铑配合物催化丁烯氢甲酰化性能的研究

制备了一系列铑配合物,并对其催化丁烯氢甲酰化的催化性能进行了研究.在1-丁烯的反应中,RhCl(PPh3)3和trans-RhCl(CO)(PPh3)2的反应速度很慢,而RhH(CO)(PPh3)3、Rh(CO)2(acac)和 Rh(CO)(acac)(PPh3)三者反应速度都很快.而不同丁烯原料氢甲酰化的反应速度也各不相同,反应速度依次为1-丁烯》2-丁烯》异丁烯.     

双亚磷酸酯和双膦混合配体在丁烯氢甲酰化反应中的应用研究

考察了双亚磷酸酯配体Bisphosphite 1、Bisphosphite 2及双膦配体DPPE、DPPP、DPPB、BISBI在丁烯氢甲酰化反应中的反应活性和选择性,并对双亚磷酸酯配体和双膦配体进行混合,应用到丁烯氢甲酰化反应当中,对混合配体进行筛选发现Bisphosphite 1与DPPB混合配体的反应效果最佳,明显提高了1-丁烯氢甲酰化产物醛的正异构比,并通过31P NMR等方法推测了混合配体与铑配位的关键配合物中间体.通过正交实验优选了铑催化剂浓度、Bisphosphite 1浓度与DPPB浓度,其优化的催化剂配方对1-丁烯氢甲酰化的正异构比达到76.3,平均TOF 1821 h-1.     

一种新型双膦亚磷酸酯配体的合成及在1-己烯氢甲酰化反应中的应用

以4,4'-二羟基二苯丙烷和2,4-二叔丁基苯酚为原料合成了一种新型双膦亚磷酸酯配体,并用此配体和Rh(acac)(CO)2原位形成的催化体系催化1-己烯的氢甲酰化反应.系统考察了反应温度、压力、P/Rh和溶剂四种反应参数对催化体系的催化性能影响.选择了最佳的反应条件,在铑浓度为0.75×10-3mol/L、P/Rh比为10、温度100℃、压力(H2/CO=1)2.0MPa的条件下反应1.0h,在溶剂甲苯中1-己烯的转化率可达到100%,醛选择性为98.7%,TOF为3498.6h-1.在相同的条件下与以三苯基膦和单膦亚磷酸三(2,4-二叔丁基苯基)酯为配体的铑催化剂相比较,以新型双膦亚磷酸酯为配体的铑催化剂的催化活性是PPh3的1.6倍,而与亚磷酸三(2,4-二叔丁基苯基)酯的催化活性相当.     

双亚磷酸酯和双膦组合配体在丁烯氢甲酰化反应中的应用研究

考察了双亚磷酸酯配体Biphephos及双膦配体DPPE、DPPP、DPPB、BISBI在丁烯氢甲酰化反应中的反应活性和选择性,并对双亚磷酸酯配体和双膦配体进行组合,应用到丁烯氢甲酰化反应当中,对组合配体进行筛选发现Biphephos与DPPB组合配体的反应效果最佳,明显提高了产物醛的正异构比。通过正交实验进一步优选了铑催化剂浓度、Biphephos浓度与DPPB浓度,其优化的催化剂配方的正异构比达到76.3,平均TOF1821h-1。     

聚氧乙烯基取代膦—铑配合物催化有机单相苯乙烯氢甲酰化反应研究

基于非离子表面活性膦配体的临界溶解温度特性 ,研究了以 Rh Cl3· 3H2 O为催化剂前体、聚氧乙烯基取代膦为配体原位合成的膦铑配合物催化剂 ,对有机单相体系中苯乙烯氢甲酰化反应的催化性能 .考察了反应温度、压力及不同聚氧乙烯基取代膦 -铑配合物催化剂对反应的影响 .以 Rh/PETPP配合物为催化剂时 ,在 T=10 0℃ ,p=6 .0 MPa (CO/H2 =1∶ 1)条件下 ,反应 3.5 h后 ,烯烃转化率和产物醛收率可分别达 96 .7%和 92 .6 %     

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,...     

新型膦配体PDBPDS在氢甲酰化反应中催化剂配体性能的研究

用量子化学 AMI方法优化了 1 -苯基二苯并膦二磺化产物 ( PDBPDS)和三磺化三苯基膦 ( TPPTS)的几何构型 .比较两种化合物的空间结构和电子结构发现 ,在氢甲酰化铑膦催化反应体系中 ,PDBPDS的配体性能优于 TPPTS.首次研究了以 PDBPDS为配体的铑膦催化剂对丙烯氢甲酰化反应的催化性能 ,考察了反应温度、压力、膦铑物质的量比和搅拌速度对催化活性和选择性的影响 .结果表明 ,在 2 .0 MPa,1 0 0℃ ,膦铑物质的量比为 35 ,搅拌速度为 5 0 0 r/min及 V( H2 ) /V( CO) =1 /1的条件下 ,催化活性可达到 2 80 0 g(丁醛 ) /[g(铑 )·h],正异构产物物质的量比为 1 2 .3,在相同条件下与传统的三磺化三苯基膦 ( TPPTS)为配体的铑膦催化剂相比 ,催化活性和选择性提高了 2倍 .反应结束后 ,有机相和水相分离简单 ,有机相铑浓度仅为3.6× 1 0 - 8mol/L,有效地解决了铑流失问题 ,表明 PDBPDS是极具开发前景的新型水溶性配体     

硅胶键合膦的制备及其对铑络合物催化1-辛烯氢甲酰化反应的影响

以硅胶为载体, 采用键合接枝法将2-(二苯膦基)乙基三乙氧基硅烷(DPPES)共价键合于硅胶表面, 制备了性能优良的硅胶键合型膦配体(以SiO₂(PPh₂)表示). 以SiO₂(PPh₂)为配体, Rh(acac)(CO)₂ (acac:乙酰丙酮)为催化前体, 负载铑膦络合物催化剂(SiO₂(PPh₂)/Rh)在1-辛烯氢甲酰化反应中原位生成. 对生成的负载型催化剂和硅胶键合型膦配体进行了傅里叶变换红外(FTIR)光谱表征, 考察了膦/铑摩尔浓度比([P]/[Rh])、温度等因素对铑催化的长链1-辛烯氢甲酰化反应的影响. 结果表明, 膦/铑摩尔浓度比的增加能显著提高反应的成醛选择性, 降低铑的流失. 在[P]/[Rh]=12、363 K、2.0 MPa、1.5 h 的温和反应条件下, 1-辛烯转化率和成醛选择性分别可达98.4%和95.3%, 其催化活性与DPPES或三苯基膦(TPP)作配体时的均相铑催化相近. 催化剂循环4 次后, 反应活性无明显下降, 1-辛烯转化率均在97.0%左右, 经电感耦合等离子体原子发射光谱(ICP-AES)检测,有机相中铑流失低于0.1%.     

长链烷基二苯基膦—铑配合物催化烯烃氢甲酰化反应研究

研究了烷基二苯基膦-铑配合物RhCl(CO0(n-C8H17PPh2)2(1)和RhCl(Co)(n-C12H25PPh2)2（2）对1-辛烯氢甲酰化反应的催化性能。结果表明,配合物1比2具有更高的催化活性,而配合物2对生成正构醛的选择性更好;当催化剂浓度或膦/铑比增加时,配合物2催化成正构醛的选择性呈下降趋势,显示出与以PPh3为配体时的不同的性能。     

新型配体1—苯基二苯并膦在丙烯氢甲酰化均相反应中的应用研究

将 1-苯基二苯并膦 (PDBP)作为膦配体用于丙烯氢甲酰化反应中 ,系统研究了反应温度、压力、铑浓度、搅拌速率对产物丁醛收率的影响 .在铑浓度为 4.0× 10 - 6 、 P/ Rh比为 15 0、温度 10 0℃、反应压力 2 .0 MPa的条件下 ,丙烯转化率可达 90 % ,催化活性为 2 6 0 9g丁醛 / (g Rh· h) ,正丁醛和异丁醛的比达 9.5 .在相同的条件下与工业上广泛采用的以三苯基膦为配体的铑催化剂相比较 ,以 PDBP为配体的铑催化剂的活性和选择性分别是它的 1.44倍和 1.90倍 .证明了 PDBP是一个很有发展前景的羰基合成的膦配体     

烯烃氢甲酰化催化剂活性物种的原位1H NMR研究

The rhodium-phosphine complex catalyst Rh(CO)(acac)(PPh3)(Ⅰ) for 1-hexene hydroformylation was studied under the following reaction conditions: CO/H2=1(mole rate), pressure 1.0 MPa, temperature 25-120℃, by using the pressurized in-situ 1H NMR technique. Experimental results indicated that the formation of a rhodium hydride complex from (Ⅰ) began at room temperature and its amount increased with increasing of reaction temperature. This intermediate complex began to decompose at 100℃ and disapeared completely at 120℃. The intensity change of the proton signal was parallel to catalytical activity in hydroformylation of olefins. Under pure CO pressure the proton signal of Ph-H bond was not observed. There was a 0.2 ppm difference in proton chemical shifts of Rh-H bond under pure H2 pressure and under H2+CO pressure. The results showed that the rhodium-hydride carbonyl complex is the active intermediate in the industrial hydroformylation process.     

Kinetics of hydroformylation of 1-decene using carbon-supported ossified HRh(CO)(TPPTS)3 catalyst

The kinetics of hydroformylation of 1-decene has been investigated using a carbon-supported ossified HRh(CO)(TPPTS)₃/Ba catalyst in a temperature range of 343–363 K. The effect of concentration of 1-decene, catalyst loading, partial pressure of H₂ and CO, and stirring speed on the reaction rate has been investigated. A first-order dependence was observed for catalyst concentration and hydrogen partial pressure. The rate showed a typical case of substrate inhibition for high 1-decene concentration. The rate varied with a linear dependence on P_CO up to a CO partial pressure of 5–6 MPa in contrast to the general trends; for most of the rhodium-phosphine catalyzed hydroformylation reactions, severe inhibition of rate is observed with an increase in CO pressure. A rate equation has been proposed, which was found to be in good agreement with the observed rate data within the limit of experimental errors. The kinetic parameters and activation energy values have been reported.     

Kinetics of hydroformylation of camphene using rhodium-phosphite catalyst

Kinetics of hydroformylation of camphene was investigated in the presence of [Rh(CO)₂(acac)]/P(OPh)₃ catalyst in a temperature range of 363–383 K. The influence of parameters such as stirring speed, camphene, catalyst, ligand concentrations, and partial pressures of H₂ and CO on the activity and selectivity of the catalyst has been studied. The rate showed a first-order dependence with respect to catalyst and camphene concentrations. The effect of partial pressure of hydrogen showed fractional order dependence. The plots of rate versus excess ligand, that is, (P(OPh)₃) concentration and rate versus CO partial pressure passed through maxima and showed typical substrate/ligand inhibited kinetics. An empirical rate equation has been proposed and found to be in good agreement with the observed rate data. The kinetic parameters and activation energy were also evaluated.     

铑膦配合物的加压原位核磁氢谱研究

在近似工业反应条件下(H2/CO=1:1, 1.0MPa, 70℃), 应用加温加压原位核磁共振技术, 考察了铑膦配合物催化剂HRh(CO)(PPh3)3-PPh3体系的烯烃醛化反应。结果表明,在烯烃醛化反应条件下, 反应液中存在羰基氢化铑中间配合物, 并在^1H NMR获得了该配合物中Rh-H键的质子讯号。     

Immobilization of Homogeneous Catalysis on Phosphinated MCM-41

Homogeneous catalysis Rh(PPh3)3Cl immobilized on MCM-41 modified with (OEt)3Si(CH2)3PPh2 results in a stable hydrogenation catalyst with turn over frequency (TOF) three times higher than that of Rh(PPh3)3C1 in the hydrogenation of cyclohexene. Leaching of the catalyst is only a minor factor with leaching rate 0.04 % for each cycle. However, immobilization of Rh(PPh3)2(CO)C1 on similar support can only have catalytic hydroformylation properties for the first few cycles. Decay of the catalyst is due to largh leaching rate with totally 22.4 % of Rh leached for the first three cycles.     

Room-temperature regioselective C-H/olefin coupling of aromatic ketones using an activated ruthenium catalyst with a carbonyl ligand and structural elucidation of key intermediates

Mechanistic studies of the ruthenium-catalyzed reaction of aromatic ketones with olefins are presented. Treatment of the original catalyst, RuH(2)(CO)(PPh(3))(3), with trimethylvinylsilane at 90 °C for 1-1.5 h afforded an activated ruthenium catalyst, Ru(o-C(6)H(4)PPh(2))(H)(CO)(PPh(3))(2), as a mixture of four geometric isomers. The activated complex showed high catalytic activity for C-H/olefin coupling, and the reaction of 2'-methylacetophenone with trimethylvinylsilane at room temperature for 48 h gave the corresponding ortho-alkylation product in 99% isolated yield. The activated catalyst was thermally robust and showed excellent catalytic activity under refluxing toluene conditions. (1)H and (31)P NMR studies of the C-H/olefin coupling at room temperature suggested that an ortho-ruthenated complex, P,P'-cis-C,H-cis-Ru(2'-(6'-MeC(6)H(4)C(O)Me))(H)(CO)(PPh(3))(2), participated in the reaction as a key intermediate. Isotope labeling studies using acetophenone-d(5) indicated that the rate-limiting step was the C-C bond formation, not the C-H bond cleavage, and that each step prior to the reductive elimination was reversible. The rate of C-H/olefin coupling was found to exhibit pseudo first-order kinetics and to show first-order dependence on the ruthenium complex concentration.     

The electron-poor phosphines P{C6H3(CF3)2-3,5}3 and P(C6F5)3 do not mimic phosphites as ligands for hydroformylation. A comparison of the coordination chemistry of P{C6H3(CF3)2-3,5}3 and P(C6F5)3 and the unexpectedly low hydroformylation activity of their rhodium complexes

The fluoroaryl phosphines P{C6H3(CF3)2-3,5}3 (La) and P(C6F5)3 (Lb) form the complexes trans-[MCl2(La)2] and trans-[MCl2(Lb)2](M = Pd or Pt) which have been isolated and fully characterised. 31P NMR studies of competition experiments show that the stability of trans-[PdCl2L2] is in the order L = Lb< La 相似文献   

The Performance of Rhodium Complex—diphosphine Systems in the Hydroformylation of 1—Dodecene

The catalytic performances of four HRh(CO)(PPh3)3-diphosphine (BISBI,BDPX,BDNA and BINAP) systems in 1-dodecene hydroformylation were investigated and compared with HRh(CO)(PPh3)3-PPh3 system.The catalyst system HRb(CO)(PPh3)3-BISBI exhibited very hig regioselectivity for the formation of linear aldehyde.