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 93
Pagina 3-53
... Formula If the data are given over equidis- tant values of the independent variable x , an interpolation formula such as the Newton formula ( see Refs . 143 and 185 ) may be used and the resulting formula differentiated analytically ...
... Formula If the data are given over equidis- tant values of the independent variable x , an interpolation formula such as the Newton formula ( see Refs . 143 and 185 ) may be used and the resulting formula differentiated analytically ...
Pagina 8-38
... formula is more appropriate for the raw material amounts and other parameters , with recipe designating the formula and the processing instructions . The above concept of a recipe permits the following three different categories of ...
... formula is more appropriate for the raw material amounts and other parameters , with recipe designating the formula and the processing instructions . The above concept of a recipe permits the following three different categories of ...
Pagina 10-20
... formula . Thus q = 0.386Lh ! √2g ( 10-38 ) In this case , no end corrections are applied even though the formula applies only for sharp - edged weirs . See Schoder and Dawson , Hydraulics , McGraw - Hill , New York , 1934 , p . 175 ...
... formula . Thus q = 0.386Lh ! √2g ( 10-38 ) In this case , no end corrections are applied even though the formula applies only for sharp - edged weirs . See Schoder and Dawson , Hydraulics , McGraw - Hill , New York , 1934 , p . 175 ...
Sommario
Conversion Factors and Mathematical Symbols James O Maloney 1 | 2-1 |
Mathematics Bruce A Finlayson James F Davis Arthur W Westerberg | 3-1 |
Fluid and Particle Dynamics James N Tilton | 6-1 |
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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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acetate acid AIChE alcohol ASHRAE average bromide calculated Carbon Chem Chemical Engineers chloride coefficient component Compounds constant convert correlation critical cubic delq density differential equation diffusion Dimensionless Dimensionless Dimensionless energy enthalpy entropy equilibrium error Ethanol ether Example flow fluid Formula function gases Gibbs energy given h kJ/kg H₂O heat transfer ideal gas integral k₁ ketone kg/m³ kJ/kg hg kJ/kg-K linear liquid m³/kg Mass Transfer mass-transfer McGraw-Hill meter method Methyl mixture molar mole mole fraction Organic Compounds oxide parameters percent phase Properties of Refrigerants Reynolds number sample Saturated solution subl sulfate sulfide surface TABLE temperature thermal conductivity Thermodynamic Thermodynamic Properties Thermophysical Properties tion tubes U.S. customary units units values vapor pressure variables velocity viscosity volume x₁ y₁ York ᎡᎢ