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Different from many past studies, here we consider the general situation that the average exit gas speed can be larger than zero, and detailed geometry of the nozzle exit radius is included.
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Furnace exit gas temperature (FEGT) is one such important design/operating parameter.
The SO3 decomposition percentage was determined using the measured O2 concentration in the exit gas stream.
Char reactivity is evaluated from the time variation of CO concentration in the exit gas.
Moreover, the exit gas is an almost pure CO2 stream, requiring little or no gas separation before compression for sequestration.
In addition, discussions of peak and exit gas temperature trends are included.
The concentration of N2 in the fuel reactor exit gas increases with the fuel reactor temperature.
The exit gas from the fuel reactor is CO2 and H2O.
There was no H2S detected in the exit gas stream.
As no SO2 is detected in the exit gas, but the sulfur is significantly decreased in the exit gas, the sulfur would be accumulated over the catalyst surface.
The non-condensable gases together with the carrier gas were passed to a flow meter where the volume of exit gases was recorded.
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