Chemical Engineers' Handbook, Volume 4,Parte 1963Robert H. Perry McGraw-Hill, 1963 - 1919 pagine Textbook on chemical industry engineering - covers theoretics, definitions, technical aspects, etc. |
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Pagina 5-59
... particle and a surrounditauid , the fluid will exert a drag upon the particle . The drag force on the particle is given by Fd = CAppu 2ge lb. force ( 5-204 ) where C = drag coefficient , dimensionless ; Ap = pro- jected area of particle ...
... particle and a surrounditauid , the fluid will exert a drag upon the particle . The drag force on the particle is given by Fd = CAppu 2ge lb. force ( 5-204 ) where C = drag coefficient , dimensionless ; Ap = pro- jected area of particle ...
Pagina 18-83
... particle with a specific gravity of 1.00 is 1 ft./sec . The forces acting on a dispersed liquid particle are identical to those acting on a solid particle suspended in a gas stream , and in general the same type of equipment is used for ...
... particle with a specific gravity of 1.00 is 1 ft./sec . The forces acting on a dispersed liquid particle are identical to those acting on a solid particle suspended in a gas stream , and in general the same type of equipment is used for ...
Pagina 20-84
... particle : attractive forces due to the field strength and the ionic image ; and repulsive forces due to the Coulomb effect . For spherical particles larger than 1 μ diameter , the ionic image effect is negligible , and charging will ...
... particle : attractive forces due to the field strength and the ionic image ; and repulsive forces due to the Coulomb effect . For spherical particles larger than 1 μ diameter , the ionic image effect is negligible , and charging will ...
Sommario
DATA AND FUNDAMENTALS Section | 1-1 |
Mathematics 2 | 2-3 |
DIFFERENTIAL EQUATIONS | 2-4 |
Copyright | |
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