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Pressure and Temperature Dependence of Liquid Density


pressure and TemperaTure dependence of liquid densiTy
This table gives data on the variation of the density of some common liquids with pressure and temperature . The pressure dependence is described to first order by the isothermal compressibility coefficient κ defined as κ = -(1/V) (?V/?P)T where V is the volume, and the temperature dependence by the cubic expansion coefficient α, α = (1/V) (?V/?T)P Substances are listed by molecular formula in the Hill order . More precise data on the variation of density with temperature over a wide temperature range can be found in Reference 1 .
Molecular formula Cl3P H2O Hg CCl4 CHBr3 CHCl3 CH2Br2 CH2Cl2 CH3I CH4O CS2 C2Cl4 C2HCl3 C2H2Cl2 C2H4Cl2 C2H4Cl2 C2H4O2 C2H5Br C2H5I C2H6O C2H6O2 C3H6O C3H7Br C3H7Cl C3H7I C3H8O C3H8O C3H8O2 C3H8O2 C3H8O3 C4H8O2 Name Phosphorus trichloride Water

references
1 . Lide, D . R ., and Kehiaian, H . V ., CRC Handbook of Thermophysical and Thermochemical Data, CRC Press, Boca Raton, FL, 1994 . 2 . Le Neindre, B ., Effets des Hautes et Très Hautes Pressions, in Techniques de l’Ingénieur, Paris, 1991 . 3 . Landolt-B?rnstein, Numerical Data and Functional Relationships in Science and Technology, New Series, IV/4, High-Pressure Properties of Matter, Springer-Verlag, Heidelberg, 1980 . 4 . Riddick, J .A ., Bunger, W .B ., and Sakano, T .K ., Organic Solvents, Fourth Edition, John Wiley & Sons, New York, 1986 . 5 . Isaacs, N . S ., Liquid Phase High Pressure Chemistry, John Wiley, New York, 1981 .

Mercury Tetrachloromethane

Tribromomethane Trichloromethane Dibromomethane Dichloromethane Iodomethane Methanol Carbon disulfide Tetrachloroethylene Trichloroethylene trans-1,2-Dichloroethylene 1,1-Dichloroethane 1,2-Dichloroethane Acetic acid Bromoethane Iodoethane Ethanol Ethylene glycol Acetone 1-Bromopropane 1-Chloropropane 1-Iodopropane 1-Propanol 2-Propanol 1,2-Propanediol 1,3-Propanediol Glycerol Ethyl acetate

Isothermal compressibility t/°C κ × 104/MPa–1 20 9 .45 20 4 .591 25 4 .524 30 4 .475 20 0 .401 20 10 .50 40 12 .20 70 15 .6 50 8 .76 20 9 .96 50 12 .9 27 6 .85 25 10 .3 27 10 .3 20 12 .14 40 13 .83 20 9 .38 40 10 .6 25 7 .56 25 8 .57 25 11 .2 20 7 .97 30 8 .46 20 9 .08 80 13 .7 20 11 .53 20 9 .82 20 11 .19 70 15 .93 20 3 .64 20 12 .62 40 15 .6 0 10 .22 0 12 .09 0 10 .22 0 8 .43 40 13 .32 0 4 .45 0 4 .09 0 2 .54 20 11 .32 60 16 .2

Cubic expansion coefficient t/°C α × 103/°C–1 20 1 .9 20 0 .206 25 0 .256 30 0 .302 20 0 .1811 20 1 .14 40 1 .21 70 1 .33 25 0 .91 20 1 .21 50 1 .33 25 25 20 40 20 35 25 25 25 25 20 20 80 20 25 20 70 20 20 40 25 20 25 0 40 20 20 20 20 60 1 .39 1 .26 1 .49 1 .59 1 .12 1 .16 1 .02 1 .17 1 .36 0 .93 1 .14 1 .08 1 .38 1 .31 1 .17 1 .40 1 .67 0 .626 1 .46 1 .57 1 .2 1 .4 1 .09 1 .22 1 .55 0 .695 0 .61 0 .520 1 .35 1 .54

6-140

Pressure and Temperature Dependence of Liquid Density
Molecular formula C4H9Br C4H9I C4H10O C4H10O C4H10O3 C5H10 C5H11Br C5H11I C5H12 C5H12O C6H5Br C6H5Cl C6H5NO2 C6H6 C6H6O C6H7N C6H12 C6H14 C6H14 C6H14 C6H14 C6H14O C6H15NO3 C7H8 C7H8O C7H14 C7H16 C8H10 C8H10 C8H10 C8H16 C8H18 C8H18O C9H12 C9H14O6 C9H20 C10H22 C11H24 C12H26 C13H28 C14H30 C15H32 C16H22O4 C16H34 C19H36O2 Name 1-Bromobutane 1-Iodobutane 1-Butanol Diethyl ether Diethylene glycol Cyclopentane 1-Bromopentane 1-Iodopentane Pentane 1-Pentanol Bromobenzene Chlorobenzene Nitrobenzene Benzene Phenol Aniline Cyclohexane Hexane 2-Methylpentane 3-Methylpentane 2,3-Dimethylbutane 1-Hexanol Triethanolamine Toluene Anisole Cycloheptane Heptane o-Xylene m-Xylene p-Xylene Cyclooctane Octane 1-Octanol Mesitylene Triacetin Nonane Decane Undecane Dodecane Tridecane Tetradecane Pentadecane Butyl phthalate Hexadecane Methyl oleate Isothermal compressibility t/°C κ × 104/MPa–1 25 10 .26 0 7 .73 0 8 .10 20 18 .65 30 20 .85 0 3 .34 20 13 .31 0 8 .42 0 7 .56 25 21 .80 0 7 .71 20 6 .46 20 7 .45 20 4 .93 25 9 .66 45 11 .28 60 6 .05 20 4 .53 80 6 .32 20 11 .30 60 15 .2 25 16 .69 45 20 .27 0 13 .97 0 14 .57 20 17 .97 25 8 .24 0 3 .61 20 8 .96 50 11 .0 20 6 .60 20 9 .22 25 14 .38 25 8 .10 20 8 .46 25 8 .59 20 8 .03 25 12 .82 45 15 .06 25 7 .64 25 8 .14 0 4 .49 25 11 .75 25 10 .94 25 10 .31 25 9 .88 25 9 .48 25 9 .10 25 8 .82 0 5 .0 25 8 .57 45 9 .78 0 6 .18 Cubic expansion coefficient t/°C α × 103/°C–1 20 1 .13 25 1 .02 0 1 .12 20 1 .65 30 1 .72 20 0 .635 20 1 .35 25 1 .04 25 0 20 20 25 25 45 60 20 80 20 60 25 45 25 25 25 25 55 20 50 20 25 25 20 25 25 45 25 25 25 25 25 25 25 25 25 25 1 .64 1 .02 0 .86 0 .94 0 .833 1 .14 1 .21 0 .82 0 .81 0 .91 1 .15 1 .29 1 .41 1 .52 1 .43 1 .40 1 .39 1 .03 0 .53 1 .05 1 .13 0 .951 1 .26 0 .96 0 .99 1 .00 1 .16 1 .23 0 .827 0 .94 0 .94 1 .08 1 .02 0 .97 0 .93 0 .90 0 .87 0 .86

6-141

60

0 .85



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