钒钼杂多酸盐相转移催化环戊烯氧化制备戊二醛

设计合成了一系列含高价态钼、钒等金属的杂多酸类相转移催化剂,用于催化环戊烯(CPE)氧化制备戊二醛的反应,筛选出催化活性最优的咪唑基钼钒酸盐催化剂[C₄H₉N₂C₃H₃(CH₃)]₅VMo₇O₂₆,并对溶剂种类、H₂O₂用量、催化剂用量、反应温度、时间等进行了条件优化.在优化的反应条件[V(乙酸乙酯)∶V(水)=4∶1,n(Cat.)∶n(H₂O₂)∶n(CPE)=1∶170∶41.6,50℃,6 h]下,得到了88.7%的环戊烯转化率和62.1%的戊二醛选择性,并且催化剂在经过7次循环使用后仍能保持较高的催化活性.     

羟基聚醚官能化杂多酸聚离子液体催化的连续酯化氧化合成环氧油酸甲酯

以乙二醇、环氧氯丙烷、三甲胺、三乙胺、三乙醇胺、H₄SiW₁₂O₄₀、H₃PW₁₂O₄₀为起始原料,经开环聚合、季铵化、分子自组装,构建了系列羟基官能化聚醚杂多酸聚离子液体HPIL-1～HPIL-6。聚离子液体兼具两亲活性、酸催化活性和氧化催化活性,以其为非均相催化剂,实现了油酸连续酯化、环氧化合成环氧油酸甲酯。当原料比n(甲醇)∶n(H₂O₂)∶n(油酸)∶n(聚离子液体)=500∶120∶40∶1,室温下酯化反应2.5h, 65℃下环氧化反应4h,环氧油酸甲酯产率92%。聚离子液体经离心分离、溶剂洗涤、真空干燥即可再生循环使用,循环使用5次,催化活性基本保持不变。     

改性VPO催化剂催化温和条件下苯乙烯液相选择性氧化

以苯乙烯为原料,分子氧为氧化剂,改性的钒磷氧化物为催化剂合成环氧苯乙烷.研究了金属修饰成分、P/V比率、溶剂和温度等因素对反应性能的影响.结果表明,Ag-VPO催化剂对环氧苯乙烷具有最好的选择性,在P/V=1、乙腈为溶剂、65℃的反应条件下,苯乙烯转化率为47.3%,环氧苯乙烷选择性达98.0%.     

纳微尺度铜金属有机框架催化过氧化氢氧化异丁香酚

通过水热法及沉淀法,合成了纳微尺度铜金属有机框架催化剂。 通过FT-IR、TG及TEM等技术手段对其性能和结构进行了表征。 系统考察了催化剂、溶剂种类及用量、反应时间等因素对异丁香酚氧化制备香草醛的影响。 结果表明,用均苯三甲酸根(BTC)作配体时制备的催化剂Cu-BTC性能较佳。 以Cu-BTC为催化剂、30%(质量分数)H₂O₂为氧化剂、乙腈为介质,当n(异丁香酚):n(H₂O₂)=1:2.4时,50 ℃,反应8 h,异丁香酚转化率为94.4%,香草醛产率达到81.8%。 纳微尺度(粒径30~300 nm)Cu-BTC催化剂体现了良好的重复使用性能,连续反应5次,异丁香酚转化率保持在90%左右。     

氨基醇杂多酸类离子液体催化环酮的Baeyer-Villiger氧化反应

合成了一系列氨基醇杂多酸类离子液体, 并将其用于催化环酮的Baeyer-Villiger氧化反应. 以2-庚基环戊酮为模板底物, H₂O₂为氧化剂, 探究了此类氨基醇杂多酸类离子液体的催化活性, 筛选出催化活性最高的催化剂为[Pro-ps]H₂PW₁₂O₄₀, 最佳反应条件: n(2-庚基环戊酮)∶n(催化剂)∶n(H₂O₂)=1∶0.03∶4, 反应温度40 ℃, 反应时间8 h, 无溶剂. 在最佳条件下, 2-庚基环戊酮的转化率为98.19%, 产物δ-十二内酯的选择性可达82.84%. 水相中的离子液体[Pro-ps]H₂PW₁₂O₄₀经干燥后可以重复使用. 经过5次循环使用后催化活性未见明显下降. [Pro-ps]H₂PW₁₂O₄₀还可用于催化其它多种环酮的Baeyer-Villiger氧化反应, 结果表明, 该催化剂具有良好的重复使用性和底物普适性.     

酸性功能化离子液体催化合成叶青素

以含磺酸基离子液体1-(4-磺酸基)丁基-3-甲基咪唑四氟硼酸盐([4-sulfbmim][BF₄])为酸性催化剂,由乙缩醛和苯甲醇合成了叶青素。 采用正交实验方法考察了合成条件的影响,固定反应温度为20 ℃条件下,确定优化合成条件为：n(苯甲醇)∶n(乙缩醛)=1∶8,反应时间60 min,催化剂用量为每摩尔苯甲醇4 g,产率为92.2%。 与H₂SO₄催化剂相比[4-sulfbmim][BF₄]的催化活性相对较弱,但综合效果优于H₂SO₄。 [4-sulfbmim][BF₄]循环使用6次,催化活性基本不变。     

过氧磷钨酸催化氧化脱除模拟油中的含硫化合物

考察了以H₂O₂为氧化剂, 过氧磷钨酸为催化剂催化氧化脱除模拟油中的含硫化合物苯并噻吩(BT)和二苯并噻吩(DBT). 讨论了催化剂用量、反应温度、反应时间和剂油体积比等因素对反应的影响. 实验结果表明, 当催化剂用量为0.48%(质量分数), V(H₂O₂)∶V(Oil)=1∶50, 反应时间为60 min, 反应温度为60 ℃时, BT的脱除率达到96.48%, DBT的脱除率达到99.42%. 动力学研究结果表明, 过氧磷钨酸为催化剂的氧化脱除模拟油中的含硫化合物的反应为表观一级反应.     

模拟油品氧化脱硫及反应动力学研究

在H₂O₂/WO₃/ZrO₂氧化体系中对以甲苯为溶剂、二苯并噻吩(DBT)为模型含硫化合物的模拟油品(硫的质量分数为1540×10^-6)进行了氧化脱硫研究,考察了反应温度、反应时间、氧化剂加入量、催化剂用量对DBT转化率的影响。实验结果表明,在反应温度50℃,反应时间90min,氧化剂加入量油/H₂O₂的体积比为20∶1和催化剂用量0.02g/mL的适宜氧化脱硫条件下,96%以上的DBT氧化为容易分离脱除的二苯并噻吩砜(DBTOs);同时研究了DBT氧化反应动力学,得知DBT氧化反应为一级反应,表观活化能E_a为55.37kJ/mol,指前因子A为3.35×10⁷min^-1。     

磷钨酸季铵盐催化异辛醇选择性氧化反应合成异辛酸

异辛酸是一种高附加值精细化学品，在有机合成和化工生产等领域有着广泛应用。本文以季铵盐负载的磷钨酸为催化剂，H₂O₂(30%,质量分数，下同)溶液为氧化剂，催化异辛醇选择性氧化合成异辛酸，产物结构经¹H NMR、¹³C NMR和MS确证。研究讨论了季铵盐种类、反应温度、催化剂用量、H₂O₂与异辛醇物质的量之比和反应时间对反应的影响，提出了可能的催化反应机理。结果表明：四聚型磷钨酸季铵盐作为该反应的催化剂表现出最好的催化活性，在最佳反应条件下(反应温度为90℃,催化剂用量为异辛醇质量的2.5%, H₂O₂与异辛醇物质的量之比为2∶1,反应时间为10 h),异辛醇转化率为90.2%,异辛酸选择性为82.8%,催化剂可回收使用4次。     

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%.     

三相相转移催化法制备二氧化双环戊二烯

以氯甲基化大孔聚苯乙烯-二乙烯基苯交联树脂（PS）接枝N-苄基-N,N-二甲基十二烷基季铵磷钨杂多酸盐为三相相转移催化剂,质量分数为50%的工业双氧水为氧化剂,制备了二氧化双环戊二烯（DCPDDO）。 采用FTIR和¹H NMR对产物进行表征。 考察了溶剂和催化剂用量、物料摩尔比、反应温度和时间对环氧化反应的影响。 采用正交试验法获得的最佳反应条件为（以0.05 mol双环戊二烯（DCPD）计）：1,2-二氯乙烷18 mL,催化剂2.25 g,n(DCPD)∶n(H₂O₂)=1∶2.75,反应温度60 ℃,反应时间12 h。 在此条件下,DCPDDO的收率可达89%以上,催化剂回收方便且重复使用7次未见活性明显降低。     

水介质中高分子配体负载微粒钯催化Suzuki偶联反应

对Wang树脂进行改性,制备了高分子负载纳米钯催化剂,并将其应用于水介质中卤代芳烃与芳硼酸的Suzuki偶联反应。 以溴苯和苯硼酸的偶联反应为模型,考察了溶剂、温度、碱种类、催化剂用量对反应的影响,确定较佳的反应条件为：n(C₆H₅Br)∶n(C₆H₅B(OH)₂)∶n(WRP-Pd)∶n(K₂CO₃)∶n(TBAB)=1.0∶1.5∶0.005∶2.0∶0.5,反应温度100℃, 反应时间4 h。 用氯代芳烃代替溴代芳烃反应时,延长反应时间,也能得到较高产率。 催化剂经过简单的过滤洗涤后,重复使用4次活性无明显降低。     

Epoxidation of propylene with hydrogen peroxide catalyzed by heteropolyphosphatotungstate

The epoxidation of propylene with hydrogen peroxide catalyzed by a reaction-controlled phase transfer catalyst (RCPT) composed of quaternary ammonium heteropolyoxotungstates in acetonitrile medium is studied. The influence of several factors on the reaction is studied, such as the reaction temperature, the effect of H₂O amount, the reaction time, the effect of the catalyst amount, solvent effect and the recycle of the catalyst. Under mild conditions, H₂O₂ conversion is 98.6%, and propylene oxide (PO) selectivity based on H₂O₂ is 97.2%. During the epoxidation, the catalyst is dissolved in the solution. However, after H₂O₂ is used up, the catalyst can be recovered as a precipitate and can be recycled. We find that the recycled catalyst has similar catalytic activity as the fresh one.     

Mixed matrix vanadium oxide catalytic nanocomposite membrane for styrene oxidation

Mesoporous nanocomposite membranes with vanadium oxide–carbon nanotubes (V_xO_y-CNTs) embedded in γ-Al₂O₃ were successfully synthesized using the dip coating method. The membranes were evaluated for styrene oxidation to determine the optimum styrene conversion and benzaldehyde selectivity. Several factors that influence the preparation of defect-free coatings, such as the type of binder, the binder addition time and surface support treatments, were investigated. The physico-chemical permeation properties of the membranes were characterized using scanning electron microscope, transmission electron microscope (TEM), X-ray Diffraction XRD, Nitrogen adsorption (BET) and Thermogravimetric TGA. Response surface methodology (RSM) was used to investigate the effects of oxidant (H₂O₂) concentration, temperature, contact time and catalyst loading on styrene conversion and the selectivity of benzaldehyde. Based on the RSM analysis, the optimal oxidation conditions included a reaction temperature of 45 °C, a differential pressure of 1.5 bars, a molar ratio of H₂O₂: styrene of 1.5:1 and a catalyst loading of 30 %. These conditions resulted in the maximal styrene conversion of 25.6 and 84.9 % benzaldehyde selectivity.     

SO42-/SnO2-硅藻土型固体酸的制备及其对正丁酸与异戊醇的催化酯化

采用质量比为1∶3的SnCl₄·5H₂O和硅藻土制备的硅藻土Sn(OH)₄溶胶,70 ℃老化12 h,90 ℃干燥12 h、3.0 mol/L硫酸浸渍3 h、550 ℃焙烧3.5 h,制备了SO₄^2-/SnO₂硅藻土型固体酸催化剂。 利用IR、 XRD、TG测试技术表征了催化剂的理化性质。 用于催化正丁酸与异戊醇的酯化反应,当n（异戊醇）∶n（正丁酸）=1.4∶1、催化剂用量为反应物总质量的2.5%、10 mL苯、反应时间70 min时,酯收率为97.7％。 结果表明,该催化剂兼具多元氧化物型固体酸和硫酸酸化改性天然粘土固体酸催化剂的优点,催化活性高,成本低廉、制备方法简单并可适当回收循环使用。     

Room temperature synthesis of Ti-SBA-15 from silatrane and titanium-glycolate and its catalytic performance towards styrene epoxidation

A novel room temperature sol–gel synthesis of Ti-SBA-15 is described using moisture stable silatrane and titanium glycolate precursors, and poly(ethylene oxide)-poly(propylene oxide)-poly(ethylene oxide) block copolymer (EO₂₀PO₇₀EO₂₀) as the structure directing agent. Catalyst performance was optimized by systematically investigating the influence of acidity, reaction time and temperature, and titanium loading. Small angle X-ray scattering (SAXS) and transmission electron microscopy (TEM) showed well-ordered 2D mesoporous hexagonal structures, while N₂ adsorption/desorption measurements yielded high surface areas (up to 670 m²/g), with large pore diameters (5.79 nm) and volumes (0.83 cm³/g). Diffuse reflectance UV–visible spectroscopy (DRUV) was found that tetravalent titanium as Ti⁴⁺O₄ tetrahedra were incorporated in the framework through displacement of Si⁴⁺O₄ after calcination (550°C/6 h) to loadings of 7 mol% Ti without perturbation of the ordered mesoporous structure, or decoration by extra-framework anatase containing Ti⁴⁺O₆ octahedra. The catalytic activity and selectivity of styrene epoxidation using hydrogen peroxide (H₂O₂) showed that the conversion of styrene increases significantly at higher titanium contents. The only products of this reaction were styrene oxide and benzaldehyde, with selectivity of 34.2 and 65.8%, respectively, at a styrene conversion of 25.8% over the 7 mol% Ti-SBA-15 catalyst. Beyond this titanium loading, anatase is deposited on the framework and catalytic activity degrades. The performance of the new catalyst is also shown to be superior to conventional materials produced by incipient wetness impregnation where Ti resides on the surface of SBA-15, giving a styrene conversion of 11.9% under identical reaction conditions.     

Gold nanoparticles supported on cellulose aerogel as a new efficient catalyst for epoxidation of styrene

A new efficient heterogeneous catalyst was introduced for the epoxidation of styrene. The catalyst was obtained from deposition of gold nanoparticles on the cellulose aerogel. The catalyst was characterized with XRD, TGA, EDX, BET, FAAS and SEM. High yield and excellent selectivity were achieved for the epoxidation of styrene in solvent-free conditions at room temperature using H₂O₂ as a green oxidant during 1 h. The reaction has some advantages such as solvent-free and mild reaction conditions, low catalyst loading, high yield, excellent selectivity, green oxidant and short reaction duration. In addition, the catalyst is recyclable and applicable for six times without decrease in yield.     

Silver and palladium nanoparticles-containing products of the low-temperature wave conversion of an energetic material: Catalytic activity in piperylene hydrogenation

The hydrogenation of 1,3-pentadiene into pentenes over the commercial 0.5% Pd/Al₂O₃ catalyst and over a new catalyst containing 1.0% Pd and 3.7% Ag (μ-catalyst) has been investigated. The new catalyst has been prepared via the flameless wave conversion of cyclotrimethylenetrinitramine in a porous composite. The catalytic properties of the new composite in the hydrogenation reaction depend on the hydrogen/1,3-pentadiene ratio and on the catalyst activation temperature. The reaction conditions for selective 1,3-pentadiene hydrogenation have been optimized. The pentenes yield as a function of temperature passes through a maximum at any H₂/C₅H₈ ratio between 1 and 2. The 2-pentene/1-pentene ratio in the reaction products increases as the temperature is raised.     

Encapsulation of a binuclear manganese(II) complex with an amino acid-based ligand in zeolite Y and its catalytic epoxidation of cyclohexene

A Schiff base ligand was synthesized by the condensation of salicylaldehyde with l-tyrosine. Interaction of this ligand with Mn(II)-exchanged zeolite Y leads to encapsulation of the ligand within the zeolite and complexation of the metal. The encapsulated complex has been characterized by spectroscopic studies and chemical analyses. This material serves as a catalyst for the oxidation of cyclohexene to cyclohexene epoxide and 2-cyclohexene-1-ol using H₂O₂ as oxidant. The reaction conditions have been optimized for solvent, temperature and amount of oxidant and catalyst. The catalyst shows high activity and selectivity toward production of cyclohexene epoxide in acetonitrile at 60 °C with [H₂O₂]/[C₆H₁₀] = 2.5 molar ratio. Comparison of the encapsulated catalyst with the corresponding homogeneous catalyst showed that the heterogeneous catalyst had higher activity and selectivity than the homogeneous catalyst.     

Graphene Oxide Supported Oxovanadium (IV) Complex for Catalytic Peroxidative Epoxidation of Styrene: An Eye-Catching Impact of Solvent

Graphene oxide (GO) supported transition metal complexes are apprised as sturdy and everlasting heterogeneous catalysts. GO surface was functionalized with 3-triethoxysilylpropylamine (TSPA) and this amino functionalized GO (A-f-GO) nanocomposite with vanadyl Schiff base complex (VO-f-GO) was prepared and to give credence of its potentiality, it was chosen for the selective epoxidation of styrene using environmentally benign 30% H₂O₂ to styrene oxide (SO). To evade the detrimental exposure of “inborn” water, a selective high boiling and potent hygroscopic solvent, ethylene glycol was chosen to make this transformation productively successful. With the assistance of theoretical studies, we have probed the effect of H₂O₂ on to structural properties, binding mechanism and electronic properties of the catalyst and substrate. Adsorption energy (E_ad), energy band gap (E_g) and HOMO-LUMO were also calculated. Based on DFT calculations, resonance Raman and UV/Vis studies, we confirmed the formation of metal-peroxo species and propose the plausible catalytic pathway. The influence of the diverse experimental parameters, like substrate to oxidant mole ratio, catalyst concentration, type of solvents, solvent amount, time, temperature and oxidant were tested. A clear relationship was found between different reaction parameters like solvent amount, oxidant, catalyst concentration and temperature etc. and product distribution. This heterogeneous catalyst yielded styrene oxide as nearly the sole product (selectivity = 98.7%) with a conversion value of 99.2% in the oxidation of styrene with hydrogen peroxide in ethylene glycol.