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 91
Pagina 3-87
... variable that cannot be measured directly but must be calculated based on results of other measurements . Suppose the computed value Y is a linear combination of the measured variables { y } , Y = α ̧y + αy2 + *** the random variables ...
... variable that cannot be measured directly but must be calculated based on results of other measurements . Suppose the computed value Y is a linear combination of the measured variables { y } , Y = α ̧y + αy2 + *** the random variables ...
Pagina 3-89
... variables . By examining the 5 × 5 matrix associated with those variables , we can see that its determinant is not zero , so the rank of the matrix is m = 5 ; thus , p = 3. These variables are thus a possible basis set . The dimensions ...
... variables . By examining the 5 × 5 matrix associated with those variables , we can see that its determinant is not zero , so the rank of the matrix is m = 5 ; thus , p = 3. These variables are thus a possible basis set . The dimensions ...
Pagina 13-22
... Variables N ; for Various Elements Homogeneous. DEFINITIONS For separation processes , a design solution is possible if the number of independent equations equals the number of unknowns . N1 = N1 - Ne where N , is the total number of ...
... Variables N ; for Various Elements Homogeneous. DEFINITIONS For separation processes , a design solution is possible if the number of independent equations equals the number of unknowns . N1 = N1 - Ne where N , is the total number of ...
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