Abstract
Ethanol steam reforming (ESR) has been a reliable and efficient process of renewable hydrogen generation. A highly stable and coke-resistant reforming catalyst was developed using La2O3 modified Ni catalyst supported on CeO2-ZrO2. A range of promoted (Ni-La/CeO2-ZrO2) and unpromoted (Ni/CeO2-ZrO2) catalysts were prepared in a laboratory and tested in a tubular fixed-bed reactor. Detailed characterizations of the fresh and spent catalyst revealed that the La2O3 promotion helped to tune the Ni dispersion, catalyst reducibility, and oxygen storage capacity of the catalyst. These properties account for the reforming activity of the catalysts and are reflected in enhanced ethanol (EtOH) conversion, H2 yield, and catalyst stability. The coke-resistance property of La2O3 enhanced the catalyst stability and activity. 7.5Ni-7.5La/CeO2-ZrO2 catalyst showed an optimum H2 selectivity (65 %) and EtOH conversion (97 %) at 600 °C, 1atm, S/C molar ratio 4.5:1 and WHSVEtOH- 2.48 g/h-gcat.
| Original language | English |
|---|---|
| Article number | 205537 |
| Journal | Gas Science and Engineering |
| Volume | 134 |
| DOIs | |
| State | Published - Feb 2025 |
| Externally published | Yes |
Bibliographical note
Publisher Copyright:© 2025 Elsevier B.V.
Keywords
- Coke-resistant
- Ethanol reforming
- Hydrogen production
- La promoter
- Ni-based catalyst
ASJC Scopus subject areas
- Geotechnical Engineering and Engineering Geology
- Energy Engineering and Power Technology
- Fuel Technology
- General Chemical Engineering
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