GAS-PHASE OXIDATION OF BENZENE TO PHENOL UNDER THE SIMULTANEOUS FEEDING OF HYDROGEN AND OXYGEN .3. CATALYST PREPARED FROM CU(II) PHOSPHATE

The performance of silica supported Pd-Cu composite catalyst developed previously for direct oxidation of benzene to phenol has been improve d by changing the copper ion source from Cu(II) sulfate to Cu(II) phos phate and by additional impregnation of phosphoric acid. The reaction proceeds under the simultaneous feeding of benzene, hydrogen and oxyge n at 200-degrees-C with a rate of phenol production ca. 0.4 mmol h-1 ( g-cat)-1, which is ten times greater than that we have reported previo usly with a catalyst prepared from Cu(II) sulfate. With this catalyst, complete oxidation to carbon dioxide is also retarded to increase the selectivity of phenol. The improvement of catalytic activity arises a pparently from the diminution of the yield of water and is ascribed to the presence of a thin liquid film over the silica surface.