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 2-348 2-348 2-360 Surface Tension ( N / m ) of Saturated Liquid Refrigerants 2-361 ... Estimate AH , of Propionaldehyde at 350 K. 2-350 Units Conversions . Example 13 Estimate AH , of Ethyl Acetate . 2-350 ...
... Estimate the Ideal Gas Heat 2-348 2-348 2-360 Surface Tension ( N / m ) of Saturated Liquid Refrigerants 2-361 ... Estimate AH , of Propionaldehyde at 350 K. 2-350 Units Conversions . Example 13 Estimate AH , of Ethyl Acetate . 2-350 ...
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 . Better than order - of- 2. Study estimate ( factored estimate ) . 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 . Better than order - of- 2. Study estimate ( factored estimate ) . magnitude ...
Pagina 1-33
... estimate of the actual component and stream flows 60 percent of the time : 40 percent of the time , the actual ... estimate . the database contains bias , this will translate into bias in the parame- ter estimates . In the flash example ...
... estimate of the actual component and stream flows 60 percent of the time : 40 percent of the time , the actual ... estimate . the database contains bias , this will translate into bias in the parame- ter estimates . In the flash example ...
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