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Variable rate filtration

Variable-Pressure, Variable-Rate Filtration The pattern of this categoiy comphcates the use of the basic rate equation. The method of Tiller and Crump (loc. cit.) can be used to integrate the equation when the characteristic curve of the feed pump is available. [Pg.1705]

Variable-pressure, variable-rate filtration. The use of a centrifugal pump results in this pattern the discharge rate decreases with increasing back pressure. [Pg.2030]

Shnato, M., Aragaki, T., Mtani, E. and Funahashi, T., 1980b, Constant rate and variable rate filtration of powor law non-Newtmiian fluids, Ch Mig. J an J. 13 pp 473-478. [Pg.81]

Tiller F.M., 1958. The role of porosity in filtration 3 Variable pressure-variable rate filtration, AIChEJ, 2, 171-174. [Pg.407]

The specific cake resistance a should be constant for incompressible cakes but it may change with time as a result of possible flow consolidation of the cake and also, in the case of variable rate filtration, because of variable approach velocity. [Pg.308]

See other pages where Variable rate filtration is mentioned: [Pg.1621]    [Pg.1442]    [Pg.1938]    [Pg.1652]    [Pg.1653]    [Pg.1926]    [Pg.1625]    [Pg.194]    [Pg.266]   
See also in sourсe #XX -- [ Pg.170 ]



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