| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 635684 | Journal of Membrane Science | 2011 | 10 Pages |
Abstract
⺠The methane steam reforming reaction was examined in a bench-scale membrane reactor. ⺠Under NGCC conditions for CO2 capture: T = 823 K, pfeed/pperm up to 35/25 bar(a). ⺠A maximum CH4 conversion and H2 production rate of 73.4% and 1.3 Nm3/h. ⺠A stability of >30 days both for the membranes and the membrane reactor. ⺠Membrane reformer not yet a viable process for pre-combustion CO2 capture with NGCC.
Related Topics
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Authors
H. Li, J.A.Z. Pieterse, J.W. Dijkstra, W.G. Haije, H.Y. Xu, C. Bao, R.W. van den Brink, D. Jansen,