苯乙烯绿色氧化合成苯甲酸的机理研究

本文报道了用GC-MS跟踪了双氧水氧化苯乙烯为苯甲酸的全过程,研究结果发现4种主要物质苯乙烯、1-苯基邻二醇、羟基苯乙酮及苯甲酸含量随反应时间的变化关系,从而提出了其主要氧化机理可能为:苯乙烯首先经过环氧化反应,水解生成1-苯基邻二醇,然后1-苯基邻二醇氧化为羟基苯乙酮,羟基苯乙酮最后氧化为苯甲酸。     

双氧水氧化苯乙烯制苯甲酸的机理研究

在苯乙烯100 mmol,n(钨酸钠)∶n(草酸)∶n(苯乙烯)∶n(30%H2O2)=2.0∶3.2∶100.0∶440.0,92℃的反应条件下,用GC-MS和GC-IR跟踪分析了反应物和反应产物。根据其含量随反应时间的变化关系,提出了苯乙烯氧化为苯甲酸可能经过两条途径的反应机理。     

相转移催化氧化合成氯代苯甲酸

研究了以季铵盐A-1作催化剂,KMnO4作氧化剂,催化氧化邻、对位氯代甲苯合成邻、对位氯代苯甲酸的反应。优化反应条件为：氯代甲苯50mmol,n(氯代甲苯)：n(KMnO4)：n(A-1)：n(H2O)=1．00：2．60：0．05：300,反应温度93℃,反应时间2．5h,pH=7。邻、对位氯代苯甲酸的产率分别为76．4％,76．9％。     

邻苯二酚衍生物与稀土元素配位反应的研究(V)——3,4-二羟基苯甲酸与铈(Ⅲ)的配位与转型反应

研究了稀土元素铈(Ⅲ)离子与3,4-二羟基苯甲酸(H3L)在水溶液体系中生成羧基配位化合物的条件,表征其组成为Ce(H2L)2(OH)·3H2O,并研究了该配合物在一定条件下,铈离子由羧基配位反应变为由两八邻酚羟基配位的配合物[Ce(HL)n]的转型反应及氧化成铈(Ⅳ)配合物的反应.     

麦秆水解-氧化-水解法制取草酸新工艺

研究了以麦秆为原料用水解-氧化-水解法制取草酸的工艺方法。最佳反应条件：麦秆用量50g,硫酸浓度70％,物料浸泡时间≥3h,m(硝酸)：m(麦秆)=2．1：1．0;氧化催化剂V2O5-FeCl3[n(V2O5):n(FeCl3)=1：1]用量0．1g,氧化-水解反应时间5h,反应温度65℃～70℃,草酸二水合物收率75．5％。     

吲唑类化合物合成新方法的研究（Ⅰ）

本文研究了2,6-二烷氧基苯乙酮腙在多聚磷酸(PPA)存在下受热脱去一分子醇环化生成3-甲基-4-烷氧基吲唑的合成反应.并研究了水杨醛、邻甲氧基苯甲醛、2,4-二羟基苯甲醛以及邻羟基苯乙酮、2-羟基-3,5-二甲基苯乙酮腙在PPA存在下的受热反应过程.     

Friedlander反应合成2-(2-羟基苯基)-6,7-亚甲二氧基喹啉及其衍生物

以6-氨基胡椒醛为原料,与邻羟基苯乙酮(2a),4-氯-2-羟基苯乙酮(2b)发生Friedlander缩合反应,得到新的喹啉衍生物2-(2-羟基苯基)-6,7-亚甲二氧基喹啉(3a)和2-(5-氯-2-羟基苯基)-6,7-亚甲二氧基喹啉(3b),新的喹啉衍生物3a～3b分别经IR红外光谱,1H NMR核磁共振谱,MS质谱,元素分析予以证实.     

氧化偶联反应和酸催化反应制备活性买麻藤醇二聚体衍生物

以天然得到的买麻藤醇为原料,以FeCl3 6H2O为氧化剂进行氧化偶联反应和酸催化二聚反应,获得了2个新的买麻藤醇二聚体及一个新的苯基萘衍生物:4-[1-(2,6-二羟基苯基)-2-(3,5-二羟基苯基)乙基]-2-[(1E)-2-(3,5-二羟基苯基)乙烯基]-1,3-苯二醇(1),2-[1-(2,6-二羟基苯基)-2-(3,5-二羟基苯基)乙基]-5-[(1E)-2-(2,6-二羟基苯基)乙烯基]-1,3-苯二醇(2)和4-(6,8-二甲氧基-2-萘基)-1,3-苯二醇(3).应用波谱分析的方法确定了它们的结构,并分别讨论了它们可能的形成机理.其中,化合物1和2首次为人工合成的二苯乙烯链状二聚体.活性测试结果表明,化合物1,2和3显示有较强的抗氧化活性,其IC50值分别为6.29×10-9,4.19×10-6和2.96×10-5mol L-1;化合物2还显示有较强的抗炎活性.     

酸性体系V催化木质素β-O-4模型物C—C键高选择性切断

研究了酸性体系下NH_4VO_3催化木质素模型物2-(苯氧基)-1-苯乙酮(1a)的C—C键氧化切断过程.通过优选反应溶剂,在温和条件下(100℃,101 kPaO_2)于DMSO-HOAc(V∶V=3∶1)溶剂中高选择性地得到了苯甲酸和苯酚(产率分别为82.1%和88.1%),并通过对反应过程的监测和催化剂的研究提出了该反应可能的反应路径.反应过程存在两条可能的途径,一是1a先发生C—O键断裂生成苯酚和2-羟基苯乙酮,再催化2-羟基苯乙酮C—C键氧化断裂生成苯甲酸;二是1a直接发生C—C键氧化断裂生成苯甲酸和苯酚.同时,催化剂表征结果表明,+5价钒氧离子是催化活性物种.钒催化剂在反应过程中通过+4和+5价循环完成催化过程.     

3,3′-偶氮-二(6-羟基苯甲酸)镉和钴的配合物:[Cd(OSA)(Phen)(H_2O)]_n和[Co(OSA)(Phen)(H_2O)]_n的合成、表征及晶体结构(英文)

利用药物奥沙拉秦钠,邻菲罗啉与Cd(ClO4)2·6H2O或Co(NO3)2·6H2O水热反应分别得到其配合物的晶体[Cd(OSA)(Phen)(H2O)]n(1)(OSA=3,3′-偶氮-二(6-羟基苯甲酸))和[Co(OSA)(Phen)(H2O)]n(2)。单晶结构分析表明两化合物均为一维链状聚合结构,两者的晶体的空间群皆为C2/c。两化合物中,中心金属的配位几何构型均为五配位的五角双锥。3,3′-偶氮-二(6-羟基苯甲酸)通过羧基桥连金属离子形成一维链状聚合物结构。     

用双氧水绿色氧化环己酮合成己二酸的研究

以30%的双氧水为氧化剂, 钨酸钠与含N或O的双齿有机配体(草酸)形成的络合物为催化剂, 在无有机溶剂、无相转移剂的条件下, 研究了环己酮氧化制己二酸的反应. 研究结果表明, 用廉价的草酸为配体, 最佳反应条件为钨酸钠∶草酸∶环己酮∶30%的双氧水的物质的量比为2.0∶3.3∶100∶350, 在92 ℃下反应12 h, 可制得80.6%的己二酸; 用GC-MS跟踪了氧化过程中三种主要物质环己酮、己内酯及己二酸含量随反应时间的变化关系, 提出了其主要氧化机理为环己酮首先经Beayer-Villiger氧化反应生成己内酯, 己内酯进一步氧化成己二酸.     

环己酮绿色氧化合成己二酸质谱分析

己二酸是合成尼龙-66的主要原料,同时在低温润滑油、合成纤维、油漆、聚亚胺酯树脂及食品添加剂的制备等方面也有重要用途,目前己二酸的世界年产量估计已达220万吨。工业上已二酸的生产是以环己烷经两步氧化合成,第一步为环己烷在金属离子催化下用氧气氧化为环己醇、环己酮,第二步用浓HNO3氧化环己醇、环己酮制得己二酸。在第二步氧化时由于用了浓HNO3故产生大量的CO、NOx、N2O等有毒气体,其中N2O是比CO2还强310倍的温室气体。在当今普遍提倡绿色化学的时代,如何减少化工生产对环境的污染是当前化学工作者首要解决的任务。过氧化氢是一种理想的清洁氧化剂,其反应的唯一预期副产物是水,反应后处理容易,同时过氧化氢的价格相对低廉,氧化成本低。为此,许多化学工作者对环己酮绿色氧化制剂己二酸已有研究。但环己酮氧化为己二酸的反应产物的研究未见报道,本文报道环己酮氧化为己二酸的12种产物。     

NaHSO4·H2O催化合成苯甲酸甲酯

以 Na HSO4 · H2 O催化苯甲酸与甲醇的酯化反应 ,合成了苯甲酸甲酯。研究结果表明 ,Na HSO4 · H2 O具有较高的催化活性。考察了苯甲酸 /甲醇摩尔比、催化剂用量及反应时间对酯产率的影响。在优化反应条件 [n(苯甲酸 )∶n(甲醇 )∶n( Na HSO4 ·H2 O) =1∶ 2∶ 0 .2 9,回流8h]下 ,苯甲酸甲酯产率达 85.3 %。     

气固相法合成的Ti-ZSM-5催化剂上苯乙烯氧化反应的宏观动力学

 采用TiCl4气固相同晶取代法制得的Ti－ZSM－5作催化剂,对H2O2氧化苯乙烯反应的宏观动力学进行了研究,考察了催化剂、苯乙烯和H2O2用量及反应温度对苯乙烯氧化反应速率的影响．结果表明,催化剂Ti－ZSM－5和底物苯乙烯对苯乙烯氧化反应速率的贡献均为一级,而H2O2为1／2级;苯乙烯氧化反应的表观活化能Ea＝48．14kJ／mol．当以丙酮为溶剂,在n（PhCH∶CH2）／n（H2O2）＝7．91,催化剂用量为20g／L,反应温度为343K的条件下,反应360min时,苯乙醛选择性和H2O2利用率分别可达91．9％和88．6％．     

Polymer supported vanadium and molybdenum complexes as potential catalysts for the oxidation and oxidative bromination of organic substrates

The Schiff base (H2fsal-ohyba) derived from 3-formylsalicylic acid and o-hydroxybenzylamine has been covalently bonded to chloromethylated polystyrene cross-linked with 5% divinylbenzene (abbreviated as PS-H(2)fsal-ohyba, I). Treatment of [VO(acac)2] with PS-H2fsal-ohyba in dimethylformamide (DMF) gave the oxovanadium(iv) complex PS-[VO(fsal-ohyba).DMF] (1). Complex 1 can be oxidized into the dioxovanadium(v) species, PS-K[VO2(fsal-ohyba)] (2) on aerial oxidation in the presence of KOH or into the oxoperoxo species, PS-K[VO(O2)(fsal-ohyba)] (3) in the presence of H2O2 and KOH in DMF suspension. Similarly, PS-[MoO(2)(fsal-ohyba).DMF] (4) has been isolated by the reaction of [MoO2(acac)2] with PS-H2fsal-ohyba. All these complexes have been characterised by various techniques. These complexes catalyse the oxidation of styrene, ethylbenzene and phenol efficiently. Styrene gives five reaction products namely styrene oxide, benzaldehyde, 1-phenylethane-1,2-diol, benzoic acid and phenylacetaldehyde, while ethylbenzene gives benzaldehyde, phenyl acetic acid, styrene and 1-phenylethane-1,2-diol. The oxidation products of phenol are catechol and p-hydroquinone. These catalysts are also able to catalyse the oxidative bromination of salicylaldehyde to 5-bromosalicylaldehyde with ca. 80% selectively in the presence of aqueous 30% H2O2/KBr, a reaction similar to that exhibited by vanadate-dependent haloperoxidases. Their corresponding neat complexes have also been prepared and their catalytic activities have been compared.     

碳酸氢钠活化过氧化氢对烯烃的环氧化

研究了碳酸氢钠活化H<,2>O<,2>(BAP)体系对苯乙烯和不饱和脂肪酸甲酯的环氧化.分别考察了碳酸氢钠、表面活性剂、加料方式、反应时间、H<,2>O<,2>用量和反应温度对BAP体系H<,2>O<,2>分解和烯烃环氧化的影响.在n(苯乙烯):n(H<,2>O<,2>):n(NaHCO<,3>)=1:10:0.25,...     

Pathway of oxygen incorporation from O2 in TiO2 photocatalytic hydroxylation of aromatics: oxygen isotope labeling studies

The hydroxylation process is the primary, and even the rate-determining step of the photocatalytic degradation of aromatic compounds. To make clear the hydroxylation pathway of aromatics, the TiO(2) photocatalytic hydroxylation of several model substrates, such as benzoic acid, benzene, nitrobenzene, and benzonitrile, has been studied by an oxygen-isotope-labeling method, which can definitively assign the origin of the O atoms (from oxidant O(2) or solvent H(2)O) in the hydroxyl groups of the hydroxylated products. It is found that the oxygen source of the hydroxylated products depends markedly on the reaction conditions. The percentage of the products with O(2)-derived hydroxyl O atoms increases with the irradiation time, while it decreases with the increase of substrate concentration. More intriguingly, when photogenerated valence-band holes (h(vb)(+)) are removed, nearly all the O atoms (>97?%) in the hydroxyl groups of the hydroxylated products of benzoic acid come from O(2), whereas the scavenging of conduction-band electrons (e(cb)(-)) makes almost all the hydroxyl O atoms (>95?%) originate from solvent H(2)O. In the photocatalytic oxidation system with benzoic acid and benzene coexisting in the same dispersion, the percentage of O(2)-derived hydroxyl O atoms in the hydroxylated products of strongly adsorbed benzoic acid (ca. 30?%) is much less than in that of weakly adsorbed benzene (phenol) (>60?%). Such dependences provide unique clues to uncover the photocatalytic hydroxylation pathway. Our experiments show that the main O(2)-incorporation pathway involves the reduction of O(2) by e(cb)(-) and the subsequent formation of free (?)OH via H(2)O(2), which was usually overlooked in the past photocatalytic studies. Moreover, in the hydroxylation initiated by h(vb)(+), unlike the conventional mechanism, the O atom in O(2) cannot incorporate into the product through the direct coupling between molecular O(2) and the substrate-based radicals.     

钨过氧酸盐离子液体催化过氧化氢氧化苯甲醇制苯甲酸

用甲基三辛基氯化铵和钨酸钠一步法合成甲基三辛基季铵钨酸盐离子液体[(CH3)N(n-C8H17)3]2W2O11,以该离子液体为催化剂,在无反应溶剂条件下催化过氧化氢氧化苯甲醇生成苯甲酸。 考察了反应温度、催化剂用量以及氧化剂过氧化氢用量对苯甲酸产率的影响。 确定优化条件：反应温度70 ℃,苯甲醇用量5 mmol,催化剂用量是底物的0.4%(摩尔分数),30%过氧化氢用量2 mL,苯甲醇的转化率可达99%,苯甲酸选择性为98%。 该方法具有反应条件温和、产率高和选择性好的优点。     

Mechanistic Insights into Selectivity Control for Heterogeneous Olefin Oxidation: Styrene Oxidation on Au(111)

We demonstrate that intermolecular interactions, controlled by both oxygen and styrene coverage, alter reaction selectivity for styrene oxidation on oxygen‐covered Au(111). Several partial oxidation products are formed—styrene oxide, acetophenone, benzoic acid, benzeneacetic acid, and phenylketene—in competition with combustion. The maximum ratio of the yields of styrene oxide to the total CO₂ produced is obtained for the maximum styrene coverage for the first two layers (0.28 ML) adsorbed on Au(111) precovered with 0.2 ML of O. Furthermore, our reactivity and infrared studies support a mechanism whereby styrene oxidation proceeds via two oxametallacycle intermediates which, under oxygen‐lean conditions, lead to the formation of styrene oxide, acetophenone, and phenylketene. Benzoate, identified on the basis of infrared reflection absorption spectroscopy, is converted into benzoic acid during temperature‐programmed reaction. These results demonstrate the ability to tune the epoxidation selectivity using reactant coverages and provide important mechanistic insight into styrene oxidation reactions.     

Macro-kinetics of styrene oxidation catalyzed by Co<Superscript>2+</Superscript>-exchanged X

The macro-kinetics and pathway of styrene oxidation catalyzed by Co²⁺-exchanged X, using O₂ as oxidant, were investigated. The effects of external diffusion, internal diffusion, the styrene concentration, O₂ pressure, the catalyst concentration and the reaction temperature on the styrene oxidation reaction rate were examined. The results showed that the reaction rate of styrene oxidation was 0.19 order with respect to the styrene concentration, 0.64 order with respect to O₂ pressure, and zero to first order with respect to the different catalyst concentration. The calculated activation energy for this reaction was 13.79 kJ/mol. On the other hand, the three products in the styrene oxidation reaction were, respectively, used as the reactant to examine the reaction pathway of styrene oxidation. The results revealed that styrene oxidation reaction occurred as two parallel reactions. One was the production of styrene oxide and the other was the production of benzaldehyde and formaldehyde with former partially oxidized to benzoic acid and the latter mostly oxidized to O₂ and H₂O. Published in Russian in Kinetika i Kataliz, 2009, vol. 50, No. 2, pp. 212–217. The article is published in the original.