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a dry 10 mL glass tube reactor with a stirring bar. The tube reactor
was sealed and evacuated by a vacuum pump. Then CO gas was
introduced through a balloon being attached to the air inlet of
the reactor. Finally, the reactor with carbon monoxide balloons
was put into a stirred oil bath at 80 ꢀC for 24 h (the subsequent
reaction process is the same as that discussed above for the
carbonylation reaction). In the case of amines on solid phase,
acetonitrile was used as solvent. The amount of amine is 2 equiv.,
the reaction process remains unchanged. The reaction mixture
was separated from the catalyst by simple centrifugation, and the
liquid was analyzed by GC, GC–MS, and 1H NMR techniques.
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The recycling of palladium catalyst
The recyclability of Pd/SiO2 for the synthesis of amide was
carried out under the optimized reaction conditions. Aer
completing the reaction, the reactor was cooled to room
temperature and the remaining CO gas was carefully vented out
to a hood aer 24 hours. The catalyst was separated from the
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reaction cycle.
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Acknowledgements
This work was nancially supported by the National Nature
Science Foundation of China 21643009, the National Basic
Research Program of China 2014CB239303, the Natural Science
Foundation of Fujian Province of China 2015J01046, and the
Independent Research Project of State Key Laboratory of Pho-
tocatalysis on Energy and Environment 2014B01.
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