“…The resulting milled mixtures were calcined at 400 • C for 2 h. He and co-workers [169] have successfully produced Pd 1 /ZnO, Ru 1 /ZnO, Rh 1 /ZnO, and Pd 1 /CuO via the afore-proposed procedure. Interestingly, no significant scaling-up effect was observed as the kg-scale, Pd 1 /ZnO exhibits almost the same catalytic performance (about 92% styrene yield via hydrogenation of phenylacetylene) as compared to the small-scale fabrication (10 g-scale) under the same conditions (10 mg of catalyst and 0.5 mmol of phenylacetylene were used, the reaction was conducted for 20 min at a temperature of 50 • C) The ball-milling method has been successfully applied to the fabrication of SACs for oxidation of benzene [99], hydrogenation of acetylene [170], phenylacetylene [169], 2-methyl-3-butyn-2-ol [171], glycerol hydrogenolysis [172], organic pollutant degradation [173], Fenton-like reaction [174], HER [175], ORR [176,177], CO oxidation [169], and photoreaction [128]. Nevertheless, (a) restricted scalability especially for co-catalyst synthesis which inevitably involves liquid-phase processes [128]; and (b) the occurrence of metallic impurities from the machinery on the catalysts are the other common weaknesses of this approach [178].…”