Vapor-Liquid Equilibria. The System Methane - Propane - n - Butane at 100° F.

Rigas, T. J.; Mason, D. F.; Thodos, George

doi:10.1021/je60003a004

Cited by 27 publications

(6 citation statements)

References 4 publications

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“…6 Estimated critical. b Molal equilibrium ratio defined by: Kk = Vk/Xk-' Experimental study (15) and extrapolation from experimental data at higher temperatures (16). See Figure 1.…”

Section: Resultsmentioning

confidence: 99%

Phase equilibriums in the hydrocarbon systems. Phase behavior in the methane-propane-n-butane system

Wiese¹,

Jacobs²,

Sage³

1970

J. Chem. Eng. Data

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“…6 Estimated critical. b Molal equilibrium ratio defined by: Kk = Vk/Xk-' Experimental study (15) and extrapolation from experimental data at higher temperatures (16). See Figure 1.…”

Section: Resultsmentioning

confidence: 99%

Phase equilibriums in the hydrocarbon systems. Phase behavior in the methane-propane-n-butane system

Wiese¹,

Jacobs²,

Sage³

1970

J. Chem. Eng. Data

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“…The experimental equipment used in this investigation has been described (5,6,7). The basic feature of the equipment resides in an equilibrium cell, which includes a mercury-driven piston that can be made to vary the volume of the equilibrium chamber and thereby control the pressure of the system.…”

mentioning

confidence: 99%

Vapor-Liquid Equilibria for the Ethane-Propane System.

Matschke¹,

Thodos²

1962

J. Chem. Eng. Data

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“…V * jk Methane-propane-zz-butane (Rigas et al, 1959) 0.750 Methane-ethane-zz-butane (Cota and Thodos, 1962) 0.857 Methane-propane-zz-pentane (Dourson et al, 1943) 0.889 Methane-ethane-zz-pentane (Billman et al, 1948) 1.000…”

Section: Application Of Methodsmentioning

confidence: 99%