Table 1. Selective Hydrogenation of 4-Nitrostyrene over Different Au Catalystsa.
sel./%c |
|||||
---|---|---|---|---|---|
entry | catalystsb | con./%c | 1 | 2 | 3 |
1 | NiAlO-2-500 | 0.3 | 58.2 | 25.9 | 15.9 |
2 | 0.43% Au/NiAlO-2-500 | 98.4 | 98.1 | 0.2 | 1.7 |
3 | 0.38% Au/NiAlO-2-500-SD | 29.4 | 95.0 | 1.5 | 3.5 |
4 | 0.15% Au/NiAlO-2-500 | 18.9 | 82.9 | 16.2 | 2.9 |
5 | 0.68% Au/NiAlO-2-500 | 98.1 | 94.6 | 0.3 | 5.1 |
6 | 0.38% Au/NiAlO-3-500 | 40.5 | 63.6 | 35.3 | 1.1 |
7 | 0.44% Au/NiAlO-4-500 | 74.8 | 2.0 | 94.5 | 3.5 |
Reaction conditions: p(H2) = 1.0 MPa; T = 100 °C; catalyst 0.1 g; 4-nitrostyrene 100 μL; toluene 5 mL; stirring speed = 500 rpm; and reaction time 4 h.
The molar ratio of Ni to Al and the Au actual loading were determined by ICP–AES.
The conversion of 4-nitrostyrene and selectivity toward the products were determined by gas chromatography (GC) and GC–mass spectrometry (MS). No other byproducts were observed, and the carbon mass balance of about 96% was obtained by using o-xylene as an internal standard.