Abstract
The evaluation of the performance of a pneumatic transport reactor operating at low gas velocity and high solid volumic concentration is presented. This reactor has a high length-diameter ratio and can be considered as a representative tube of a multitubular reactor with gas—solid suspension circulating inside the tubes. Two experimental techniques have been used: ozone adsorption or catalytic ozone decomposition on a porous solid. The agregation of the particles, which has an important effect on the hydrodynamics, does not contribute to the diffusional resistance. The design of an industrial reactor should be accordingly relatively simple.
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