Chemical Engineers' HandbookJohn Howard Perry McGraw-Hill book Company, Incorporated, 1941 - 3029 pagine |
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Pagina 620
... Critical Constants . Gases and vapors may be liquefied by the application of pressure provided the temperature is at ... critical temperature Te of the gas . The pressure required to liquefy the gas at this critical temper- ature is the ...
... Critical Constants . Gases and vapors may be liquefied by the application of pressure provided the temperature is at ... critical temperature Te of the gas . The pressure required to liquefy the gas at this critical temper- ature is the ...
Pagina 621
... critical constants for these gases from the van der Waals relations given above . Solution . For nitrogen : a Pe = = 2762 8a Tc = = 276R For ethane : 1.31 X 106 27 ( 37.3 ) 2 = 34.8 atm . 8 X 1.31 X 106 27 X 37.3 X 82.07 6.0 X 106 = 127 ...
... critical constants for these gases from the van der Waals relations given above . Solution . For nitrogen : a Pe = = 2762 8a Tc = = 276R For ethane : 1.31 X 106 27 ( 37.3 ) 2 = 34.8 atm . 8 X 1.31 X 106 27 X 37.3 X 82.07 6.0 X 106 = 127 ...
Pagina 1368
... critical points of the components . A brief summary of these results as applied to vapor - liquid equilibrium ... critical pressure of either pure component develop discontinuities in the vapor- liquid equilibrium relation at pressures ...
... critical points of the components . A brief summary of these results as applied to vapor - liquid equilibrium ... critical pressure of either pure component develop discontinuities in the vapor- liquid equilibrium relation at pressures ...
Sommario
Mathematical Signs and Symbols | 3 |
Natural Logarithms of Numbers | 36 |
Values and Logarithms of Expo | 46 |
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acetate acid alcohol aldehydes amines ammonia angle benzene bromide calculated Carbon cent chart Chem Chemical Engineering chloride circle coefficient Common Logarithms compounds Compounds-(Continued constant curve density diam diameter dimensions entropy equal equation equilibrium ether Ethyl Ethyl chloride Example factor flange flow fluid Formula fraction free energy fugacity gage gases given heat capacity heat of vaporization HNO3 hydrogen Inorganic insol ketone latent heat length linear liquid Logarithms measured metal meter method mixture molal obtained orifice oxide phase Phenol pipe Precipitate Radians radius reactants reaction salts scale side sodium solid Solubility solution specific heat standard substances sulfate Sulfur sulfuric acid surface temperature tion triangle tube units values vapor pressure velocity viscosity volume weight