Skip to main content
. 2015 Mar 4;6(5):2928–2931. doi: 10.1039/c5sc00248f

Table 2. Optimization of reaction conditions a .

Inline graphic
Entry P(H2)/P(CO2) (atm) KOH (M) Yield b (%) TON c (×103)
1 30/30 1 81 81
2 20/20 1 35 35
3 40/20 1 99 99
4 50/10 1 99 99
5 d 40/20 1 20 200
6 d 40/20 2 34 340
7 d 40/20 5 45 450

aGeneral reaction conditions: 5 mL aqueous KOH solution, 0.001 mol% iridium catalyst 1b relative to KOH in 100 μL THF, under the desired CO2 : H2 pressure, 140 °C, 20 h.

bYield, which represents conversion of the added KOH, based on 1H NMR analysis with sodium 3-(trimethylsilyl)-1-propanesulfonate as an internal standard.

cTON = turnover number; number of moles of product formed per mole of catalyst.

dCatalyst loading was 0.0001 mol% relative to KOH.