Light gas solubility in phenanthrene: the hydrogen—phenanthrene and methane—phenanthrene systems

Malone, Patrick V.; Kobayashi, Riki

doi:10.1016/0378-3812(90)85012-y

Cited by 24 publications

(11 citation statements)

References 9 publications

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“…A comparison of data on hydrogen + phenanthrene is shown in Figure 14. The observeddeviations indicate remarkablygood agreement between the dataof Malone [35] and those measuredin this study. The EOS representationsof the hydrogen solubilitiesin n-paraffins are shown in Table VI.…”

Section: Hydroeen+ Hydrocarbonssupporting

confidence: 87%

Equilibrium and volumetric data and model development for coal fluids. Final report, October 1, 1990--September 30, 1993

Robinson¹,

Gasem²,

Park³

et al. 1994

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Section: Hydroeen+ Hydrocarbonssupporting

confidence: 87%

Equilibrium and volumetric data and model development for coal fluids. Final report, October 1, 1990--September 30, 1993

Robinson¹,

Gasem²,

Park³

et al. 1994

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“…Experimental data taken from Malone and Kobayashi[45]. gen/phenanthrene system at 423.15 and 473.15 K (experimental data taken from Malone and Kobayashi[45]). The results of simulations and EOS calculations are plotted on the Figs.…”

mentioning

confidence: 99%

Hydrogen/hydrocarbon phase equilibrium modelling with a cubic equation of state and a Monte Carlo method

Ferrando

Ungerer

2007

Fluid Phase Equilibria

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“…This is also the case for the mixture for C 1 /phenanthrene (Fig. 7) where k ij values obtained from the low pressure VLE data of Malone and Kobayashi (1990) and Darwish et al (1994), are totally unacceptable at high pressures. Therefore, high pressure experimental VLE data are required for asymmetric systems in order to improve the prediction capability of EoS.…”

Section: Prediction Of High Pressure Vlementioning

confidence: 60%

Performance of Cubic Eos At High Pressures

Stamataki

Tassios

1998

Rev. Inst. Fr. Pét.

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Cet article prŽsente une Žvaluation des performances des Žquations d'Žtats (EoS) cubiques pour la prŽvision des comportements de phases des mŽlanges hyperbares. Il met en Žvidence un certain nombre de probl•mes auxquels il devrait •tre rŽpondu d'une mani•re coopŽrative. Les points relatifs ˆ la dŽfinition des param•tres des EoS, tels que les coefficients d'interaction, les propriŽtŽs critiques des composants hydrocarbonŽs et la translation de volume sont examinŽs. Plusieurs types dÕinformations ont ŽtŽ pris en compte dans cette Žtude : les donnŽes expŽrimentales dÕŽquilibre liquide-vapeur (ELV), les donnŽes compositionnelles et volumŽtriques issues dÕŽquilibres isothermes jusquÕˆ 4 000 bar pour les mŽlanges binaires, les donnŽes PVT jusquÕˆ 2 000 bar pour des mŽlanges binaires et des syst•mes synthŽtiques multicomponants. PERFORMANCE OF CUBIC EOS AT HIGH PRESSURESThis paper presents an evaluation of the performance of cubic equations of state in the prediction of the phase behavior of hyperbaric mixtures. It points out a number of problems that should be resolved in a cooperative way. Items related to EoS parameter definitions such as interaction coefficients, critical properties of hydrocarbon compounds and volume translation are investigated. VLE experimental data, isothermal flash compositional and volumetric data up to 4000 bar as well as PVT data up to 2000 bar for binary mixtures and synthetic multicomponent systems have been considered in this study.Correlation and prediction results are presented with the translated and modified Peng-Robinson (t-mPR) EoS. It is shown that serious problems are encountered at high pressure, when extrapolated interaction coefficients are used. Prediction of saturation pressures of gas condensates is more satisfactory when binary interaction RESULTADO DE LAS ECUACIONES DE ESTADO CòBICAS DE ALTAS PRESIONESSe presenta en este art'culo una evaluaci-n de los resultados de las ecuaciones de estado (EoS) coebicas para la previsi-n de los comportamientos de fases de mezclas hiperb ‡ricas y se hace resaltar cierto noemero de problemas a que se deber'a poder responder de forma cooperativa. Se examinan los puntos relativos a la definici-n de los par ‡metros de las EoS, como, por ejemplo, los coeficientes de interacci-n, las propiedades cr'ticas de los componentes hidrocarbonados y la traslaci-n de volumen. Se han tenido en cuenta y debidamente comentados en el presente estudio, los datos experimentales de ELV, las isotermas flash molares y volumŽtricas hasta 4000 bar para mezclas binarias, as' como los datos PVT hasta 2000 bar para las mezclas binarias y los sistemas sintŽticos de componentes moeltiples.Tomando como punto de partida la ecuaci-n de Peng-Robinson (t-mPR) trasladada y modificada se presentan diversas correlaciones y resultados previsionales. Se demuestra que se habr ‡ de tropezar con serios problemas al alcanzar las altas presiones en caso de que se utilicen coeficientes de interacci-n extrapolados. Las previsiones de las presiones de saturaci-n de los gases de condens...

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Light gas solubility in phenanthrene: the hydrogen—phenanthrene and methane—phenanthrene systems

Cited by 24 publications

References 9 publications

Equilibrium and volumetric data and model development for coal fluids. Final report, October 1, 1990--September 30, 1993

Equilibrium and volumetric data and model development for coal fluids. Final report, October 1, 1990--September 30, 1993

Hydrogen/hydrocarbon phase equilibrium modelling with a cubic equation of state and a Monte Carlo method

Performance of Cubic Eos At High Pressures

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