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850                                                                 Appendix G:  Dimensionless Numbers



            TABLE G.2 (continued)
            Selection of Dimensionless Numbers Applicable to Water Treatment Process Design
            Name                             Grouping                 Variables                 Ratio and Description
            Specific speed (Rouse, 1946, p. 304, 305)  nQ 0:5  N s ¼ specific speed             N s   0.05, radial flow pump
                                               (gDH)     n ¼ rotational velocity (rev=s)      N s   0.1, radial mixed flow
                                           N s ¼   0:75
                                                                  3
                                                         Q ¼ flow (m =s)                       N s   0.2, mixed flow
                                                                                 2
                                                         g ¼ gravitational constant (9.18 m=s )  N s   0.4, axial mixed flow
                                                         DH ¼ head developed by pump (m)      N s   0.8, axial flow
                                                 v                                               inertia forces
            Weber (Rouse, 1946; McCabe et al., 1993)     D ¼ length of contact (m)
                                               (s=rD)                                         surface tension forces
                                           W ¼
                                                                           3
                                                         r ¼ density of fluid (kg=m )
                                                         v ¼ velocity (m=s)
                                                                                         2
                                                         s ¼ coefficient of surface energy (N=m) or (kg=s )

            TABLE CDG.3
            Matrix of Physical Phenomena and Associated Dimensionless Numbers
            Source: Omega Engineering, Inc., The land chart of dimensionless numbers, U.S. Patent No. 5,465,838, Omega Engineering, Inc., Stamford, CT, 1997.)




                                                               range of conditions not investigated. The selection of the proper
                         E =f(R)         E ≠f(R)
                                                               dimensionless numbers also identifies the key variables
                                                               involved in an experiment, e.g., viscosity, diffusion, and gravity.

                    E                                          REFERENCES

                                                               Einstein, H. A., Engineering derivation of the Navier–Stokes equa-
                                                                    tions, Journal of the Engineering Mechanics Division,
                                                                    Proceedings of the American Society of Civil Engineers,
                                                                    Proceedings Paper 3533, Vol. 89(EM3):1–7, June 1963.
                                     R
                                                               McCabe, W. L., Smith, J. C., and Harriot, P., Unit Operations of
            FIGURE G.1  Euler number versus Reynolds.               Chemical Engineering, 5th edn., McGraw-Hill, New York,
                                                                    1993, ISBN 0-07-112721-6.
                                                               Omega Engineering, Inc., The land chart of dimensionless numbers,
                                                                    U.S. Patent No. 5,465,838, Omega Engineering, Inc.,
            involving an immersed object (form drag), Sherwood num-  Stamford, CT, 1997.
                                                               Rouse, H., Elementary Mechanics of Fluids, John Wiley & Sons,
            ber versus Reynolds number, etc.
                                                                    New York, 1946.
              Dimensionless numbers may be used to express experimental
                                                               Weber, W. J. Jr. and DiGiano, G. A., Process Dynamics in Environ-
            results in which many variables may be involved. The consoli-  mental Systems, John Wiley & Sons, New York, 1996, ISBN
            dation of variables into dimensionless numbers means that a  0-471-01711-6.
            given set of experimental results may be applicable to a wide  White, F. M., Fluid Mechanics, McGraw-Hill, New York, 1979.
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