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In any laboratory or pilot plant tests, the rst thing to vary is the impeller speed. This changes pumping capacity, blend time, and shear rates. On-bottom motion or partial suspension is rarely a useful desired mixing result except, perhaps, for the dissolution of very soluble solids. Complete suspension is the minimum desired mixing goal for most solid liquid mixing operations involving settling solids. The equivalent condition for oating solids is complete incorporation and dispersion of the oating solids. Uniform suspension is required for crystallization, solid-catalyzed reactions, and suspension polymerization where high local concentrations may lead to poor yields of the desired product. Also, as practical as possible, crystallization slurries must be fed to a centrifuge at a uniform solids concentration for the proper cake buildup required for effective ltration and washing of the solid cake. Speci ed mass transfer rate such as dissolution rate, reaction rate, and so on, may be the desired process result to achieve a given production capacity. Particle size control may be the desired result in certain formulation operations. The measurement of power on a full or pilot scale vessel is best accomplished with a wattmeter. Ammeter readings, at best, must be ratioed to the full-load nameplate amperage, which varies with voltage, power factor, and motor type. For the fractional-horsepower motor used in the laboratory or pilot plant, power draw is best determined by calculation using the de ning equation for the power number. This requires power number versus Reynolds number data or correlation. To estimate the viscosity of complex non-Newtonian slurries, Oldshue and Sprague (1974) recommend the use of a mixing viscometer that mimics the hydrodynamic environment likely to be encountered in an agitated vessel.

1. Switch to Layout mode by choosing View Layout Mode or pressing Ctrl+L. 2. Choose the layout into which you want to insert an OLE object. 3. Choose Insert Object. The Insert Object dialog appears. (See Figure 6-26.) 4. Select the Create New radio button to create a new OLE object. or To create an OLE object from an existing file, go to Step 7. 5. Select the object type (the application for creating the OLE object) from the Object Type list and click OK. FileMaker Pro opens the selected application.

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Adrian, R J (1991) Particle imaging techniques for experimental uid mechanics, Annu Rev Fluid Mech, 23, 261 304 All-Saeedi, J N, M O Kirkpatrick, and R W Pike (1995) Optical tomography for measurement of concentration distributions in a stirred tank, Paper 115, presented at Mixing XVI, Banff, Alberta, Canada Bakker, A K, J Myers, R W Ward, and C K Lee (1996) The laminar and turbulence ow pattern of a pitched blade turbine, Trans Inst Chem Eng, 74, 485 491 Barnes, H A, J F Hutton, and K Walters (1989) An Introduction to Rheology, Elsevier, New York Benedict, L H, and R D Gould (1996) Towards better uncertainty estimates for turbulence statistics, Exp Fluids, 22, 129 136 Benedict, L H, and R D Gould (1999) Understanding biases in the near- eld region of LDA two-point correlation measurements, Exp Fluids, 26, 381 388.

Places a copy of the object or text on the Clipboard. Places a copy of the object or text on the Clipboard.

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