Chemical Engineers' Handbook, Volume 4,Parte 1963Robert H. Perry McGraw-Hill, 1963 - 1919 pagine Textbook on chemical industry engineering - covers theoretics, definitions, technical aspects, etc. |
Dall'interno del libro
Risultati 1-3 di 78
Pagina 4-60
... Standard States . It is often impossible or impractical because of the lack of thermodynamic data to determine the fugacity of a component in solution . It is therefore advantageous to use the ratio between the fugacity } ; of component ...
... Standard States . It is often impossible or impractical because of the lack of thermodynamic data to determine the fugacity of a component in solution . It is therefore advantageous to use the ratio between the fugacity } ; of component ...
Pagina 4-63
... standard states are defined , K , may or may not be identically equal to Ka . For example , in the special case where all products and reactants are in the gaseous state and if the standard state for each gaseous component is taken as ...
... standard states are defined , K , may or may not be identically equal to Ka . For example , in the special case where all products and reactants are in the gaseous state and if the standard state for each gaseous component is taken as ...
Pagina 4-67
... standard- state values as is done for other thermodynamic proper- ties . The standard state for solids and liquids is taken as the pure component at 1 atm . pressure . The standard state for entropies of gases is the hypothetical ideal ...
... standard- state values as is done for other thermodynamic proper- ties . The standard state for solids and liquids is taken as the pure component at 1 atm . pressure . The standard state for entropies of gases is the hypothetical ideal ...
Sommario
DATA AND FUNDAMENTALS Section | 1-1 |
Mathematics 2 | 2-3 |
DIFFERENTIAL EQUATIONS | 2-4 |
Copyright | |
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