Water/Oil Biphasic Hydroformylation of Higher Olefins over a TPPTS-Rh/SiO2 Catalyst

A novel TPPTS-Rh/SiO2 catalyst, prepared by directly modifying a heterogeneous highsurface-area Rh/SiO2 catalyst with water-soluble TPPTS ligands, could decrease the resistance of mass transfer in water/oil biphasic media for the hydroformylation of higher olefins. The catalytic performance for hydroformylation on this biphasic TPPTS-Rh/SiO2 catalyst system was higher than those of the traditional biphasic HRhCO(TPPTS)3 systems, owing to the chemical bonds between the highly dispersed Rh metal particles and the TPPTS ligands. The catalyst system is applicable for hydroformylation of higher olefins such as 1-dodecene.     

Water／Oil Biphasic Hydroformylation of Higher Olefins over a TPPTS-Rh／SiO2 Catalyst

A novel TPPTS-Rh/SiO2 catalyst, prepared by directly modifying a heterogeneous high-surface-area Rh/SiO2 catalyst with water-soluble TPPTS ligands, could decrease the resistance of masstransfer in water/oil biphasic media for the hydroformylation of higher olefins. The catalytic performancefor hydroformylation on this biphasic TPPTS-Rh/SiO2 catalyst system was higher than those of thetraditional biphasic HRhCO(TPPTS)3 systems, owing to the chemical bonds between the highly dispersedRh metal particles and the TPPTS ligands. The catalyst system is applicable for hydroformylation ofhigher olefins such as 1-dodecene.     

Hydroformylation of methyl-3-pentenoate over a phosphite ligand modified Rh/SiO2 catalyst

A phosphite ligand modified Rh/SiO2 catalyst has been developed for hydroformylation of internal olefins to linear aldehydes, which showed high activity and regioselectivity and could be separated easily by filtration after reaction in an autoclave. Effects of reaction temperature and syngas pressure on the performances of the catalyst in the reaction were also investigated.     

Mo—Bi—Ce／SiO2催化剂的XPS研究

用XPS研究了甲醇还原前后的Mo-Bi-Ce/SiO_2催化剂并进行了测定。结果表明,反应前催化剂表面主要由Bi_2(MoO_4)_3与CeO_2组成,而反应后Ce~(4+)还原为Ce~0并出现少量Ce_2O_3,同时Bi、Mo均还原为低价态,还原顺序为Ce、Bi、Mo。还原前Bi处于催化剂表层,反应过程中扩散进入体相,再经氧脉冲氧化Bi迁回表层。活性组份被氧化的顺序为Mo、Bi、Ce。     

Domino Hydroformylation/Aldol Condensation/Hydrogenation Catalysis: Highly Selective Synthesis of Ketones from Olefins

A general and highly chemo‐ and regioselective synthesis of ketones from olefins by domino hydroformylation/aldol condensation/hydrogenation reaction has been developed. A variety of olefins are efficiently converted into various ketones in good to excellent yields and regioselectivities in the presence of a specific rhodium phosphine/base–acid catalyst system.     

Hydroformylation of 1-hexene in the presence of rhodium complexes immobilized on polyorganosiloxanes

It was demonstrated that the catalyst system based on acacRh(CO)₂ and polyorgano-siloxanes exhibits high activity and stability in hydroformylation of 1-hexene. The effects of the nature of the oligomer, the ratio of oligomers, and the oligomer: rhodium ratio in the polymer on the synthesis and catalytic properties of the system were studied. Translated fromIzvestiya Akademii Nauk. Seriya Khimicheskaya, No. 6, pp. 1155–1157, June, 1997.     

温控相分离催化的高碳烯烃氢甲酰化反应研究

考察了非离子表面活性膦配体P[p-C6H4O(CH2CH2O)nH]3(PETPP,n=6～12,N=3n)在有机溶剂中的溶解度－温度关系,发现其在甲苯中具有临界溶解温度（CST）现象。基于PETPP在甲苯中低温分相、高温互溶的CST特性,提出了温控相分离催化的新概念。并将其应用于癸烯氢甲酰化反应,转化率及醛收率分别达到98.7%和96.0%,催化剂循环使用10次,活性基本保持不变。     

膦配体修饰的Rh／SiO2用于3-戊烯酸甲酯氢甲酰化反应

制备了膦配体修饰的Rh/SiO2多相催化剂(L-Rh/SiO2),该催化剂在内烯烃氢甲酰化制备正构醛反应中表现出了高活性和高区域选择性,而且在高压釜反应器中可以通过简单的过滤与产物分离.通过使用不同的单齿和螯合双齿膦配体考察了配体的电子及空间效应对L-Rh/SiO2催化剂催化性能的影响。     

Mn-Na_2WO_4/SiO_2催化剂表面活性中心结构的DFT研究

利用密度泛函方法(DFT)研究了Mn-Na2WO4/SiO2催化剂表面的活性中心结构.计算表明,在α-方石英的(111)面上,W能以单个或三个桥氧与载体作用形成稳定的四面体配位结构,Mn则能以单个桥氧与载体配位或形成不同结构的氧化物团簇;以单个桥氧担载的[WO4]四面体是最可能的甲烷活化中心.     

Spiroketal‐Based Phosphorus Ligands for Highly Regioselective Hydroformylation of Terminal and Internal Olefins

A new class of bidentate phosphoramidite ligands, based on a spiroketal backbone, has been developed for the rhodium‐catalyzed hydroformylation reactions. A range of short‐ and long‐chain olefins, were found amenable to the protocol, affording high catalytic activity and excellent regioselectivity for the linear aldehydes. Under the optimized reaction conditions, a turnover number (TON) of up to 2.3×10⁴ and linear to branched ratio (l/b) of up to 174.4 were obtained in the Rh^I‐catalyzed hydroformylation of terminal olefins. Remarkably, the catalysts were also found to be efficient in the isomerization–hydroformylation of some internal olefins, to regioselectively afford the linear aldehydes with TON values of up to 2.0×10⁴ and l/b ratios in the range of 23.4–30.6. X‐ray crystallographic analysis revealed the cis coordination of the ligand in the precatalyst [Rh( 3 d )(acac)], whereas NMR and IR studies on the catalytically active hydride complex [HRh(CO)₂( 3 d )] suggested an eq–eq coordination of the ligand in the species.     

Phosphorus Ligand Modified Rh/SiO2 Catalyst for Hydroformylation of Methyl-3-pentenoate

A phosphorus ligand-modified Rh/SiO₂ catalyst (L-Rh/SiO₂) has been developed for hydroformylation of internal olefins to linear aldehydes. This catalyst has high activity and regioselectivity and can be separated easily by filtration after reaction in an autoclave. Moreover, the electronic and steric effects of phosphorus ligands on the catalytic performance of the L-Rh/SiO₂ catalyst have been investigated by using various monodentate and chelating diphosphorus ligands.     

In-Situ FT-IR Investigation Methane to Syngas over of Partial Oxidation of Rh/SiO2 Catalyst

Partial oxidation of methane to syngas （POM） over Rh/SiO2 catalyst was investigated using in-situ FT-IR. When methane interacted with 1.0wt%Rh/SiO2 catalyst, it was dissociated to adsorbed hydrogen and CHx species. The adsorbed hydrogen atoms were transferred to SiO2 surface by ＂spill-over＂ and reacted with lattice oxygen to form surface -OH species. POM mechanism was investigated over Rh/SiO2 catalyst using in-situ FT-IR. It was found that CO2 was formed before CO could be detected when CH4 and O2 were introduced over the preoxidized Rh/SiO2 catalyst, whereas CO was detected before CO2 was formed over the prereduced Rh/SiO2 catalyst.     

Domino‐Hydroformylation/Aldol Condensation Catalysis: Highly Selective Synthesis of α,β‐Unsaturated Aldehydes from Olefins

A general and highly chemo‐, regio‐, and stereoselective synthesis of α,β‐unsaturated aldehydes by a domino hydroformylation/aldol condensation reaction has been developed. A variety of olefins and aromatic aldehydes were efficiently converted into various substituted α,β‐unsaturated aldehydes in good to excellent yields in the presence of a rhodium phosphine/acid–base catalyst system. In view of the easy availability of the substrates, the high atom‐efficiency, the excellent selectivity, and the mild conditions, this method is expected to complement current methodologies for the preparation of α,β‐unsaturated aldehydes.     

温控离子液体/有机两相体系中纳米Rh催化烯烃氢甲酰化反应

将具有"高温混溶、室温分相"功能的离子液体[CH3(OCH2CH2)16N+Et3][CH3SO3–](ILPEG750)与甲苯-正庚烷组成的两相体系用于纳米Rh催化的烯烃氢甲酰化反应中,在优化的反应条件下,1-辛烯转化率和醛收率分别为99%和91%.催化剂经简单分相即可与产物分离,且可连续使用8次,其活性基本保持不变.     

Synthesis of Methyl Glycolate by Hydrogenation of Dimethyl Oxalate over Cu-Ag/SiO2 Catalyst

Methyl glycolate is a good solvent and can be used as feedstock for the synthesis of some important organic chemicals. Catalytic hydrogenation of dimethyl oxalate (DMO) over copper-silver catalyst supported on silica was studied. The Cu-Ag/SiO2 catalyst supported on silica sol was prepared by homogeneous deposition-precipitation of the mixture of aqueous cuprammonia complex and silica sol. The proper active temperature of Cu-Ag/SiO2 catalyst for hydrogenation of DMO was 523—623 K. The most preferable reaction conditions for methyl glycolate (MG) were optimized: temperature at 468—478 K, 40—60 mesh catalyst diameter, H2/DMO ratio 40, and 1.0 h-1 of LHSV.     

甲烷氧化偶联Na-W-Mn/SiO2催化剂的喇曼光谱

Ｎａ Ｗ Ｍｎ／ＳｉＯ２ 是甲烷氧化偶联反应的最好催化剂之一．该体系不仅具有良好的活化甲烷能力和Ｃ２ 烃选择性,且具有较好的稳定性并适合于加压反应 ［１ -３］．对于该催化剂,我们用不同的表征手段做了大量的研究,对各组分的作用及甲烷的活化机理都有了较深入的认识．我们也曾用Ｒａｍａｎ光谱对该体系进行过研究［４,５］,但由于焙烧过程中载体结构及伴随的振动光谱变化,使谱峰的解析出现错误,将载体结构变化出现的新峰归属成了钨氧四面体的畸变．最近我们在确认载体振动光谱及其变化的基础上又对该体系进行了细致的研究,确…     

Fe_2O_3/SiO_2对异辛醇氧化生成异辛酸反应的催化性能研究

采用浸渍法制备了系列的Fe_2O_3/SiO_2催化剂, 并用XRD, BET, TG-DTG和SEM等手段对催化剂进行了表征;考察了不同Fe负载量和焙烧温度的Fe_2O_3/SiO_2催化剂对异辛醇氧化生成异辛酸反应的催化活性的影响, 确定了最佳催化剂制备条件. 结果表明, Fe负载量为4%, 焙烧温度为500℃时, 催化剂活性组分Fe_2O_3的在载体上分散均匀, 晶粒大小基本一致, 催化剂比表面积较大, 催化剂活性达到最佳, 异辛酸选择性最高可达55.14%, 收率可达22.41%.     

Photocatalytic Synthesis of Hydrocarbon Oxygenates from C2H6 and CO2 over Pd-MoO3/SiO2 Catalyst

Pd-MoO3/SiO2 catalyst has been prepared using the method of incipient wetness impregnation. The photo absorbing behaviors and chemisorbing properties of the catalyst have been characterized by UV-vis spectra and TPD-MS experiments. The results indicated that metal Pd loaded on MoOe/SiO2 has a significant effect on the photo absorbing performance of MoO3/SiO2, and an obvious blue shift of the absorption edge is produced. Under UV irradiation, the chemisorption state of CO2 undergoes decomposing process to form CO at 481 K, and a two-site adsorption state of ethane can be formed at around 496 K. Photo-oxidation of ethane using carbon dioxide can mainly produce propanal, ethanol and acetaldehyde in the temperature range of 353-423 K. The presence of metal Pd improves the catalytic activity remarkably.     

Lacunary Keggin Polyoxotungstate as Reaction-controlled Phase-transfer Catalyst for Catalytic Epoxidation of Olefins

A new reaction-controlled phase-transfer catalyst system, lacunary Keggin polyoxotungstate [C7H7N(CH3)3]9PW9O34 has been synthesized and used for catalytic epoxidation of olefins with H2O2 as the oxidant. Infrared spectra were used to analyze the behavior of the phase transfer of catalyst. In this system, the catalyst not only can act as homogeneous catalyst but also as heterogeneous catalyst to be easily filtered and reused. The epoxidarion reaction is clean and exhibits high conversion and selectivity as well as excellent catalyst stability.     

磁性纳米TiO2/SiO2/NiFe2O4的制备及其催化性能

采用溶胶凝胶法制备了核壳结构磁性纳米TiO2/SiO2/NiFe2O4催化剂.利用XRD、TEM、VSM等手段对样品的粒径、晶体结构、磁性和光催化性能进行了研究.结果表明:SiO2/NiFe2O4的加入抑制了TiO2纳米粒子的生长,使晶粒尺寸减小,促进了锐钛矿相向金红石相的转变,催化剂的回收率和光催化性能均得到提高.光催化实验结果表明,当SiO2/NiFe2O4的负载量为15%时,焙烧温度为500℃时对亚甲基兰的脱色率最高.