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 90
Pagina 3-44
... functions fand g whose Laplace transforms exist . 2. The Laplace transform of a real - valued function is real for real s . If f ( t ) is a complex - valued function , f ( t ) = u ( t ) + iv ( t ) , where u and v are real , then L { f ...
... functions fand g whose Laplace transforms exist . 2. The Laplace transform of a real - valued function is real for real s . If f ( t ) is a complex - valued function , f ( t ) = u ( t ) + iv ( t ) , where u and v are real , then L { f ...
Pagina 3-66
... function , called the Lagrange function , by adding each of the equality constraints multiplied by an arbitrary multiplier to the objective function . At any point where the functions h ( z ) are zero , the Lagrange function equals the ...
... function , called the Lagrange function , by adding each of the equality constraints multiplied by an arbitrary multiplier to the objective function . At any point where the functions h ( z ) are zero , the Lagrange function equals the ...
Pagina 8-3
... function Error Economy of evaporator Function of time Distillate flow rate Limit on output Feed flow rate Pressure recovery factor Unit conversion constant Algebraic inequality constraint Transfer function Controller transfer function ...
... function Error Economy of evaporator Function of time Distillate flow rate Limit on output Feed flow rate Pressure recovery factor Unit conversion constant Algebraic inequality constraint Transfer function Controller transfer function ...
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 |
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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