Carbon−Carbon Coupling Reactions Catalyzed by Heterogeneous ...
Carbon−Carbon Coupling Reactions Catalyzed by Heterogeneous ...
Carbon−Carbon Coupling Reactions Catalyzed by Heterogeneous ...
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<strong>Heterogeneous</strong> Pd <strong>Catalyzed</strong> C−C <strong>Coupling</strong> <strong>Reactions</strong> Chemical Reviews, 2007, Vol. 107, No. 1 151<br />
Djakovitch and Köhler studied a series of palladium<br />
catalysts obtained <strong>by</strong> ion exchange at Na- or H-zeolites<br />
(mordenite, Y) with Pd(NH3)4Cl2. Pd-modified zeolites<br />
exhibited a high activity comparable to homogeneous<br />
catalysis toward the Heck reaction of aryl bromides with<br />
styrene for small Pd concentrations. 10,16-18,21,27 The zeolite<br />
obviously controlled the selectivity of the reaction. 16 Reaction<br />
temperature plays an important role. No substantial leaching<br />
was observed in most cases. But evidence for dissolved<br />
molecular Pd species being responsible for the catalysis was<br />
found. 27 The catalysts could be easily separated from the<br />
reaction mixture and reused up to five times without a<br />
considerable loss in activity. Some of the results are<br />
summarized in Table 39. 16,18 The catalyst could also be<br />
applied to Heck coupling of 4-chloroacetophenone but did<br />
not perform so well even at higher temperatures. 18<br />
Table 39. Heck Reaction of Various Aryl Bromides with Alkenes<br />
<strong>by</strong> Pd-Zeolite Catalysts<br />
GLC yielda T<br />
(%)<br />
Pd-zeolite R R′ (°C) 101 102 103<br />
[Pd(0)]-NaY F Ph 140 89.4 (86.0) 0.9 8.2<br />
100 85.1 (80.1) 1.0 7.9<br />
[Pd(NH3)4] 2+ -NaY F Ph 140 93.0 (80.9) 1.0 8.8<br />
100 94.5 (89.5) 0.7 6.7<br />
[Pd(OAc)2]-NaY F Ph 140 79.2 (81.2) 0.9 7.2<br />
100 57.6 (39.9) 0.4 3.9<br />
[Pd(NH3)4] 2+ -NaY OMe Ph 140 81.2 (75.8) 9.5 9.5<br />
[Pd(NH3)4] 2+ -NaY<br />
[Pd(NH3)4]<br />
NO2 Ph 140 94.8 (89.8) 1.1 4.1<br />
2+ -NaY<br />
[Pd(NH3)4]<br />
H Ph 140 84.9 (75.8) 0.7 6.5<br />
2+ -NaY<br />
[Pd(NH3)4]<br />
H BuO 140 25.7 20.4 12.4<br />
2+ -NaY H CO2Me 140 91.0 (69.4) 0.5 0.4<br />
a Isolated yields in parenthesis.<br />
K + - and Cs + -exchanged X-zeolites containing PdCl2<br />
(bifunctional catalysts) developed <strong>by</strong> Garcia and co-workers<br />
allowed implementation of the Heck reaction of iodo- and<br />
bromobenzene with styrene in the absence of an extrinsic<br />
base. 49 Obviously, sites of the support act as base in these<br />
cases. No leaching was observed. The activity of the used<br />
catalyst could be regained to a large extent <strong>by</strong> reactivation<br />
<strong>by</strong> washing with water. As an alternative to styrenes 104,<br />
the formation of 1,1-diphenylethene regioisomer can be<br />
favored <strong>by</strong> high Pd loadings (Scheme 27). The authors also<br />
investigated the effect of pore size and Pd loading of different<br />
zeolites on the catalytic activity. When DMF was used as<br />
solvent, the catalytic activity was mainly attributed to leached<br />
Pd.<br />
Scheme 27<br />
In contrast to the conclusions of Djakovitch and Köhler<br />
to the nature of catalysis of Pd on zeolites (molecular Pd<br />
species in solution, Vide supra), Dams and co-workers. 61,150<br />
and Okumura 84 et al. assumed that the heterogeneous nature<br />
of the catalysis with Pd-zeolites in Heck reactions largely<br />
depended on the pretreatment of the catalyst, the oxidation<br />
state of Pd, the solvent, and the base. For a critical review<br />
about this subject favoring homogeneous catalysis as the<br />
general mode of action see Jones et al. 36 The excellent<br />
performance of Pd(0)/HY was attributed to the formation of<br />
stable Pd13 clusters kept inside the supercage of HY. 84 This<br />
catalyst had to be generated <strong>by</strong> calcination in O2 and<br />
reduction <strong>by</strong> H2 before it could be reused. With tributylamine<br />
as the base in toluene, the Heck olefination with Pd-<br />
(NH3)4 2+ -zeolites (0.4 wt % Pd; mordenite, Y, ZSM-5) and<br />
Pd(0)-mordenite (0.4 and 4 wt % Pd) were concluded as<br />
truly heterogeneous. 61,150 Pd leaching from the zeolites was<br />
evaluated in a very strict filtrate activity test. It was clearly<br />
related to the presence of oxidized Pd(II) in an all-oxygen<br />
environment, that is, ionic Pd(II) or PdO. The heterogeneous<br />
reactions with the zeolite-supported catalyst can be accelerated<br />
<strong>by</strong> the addition of a quaternary ammonium salt promoter.<br />
The catalytic activity of Pd-zeolites in Heck reaction<br />
followed the order<br />
2+ 2+<br />
Pd(NH3 ) 4 -Y > Pd(NH3 ) 4 -mordenite ><br />
2+<br />
Pd(NH3 ) 4 -ZSM-5<br />
Pd on porous glass served as a useful, reusable catalyst<br />
for Heck reaction of iodobenzene and 4-bromoacetophenone<br />
with styrene and allylic alcohol allowing the reaction to be<br />
carried out in the presence of air. 24<br />
3.4. Pd on Modified Silica (Organic−Inorganic<br />
Hybrid Support)<br />
Organochemically modified silica can also serve as solid<br />
support for Pd catalysts. Silica was modified <strong>by</strong> various<br />
chlorohydrosilanes (trichloro-, dichloromethyl-, chlorodimethyl-,<br />
dichlorophenyl-, and chlorodiphenylsilane). The<br />
resulting materials, which were modified at the surface <strong>by</strong><br />
methyl or aryl groups, were treated with saturated solutions<br />
of PdCl2 in methanol to form different Pd-on-silica catalysts<br />
with various Pd loadings (Pd/SiO2Me, Pd/SiO2Me2, Pd/SiO2-<br />
Ph, Pd/SiO2Ph2).<br />
Pd/SiO2Ph exhibited high catalytic activity in the Heck<br />
reaction of aryl iodides and bromides with styrene or methyl<br />
acrylate (Table 40). 151,152 The catalyst could be recovered<br />
and reused.<br />
Table 40. Catalytic Performance of 0.3% Pd-Silica Catalysts in<br />
Heck <strong>Coupling</strong><br />
Pd cat. R1 ,X R2 t (h) conv (%) select. (%)<br />
Pd/SiO2Me<br />
Pd/SiO2Me2<br />
Pd/SiO2Ph<br />
Pd/SiO2Ph2<br />
Pd/SiO2Me<br />
Pd/SiO2Me2<br />
Pd/SiO2Ph<br />
Pd/SiO2Ph2<br />
Pd/SiO2Me<br />
Pd/SiO2Ph<br />
Pd/SiO2Me<br />
Pd/SiO2Ph<br />
H, I<br />
H, I<br />
H, I<br />
H, I<br />
NO2,Br<br />
NO2,Br<br />
NO2,Br<br />
NO2,Br<br />
Ac, Br<br />
Ac, Br<br />
H, I<br />
H, I<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
CO2Me<br />
Ph<br />
Ph<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
2<br />
5<br />
5<br />
84<br />
54<br />
97<br />
51<br />
100<br />
68<br />
100<br />
66<br />
67<br />
75<br />
58<br />
80<br />
99<br />
99<br />
99<br />
99<br />
99<br />
99<br />
99<br />
99<br />
99<br />
99<br />
86<br />
83<br />
As an alternative to mercaptopropyl modification, also<br />
arsanopropyl or methylselenoundecyl groups were introduced