Angewandte
Communications
Chemie
Table 1: Comparison of homogeneous and MOFs systems for the
desulfitative oxidative coupling reaction between 1a and 2a.[a]
conducted to prove the change of valence state of Cu and Pd
species (Figures 1d,e). The absence of two satellite peaks at
the copper 2p level and the presence of two new peaks (334
and 341 eV) at the palladium 3d level demonstrate that
[11]
almost all CuII has been converted into CuI
and that
a number of Pd species were in the reduced form.[14]
Entry Catalytic system
Yield[%][b] TON[c]
Decreasing the loading of UiO-67-phen-Pd/Cu(1:2) to
1 mol% (based on Pd) could also catalyze the reaction
without compromising the reactivity, leading to a 10 times
higher TON and 50 times less Cu consumption than
homogeneous counterparts (Table 1, entries 6 and 15). Fur-
ther lowering the catalyst loading to 0.2 mol% leads to
a TON of 230 (entry 16). The above findings indicate that the
PdII and ETM species in the framework display prominent
activities, especially at low catalyst/substrate ratio, probably
as a result of the confinement effect of the framework and/or
high surface utilization of MOF nanoparticles. Note that UiO-
67-phen-Pd/Cu(1:2) could be reused for at least five cycles
without apparent loss of activity (see Figure S10). ICP-MS of
the reaction filtrate showed negligible leaking of PdII and CuII
ions into the solution, confirming the heterogeneous nature of
this reaction. The PXRD pattern and N2 adsorption isotherm
of the recovered catalyst revealed that the porosity and
crystallinity were maintained after the catalysis (Figure 1a;
see Figure S3). XPS data imply that the oxidation states of Pd
and Cu remain at + 2 after the catalysis (Figures 1d,e), and
the TEM image showed no detectable Pd0 nanoparticles over
the framework (see Figure S9).
Next, the general applicability was examined, and a series
of different sodium arylsulfinates bearing electron-donating
and electron-withdrawing groups at the para-position were
found to be suitable substrates, producing the corresponding
b-aryl ketones in good to excellent yields (see Table S1, 3b–
e). Phenyl-substituted allyl alcohol was well tolerated to this
reaction, giving the desired product in moderate yield (see
Table S1, 3 f). An aliphatic allyl alcohol with an elongated
chain could also be converted into the corresponding product
in excellent yield (see Table S1, 3g). Besides, allyl primary
alcohol was found to be active, resulting in the formation of b-
aryl aldehyde in good yield (see Table S1, 3h).
Homogeneous system[d]
1[e]
2
3
4
5
Pd(TFA)2 [10 mol%]/Cu(TFA)2 [100 mol%] 80
8
Pd(TFA)2 [10 mol%]/Cu(TFA)2 [60 mol%]
Pd(TFA)2 [10 mol%]/Cu(TFA)2 [20 mol%]
Pd(TFA)2 [10 mol%]/Cu(TFA)2 [10 mol%]
Pd(TFA)2 [10 mol%]
52
20
11
6
5.2
2
1.1
0.6
4
6
Pd(TFA)2 [1 mol%]/Cu(TFA)2 [2 mol%]
4
MOFs system
7
UiO-67-phen (or no catalyst)
–
87
88
71
52
–
–
8
9
UiO-67-phen-Pd/Cu(1:6) [10 mol% Pd]
UiO-67-phen-Pd/Cu(1:2) [10 mol% Pd]
UiO-67-phen-Pd/Cu(1:1) [10 mol% Pd]
UiO-67-phen-Pd/Cu(1:0) [10 mol% Pd]
UiO-67-phen-Pd/Cu(0:1) [20 mol% Cu]
UiO-67-phen-Pd/Cu(1:2) [10 mol% Pd]
UiO-67-phen-Pd/Cu(1:2) [5 mol% Pd]
UiO-67-phen-Pd/Cu(1:2) [1 mol% Pd]
UiO-67-phen-Pd/Cu(1:2) [0.2 mol% Pd]
8.7
8.8
7.1
5.2
–
10
11
12
13[e]
14
15
16
38
86
89
46
3.8
17.2
89
230
[a] The reaction conditions were: 1a (0.5 mmol), 2a (2 mmol), O2
(1 atm), 1,4-dioxane (3 mL), 1008C and 20 h. [b] Determined by GC-MS
with n-dodecane as internal standard. [c] TON (turnover number): moles
of product per mole of catalyst used. [d] For homogeneous system, 4,7-
dimethyl-1,10-phenanthroline (20 mol%) was added. [e] Under anaero-
bic conditions.
(entries 3 and 9). As stoichiometric quantities or an excess
amount of the ETM are usually required to regenerate PdII in
homogeneous systems,[3b] the decreased ETM loading should
reduce the interaction between Pd0 and the ETM in solution,
leading to an unfavorable electron transfer and thus a dra-
matic decrease in activity. For the MOF system, the aggre-
gation of the in situ generated Pd0 should be prohibited by the
MOFs site isolation, and the fast electron transfer from Pd0 to
adjacent Cu2+ atoms should be achieved given their close
positioning within the confined pores of UiO-67-phen, even at
lower Cu2+ loadings. Although further reduction in the
amount of CuII to 10 mol% leads to slightly decreased yield
(entry 10), the MOF still outperforms the homogeneous
system.
Based on above results and previous reports,[7] we propose
a plausible mechanism of the Pd-catalyzed oxidative coupling
reaction within UiO-67-phen-Pd/Cu(1:2) (Scheme 3). The
aromatic sulfinic sodium is firstly coordinated to PdII in the
MOF with the extrusion of SO2. Then, the Heck-type
insertion of the allyl alcohol to the arylpalladium complex I
occurrs, affording the s-allkylpalladium complex II. The
selective b-hydride elimination of II gives the enol complex
III, which subsequently changes to IV with the transfer of
hydrogen to the a-carbon atom by spontaneous insertion of
2CuII-[MOF]-PdIIH. Either elimination of IV from the a-OH
or an anion-mediated reductive elimination is possible to
afford the final product, accompanied by the generation of
a Pd0 species. Different from a homogeneous system, the
efficient catalyst cycle was accomplished through the fast
electron transfer within the MOF. Initially, the in situ
generated Pd0 is prohibited from fast aggregation by the
MOFs catalytic site isolation. Subsequently, two electrons
transfer immediately from the generated Pd0 to adjacent CuII
When O2 (1 atm) was utilized as the sole oxidant, UiO-67-
phen-Pd/Cu(1:0) still gave
a moderate yield (Table 1,
entry 11), while only 6% yield could be observed for the
homogeneous system (entry 5). These findings distinctly
suggest a different behavior of O2 within MOF relative to
the homogeneous system. The entrapment of O2 within UiO-
67-phen-Pd/Cu(1:0) (see Figure S5) may form a local high-
pressure O2 atmosphere within the framework, thus enhanc-
ing the electron-transfer efficiency between O2 and Pd0, as
high-pressure O2 has been evidenced to increase the reox-
idation rate of Pd0 in homogeneous systems.[13] Additionally,
when UiO-67-phen-Pd/Cu(1:2) was utilized under anaerobic
conditions, an obviously reduced yield was observed
(entry 13). XPS investigation of this recovered catalyst was
Angew. Chem. Int. Ed. 2019, 58, 1 – 5
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