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 18-3
... Liquid - gas transfer systems are utilized for the separa- tion of materials based on phase - equilibria relationships , with the rate of transfer controlled by molecular and eddy - diffusion mechanisms . Process equipment utilized for ...
... Liquid - gas transfer systems are utilized for the separa- tion of materials based on phase - equilibria relationships , with the rate of transfer controlled by molecular and eddy - diffusion mechanisms . Process equipment utilized for ...
Pagina 18-9
... liquid - phase efficiency occurs with increase in slot submergence as a result of increase in liquid- residence time . The choice of submergence is then a function of optimization of tray pressure drop and efficiency . The weir crest ...
... liquid - phase efficiency occurs with increase in slot submergence as a result of increase in liquid- residence time . The choice of submergence is then a function of optimization of tray pressure drop and efficiency . The weir crest ...
Pagina 19-88
... liquid batches , but production equipment is almost in- variably continuous . Tubular Centrifuges . A common type of ... liquid flow , so that their trajectory in the bowl is curved toward the wall . If the trajectory of a given particle ...
... liquid batches , but production equipment is almost in- variably continuous . Tubular Centrifuges . A common type of ... liquid flow , so that their trajectory in the bowl is curved toward the wall . If the trajectory of a given particle ...
Sommario
DATA AND FUNDAMENTALS Section | 1-1 |
Mathematics 2 | 2-3 |
DIFFERENTIAL EQUATIONS | 2-4 |
Copyright | |
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2,2-Dimethylhexane 4-Methylheptane acetate acid alcohol applied benzene bromide calculated Carbon cent centipoise Chem Chemical Engineering chloride coefficient Compounds compressor computed constant conveyor curve delq density diam differential equation dimensionless dimensionless groups discharge E. I. du Pont energy Engrs Enthalpy entropy equilibrium Ethyl Example factor flanges flow fluid force/sq Formula friction ft./sec fugacity function gases given horsepower Hydrogen integral joints ketone length linear Liquid Vapor materials McGraw-Hill Mech method molal mole Organic Compounds oxide particle Phys pressure drop properties pump ratio reaction reactor Reynolds number solids solution subl sulfate Sulfuric acid surface Table tank Temp temperature Thermal Conductivity Thermodynamics tion Trans tube values valves vapor pressure variables velocity viscosity volume weight York zero