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 86
Pagina 3-25
... derivatives Example Given fx = 3x + 2x + 1 calculate all derivative values at x = 3 đi x dx x = 3f3 = 99 + + 2 = 53 ... derivatives are continuous For = fox , y it follows : af -- = ду дду дх ду == af by on by de dy General Form for ...
... derivatives Example Given fx = 3x + 2x + 1 calculate all derivative values at x = 3 đi x dx x = 3f3 = 99 + + 2 = 53 ... derivatives are continuous For = fox , y it follows : af -- = ду дду дх ду == af by on by de dy General Form for ...
Pagina 3-27
... derivative using Eq - 3-45 · ᏧᏑ ( 37 ) = ( 32 ) , ( 35 ) as ᏧᏚ ᏧᎢ . OS V Then evaluate the numerator and denominator as type II derivatives ᏧᏑ ( 7 ) C T ( 3 ) ( 2 ) , Cop T ( a ) , ( 79 ) These derivatives are of importance for ...
... derivative using Eq - 3-45 · ᏧᏑ ( 37 ) = ( 32 ) , ( 35 ) as ᏧᏚ ᏧᎢ . OS V Then evaluate the numerator and denominator as type II derivatives ᏧᏑ ( 7 ) C T ( 3 ) ( 2 ) , Cop T ( a ) , ( 79 ) These derivatives are of importance for ...
Pagina 3-64
... derivatives at the knots . Two more conditions can be specified arbitrarily . These are usually the sec- ond derivatives at the two end points , which are commonly taken as zero ; this gives the natural cubic splines . ་ Take y1 = y ( x ...
... derivatives at the knots . Two more conditions can be specified arbitrarily . These are usually the sec- ond derivatives at the two end points , which are commonly taken as zero ; this gives the natural cubic splines . ་ Take y1 = y ( x ...
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 | |
16 sezioni non visualizzate
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