Abstract
Herein, a straightforward method is proposed for the selective conversion of CO2 and H2 into propane. This is achieved in a 50 mL batch reactor (45 bar and 230–270 °C) by combining a RhIn/MgOx catalyst with highly acidic ZSM-5 and co-feeding benzene. The addition of 50 mg of benzene is found to be optimal to skew the hydrocarbon selectivity away from C2 and C4–6 towards C3, while maintaining high conversion (>60%) and low CO selectivity (27%) during the 10-hour reaction. Benzene promotes the formation of propane by enhancing the aromatic hydrocarbon pool cycle at the expense of the olefinic cycle. Benzene achieves this by “grabbing” in-situ produced methanol and preventing the over-methylation of aliphatics. In turn, the generated polymethyl benzene species undergo a paring mechanism to produce propylene, which is converted to propane. The role of benzene is elucidated through comprehensive characterisations and extensive control experiments.
| Original language | English |
|---|---|
| Article number | 121067 |
| Journal | Applied Catalysis A: General |
| Volume | 724 |
| DOIs | |
| Publication status | Published - 25 Aug 2026 |
Keywords
- CO2 hydrogenation
- Hydrocarbon pool mechanism
- Tandem catalysis
- ZSM-5 zeolite
ASJC Scopus subject areas
- Catalysis
- Process Chemistry and Technology
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