Chemical Engineer's Handbook: Prepared by a Staff of SpecialistJohn Howard Perry McGraw-Hill, 1941 - 3029 pagine |
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Pagina 479
... International Critical Tables , " vol . 2 , p . 83 . Temp . , ° C . 2000 1750-2000 1750-2000 1565-1785 2200-2240 1990 1850-2050 1500-1750 2800 2200-2600 2150-2165 1700 1685-1800 1816 . 2135 2500-2950 2000-2600 Table 147. Producing and ...
... International Critical Tables , " vol . 2 , p . 83 . Temp . , ° C . 2000 1750-2000 1750-2000 1565-1785 2200-2240 1990 1850-2050 1500-1750 2800 2200-2600 2150-2165 1700 1685-1800 1816 . 2135 2500-2950 2000-2600 Table 147. Producing and ...
Pagina 1127
... International Critical Tables , " vol . 3 , p . 259 . Table 16.2 Methane ( CH4 ) 1. ° C .... 0 5 10 15 20 25 30 35 35 10X H. 2.24 2.59 2.97 3.37 3.76 4.13 4.49 4.86 t , ° C .. 40 45 50 60 70 80 90 100 10X H. 5.20 5.51 5.77 6.26 6.66 ...
... International Critical Tables , " vol . 3 , p . 259 . Table 16.2 Methane ( CH4 ) 1. ° C .... 0 5 10 15 20 25 30 35 35 10X H. 2.24 2.59 2.97 3.37 3.76 4.13 4.49 4.86 t , ° C .. 40 45 50 60 70 80 90 100 10X H. 5.20 5.51 5.77 6.26 6.66 ...
Pagina 1131
... tables appearing in the " International Critical Tables , " vol . 3 , pp . 261–270 , does not include , by any means , all the solutes and solvents considered in the " International Critical Tables , " but only some of those most ...
... tables appearing in the " International Critical Tables , " vol . 3 , pp . 261–270 , does not include , by any means , all the solutes and solvents considered in the " International Critical Tables , " but only some of those most ...
Sommario
Mathematical Tables and Weights and Measures | 1 |
Mathematics 2 | 133 |
Physical and Chemical Data | 270 |
Copyright | |
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acetate acid alcohol aldehydes amines angle benzene bromide calculated Carbon catalyst cent chart Chem CHEMICAL DATA Chemical Engineering chloride circle coefficient Common Logarithms constant pressure curve density diameter entropy equal equation equilibrium ether Ethyl Ethyl alcohol Ethyl chloride Example flow fluid Formula fraction free energy fugacity function gage gases given H₂O heat capacity heat content heat of vaporization HNO3 hydrogen Inorganic insol ketone latent heat linear liquid Logarithms measured meter method mixture molal molecules nitrate obtained Organic Compounds orifice oxide phase Phenol PHYSICAL AND CHEMICAL pipe Precipitate Radians reactants reaction salts scale Sodium solid Solubility solution Specific Heats standard substances sulfate Sulfur sulfuric acid surface temperature thermodynamic tion triangle tube values vapor pressure velocity viscosity volume weight