Abstract

Electrically heated beds of silica sand have been fluidized by mixtures of propane and air, which attain the temperature of the bed very quickly. With the bed below 760°C, these gases burn only in the bubbles bursting through the upper surface of the sand. With beds slightly hotter than 760°C combustion occurs in bubbles during their ascent through the fluidized sand. At ≈900°C, the gas mixture burns in the small bubbles formed at the distributor of the bed: below 1000°C, no combustion of C 3 H 8 appears to occur in the particulate phase, that is, between the sand particles, but only in the bubble phase. However, when catalyst pellets (of Al 2 O 3 coated with Pt) are added to fluidized sand below 760°C, measurements of [CO 2 ] in the bed reveal that C 3 H 8 oxidizes on the Pt. The measured temperature difference between a catalyst particle and the cooler sand shows that the catalyzed burning of C 3 H 8 on Pt is first order in C 3 H 8 and zeroth order in O 2 . The reaction is that producing CO and H 2 O from C 3 H 8 : actually the CO tends to diffuse well away from the catalyst before burning, most probably in a bubble. However, some limited oxidation of CO to CO 2 can occur on the platinum. The overall rate of oxidation is controlled by mass transfer of C 3 H 8 from the particulate phase to a catalyst particle. Thus, sand inhibits the combustion of C 3 H 8 in air, whereas platinized alumina particles catalyze it, thereby enabling more of the heat of combustion to be released inside a fluidized bed. The above considerations are affected by some of the off gases being recycled back into the bed, when U/U mf >6.

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