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. 2016 Feb 25;6:21365. doi: 10.1038/srep21365

Table 3. Self-condensation of butanol catalyzed by Ir catalysts in aqueous phasea.

Entry Catalyst T (°C) Conv. (%) Yield (Sele.) of2-ethylhexanol (%) TOFb (h−1)
1 170
2 5%Ir-MC-550 170 3.2 1 1
3 5%Ir-0.25DMC-550 170 37.8 34.5 (83.1) 17
4 5%Ir-0.4DMC-550 170 41.2 39.9 (96.7) 19
5 5%Ir-0.5DMC-550 170 28.2 27.2 (96.5) 13
6 5%Ir-0.6DMC-550 170 19 16.9 (88.5) 9
7 5%Ir-0.7DMC-550 170 18 16.5 (91.5) 8
8 5%Ir-0.4DMC-700 170 49.8 46.5 (93.2) 23
9 5%Ir-0.4DMC-800 170 40.8 38.4 (94.1) 19
10 5%Ir-0.4DMC-900 170 32.6 30.7 (94.3) 15
11 5%Ir-0.4DMC-550 150 31.7 27.3 (86.1) 15
12 5%Ir-0.4DMC-550 190 55.3 42.8 (77.3) 25
13 1%Ir-0.4DMC-550 170 27.5 27 (98) 63
14 3%Ir-0.4DMC-550 170 44.9 43.6 (97.1) 34
15c Reuse entry 4 for 2nd 170 41.8 40.2 (96.2) 19
16c Reuse entry 4 for 3rd 170 40.2 38.9 (96.9) 18
17c Reuse entry 4 for 4th 170 40.7 39.2 (96.3) 19
18c Reuse entry 4 for 5th 170 39.6 37.9 (95.6) 18

aReaction conditions: 1 g butanol, 0.1 g iridium catalysts, 1.0 equiv. of NaOH, 15 ml H2O, 17 h.

bTOF = [reacted mol butanol]/[(total mol metal) * (reacton time)].

cThe catalysts were washed with ethanol and water, and then dried for the recycling test.