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In comparison, STY increased with growing feed flow price. Our flow-type membrane layer reactor exhibited a somewhat huge STY of 430 kg m-3 h-1 compared with the batch-type membrane reactor formerly reported.Structured catalytic membranes with a high porosity and a decreased stress drop are especially appropriate professional procedures performed at large room velocities. One of these simple procedures is the catalytic total oxidation of volatile organic compounds, that will be an economically
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