Abstract
Abstract A series of monolithic nickel-foam-structured Ni-MOx(M = Al, Zr or Y) binary catalysts to be used in the catalytic oxy-methane reforming have been developed, of which the Ni-MOx catalysts are formed in-situ and embedded onto the Ni-foam struts by chemically etching Ni-foam using solution containing Al (or Zr, Y) nitrate. Among these catalysts, Ni-Al2O3/Ni-foam possesses the largest specific surface area and the highest amount of NiO species (i.e., Ni active site precursors), and as a result, exhibits the best catalytic performance with promising stability. Over this catalyst, CH4 conversion of 86.4% can be obtained with H2 selectivity of 96.6% and CO selectivity of 91.2% for a fed of CH4/O2 (2/1) at 700°C and a high gas hourly space velocity of 100 L g- 1 h- 1. We anticipate our assay to be a new point which might stimulate commercial exploitation of the new-generation structured catalyst technology for the high-throughput catalytic oxy-methane reforming reaction.
| Original language | English |
|---|---|
| Article number | 4379 |
| Pages (from-to) | 1-5 |
| Number of pages | 5 |
| Journal | Catalysis Communications |
| Volume | 70 |
| DOIs | |
| State | Published - 20 Jul 2015 |
Keywords
- Catalytic oxy-methane reforming
- Foam
- Monolithic catalyst
- Nickel catalyst
- Syngas