The partial oxidation of methane to synthesis gas over Ni/a-Al 2 O 3 catalysts (1 and 5 wt.-% Ni loading, 71±160 and 250±355 mm particle diameter) was investigated in different types of fluidized-bed reactors, i.e., the bubbling fluidized bed (FlB), the spout fluid bed (SFB) and the internally circu
✦ LIBER ✦
Catalytic partial oxidation of methane in a high-temperature reverse-flow reactor
✍ Scribed by Dirk Neumann; Götz Veser
- Publisher
- American Institute of Chemical Engineers
- Year
- 2004
- Tongue
- English
- Weight
- 253 KB
- Volume
- 51
- Category
- Article
- ISSN
- 0001-1541
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EIVI Fig. 1. Cyclovoltammograins of 1 and 4. (---): Voltammogram of 1 embedded in a carbon paste electrode [12] in DMSO/O.l M Bu,NC10,, scan rate 1 mVs-', Ep(red) = -0.20, -0.46, -0.69 V; E,(ox) = -0.15, -0.41, -0.58 V. (--): Solution cyclic voltammogram of 4 in DMSO/O.I M Bu,NCIO, on a 0.07 cm2 Pt