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. |
Dall'interno del libro
Risultati 1-3 di 80
Pagina 3-52
... gives a straight line through ( xo , yo ) - ( x1 , y1 ) ; keeping the first three terms gives a quadratic function of position going through those points plus ( x2 , y2 ) . The value α = 0 gives x = xo ; α = 1 gives x = x1 , and so on ...
... gives a straight line through ( xo , yo ) - ( x1 , y1 ) ; keeping the first three terms gives a quadratic function of position going through those points plus ( x2 , y2 ) . The value α = 0 gives x = xo ; α = 1 gives x = x1 , and so on ...
Pagina 4-6
... gives Replacement of each of the four partial derivatives through the appro- priate Maxwell relation gives finally ( 4-38 ) These equations clearly show that for an ideal gas UH. ӘН as = T ƏT P ӘТ ӘН as = T + V apr In view of Eq . ( 4-31 ) ...
... gives Replacement of each of the four partial derivatives through the appro- priate Maxwell relation gives finally ( 4-38 ) These equations clearly show that for an ideal gas UH. ӘН as = T ƏT P ӘТ ӘН as = T + V apr In view of Eq . ( 4-31 ) ...
Pagina 16-15
... gives the constant separation factor isotherm ni = ci r + ( 1 - rci ( 16-31 ) The separation factor r identifies the equilibrium increase in n from 0 to 1 , which accompanies an increase in c from 0 to 1. For a concen- tration change ...
... gives the constant separation factor isotherm ni = ci r + ( 1 - rci ( 16-31 ) The separation factor r identifies the equilibrium increase in n from 0 to 1 , which accompanies an increase in c from 0 to 1. For a concen- tration change ...
Sommario
Mathematics Bruce A Finlayson James F Davis Arthur W Westerberg | 3-1 |
Fluid and Particle Dynamics James N Tilton | 5-69 |
Process Control | 6-44 |
Copyright | |
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Altre edizioni - Visualizza tutto
Perry's Chemical Engineers' Handbook, Volume 7,Parte 1997 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 |
Parole e frasi comuni
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