Abstract
Oxy-fuel combustion is a promising technique to achieve significant reduction of CO2 emissions. However, due to change in the combustion medium from N2 (inert) to CO2 (reactive), significant changes in heat transfer, pollutant emissions and combustion behavior are expected. These changes have caused concerns for successful commercial application of this approach. In this paper, the effect of gas media on pyrolysis and combustion behavior is studied experimentally by conducting tests in a drop tube reactor, and numerically by computational fluid dynamics code FLUENT. Similar weight loss values were obtained when gas was switched from inert N2 to CO2 during the pyrolysis tests. To obtain the intrinsic char oxidation rate parameters three well known approaches were used: average reactivity up to certain burnoff range, reactivity at a fixed burn off and maximum reactivity. The reactivity parameters obtained using these approaches were then used to predict the char burnout at different furnace temperatures of a DTR using a FLUENT computational fluid dynamic code (CFD). The predicted results have suggested a significant effect of these rate parameters on the char burnout.
Original language | English (US) |
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Title of host publication | 24th Annual International Pittsburgh Coal Conference 2007, PCC 2007 |
Pages | 900-909 |
Number of pages | 10 |
Volume | 2 |
State | Published - Dec 1 2007 |
Event | 24th Annual International Pittsburgh Coal Conference 2007, PCC 2007 - Johannesburg, South Africa Duration: Sep 10 2007 → Sep 14 2007 |
Other
Other | 24th Annual International Pittsburgh Coal Conference 2007, PCC 2007 |
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Country/Territory | South Africa |
City | Johannesburg |
Period | 9/10/07 → 9/14/07 |
All Science Journal Classification (ASJC) codes
- Geochemistry and Petrology
- Geotechnical Engineering and Engineering Geology