DOI: 10.1039/C3CC46097E
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complex degradation/rearrangment.
Table 1. Solutions analyzed by ICP after each catalytic run.
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Gold loaded in f-MWNTs 5 before catalysis: 82.4 ppm. [a] Leaching of gold in ppm
5 run by run. [b] Percentage of gold lost run by run (Au leaching (ppm) divided by the
initial quantity: 82.4 ppm)
Heterogenization of Gold (I) complexes is rare irrespective of
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10 functionalized coordination polymers and delaminated zeolite
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15 throughout the catalytic cycles, which falls in the range of the
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unravelled which allows the gold complex to act as soluble
species. Nevertheless, the covalent anchoring realized in the
25 present work enabled to obtain significant advantages.
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higher conversion along the runs were obtained. The gold
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Conclusions
A gold complex with a pendant amine group was designed for
35 its covalent anchoring onto modified MWNTs in order to give a
supported homogeneous catalyst. Compared to its homogeneous
counterpart, the selectivity to the cyclized products was
unchanged but the activity was considerably improved. Recycling
is conceivable and is combined with a fairly low gold leaching.
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