水溶性钯配合物催化柠檬醛的选择加氢反应研究：I.反应条件的影响

研究了在水／有机物两相体系中水溶性钯－膦配合物催化柠檬酸的加氢反应。考察了反应温度、氢气压力、底物和催化剂浓度、反应时间、水相ｐＨ值等对该反应的影响，并与几种柠檬醛衍生物的加氢结果进行了比较。发现仅用蒸馏水作水相，则主要产物是二氢香茅醛（〉９３％）；而水相水加入Ｎａ２ＣＯ３后，则主要产物为香茅醛（９７％），且加氢速度比同样条件下使用Ｐｄ／Ｃ催化剂快得多。     

烯烃羰化—步制醇铑系催化新体系的研究

羰基铑催化剂由于其加氢性能较弱，在羰基化反应的研究中，通常仅作为烯烃氢甲酰化制醛的催化剂。产物中得不到醇。本文则报道了以Ｒｈ＿２（ＡｃＯ）＿４和Ｒｈ＿６（ＣＯ）＿１６为催化剂，在一个反应器内进行烯烃氢甲酰化，加氢制醇的研究。系统考察了Ｒｈ／Ｐｂｕ＿３／ＥｔＯＨ催化体系受各种反应条件的影响。在最佳反应条件下，烯烃转化率达１００％。对醇选择性亦在９９．５％以上，正异构比在２以上．为烯烃一步制醇建立了铑系催化新体系。文中并利用红外光谱测定了反应过程的催化剂物种．实验证明，由烯烃一步制醇是由烯烃首先进行氢甲酰化反应，然后由生成的醛进一步加氢成醇的一个串联反应过程。前一步骤反应速度较快，２ｈ内可使９５％以上的烯烃转化为醛，后面由醛加氢成醇则进行缓慢，在１００—１２０℃下，至少２２ｈ，才能使醛全部转化为醇。     

烯烃羰化一步制醇铑系催化新体系的研究

羰基铑催化剂由于基加氢性能较弱，在羰基化反应的研究中，通常仅作为烯烃氢甲酰化制醛的催化剂。产物中得不到醇。本文则报道了以Ｒｈ２（ＡｃＯ）４和Ｒｈ６（ＣＯ）１６为催化剂，在一个反应器内进行烯烃氢甲酰化，加氢制醇的研究。系统考察了Ｒｈ／ＰＢｕ２／ＥｔＯＨ催化体系受各种反应条件的影响。在最佳反应条件下，烯烃转化率达１００％。对醇选择性亦在９９．５％以上，正异构比在２以上。为烯烃一步制醇建立了铑系催化新体     

二苯并噻吩在分散型钼催化剂和原位产生的氢存在下的加氢脱硫Ⅲ. 催化剂前身物、硫化氢、一氧化碳和水对反应的影响(英)

研究了水／ 甲苯乳化液中二苯并噻吩（ 硫芴） 在分散型钼酸、磷钼酸和四硫钼酸铵催化剂存在下的加氢脱硫反应． 反应在高压釜中于３４０ ℃及三种不同的气氛即Ｈ２ ，Ｈ２／Ｈ２ Ｏ和ＣＯ／Ｈ２Ｏ（ＣＯ 和Ｈ２Ｏ 经水煤气转换反应（ ＷＧＳＲ） 产生原位氢） 的存在下进行． 用ＧＣ和ＧＣＭＳ鉴定、分析了气体和液体产物的组成． 结果表明： 对硫芴的加氢脱硫反应，在分散型四硫钼酸铵催化剂存在下，原位产生的氢的效果仅比加入的氢气稍好，而在分散型钼酸和磷钼酸催化剂存在下，原位产生的氢远比加入的氢气有效． 实验结果还表明： 硫化氢能显著提高分散型钼酸和磷钼酸催化剂的加氢脱硫活性，但在分散型四硫钼酸铵催化剂存在下，硫化氢能促进加氢反应而抑制氢解反应． 一氧化碳和水均选择性地抑制氢解反应．     

水溶性钯配合物催化柠檬醛的选择加氢研究 Ⅱ.催化剂的循环使用

研究了以水溶性ＰｄＣｌ２（ＴＰＰＴＳ）２为催化剂，在水／有机物两相体系中，添加ＴＰＰＴＳ、ＣＴＡＢ、ＰＶＡ、明胶和碳酸钠对柠檬醛加氢反应及催化剂稳定性的影响．添加配体ＴＰＰＴＳ、明胶或表面活性剂ＣＴＡＢ有利于减少钯黑的形成，但会引起催化活性的降低；而添加ＰＶＡ和Ｎａ２ＣＯ３，虽然都不能抑制钯黑的形成，但后者的添加会明显提高加氢速度；发现，明胶加碳酸钠的体系不仅可以稳定催化剂的活性物种，避免钯黑的析出，而且催化反应的转化率及选择性都较高．     

两相催化体系中α，β－不饱和醛的选择性加氢反应研究Ⅰ．水溶性钌－膦配合物催化肉桂醛的加氢性能

本文研究了两种水溶性钌－膦配合物ＲｕＣｌ_２（ＴＰＰＴＳ）_３和Ｒｕｃｌ_２（ＣＯ）_２（ＴＰＰＴＳ）_２［ＴＰＰＴＳ为：Ｐ（ｍ－Ｃ_６Ｈ_４ＳＯ_３Ｎａ）_３］的合成，在水相和有机相组成的两相催化体系中，考察了它们衍生出的活性物种和以ＲｕＣｌ３－ＴＰＰＴＳ原位合成的活性物种对肉桂醛的选择加氢性能，并对反应温度（２０—８０℃），氢压（２—６ＭＰａ），催化剂浓度（１．１２×１０~（－３）～４．５０×１０~（－３）ｍｏｌ／Ｌ），配体ＴＰＰＴＳ浓度（９．０×１０~（－３）～５．４×１０~（－２）ｍｏｌ／Ｌ），表面活性剂浓度和反应时间的变化对选择加氢反应的影响进行了详细研究。实验结果表明，ＲｕＣｌ_３－ＴＰＰＴＳ原位合成配合物的催化加氢活性最高，而在金属Ｒｕ上羰基的配位将使加氢活性降低，表面活性剂ＣＴＡＢ是有效的促进剂，它的加入可大大提高加氢活性，选择适当的ＣＴＡＢ浓度，在反应结束后水相与有机相分层迅速，有利于Ｒｕ催化剂的分离，在所考察的反应条件下，肉桂醛选择加氢生成肉桂醇的转化率大于８０％，选择性达９６％以上。     

水溶性钯配合物催化化柠檬醛的选择加氢研究

研究了以水溶性ＰｄＣｌ２（ＴＰＰＴＳ）２为催化剂，在水／有化机物两相体系中，添加ＴＰＴＳ、ＣＴＡＢ、ＰＶＡ、明胶和碳酸钠和柠檬醛加氢反应及催化剂稳定性的影响，添加配体ＴＰＰＴＳ、明胶或表面活性ＣＴＡＢ有利于减少钯黑的形成，但会引起催化活性降低；而添加ＰＶＡ和Ｎａ２Ｃｏ３，虽然都不能抑制钯黑的形成，但后者的添加会明显提高加氢速度；发现，明胶加碳酸钠的体系不仅可以稳定催化剂的活性物种，避免钯黑的析出，     

水溶性钯膦络合物催化1-辛烯的氢羧基化反应

利用水溶性配体TPPTS与Pd（OAc）2在水相中催化1-辛烯的氢羧基化反应,能实现有机相产物与水相催化剂的清洁分离和催化剂的循环利用．分别考察了钯浓度、表面活性剂（CTAB）、酸助剂、反应时间、CO压力以及温度对该反应的影响．在H2O=16mL,C（Pd）=2．0mmol／L,C（TPTS）／c（Pd）=25,C（p...     

阴离子交换树脂担载氟离子催化合成假性甲基紫罗兰酮

用阴离子交换树脂担载氟离子催化柠檬醛与丁酮的反应,合成了假性甲基紫罗兰。探讨了催化剂用量、反应物配比、反应温度和反应时间等因素对收率的影响,在柠檬醛为100mmol,n(柠檬醛)：n(丁酮)=1：10,催化剂用量为柠檬醛质量的75％,室温反应1h的最佳反应条件下,产物收率87．1％,纯度99．1％。     

水溶性双金属催化剂在硝基化合物加氢反应中的协同效应

采用水溶性催化剂在两相体系下进行的催化反应既保持了均相催化剂的优点，又可通过简单的相分离达到使产物与催化剂分离的目的［’1．对于水溶性催化剂在两相体系中催化加氢反应，文献中大多采用水溶性铐一瞬、铱一脚和钉一碟络合物为催化剂对a、“不饱和醛、酮、酸等化合物的选择加氢进行考察［’‘．然而对水溶性把一脚络合物催化加氢反应性能研究的报道甚少［‘j．在多相催化中，双（或多）金属的协同效应是常见的现象，但在均相及高分子负载的催化体系中双（或多）金属的协同效应的报道较少［‘］．我们曾报道了高分子负载的Pd／RU双…     

Studies on catalytic hydrogenation of citral by water-soluble palladium complex

The hydrogenation of citral has been studied in biphasic system using water-soluble PdCl₂(TPPTS)₂ as catalyst. The selectivity to form citronellal increased with increasing pH values of the aqueous phase. At the same pH value, the selectivity was higher when the hydrogenation was carried out in the presence of Na₂CO₃ than in the presence of NaOH. The main product was citronellal and a maximum yield of 93% had been obtained using Na₂CO₃ solution at pH 11.6. The CC bond in citronellal could be further hydrogenated to form dihydrocitronellal when the hydrogenation was carried out in distilled water at pH 6.0. The yield of dihydrocitronellal could reach 93% with prolonged reaction time to 6 h. Therefore, high yields of either citronellal or dihydrocitronellal could be obtained from citral by selecting the corresponding reaction conditions.     

两相体系中催化氢化丙烯腈制备丙腈

膦配体TPPTS(三-间磺酸钠-三苯基膦)的水溶性很好，有关其过渡金属配合物催化剂的应用与研究活跃。近年来，对丙烯腈C=C双键加氢的研究多集中在以钯为中心金属的多相催化体系上，已报道的有聚硅氧烷钯体系，膦酸锆负载钯体系，高分子负载钯．金属氧化物催化剂，SiO2负     

两相体系中钌膦配合物催化4—苯基—3—丁烯—2—酮加氢反应的研究

研究了水和有机物组成的两相催化体系中,由ＲｕＣｌ３－ＴＰＰＴＳ（ＴＰＰＴＳ：Ｐ（ｍ－Ｃ６Ｈ４ＳＯ３Ｎａ）３）原位反应生成的催化活性物种对４－苯基－３－丁烯－２－酮（又名苄叉丙酮）的催化加氢反应．考察了钌浓度（１．０×１０－３～６．０×１０－３ｍｏｌ／Ｌ）、氢压（１．０～６．０ＭＰａ）、反应温度（３０～７０℃）、配体浓度（１．２～７．２×１０－２ｍｏｌ／Ｌ）、阳离子表面活性剂（ＣＴＡＢ：十六烷基三甲基溴化铵）及反应时间等对加氢反应活性和选择性的影响,并与以配合物ＲｕＣｌ２（ＴＰＰＴＳ）３为催化剂前体生成的催化活性物种对加氢反应的活性及选择性进行了比较．结果表明,分别由配合物ＲｕＣｌ２（ＴＰＰＴＳ）３及ＲｕＣｌ３－ＴＰＰＴＳ原位反应生成的催化活性物种,都只催化４－苯基－３－丁烯－２－酮的Ｃ＝Ｃ键选择加氢．由配合物ＲｕＣｌ２（ＴＰＰＴＳ）３形成的催化体系的加氢活性及选择性均优于ＲｕＣｌ３－ＴＰＰＴＳ原位反应生成的催化活性物种．阳离子表面活性剂的加入,使加氢反应活性下降,选择性略有提高     

阳离子表面活性剂存在下水/有机两相体系中双环戊二烯氢甲酰化

研究了在阳离子表面活性剂存在下水/有机两相中水溶性铑配合物RhCI(CO)(TPPTS)2(TPPTS:P(m-C6H4SO3Na)3)催化双环戊二烯氢甲酰化反应,考察了反应温度、催化剂浓度、不同水溶性膦配体TPPTS和TPPDS(C5H5P(m-C6H4SO3Na)2),以及表面活性剂结构对催化反应的影响.结果表明,...     

Hydrogenation of crotonaldehyde and cinnamaldehyde catalyzed by water-soluble palladium complex

The selective hydrogenations of crotonaldehyde and cinnamaldehyde in the aqueous-benzene biphasic system were investigated using water-soluble palladium complex PdCl₂(TPPTS)₂ as catalyst. The hydrogenation rate of crotonaldehyde was higher than that of cinnamaldehyde under similar reaction conditions. The palladium complex selectively catalyzed the hydrogenation of CC bond in crotonaldehyde to form butanal (100%). On the contrary, hydrogenation of both CC and CO bonds in cinnamaldehyde occurred simultaneously, with the amount of phenylpropanal only slightly higher than that of phenylpropanol. However, the reduction of CO bond of cinnamaldehyde could be inhibited by the addition of Na₂CO₃ solution. Therefore, high selectivity to form phenylpropanal (91%) could be obtained by using Na₂CO₃ solution at pH 12.2. Other factors affecting the hydrogenation conversion and selectivity of crotonaldehyde and cinnamaldehyde were also discussed.     

Selective Hydrogenation of Citral over a Carbon‐titania Composite Supported Palladium Catalyst

A novel carbon‐titania composite material, C/TiO₂, has been prepared by growing carbon nanofibers (CNFs) on TiO₂ surface via methane decomposition using Ni‐Cu as a catalyst. The C/TiO₂ was used for preparing supported palladium catalyst, Pd/C/TiO₂. The support and Pd/C/TiO₂ catalyst were characterized by BET, SEM, XRD and TG‐DTG. Its catalytic performance was evaluated in selective hydrogenation of citral to citronellal, and compared with that of activated carbon supported Pd catalyst. It was found that the Pd/C/TiO₂ catalyst contains 97% of mesopores. And it exhibited 88% of selectivity to citronellal at citral conversion of 90% in citral hydrogenation, which was much higher than that of activated carbon supported Pd catalyst. This result may be attributed to elimination of internal diffusion limitations, which were significant in activated carbon supported Pd catalyst, due to its microporous structure.     

Micelle-hosted palladium nanoparticles catalyze citral molecule hydrogenation in supercritical carbon dioxide

A new approach of employing metal particles in micelles for the hydrogenation of organic molecules in the presence of fluorinated surfactant and water in supercritical carbon dioxide has very recently been introduced. This is allegedly to deliver many advantages for carrying out catalysis including the use of supercritical carbon dioxide (scCO2) as a greener solvent. Following this preliminary account, the present work aims to provide direct visual evidence on the formation of metal microemulsions and to investigate whether metal located in the soft micellar assemblies could affect reaction selectivity. Synthesis of Pd nanoparticles in perfluorohydrocarboxylate anionic micelles in scCO2 is therefore carried out in a stainless steel batch reactor at 40 degrees C and in a 150 bar CO2/H2 mixture. Homogeneous dispersion of the microemulsion containing Pd nanoparticles in scCO2 is observed through a sapphire window reactor at W0 ratios (molar water-to-surfactant ratios) ranging from 2 to 30. It is also evidenced that the use of micelle assemblies as new metal catalyst nanocarriers could indeed exert a great influence on product selectivity. The hydrogenation of a citral molecule that contains three reducible groups (aldehyde, double bonds at the 2,3-position and the 6,7-position) is studied. An unusually high selectivity toward citronellal (a high regioselectivity toward the reduction of the 2,3-unsaturation) is observed in supercritical carbon dioxide. On the other hand, when the catalysis is carried out in the conventional liquid or vapor phase over the same reaction time, total hydrogenation of the two double bonds is achieved. It is thought that the high kinetic reluctance for double bond hydrogenation of the citral molecule at the hydrophobic end (the 6,7-position) is due to the unique micelle environment that is in close proximity to the metal surface in supercritical carbon dioxide that guides a head-on attack of the molecule toward the core metal particle.     

Na—W—Mn／SiO2催化剂表面甲烷脉冲反应I.单组分Na／、W／、Mn／SiO2催化剂

制备了单组分Na/、W/、Mn/SiO2催化剂，在ITD（Ion Trap Detector）装置上进行了催化剂表面晶格氧脱附前后的甲烷恒温脉冲反应（CH4-CTPR），研究结果表明，N a/SiO2表面晶格氧具有一定的C2烃选择性，并能强烈抑制CO2的生成，W/SiO2表面晶格氧对C2烃的选择性较差，但对Cox具有高的选择性；Mn/SiO2表面的晶格氧对C2H4和CO具有高选择性，而较深部位的晶格氧则对C2H6和CO2具有高的选择性。     

Liquid phase hydrogenation of citral and intermediaries over Ir/TiO2/SiO2 catalysts: Kinetic study

Kinetics of the hydrogenation of citral and its intermediates over Ir/TiO₂/SiO₂ catalysts has been studied. The effect of various parameters such as the initial concentration, H₂ pressure partial, temperature and weight of catalyst were examined. A high selectivity towards unsaturated alcohols using this catalyst was demonstrated. The initial rates increased linearly with the catalyst weight. The reaction rate obeys a kinetics represented by the Langmuir–Hinshelwood model. A single site model suggesting the surface reaction as the rate determining step provided the best fit of the experimental data for the hydrogenation of citral and alcohols (geraniol, nerol and citronellol), while a dual site represent the best kinetics for the hydrogenation of citronellal.     

Adsorption at the liquid-liquid interface in the biphasic rhodium catalyzed hydroformylation of olefins promoted by cyclodextrins: a molecular dynamics study

Using molecular dynamics (MD) simulations, we investigate the interfacial distribution of partners involved in the phase transfer rhodium catalyzed hydroformylation of olefins promoted by beta-cyclodextrins (beta-CDs). The beta-CDs, the reactant (alkene), product (aldehyde), several rhodium complexes (the catalyst, its precursor, and its alkene adduct) are simulated at the water-"oil" interface, where oil is represented by chloroform or hexane. It is shown that unsubstituted beta-CD and its 6-methylated and 2,6-dimethylated analogues adsorb at the interface, whereas the liposoluble permethylated CD does not. The precursor of the catalyst [RhH(CO)(TPPTS)3]9- (with triphenylphosphine trisulfonated TPPTS3- ligands) sits in water, but the less charged [RhH(CO)(TPPTS)2]6- catalyst and the [RhH(CO)(TPPTS)2(alkene)]6- reaction intermediate are clearly surface active. The TPPTS3- anions also concentrate at the interface, where they adopt an amphiphilic conformation, forming an electrical double layer with their Na+ counterions. Thus, the most important key partners involved in the hydroformylation reaction concentrate at the interface, thereby facilitating the reaction, a process which may be further facilitated upon complexation by CDs. These results point to the importance of adsorption at the liquid-liquid interface in the two-phase hydroformylation reaction of olefins promoted by beta-CDs and provide microscopic pictures of this peculiar region of the solution.