Table 1 Methane oxidation on CTF-1, TiO2, g-C3N4, PtOx/CTF-1 and RuOx/CTF-1 in a packed-bed flow reactora

From: Methane oxidation to ethanol by a molecular junction photocatalyst

Photocatalyst

CH4 Conversion, %

Product yield, μmol h−1

Product selectivity on the basis of carbon, %

Reactants flow rate, mmol h−1

C2H5OH

CH3OH

C2H6

CO2

C2H5OH

CH3OH

C2H6

CO2

CH4

O2

CH4/O2

CTF-1

1.65 (±0.10)

122.4 (±2.6)

4.0 (±1.9)

26.0 (±1.2)

78.6 (±1.7)

1.1 (±0.7)

8.2 (±0.5)

18.9 (±0.5)

1.2 (±0.1)

15.8

TiO2

0.81 (±0.06)

0

121.8 (±17.6)

86.8 (±11.6)

19.3 (±0.4)

1.2 (±0.1)

16.1

g-C3N4

0.61 (±0.16)

29.2 (±0.1)

57.3 (±0.5)

2.04 (±0.5)

46.1 (±0.7)

45.67 (±0.4)

1.5 (±0.4)

20.7 (±0.7)

1.3 (±0.1)

15.9

3 wt% PtOx/CTF-1

2.33 (±0.13)

167.6 (±14.7)

2.0 (±1.8)

52.3 (±5.8)

79.6 (±7.0)

0.8 (±0.5)

11.8 (±1.2)

17.3 (±0.3)

1.1 (±0.1)

15.7

3 wt% RuOx/CTF-1

1.54 (±0.10)

99.2 (±10.3)

3.2 (±2.5)

26.0 (±2.5)

72.2 (±7.5)

1.4 (±0.9)

9.8 (±1.1)

17.6 (±0.3)

1.1 (±0.1)

16.0

  1. aCH4 source is 20% CH4/Ar and O2 source is the humidified simulated air (20% O2/N2). Values of yield and selectivity are averages during 4-h light irradiation. The error in parenthesis is the calculated s.d. over three samples with each measured three times. The reactant flow rates were obtained from the average value of flow concentrations after pouring for 6 h in the dark.