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 83
Pagina 2-5
... Estimate the Ideal Gas Heat 2-358 Saturated Xenon 2-315 Capacity of Acetone ( C3H6O ) at 600 K 2-359 Compressed ... Estimate AH , of Propionaldehyde at 350 K. 2-318 Example 13 Estimate AH , of Ethyl Acetate . 2-318 Example 14 Estimate AH ...
... Estimate the Ideal Gas Heat 2-358 Saturated Xenon 2-315 Capacity of Acetone ( C3H6O ) at 600 K 2-359 Compressed ... Estimate AH , of Propionaldehyde at 350 K. 2-318 Example 13 Estimate AH , of Ethyl Acetate . 2-318 Example 14 Estimate AH ...
Pagina 9-64
... estimate ( ratio estimate ) . Rule - of - thumb method based on cost data for previous similar types of plant ; proba- ble error within 10 to 50 percent . 2. Study estimate ( factored estimate ) . Better than order - of- magnitude ...
... estimate ( ratio estimate ) . Rule - of - thumb method based on cost data for previous similar types of plant ; proba- ble error within 10 to 50 percent . 2. Study estimate ( factored estimate ) . Better than order - of- magnitude ...
Pagina 30-33
... estimate . the database contains bias , this will translate into bias in the parame- ter estimates . In the flash example referenced above , including rea- sonable database uncertainty in the phase equilibria increases the 95 percent ...
... estimate . the database contains bias , this will translate into bias in the parame- ter estimates . In the flash example referenced above , including rea- sonable database uncertainty in the phase equilibria increases the 95 percent ...
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