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Ethane thermodynamic properties

The increasing ranges of pressure and temperature of interest to technology for an ever-increasing number of substances would necessitate additional tables in this subsection as well as in the subsec tion Thermodynamic Properties. Space restrictions preclude this. Hence, in the present revision, an attempt was made to update the fluid-compressibihty tables for selected fluids and to omit tables for other fluids. The reader is thus referred to the fourth edition for tables on miscellaneous gases at 0°C, acetylene, ammonia, ethane, ethylene, hydrogen-nitrogen mixtures, and methyl chloride. The reader is also... [Pg.184]

Figure 11-30. Vapor pressure curve for ethane refrigerant. (Used by permission Starling, K. E. Fluid Thermodynamic Properties for Light Petroleum Systems, 1973. Gulf Publishing Co., Houston, Texas. All rights reserved.)... Figure 11-30. Vapor pressure curve for ethane refrigerant. (Used by permission Starling, K. E. Fluid Thermodynamic Properties for Light Petroleum Systems, 1973. Gulf Publishing Co., Houston, Texas. All rights reserved.)...
Benedict, M., Webb, G.B., and Rubin, L.C. An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures, I. Methane, Ethane, Propane and n-Butane, J. Chem. Phys. (April 1940) 8, 334-345. [Pg.145]

Benning, A.F., McHamess, R.C. (1940) Thermodynamic properties of fluorochloromethanes and ethanes. Ind. Eng. Chem. 32,497-499. Beyerlein, A.L., DesMarteau, D.D., Kul, I., Zhao, G. (1998) Properties of novel fluorinated compounds and their mixtures as alternative refrigerants. Fluid Phase Equilibria 150-151, 287-296. [Pg.325]

Figure 11 Plots of the ethane solvent parameters vs. density for the thermodynamic properties that enter the theory at the two temperature, 34°C (solid lines) and 50°C (dashed lines), the temperatures for the data and theory curves in Fig. 10. Most of the parameters change dramatically with temperature. Figure 11 Plots of the ethane solvent parameters vs. density for the thermodynamic properties that enter the theory at the two temperature, 34°C (solid lines) and 50°C (dashed lines), the temperatures for the data and theory curves in Fig. 10. Most of the parameters change dramatically with temperature.
The values in these tables were generated from the NIST REFPROP software (Lemmon, E.W., McLinden, M.O., and Huber, M.L., NIST Standard Reference Database 23 Reference Fluid Thermodynamic and Transport Properties—REFPROP, National Institute of Standards and Technology, Standard Reference Data Program, Gaithersburg, Md., 2002, Version 7.1). The primary source for the thermodynamic properties is Buecker, D., and Wagner, W, A Reference Equation of State forthe Thermodynamic Properties of Ethane for Temperatures from the Melting Line to 675 K and Pressures up to 900 MPa, J. Phys. Chem. Ref. Data, 35(1) 205-206, 2006. The source for viscosity and thermal conductivity is Friend, D.G., Ingham, H., and Ely, J.E, Thermophysical Properties of Ethane, /. Phys. Chem. R. Data, 35(l) 205-266, 2006. [Pg.293]

Utility of the present type of equation of state for tabulating thermodynamic properties has been demonstrated in major NBS publications on methane, ethane, and propane. For readers accustomed to BWR-type equations, with their attendant difficulties, the programming of the present equation, including numerical integrations, probably is no more complicated, and may be logically much simpler. [Pg.360]

Buecker, D. and Wagner, W, A Reference Equation of State for the Thermodynamic Properties of Ethane for Temperatures from the Melting Line to 675 K and Pressures up to 900 MPa, J. Phys. Chem. Ref. Data, 35, 205, 2006. [Pg.926]


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Ethane properties

Thermodynamic Properties of Ethane

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