Table 2 Dehydrogenation of HCOOK: Variation of catalysts and solvent
From: Development of a practical formate/bicarbonate energy system
Entry | Cat. | Solvent/H2O[x/y mL] | Gas volume [mL] | H2/CO2 [%] | H2 yield [%] | TON H2 | Rate H2release [mL h−1]max |
|---|---|---|---|---|---|---|---|
1 | Ru-1 | DMF/H2O (20/5) | 285 | 99/1 | 6 | 1150 | 30 |
2 | Ru-2 | DMF/H2O (20/5) | 390 | 99/1 | 14 | 1580 | 80 |
3 | Ru-3 | DMF/H2O (20/5) | 18 | 99/1 | <1 | 70 | 4 |
4 | Ru-4 | DMF/H2O (20/5) | 540 | 99/1 | 19 | 2180 | 90 |
5 | Ru-5 | DMF/H2O (20/5) | 1765 | 99.6/0.4 | 63 | 7110 | 330 |
6 | Ru-6 | DMF/H2O (20/5) | 1420 | 99.5/0.5 | 51 | 5770 | 500 |
7 | Ru-7 | DMF/H2O (20/5) | 1415 | 99.6/0.4 | 51 | 5760 | 420 |
8 | Ru-8 | DMF/H2O (20/5) | 87 | 99.5/0.5 | 3 | 350 | 18 |
9 | Ir-1 | DMF/H2O (20/5) | 1915 | 99.5/0.5 | 69 | 7790 | 3600 |
10 | Ir-2 | DMF/H2O (20/5) | 0 | – | – | – | – |
11 | Ir-3 | DMF/H2O (20/5) | 0 | – | – | – | – |
12[a] | Ru-5 | DMF/H2O (20/5) | 1100 | 85/15 | 34 | 3820 | 165 |
13[b] | Ru-5 | DMF/H2O (20/5) | 2765 | 99.7/0.3 | 99 | 11,260 | 400 |
14[b,c] | Ru-5 | DMF/H2O (20/5) | 4275 | 99.6/0.4 | 62 | 17,390 | 600 |
15[d] | Ru-5 | DMF/H2O (20/5) | 2920 | 98/2 | 99 | 11,630 | 4650 |
16[c,d] | Ru-5 | DMF/H2O (20/5) | 7005 | 96/4 | 99 | 27,470 | 4800 |
17[c,d,e] | Ru-5 | DMF/H2O (20/5) | 6575 | 98/2 | 94 | 263,200 | 2700 |
18 | Ru-5 | DMF/H2O (15/10) | 6700 | 98/2 | 98 | 26,820 | 5100 |
19 | Ru-5 | Triglyme/H2O (15/10) | 764 | 94/6 | 32 | 3181 | 360 |
20[c, d] | Ru-5 | Triglyme/H2O (15/10) | 2210 | 92/8 | 30 | 8342 | 500 |
21[f] | Ru-5 | Triglyme/H2O (15/10) | 2799 | 90/10 | 91 | 10,283 | 360 |
