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 95
Pagina 5-5
... temperature ; temperature at a given point in a body at time ✪ Temperature at points 1 , 2 , and n in a system through which heat is being transferred Temperature of surroundings Inlet and outlet temperature respectively of hotter ...
... temperature ; temperature at a given point in a body at time ✪ Temperature at points 1 , 2 , and n in a system through which heat is being transferred Temperature of surroundings Inlet and outlet temperature respectively of hotter ...
Pagina 11-110
... temperature . Thus the true temperature dif- ference in the boiling zone is always less than the total temperature difference as measured from steam and vapor - head temperatures . Although the true heat - transfer coefficients in the ...
... temperature . Thus the true temperature dif- ference in the boiling zone is always less than the total temperature difference as measured from steam and vapor - head temperatures . Although the true heat - transfer coefficients in the ...
Pagina 12-23
... temperature in - water temperature out h2 = 61.63 Btu / lb h2-41.58 = 2.05 = 10 Corresponding wet - bulb temperature = 94 ° F air leaving pond . Approach possible to air leaving ( from Table 12-4 ) = -2 ° F . Water temperature leaving ...
... temperature in - water temperature out h2 = 61.63 Btu / lb h2-41.58 = 2.05 = 10 Corresponding wet - bulb temperature = 94 ° F air leaving pond . Approach possible to air leaving ( from Table 12-4 ) = -2 ° F . Water temperature leaving ...
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 |
Copyright | |
15 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
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