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Compres sibility

Kj = valve coefficient of discharge = 0.92 Pi = flowing pressure, psia MW = molecular weight of gas = 17,4 Z = compres-sibility factor = 0.9561 C = gas constant based on ratio of specific heats Cp/C T = flowing temperature, R Kb = back-pressure correction factor... [Pg.384]

Figure 6.6-2 Compres.sibility factors for different fluids as a function of the reduced temperature and pressure. [Reprinted with permi.ssion from G.-J. Su, hid. Eng. Chem. 38. 803 (1946). Copyright American Chemical Society.]... Figure 6.6-2 Compres.sibility factors for different fluids as a function of the reduced temperature and pressure. [Reprinted with permi.ssion from G.-J. Su, hid. Eng. Chem. 38. 803 (1946). Copyright American Chemical Society.]...
Figure 9.4-1 Compres.sibility factors for nitrogen-butane mixtures at 444.3 K. [Data of R. B. Evans and C. M. Watson, Chem. Eng. Data Sen, 1, 67 (1956). Based on figure in J. M. Prausnitz, Molecular Thermodynamics of Fluid-Phase Equilibria, 1969. Reprinted with permission from Prentice Hall, Englewood. Cliffs, N.J.]... Figure 9.4-1 Compres.sibility factors for nitrogen-butane mixtures at 444.3 K. [Data of R. B. Evans and C. M. Watson, Chem. Eng. Data Sen, 1, 67 (1956). Based on figure in J. M. Prausnitz, Molecular Thermodynamics of Fluid-Phase Equilibria, 1969. Reprinted with permission from Prentice Hall, Englewood. Cliffs, N.J.]...
Water differs from simple liquids. Figures 9.5 and 9.6 show that the thermal expansion coefficient = IV)(dVldT)p and isothermal compres.sibility k =... [Pg.169]

See other pages where Compres sibility is mentioned: [Pg.225]    [Pg.487]    [Pg.225]    [Pg.94]    [Pg.225]    [Pg.487]    [Pg.225]    [Pg.94]   
See also in sourсe #XX -- [ Pg.131 ]



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