硅钼钒和硅钨钒杂多酸催化过氧化氢直接氧化苯制苯酚的活性研究

以自制的两种Keggin型杂多酸,硅钼钒杂多酸和硅钨钒杂多酸作催化剂,冰醋酸作溶剂,过氧化氢作氧化剂,研究了由苯直接羟基化制苯酚的催化活性,发现对于所研究的体系,即苯为0.02mol,过氧化氢为0.16mol,冰醋酸为0.24mol,当杂多酸的用量为0.10~0.15mmol、反应温度323K、反应时间80min时,硅钼钒和硅钨钒上苯酚的收率分别可达17.2%和4.3%,选择性达90.3%和87.4%.     

钒钼磷杂多酸催化苯直接羟化为苯酚的动力学研究

以钒钼磷杂多酸作为催化剂,用紫外可见分光光度法研究了过氧化氢直接将苯氧化羟基化为苯酚反应的动力学行为。结果表明,该氧化羟化反应速率对底物苯、氧化剂和催化剂都是一级反应,反应的活化能为57.73kJ.mol-1。本文推测了杂多酸配合物催化苯氧化羟化为苯酚反应的过程,建立了该反应动力学数学模型,模型很好地解释了实验结果。     

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。     

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.     

Keggin型磷钼钒季铵盐催化氧化苯制苯酚反应研究

采用分步反应、分步酸化法制备了磷钼钒缺位型杂多酸,用（C4H9）4N^＋（以下简写为Bu4N^＋）阳离子取代杂多酸中H^＋作为反荷离子合成了杂多季铵盐（用于苯氧化制苯酚反应）．FT-IR分析反应前后催化剂结构的变化．以苯为原料,乙酸为溶剂,30％H2O2作氧化剂,系统考察了催化剂类型、催化剂用量、氧化剂用量、反应时间及温度对反应的影响．实验结果表明,56．4mmol苯在（Bu4N）5PMo10V2O40用量0．25mmol,30％H2O2用量10mL,溶剂乙酸10mL,70℃条件下回流反应6h,苯酚收率可达到27．9％．     

用于苯与分子氧羟基化制苯酚的长链脂肪胺修饰的杂多酸催化剂

 将十二胺或十八胺与磷钼钒杂多酸结合, 制备了有机-无机杂化催化剂, 并在高压釜中考察了它们在苯与分子氧羟基化制苯酚反应中的催化性能. 结果表明, 当十二胺与杂多酸的摩尔比为 4:1 时, 所制备的杂化催化剂上苯酚产率为 11.5%, 大大高于纯杂多酸催化剂上的 3.9%. 结合长链脂肪胺与杂多酸之间的相互作用, 以及杂多酸的“假液相”特性, 初步讨论了长链脂肪胺的促进作用.     

纳米钼钒砷杂多酸盐催化苯羟化合成苯酚的研究

过氧化氢作为一种清洁氧化剂,在苯的直接羟化的研究中受到重视。催化剂主要有含钛催化剂系列、含铁催化剂系列和含铜催化剂系列、含钒催化剂系列和其它杂原子催化剂。杂多化合物是一类酸性和氧化性较强的双功能催化剂,但由于受其低比表面积的限制,导致杂多化合物固有的高催化活性在苯的过氧化氢羟化反应中难以充分发挥。本文对所制得的4种过渡金属钼钒砷杂多酸盐纳米催化剂应用于苯的过氧化氢直接羟化合成苯酚的反应,取得了苯酚收率〉50％,选择性〉98％的结果。     

V-AlPO5分子筛催化苯直接羟基化制苯酚

采用水热法合成了V-AlPO5分子筛催化剂,通过XRD表征确定其具有AlPO-5微孔分子筛的晶体结构。不同合成条件对V-AlPO5分子筛的催化活性有一定影响,优化合成条件下制备的V-AlPO5分子筛,在以过氧化氢为氧化剂的苯羟基化制苯酚反应中表现出较佳的催化活性。反应温度55 ℃,乙腈6 mL,苯10 mmol,质量分数35%过氧化氢15 mmol,氧化剂用量0.2 g,共还原剂抗坏血酸0.2 g,反应24 h,苯酚收率可达16.1%,选择性为86.8%。     

反应控制相转移催化剂K3PV4O24催化苯合成苯酚

 设计了一种反应控制相转移催化剂K3PV4O24,用于催化以过氧化氢为氧化剂的苯氧化制苯酚反应. 此催化剂既可象均相催化剂那样进行催化反应,又可象多相催化剂那样进行回收利用,从而解决了均相催化剂难回收的问题. 在反应体系中,红色的钒磷杂多酸盐可溶于溶剂中; 当过氧化氢消耗尽时,红色的钒磷杂多酸盐被还原成蓝色的钒磷杂多蓝并以沉淀形式从溶液中析出,从而可方便地回收利用. 苯氧化反应得到的主要产物为苯酚和水,副产物为氧. 在313 K下,苯的转化率可达到48%,苯酚的选择性可达到99%以上.     

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%.     

Hydroxylation of benzene in the system vanadium(V)-hydrogen peroxide-acetic acid

Hydroxylation of benzene in acetic acid at 323 K was studied in the presence of a sodium orthovanadate catalyst. With hydrogen peroxide as aqueous solution, the yield of phenol was 12–14%. With hydrogen peroxide generated from dry sodium peroxide, the yield of phenol could be improved to 21–23%. The apparent decomposition rate constants of hydrogen peroxide in acetic acid are presented.     

Surface characterization and catalytic evaluation of manganese nodule leached residue toward oxidation of benzene to phenol

Water washed manganese nodule leached residue (WMNLR) calcined at different temperatures was characterized by XRD, FTIR, TG-DTA, surface area, surface oxygen, and surface acid sites. Surface area, surface oxygen, surface hydroxyl group, and surface acid sites increase up to 400 degrees C and then decrease with further rise in calcination temperature up to 700 degrees C. The catalytic activity of the calcined samples was tested for single-step oxidation of benzene to phenol using hydrogen peroxide as the oxidant and acetic acid as the solvent at room temperature. The influence of various reaction parameters such as solvent, concentration of solvent, oxidant amount, time, temperature, and catalyst amount was studied to optimize the reaction conditions. WMNLR calcined at 400 degrees C showed the highest catalytic activity towards oxidation of benzene with 12.7% conversion and 98% selectivity.     

Dawson结构钼钒磷杂多化合物催化乙苯选择氧化的活性研究

合成了系列Ｄａｗｓｏｎ结构钼钒杂多化合物，并将其用于 苯的过氧化氢选择氧化研究，实验发现，对于该类反应，其最佳的工艺条件为：乙苯２．５ｍｍｏｌ，催化剂０．０２ｍｍｏｌ，溶剂１０ｍＬ、３０％Ｈ２Ｏ２２．５ｍｍｏｌ，乙酸为该类最佳溶剂，而在与之性质相近的甲酸中则活性极低，即该反应过程与过氧酸的存在无关，讨论了反应过程中催化剂的状态及活性中间体，并运用ＵＶ－Ｖｉｓ、ＥＳＲ等手段进行了表征，实验结果有最佳     

Phenol synthesis by liquid-phase oxidation of benzene with molecular oxygen over iron-heteropoly acid

The phenol synthesis by liquid-phase oxidation of benzene with molecular oxygen over iron-heteropoly acid (HPA) system was studied. When iron salts were used with H₃PW₁₂O₄₀, the highest activity was obtained. Spectroscopic studies showed that the state of the iron ion was changed after interaction with heteropoly acid (HPA) while the Keggin structure of HPA remained. The acidic nature of HPA activated benzene to form cationic species. Insoluble iron ion-exchanged heteropoly acid was obtained by partial ion exchange method, which also showed high activity on oxidation of benzene with molecular oxygen. The effects of reaction conditions were studied and the mechanism of deactivation was discussed. For the regeneration of catalytic activity, the addition of -ascorbic acid as a reducing agent was suggested.     

过氧化氢直接氧化苯制备苯酚的多相催化研究进展*

作为一种绿色、洁净的氧化剂,使用过氧化氢直接氧化苯来制备苯酚的过程极具吸引力。综述了分子筛、碳基材料、金属氧化物、金属有机框架等多相催化剂在氧化苯制备苯酚反应中的应用,主要讨论了催化剂的合成路线、反应机理和催化性能,希望能为新的多相催化体系的合理设计提供有益的视角。     

Transition metal substituted polyoxometalates and their application in the direct hydroxylation of benzene to phenol with hydrogen peroxide

A series of transition metal substituted polyoxometalates with a Keggin structure were prepared and utilized for the hydroxylation of benzene to phenol. Among the compounds tested, [(CH₃)₄N]₄PMo₁₁VO₄₀ exhibits the highest phenol yield (13.0%) and selectivity (90.6%) in acetic acid/acetonitrile. Vanadium peroxo is the active site of the reaction, and ammonium also plays an important role. The influence of various reaction parameters, such as solvent, reaction time, reaction temperature, and amount of hydrogen peroxide used were investigated to obtain the optimal reaction conditions.     

Direct, copper-catalyzed oxidation of aromatic C-H bonds with hydrogen peroxide under acid-free conditions

The direct oxidation of benzene into phenol using hydrogen peroxide has been achieved in the absence of any acid with Tp(x)Cu(NCMe) complexes as the catalysts. In the case of anthracenes as the substrates, valuable anthraquinones have been quantitatively obtained in the same manner.     

Pyridine-H_5PMo_(10)V_2O_(40) hybrid catalysts for liquid-phase hydroxylation of benzene to phenol with molecular oxygen

Pyridine(Py)-modified Keggin-type vanadium-substituted heteropoly acids(PynPMo10V2O40,n=1 to 5) were prepared by a precipitation method as organic/inorganic hybrid catalysts for direct hydroxylation of benzene to phenol in a pressured batch reactor and their structures were detected by FT-IR.Among various catalysts,Py3PMo10V2O40 exhibits the highest catalytic activity(yield of phenol,11.5%),without observing the formation of catechol,hydroquinone and benzoquinone in the reaction with 80 vol% aqueous acetic ...     

Oxidation of benzene with hydrogen peroxide catalyzed with ferrocene in the presence of pyrazine carboxylic acid

It is found that ferrocene in the presence of small amounts of pyrazine carboxylic acid (PCA) effectively catalyzes the oxidation of benzene to phenol with hydrogen peroxide. Two main differences upon the oxidation of two different substrates, i.e., cyclohexane and benzene, with the same H₂O₂-ferrocene-PCA catalytic system are revealed: the rates of benzene oxidation and hydrogen peroxide decomposition are several times lower than the rate of cyclohexane oxidation at close concentrations of both substrates, and the rate constant ratios for the reactions of oxidizing particles with benzene and acetonitrile are significantly lower than would be expected for reactions involving free hydroxyl radicals. The overall rate of hydrogen peroxide decomposition, including both the catalase and oxidase routes, is lower in the presence of benzene than in the presence of cyclohexane. It is suggested on the grounds of these data that a catalytically active particle different from the one generated in the absence of benzene is formed in the presence of benzene. This particle catalyzes hydrogen peroxide decomposition less efficiently than the initial complex and generates a dissimilar oxidizing particle that exhibits higher selectivity. It is shown that reactivity of the system at higher concentrations of benzene differs from that of an initial system not containing an aromatic component with the capability of π-coordination with metal ions.