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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

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