Chemical Engineers' HandbookJohn Howard Perry McGraw-Hill book Company, Incorporated, 1941 - 3029 pagine |
Dall'interno del libro
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Pagina 1049
... effect to multiple effect does not alter in any way the major features of body con- struction . It merely affects the interconnecting piping and the operation . The purpose of multiple - effect evaporation is to reduce the steam consump ...
... effect to multiple effect does not alter in any way the major features of body con- struction . It merely affects the interconnecting piping and the operation . The purpose of multiple - effect evaporation is to reduce the steam consump ...
Pagina 1050
... effect , that effect will deviate somewhat from this relationship . In the same way it may be shown that for a triple effect that fulfills the assumptions here made U1A1 ( toti ) = U2A2 ( t1 - t2 ) = UзA3 ( t2tv ) and for n effects ...
... effect , that effect will deviate somewhat from this relationship . In the same way it may be shown that for a triple effect that fulfills the assumptions here made U1A1 ( toti ) = U2A2 ( t1 - t2 ) = UзA3 ( t2tv ) and for n effects ...
Pagina 1054
... effect evapora- tors requires no special comment . In very large evaporators it may be desir- able to introduce a number of condensate connections rather than one large one . It is obvious that the condensate from any effect that takes ...
... effect evapora- tors requires no special comment . In very large evaporators it may be desir- able to introduce a number of condensate connections rather than one large one . It is obvious that the condensate from any effect that takes ...
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