Table 8. Catalytic Testing Results upon Reuse, Metal Leaching and XPS-Derived Au/Pd of PAA-Stabilized 1%AuPd/C Catalyst Prepared with or without Acid and Corresponding Metal Leaching (Au, Pd)a.
| leaching (%) |
|||||||
|---|---|---|---|---|---|---|---|
| catalyst | use (−) | actual metal loading (wt %) | productivityb (molH2O2 mmol–1Metal h–1) | degradationc (molH2O2 mmol–1Metal h–1) | Au | Pd | Au/Pd (−) |
| 1%AuPd/GNP | 1 | 0.48 | 1.9 | 1.7 | 0 | 0.06 | 0.2 |
| 2 | 0.1 | 0.3 | 0.2 | ||||
| 1%AuPd/GNP-H+ | 1 | 1.00 | 2.8 | 6.4 | 0 | 0.04 | 0.8 |
| 2 | 0.9 | 3.1 | 0.8 | ||||
| 1%AuPd/KBB | 1 | 0.21 | 1.2 | 3.3 | 0 | 0.12 | 1.1 |
| 2 | 0.1 | 0.1 | N/Ad | ||||
| 1%AuPd/KBB-H+ | 1 | 1.00 | 1.9 | 7.3 | 0 | 0.10 | 1.5 |
| 2 | 1.4 | 2.8 | 1.3 | ||||
Metal leaching calculations are based on the actual metal loading of the catalyst.
H2O2 direct synthesis reaction conditions: catalyst (0.01 g), H2O (2.9 g), MeOH (5.6 g), 5%H2/CO2 (2.9 MPa), 25%O2/CO2 (1.2 MPa), 0.5 h, 2 °C, 1200 rpm.
H2O2 degradation reaction conditions: catalyst (0.01 g), H2O2 (50 wt % 0.68 g), H2O (2.22 g), MeOH (5.6 g), 5% H2/CO2 (2.9 MPa), 0.5 h, 2 °C, 1200 rpm.
No Pd detected.