Abstract
Monolithic Ni-Al2O3/Ni-foam catalyst is developed by modified wet chemical etching of Ni-foam, being highly active/selective and stable in strongly exothermic CO2 methanation process. The as-prepared catalysts are characterized by x-ray diffraction scanning electron microscopy, inductively coupled plasma atomic emission spectrometry, and H2-temperature programmed reduction-mass spectrometry. The results indicate that modified wet chemical etching method is working efficiently for one-step creating and firmly embedding NiO-Al2O3 composite catalyst layer (~2 μm) into the Ni-foam struts. High CO2 conversion of 90% and high CH4 selectivity of >99.9% can be obtained and maintained for a feed of H2/CO2 (molar ratio of 4/1) at 320°C and 0.1 MPa with a gas hourly space velocity of 5000 h-1, throughout entire 1200 h test over 10.2 mL such monolithic catalysts. Computational fluid dynamics calculation and experimental measurement consistently confirm a dramatic reduction of "hotspot" temperature due to enhanced heat transfer.
| Original language | English |
|---|---|
| Pages (from-to) | 4323-4331 |
| Number of pages | 9 |
| Journal | AIChE Journal |
| Volume | 61 |
| Issue number | 12 |
| DOIs | |
| State | Published - Dec 2015 |
Keywords
- Computational fluid dynamics simulation
- Foam
- Heterogeneous catalysis
- Methanation
- Structured catalyst