Virial coefficients of ethanol from 373.07 to 473.15 K

Wilson, Karen; Lindley, Daniel D.; Kay, Webster B.; Hershey, Harry C.

doi:10.1021/je00037a003

Cited by 15 publications

(2 citation statements)

References 8 publications

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“…The (p,r,T ) properties for gaseous ethanol have been measured in the temperature range from T=373 K to T=473 K at pressures up to 0.39 MPa. (13) No measurements for liquid ethanol are available in the temperature range between T=363 K and T=473 K, as far as we have surveyed.…”

Section: Introductionmentioning

confidence: 99%

Densities for liquid ethanol in the temperature range from 310 K to 480 K at pressures up to 200 MPa

Takiguchi

Uematsu

1996

The Journal of Chemical Thermodynamics

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Density measurements at given temperatures and pressures in the compressed liquid phase for ethanol were carried out with a metal-bellows variable volumometer along eight isotherms between 310 K and 480 K at pressures from the vapor pressure to 200 MPa. The results cover the high-density region from 536 kg·m −3 to 882 kg·m −3 . The experimental uncertainties of temperature T, pressure p, and density r were estimated to be 24 mK, 20.0010·p, and 20.0010·r, respectively. Measurements of saturated liquid density at temperatures from 320 K to 480 K are also reported. The isothermal compressibility and isobaric expansivity on the basis of the present results are presented. 7

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Section: Introductionmentioning

confidence: 99%

Densities for liquid ethanol in the temperature range from 310 K to 480 K at pressures up to 200 MPa

Takiguchi

Uematsu

1996

The Journal of Chemical Thermodynamics

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“…3 Dymond and Smith phenol (Figure 10) 1 Kudchadker et al 4 Kretschmer and Wiebe 2 Opel 5 Knoebel and Edmister 27 hydrogen (Figure 4) 1 TRC 21 6 Wilson et al 4 Dymond and Smith 29 7 Smith and Srivastava helium (Figure 3) 1 TRC 21 Neon (Figure 5) 2 Dymond and Smith 29 2 McCarty 4 Dymond and Smith 29 4 Kestin et al …”

Section: Evaluation Of Hydrogen-bonding Substancesmentioning

confidence: 99%

The Second Virial Coefficient and the Redlich−Kwong Equation

Mathias

2003

Ind. Eng. Chem. Res.

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A two-parameter corresponding-states correlation, based upon the Redlich−Kwong equation, is proposed for the second virial coefficient at relatively high temperature (reduced temperature above 0.8). This remarkably simple correlation suggests an improvement to the venerable Redlich−Kwong equation of state, gives guidance for the high-temperature extrapolation of α-functions, and provides an independent tool to evaluate theoretical and empirical correlations for the second virial coefficient.

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