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Investigation of an Ozone Membrane Contactor System
Authors:David S. Pines  Kyung-Nan Min  Sarina J. Ergas  David A. Reckhow
Affiliation:1. Department of Civil and Environmental Engineering , University of Hartford , West Hartford, CT, USA;2. Department of Civil and Environmental Engineering , University of Massachusetts , Amherst, MA, USA
Abstract:Ozone mass transfer rates were determined for nine expanded porous Teflon membranes that had different pore size, thickness, and pore volume, a nonporous Teflon membrane, and a PVDF membrane. The mass transfer coefficient was 7.6 ± 0.5 × 10?5 m/s at Re of 2000 for all membranes tested even though pore sizes ranged from 0.07 to 6 μm and thickness from 0.076 to 0.25 mm. Mass transfer increased with liquid side Reynolds number. Therefore, it is likely that ozone mass transfer is liquid phase controlling and not membrane limited. For a hypothetical case of 4000 m3/d and 2 mg/L ozone transferred, plate and frame membrane and hollow fiber contactors are approximately one and two orders of magnitude smaller, respectively, than fine-bubble diffusers.
Keywords:Ozone  Membranes  Membrane Reactors  Ozone Contactors  Fine Bubble Diffusers  Wastewater Treatment  Drinking Water Treatment  Disinfection  Oxidation
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