Abstract
Hydrogen production with integrated CO2 capture by autothermal reforming of methane has been investigated in a novel fluidized bed membrane reactor configuration. With a phenomenological reactor model the reactor performance has been investigated over a wide range of operating conditions, viz. temperature, pressure, H2O/CH4 ratio, and membrane area.
The results obtained show that pure hydrogen production with integrated CO2 capture is feasible, however, only with a relatively low load/surface ratio (L/S) (
| Original language | English |
|---|---|
| Pages (from-to) | 334-344 |
| Journal | Asia-Pacific Journal of Chemical Engineering |
| Volume | 4 |
| Issue number | 3 |
| DOIs | |
| Publication status | Published - 2009 |
UN SDGs
This output contributes to the following UN Sustainable Development Goals (SDGs)
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SDG 7 Affordable and Clean Energy
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