Chemical Engineers' HandbookJohn Howard Perry McGraw-Hill book Company, Incorporated, 1941 - 3029 pagine |
Dall'interno del libro
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Pagina 640
... calculated , if a value at one temperature T and the critical temperature Te are known , by the following graphical method due to Watson ( op . cit . , p . 363 ) , which is applicable to all liquids . Watson has plotted values of ( L ...
... calculated , if a value at one temperature T and the critical temperature Te are known , by the following graphical method due to Watson ( op . cit . , p . 363 ) , which is applicable to all liquids . Watson has plotted values of ( L ...
Pagina 747
... calculated from S298 data as follows : - AS298 AS298 = ES298 ( products ) == TAS298 == - ZS298 ( reactants ) 66.4 ( 52.75 + 45.17 ) = -31.52 E.U. ( entropy units ) ( -31.52 ) ( 298 ) ( -31.52 ) ( 298 ) = -9390 cal . AH298 is calculated ...
... calculated from S298 data as follows : - AS298 AS298 = ES298 ( products ) == TAS298 == - ZS298 ( reactants ) 66.4 ( 52.75 + 45.17 ) = -31.52 E.U. ( entropy units ) ( -31.52 ) ( 298 ) ( -31.52 ) ( 298 ) = -9390 cal . AH298 is calculated ...
Pagina 1033
... calculated on this basis . Apparent Temperature Drops and Apparent Coefficients . In ordi- nary evaporator practice , pressures may be determined more simply and accurately than temperatures . As a result , certain rather arbitrary ...
... calculated on this basis . Apparent Temperature Drops and Apparent Coefficients . In ordi- nary evaporator practice , pressures may be determined more simply and accurately than temperatures . As a result , certain rather arbitrary ...
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