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 77
Pagina xxviii
... volume ft3 / lbm m3 / kg 6.242 796 E - 02 m3 / g 6.242 796 E - 05 ft / bm dm3 / kg 6.242 796 E + 01 Specific volume ( mole basis ) Specific volume Yield U.S. galЛbm L / ( g - mol ) ft / lb mol ) bbl / U.S . ton bbl / U.K . ton bbl / U.S ...
... volume ft3 / lbm m3 / kg 6.242 796 E - 02 m3 / g 6.242 796 E - 05 ft / bm dm3 / kg 6.242 796 E + 01 Specific volume ( mole basis ) Specific volume Yield U.S. galЛbm L / ( g - mol ) ft / lb mol ) bbl / U.S . ton bbl / U.K . ton bbl / U.S ...
Pagina 6-6
... volume of finite size V , is bounded by a surface of area A , with an outwardly directed unit normal vector n . The control volume is not necessarily fixed in space . Its boundary moves with velocity w . The fluid velocity is v . Fig ...
... volume of finite size V , is bounded by a surface of area A , with an outwardly directed unit normal vector n . The control volume is not necessarily fixed in space . Its boundary moves with velocity w . The fluid velocity is v . Fig ...
Pagina 10-139
... volume , each geometrical element usually must be calculated separately . Cal- culations for a full tank are usually simple , but calculations for partially filled tanks may be complicated . To calculate the volume of a partially filled ...
... volume , each geometrical element usually must be calculated separately . Cal- culations for a full tank are usually simple , but calculations for partially filled tanks may be complicated . To calculate the volume of a partially filled ...
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 |
Parole e frasi comuni
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