Table 2 Comparison of heterogeneous catalysts for CO2 hydrogenation to methanol

From: Atomic-scale engineering of indium oxide promotion by palladium for methanol production via CO2 hydrogenation

Catalyst

T [K]

P [MPa]

WHSV (cm3 h−1 gcat−1)

Initial SMeOH (%)

Initial STYMeOH (gMeOH h−1 gcat−1)

Reference

Pd–In2O3 CP

553

5

48,000

78

1.01a

This work

Pd–In2O3 CP

553

5

24,000

75

0.61

This work

ZnO−ZrO2

593

5

24,000

86

0.71

10

Pd−Zn

543

2

18,000

70

0.60

56

LDH30−Ga

543

4.5

18,000

49

0.59

57

PdP−In2O3

593

5

21,000

67

0.89

28

CeO2 MoPK/SiO2

503

3.1

10,800

76

0.41

58

PdIn−In2O3/SiO2

573

5.0

63’000

24

ca. 0.3

44

  1. aSustained at 0.96 gMeOH h−1 gcat−1 after 500 h on stream