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. |
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Risultati 1-3 di 80
Pagina 11-24
... transfer surface , Q quantity of heat required to be transferred , At = temperature difference of the process , and U overall heat - transfer coefficient . It is helpful to define the modes of heat transfer and the corresponding overall ...
... transfer surface , Q quantity of heat required to be transferred , At = temperature difference of the process , and U overall heat - transfer coefficient . It is helpful to define the modes of heat transfer and the corresponding overall ...
Pagina 14-79
... transfer in plate and packed gas - liquid con- tactors has been covered earlier in this subsection . Attention here will be limited to deep - bed contactors bubble columns and agitated ves- sels . Theory underlying mass transfer between ...
... transfer in plate and packed gas - liquid con- tactors has been covered earlier in this subsection . Attention here will be limited to deep - bed contactors bubble columns and agitated ves- sels . Theory underlying mass transfer between ...
Pagina 15-20
... transfer units be envisioned . The height equivalent to a theoretical stage ( HETS ) in an extrac- tion tower is simply the height of the tower Z , divided by the number of theoretical stages achieved [ Eq . ( 15-29 ) ] . FIG . 15-18 ...
... transfer units be envisioned . The height equivalent to a theoretical stage ( HETS ) in an extrac- tion tower is simply the height of the tower Z , divided by the number of theoretical stages achieved [ Eq . ( 15-29 ) ] . FIG . 15-18 ...
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 |
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