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 80
Pagina 9-16
... calculated in the same way and listed in Table 9-4 . Annual amount of tax Ar for Year 1 , when Acı = $ 300,000 per year , AD = $ 100,000 per year , A1 = $ 0 per year , and t = 0.5 , is found from Eq . ( 9-3 ) to be ATT = [ ( $ 300,000 ...
... calculated in the same way and listed in Table 9-4 . Annual amount of tax Ar for Year 1 , when Acı = $ 300,000 per year , AD = $ 100,000 per year , A1 = $ 0 per year , and t = 0.5 , is found from Eq . ( 9-3 ) to be ATT = [ ( $ 300,000 ...
Pagina 10-139
... 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 horizontal cylinder refer to Fig . 10-183 . Calculate ...
... 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 horizontal cylinder refer to Fig . 10-183 . Calculate ...
Pagina 15-19
... calculated by an iterative method . From equilibrium data ( Table 15-1 ) the extraction - solvent ( MIBK ) loss in the raffinate will be about 0.016 / 0.984 = 0.0163 kg MIBK / kg water , and the feed- solvent ( water ) loss in the ...
... calculated by an iterative method . From equilibrium data ( Table 15-1 ) the extraction - solvent ( MIBK ) loss in the raffinate will be about 0.016 / 0.984 = 0.0163 kg MIBK / kg water , and the feed- solvent ( water ) loss in the ...
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