Table 1.
cat | cat./11 (ppm) | time (min)b | conv.(%)c | selectivity (%)d | yield (%)e | TONf |
---|---|---|---|---|---|---|
1 | 100 | 120 | 58 | 93 | 54 | 5400 |
1 | 35 | 240 | 48 | 94 | 45 | 12 900 |
1 | 10 | 120 | 13 | >97 | 13 | 12 700 |
1a | 100 | 30 | 51 | 94 | 48 | 4800 |
2 | 100 | 120 | 64 | 44 | 28 | 2800 |
3 | 100 | 30 | 60 | 33 | 20 | 2000 |
4 | 100 | 1,320 | 61 | 92 | 56 | 5600 |
4 | 50 | 1,200 | 61 | 93 | 57 | 11 400 |
5 | 100 | 360 | 46 | 94 | 43 | 4 200 |
6 | 100 | <30 | 73 | 73 | 53 | 5300 |
6 | 35 | 60 | 75 | 75 | 56 | 16 000 |
6 | 10 | <30 | 42 | 83 | 35 | 35 000 |
General conditions: neat 11, 150 psi ethylene, 40 °C.
Time to maximum conversion.
Conversion = 100 − [(final moles of 11) × 100/(initial moles of 11)].
Selectivity = (moles of ethenolysis products 12 + 13) × 100/(moles of total products 12 + 13 + 14 + 15).
Yield = (moles of ethenolysis products 12 + 13) × 100/(initial moles of 11) conversion × selectivity/100.
TON = yield × [(moles of 11)/(moles of cat.)].