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 85
Pagina 3-55
... solved iteratively . The set of equations can be solved using the successive substitution method or Newton - Raphson method . See Ref . 36 for an application to dynamic distillation problems . The best packages for stiff equations ( see ...
... solved iteratively . The set of equations can be solved using the successive substitution method or Newton - Raphson method . See Ref . 36 for an application to dynamic distillation problems . The best packages for stiff equations ( see ...
Pagina 3-57
... solved and the tolerance desired . Now the method is implicit and therefore stable for any step size . The accuracy may not be acceptable however and sets of nonlinear equations must be solved Thus , in practice the step size is limited ...
... solved and the tolerance desired . Now the method is implicit and therefore stable for any step size . The accuracy may not be acceptable however and sets of nonlinear equations must be solved Thus , in practice the step size is limited ...
Pagina 3-58
... solved using the Newton - Raphson method . The first form of the derivative gives a tridiagonal system of equations , and the stan- dard routines for solving tridiagonal equations suffice . For the other two options , some manipulation ...
... solved using the Newton - Raphson method . The first form of the derivative gives a tridiagonal system of equations , and the stan- dard routines for solving tridiagonal equations suffice . For the other two options , some manipulation ...
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