Perry's Chemical Engineers' Handbook, Volume 7,Parte 1997McGraw-Hill, 1997 - 2640 pagine From the fundamentals to details on computer applications and control, this handbook provides unrivaled, state-of-the-art coverage of all aspects of chemical engineering. The seventh edition is completely updated and includes new topics such as biochemical engineering, waste management, plant safety, analysis of plant performance, and handling of hazardous materials. Over 1,700 illus. |
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Risultati 1-3 di 80
Pagina 2-340
... critical temperature of pure hydrocarbons only , is the method of Nokay and requires the normal boiling point , the relative density , and the compound family . T , and T are the critical and normal boiling temperatures , respec- tively ...
... critical temperature of pure hydrocarbons only , is the method of Nokay and requires the normal boiling point , the relative density , and the compound family . T , and T are the critical and normal boiling temperatures , respec- tively ...
Pagina 2-344
... critical temperature is 536.05 K. P = 0.101325M ( 0.101325 ) ( 74.12 ) ( 0.34 + Σ Ap ) 2 ( 0.34 +0.951 ) 2 P4.506 MPa The accurate experimental critical pressure is 4.179 MPa . No known method is available to predict the critical ...
... critical temperature is 536.05 K. P = 0.101325M ( 0.101325 ) ( 74.12 ) ( 0.34 + Σ Ap ) 2 ( 0.34 +0.951 ) 2 P4.506 MPa The accurate experimental critical pressure is 4.179 MPa . No known method is available to predict the critical ...
Pagina 2-358
... critical properties with pseudocritical properties defined in Eqs . ( 2-80 ) and ( 2-81 ) by Kay . * 47 0.35 -0.083 ... critical region , where 15 percent errors may be expected and 50 percent errors can occur . For mixtures near ...
... critical properties with pseudocritical properties defined in Eqs . ( 2-80 ) and ( 2-81 ) by Kay . * 47 0.35 -0.083 ... critical region , where 15 percent errors may be expected and 50 percent errors can occur . For mixtures near ...
Sommario
Mathematics Bruce A Finlayson James F Davis Arthur W Westerberg | 3-1 |
Fluid and Particle Dynamics James N Tilton | 6-1 |
Reaction Kinetics | 7-1 |
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Altre edizioni - Visualizza tutto
Perry's Chemical Engineers' Handbook, Volume 7,Parte 1997 Robert H. Perry,Don W. Green,James O. Maloney Visualizzazione estratti - 1997 |
Perry's Chemical Engineers' Platinum Edition Robert H. Perry,Don W. Green Anteprima non disponibile - 1999 |
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2,3,3-Trimethylpentane 2H₂O acetate acid AIChE alcohol ASHRAE Benzene binary bromide calculated Carbon Chem Chemical Engineers chloride coefficient Compressibility Factors constant convert correlation critical cubic delq density differential equation diffusion Dimensionless Dimensionless Dimensionless emissivity energy enthalpy entropy equilibrium error Ethanol ether Ethyl acetate Ethyl propionate Example fluid Formula function gases Gibbs energy given h kJ/kg H₂O heat capacity heat transfer hydrocarbons ideal gas integral k₁ ketone linear liquid m³/kg Mass Transfer mass-transfer meter method Methyl mixture molar mole normal boiling Organic Compounds oxide parameters percent Phenol problem Properties of Refrigerants sample Saturated solution subl sulfate sulfide sulfonic acid surface TABLE temperature thermal conductivity Thermodynamic Thermodynamic Properties Thermophysical Properties tion tubes units values vapor pressure variables viscosity y₁ York ᎡᎢ