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. 2018 Aug 27;9:3457. doi: 10.1038/s41467-018-05880-4

Fig. 3.

Fig. 3

The results of selectivity optimization for CO2 hydrogenation. a The effect of H2/CO2 ratio over ZnAlOx&H-ZSM-5. Reaction conditions: Space velocity = 6000 ml g−1 h−1, 3.0 MPa, 593 K. b The effect of CO introduction over ZnAlOx&H-ZSM-5. Reaction conditions: catalyst weight = 667 mg, 3.0 MPa, 593 K, inlet gas containing 66.7 ml min−1 mixed gas (H2/CO2/Ar = 3/1/0.2) and 0–26.6 ml min−1 CO. c Comparisons of catalytic behaviors over ZnAlOx&H-ZSM-5 and ZnAlOx&Si-H-ZSM-5. Reaction conditions: Space velocity = 6000 ml g−1 h−1, 3.0 MPa, 593 K, H2/CO2/Ar = 3/1/0.2. A9 and A10 are representative of aromatics containing 9 and 10 carbon atoms, respectively