,2）及1-丁基-3-甲基咪唑溴盐离子液体（[C₄mim]Br）,并采用离子交换的方法制备了系列杂化材料（[C₄mim]3+xPMo_12-xV_xO₄₀,x=0,1,2）;采用X射线衍射（XRD）、傅里叶变换红外光谱（FT-IR）、紫外-可见漫反射光谱（UV-Vis DRS）对所制备样品进行了表征;以H₂O₂为氧化剂,考察了所得样品催化苯羟基化制苯酚的活性。结果表明,和相应的离子液体及杂多酸相比,杂化材料的催化活性得到了很大的提高,尤其是催化剂[C₄mim]₅PMo₁₀V₂O₄₀,在优化后的条件下,苯的转化率可达到21%,苯酚的选择性在99%以上。而且,该催化剂具有很好的可重复使用性,连续使用五次后,苯的转化率和苯酚的选择性没有明显降低。     

超支化铬系催化剂的合成及乙烯齐聚性能研究

以正辛胺和十二胺为原料,分别制备了两种超支化PNP配体,通过引入金属铬活性位点的方法合成了具有不同烷基链长度的超支化PNP铬系催化剂.采用红外光谱(IR)、核磁共振磷谱(~(31)P-NMR)、核磁共振氢谱(~1H-NMR)、紫外光谱(UV)和质谱(MS)等表征方法证明合成催化剂的结构与理论结构预测相符.详细考察了催化剂用量、溶剂种类、反应条件以及配合物结构对乙烯齐聚性能的影响.实验结果显示,超支化PNP铬系催化剂在甲苯作溶剂,甲基铝氧烷(MAO)做助催化剂时表现出良好的催化乙烯齐聚性能,产物主要为低碳烯烃.在最佳条件下,催化活性最高可达到1.69×10~5 g·(mol Cr·h)~(-1),己烯和辛烯的选择性为43.3%以上.相同聚合条件下,其催化活性随着端基烷基链长度的增加而下降.     

有机-无机杂化材料负载钯催化苯酚氧化羰化合成碳酸二苯酯

 采用溶胶-凝胶法合成了有机-无机杂化材料(OIH),通过与PdCl2(PhCN)2反应,制备了固载化PdCl2/OIH非均相催化剂. 考察了此催化剂在苯酚直接氧化羰化合成碳酸二苯酯反应中的催化活性,并与均相PdCl2催化体系进行了比较. 结果表明,负载型催化剂的催化活性与均相体系相当. 当使用Cu2O和四氢呋喃分别作无机助剂和溶剂时,PdCl2/OIH催化剂重复使用5次后,碳酸二苯酯的产率基本保持不变,钯流失量仅为12.3%.     

醇脱氢胺化合成低级脂肪胺催化剂载体的选择

乙胺等低级脂肪胺是重要的精细化工商品.低级脂肪胺及其下游产品广泛应用于合成材料、纺织、医药、农药等行业.目前世界上生产低级脂肪胺的主要方法是低级脂肪醇气固相脱氢胺化法,催化剂为金属负载型.钴系催化剂是乙醇脱氢胺化比较适合的催化剂.本文是针对钴催化剂研制过程中选择载体的讨论.在试验中分别取几种不同的催化剂载体SiO2、Al2O3、硅铝胶(SiO2-(X)Al2O3)用于制备钴催化剂,通过评价试验证明了几种不同载体制备的钴催化剂性能差别较大,Co/SiO2型催化剂用于乙醇脱氢胺化具有很好的活性.     

奎宁-杂多酸杂化催化剂催化H2O2为氧源的苯羟基化反应

将奎宁与Keggin结构磷钼钒杂多酸结合制备出一种新颖的多相苯羟基化杂化催化剂, 采用傅里叶变换红外光谱、紫外-可见光谱、X射线衍射、扫描电镜、热重、N₂吸附-脱附和CHN元素分析等表征手段对催化剂进行了分析. 结果表明, 该催化剂是一种具有较高比表面积和孔体积的半无定形有机杂多酸盐. 在H₂O₂为氧源的苯羟基化反应中, 杂化催化剂引导了液-固两相催化体系, 表现出较高催化活性和重复使用稳定性. 催化剂中奎宁与杂多阴离子间的氢键和电子相互作用赋予了其高熔点和难溶性, 而高比表面积和因奎宁而改善的杂多阴离子的氧化还原性是其获得优异催化性能的主要原因. 这为多相苯羟基化反应提供了一种新的且制备便捷的基于多金属氧酸盐的高效催化剂.     

超支化PAMAM桥联乙烯齐聚用镍系催化剂的合成与表征

以系列直链脂肪胺为核的低代超支化聚酰胺-胺(PAMAM)和水杨醛为原料,通过席夫碱反应制备系列新型超支化PAMAM桥联水杨醛亚胺配体;以无水Ni Cl2为络合试剂,通过络合反应合成系列超支化PAMAM桥联镍催化剂,采用FT-IR和1H NMR证实合成的系列新型配体和镍系催化剂的结构与其理论结构相符.对系列超支化PAMAM桥联镍催化剂催化乙烯齐聚的性能进行了研究,结果表明,超支化PAMAM桥联镍系催化剂配体骨架烷基链长度对其催化活性和选择性影响较小,助催化剂和溶剂影响较大;倍半乙基氯化铝为助催化剂,甲苯为溶剂时,聚合活性较高,产物中C8以上的高碳产物的含量最高;其中以十四胺为核的超支化PAMAM桥联镍催化剂为主催化剂、倍半乙基氯化铝为助催化剂、甲苯为溶剂时,催化乙烯齐聚活性高达1.96×106 g/(mol·h),齐聚产物中C8以上的高碳产物含量为98.77%.     

Synthesis of Bisphenols Carrying Long Hydrocarbon Side Chains

Bisphenols containing long aliphatic hydrocarbon side chains were synthesized by the condensation of phenol with aldehyde or ketone in the presence of heteropolyacid. Their structures were characterized by IR, ^1H NMR, ^13C NMR and element analysis. The experiment results show that when heteropolyacid was used as a catalyst, these bisphenols were obtained in high selectivity and high yields.     

Alkylation of phenol with camphene in the presence of heteropolyacids supported on metal oxides

Alkylation of phenol with camphene in the presence of supported heteropolyacids is studied. The main reaction products are found to be phenyl isobornyl ether, 2-isobornylphenol and 2-isocamphylphenol, the ratio between them being determined by the nature of heteropolyacid and carrier (ZrO₂ or TiO₂).     

Selective Acetylation of Alcohols and Amines with Ethyl Acetate in the Presence of H<Subscript>6</Subscript>[PMo<Subscript>9</Subscript>V<Subscript>3</Subscript>O<Subscript>40</Subscript>] as the Catalyst

Summary. Acetylation of various alcohols and benzyl amine was tested in the presence of H₆[PMo₉V₃O₄₀], a mixed addenda heteropolyacid, in ethyl acetate under reflux condition. Phenols and anilines are not affected under the reaction conditions. Selective transestrification of alcohols can be achieved in the presence of phenol and aniline derivatives using this method.     

Triethylamine-modified Keggin heteropolyacid: a novel phase-transfer catalyst for hydroxylation of benzene with H2O2

The Keggin-structured heteropolyacid H₄PMo₁₁VO₄₀ and its triethylamine-modified derivative [(C₂H₅)₃NH]₄PMo₁₁VO₄₀ were prepared and characterized by FT-IR and UV–visible spectrometry, and elemental analysis. Direct hydroxylation of benzene to phenol by H₂O₂ over these two catalysts was then compared. The effect of the triethylamine in [(C₂H₅)₃NH]₄PMo₁₁VO₄₀ on the catalytic hydroxylation of benzene was investigated in detail. The results showed that although the triethylamine-modified catalyst is not significantly more active than the parent heteropolyacid catalyst, its reaction-controlled phase-transfer characteristics enable easy separation of the catalyst from the reaction medium, and its reuse, suggesting its potential for application to the hydroxylation of benzene to phenol with H₂O₂.     

H5PMo10V2O40/SBA-15催化剂的制备及其催化性能

以Keggin型杂多酸H5PMo10V2O40为主体,SBA-15介孔分子筛为载体,利用溶胶-凝胶法制备了不同负载量的H5PM10V2O40/SBA-15负载型催化剂,通过XRD、FTIR、TEM、H2-TPR和N2吸脱附法对样品进行了分析和表征,并将制得的负载型催化剂应用于苯氧化苯酚的反应中,研究了不同条件(温度、时间和催化剂用量等)下的催化性能.研究结果表明:H5PMo10V2O40杂多酸能均匀地分散于SBA-15孔道中且SBA-15的六方介孔结构并未发生改变:较好地解决了活性组分大量溶脱的问题;与H5PMo10V2O40杂多酸相比,H5PMo10V2O40/SBA-15催化剂在苯氧化为苯酚的反应中具有更高的转化率和更好的选择性,当反应温度为70℃,催化剂的使用量为0.25 g,反应时间为2 h和H5PMo10V2O40负载量为60%时苯酚的选择性达到了82.53%.     

Kinetics of gas phase synthesis of ethyl-tert-butyl ether (ETBE) on Wells–Dawson catalyst

Mechanism and kinetics of gas phase synthesis of ethyl-tert-butyl ether (ETBE) over Wells–Dawson heteropolyacid H₆P₂W₁₈O₆₂ in an anhydrous system have been discussed. The rates of ETBE synthesis were measured in a differential reactor for ethanol–isobutene system, far from the limitation by chemical equilibrium. In the pressure range studied, kinetic measurements show that isobutene has an enhancing effect on the reaction while ethanol has an inhibitory one.

Catalytic and sorption experiments allowed to formulate the mechanism of ETBE synthesis which assumed isobutene adsorption and oligomerization at the surface of heteropolyacid crystallites and the formation of carbocation using protons supplied from the bulk of catalyst. Kinetic equations were deduced indicating that it is the concentration of protons forming inter-anionic bonds between heteropolyacid anions which determines the catalytic activity of heteropolyacid.     

One pot production of 5-hydroxymethylfurfural with high yield from cellulose by a Brønsted-Lewis-surfactant-combined heteropolyacid catalyst

A Br?nsted-Lewis-surfactant-combined heteropolyacid (HPA) Cr[(DS)H(2)PW(12)O(40)](3) has been synthesized, and is used as a heterogeneous catalyst for the conversion of cellulose to 5-hydroxymethylfurfural in one pot within 2 h at 150 °C with 77.1% conversion and 52.7% yield. This micellar HPA catalyst shows stability and can be recycled by simple separation process.     

硅胶固载杂多酸离子液体催化剂bmim-PW12/SiO2的制备及其在酯化反应中的应用

采用溶胶-凝胶法将杂多酸功能化离子液体bmim-PW12(1)固载到硅胶上制得硅胶固载杂多酸功能化离子液体催化剂bmim-PW12/SiO2[2-x(x=5,15,25,35,50)],采用TG-DTG,FT-IR,N2低温吸附脱附,XRD和正丁胺电位滴定等方法表征2的结构、织构性能和酸性。结果表明,2-x保持了1的Keggin结构,且1被较好地固载在硅胶上;2-x具有大的比表面积和强酸性。用7%的2-35催化乙酸与正丁醇的酯化反应,收率88.5%,且2-35重复使用5次后收率仍可达到75.4%。     

New evidence on the structure of potassium salts of 12-tungstophosphoric acid, KxH3-xPW12O40

Physicochemical properties and compositions of KxH(3-x)PW12O40 salts, where 2 < or = x < or = 3, have been investigated. It has been found that freshly prepared K2HPW12O40 salt (drying at 313 K) contains particles of heteropolyacid and particles of the neutral potassium salt, the sample being in 78.6% amorphous. On aging at room temperature, the heteropolyacid spreads to form a surface layer covering the neutral potassium salt particles K3PW12O40. Heat treatment of KxH(3-x)PW12O40 salts, where 2 < or = x < 3, from 313 K to higher temperatures induces the transformation of the heteropolyacid-covering K(3) core into a well-dispersed, amorphous surface layer. On further heating of the acidic potassium salts, the surface layer decomposes between 855 and 915 K with the formation of a PW8O26-type bronze as a new phase, the K3PW12O40 salt remaining unchanged. The latter starts to decompose at 1093 K, and in the case of all samples, the process is completed at about 1183 K. Rietveld structure refinement, XPS, and 31P NMR measurements of acidic potassium salts indicate that the core of these salts is always formed by the K3PW12O40 salt, which is covered by a heteropolyacid. Comparison of lattice parameters of the K3 salt and HPW leads to the conclusion that the layer is composed of partially or completely dehydrated heteropolyacid molecules. The coverage of the core by HPW in the K2 sample was estimated to be equal to one monolayer.