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Advances in Water Treatment and Enviromental Management

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GAS LIQUID MIXING AND MASS TRANSFER 1192. The scale of operation. The size of operation of waste treatment equipmentmay be orders of magnitude greater than a chemical production plant,although the largest vessels may be a few 10’s of metres <strong>in</strong> diameter.Direct scaleup of a chemical/pharmaceutical plant geometry to thatrequired for water treatment may not be feasible from a physical/mechanical eng<strong>in</strong>eer<strong>in</strong>g st<strong>and</strong>po<strong>in</strong>t. Additionally, at large scale, waterdepth considerations become very important, because of the <strong>in</strong>creasedpressure required from any air supply to cope with the head of water.3. The rate of mass transfer <strong>and</strong> <strong>in</strong>tensity of mix<strong>in</strong>g employed. For watertreatment, only slow mass transfer is required to supply the biologicaldem<strong>and</strong>s. Typical values of K a are of the order of 10 s -1 . For chemical/Lpharmaceutical operations, values up to 0.1 s -1 are common.These differences will be considered further <strong>in</strong> the Discussion Section.4. Chemical <strong>and</strong> Pharmaceutical Techniques4.1 Agitated VesselsThe “workhorse” of the chemical process <strong>in</strong>dustry for gas liquid mass transfer isthe agitated mix<strong>in</strong>g vessel. Although a wide range of geometries are used, two of themost common are illustrated <strong>in</strong> Figures 1 <strong>and</strong> 2. Tall vessels, eg Figure 2, have agreater surface area/unit volume than the st<strong>and</strong>ard geometry vessels, Figure 1,<strong>and</strong> are therefore used when heat transfer is critical, as is the case <strong>in</strong> somepharmaceutical processes.Figure 1: St<strong>and</strong>ard geometry vessel with a s<strong>in</strong>gle impeller

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