1986
DOI: 10.1016/0021-9614(86)90020-0
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The excess enthalpies of (carbon dioxide + pentane) at 348.15, 373.15, 413.15, 470.15, and 573.15 K from 7.58 to 12.45 MPa

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Cited by 19 publications
(8 citation statements)
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“…To fit experimental data with changes of sign, Christensen et al [12][13][14] use an extended version of the Redlich + Kister model. A new polynomial is added as a denominator in equation (1):…”
Section: Empirical Correlationsmentioning
confidence: 99%
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“…To fit experimental data with changes of sign, Christensen et al [12][13][14] use an extended version of the Redlich + Kister model. A new polynomial is added as a denominator in equation (1):…”
Section: Empirical Correlationsmentioning
confidence: 99%
“…Even when the model is appropriate for other ranges and deviations for each experimental point, and also the mean deviation, are small, the denominator can be zero for some values of x, thus leading to a discontinuity. In some cases [11][12][13][14], equation (2) has been used together with other simple models for certain ranges of the mole fraction. This possibility will not be taken into account in this present work, i.e., we shall study the fit with only a single model.…”
Section: Empirical Correlationsmentioning
confidence: 99%
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“…Simultaneously, Christensen et al [4,5] were setting up a new highpressure flow calorimeter able to detect both exothermic and endothermic processes which was quickly applied to determine the excess enthalpies of CO 2 þ hydrocarbon mixtures in the critical region. From 1983 to his early dead, James J. Christensen published data of mixtures such as CO 2 þ ethane [6], þ pentane [7,8], þ hexane [9,10], þ cyclohexane [11][12][13][14], þ decane [15,16], þ toluene [17][18][19][20] and þ pyridine [21,22]. Figure 1 shows the experimental P,T conditions at which data are available for three of these systems.…”
mentioning
confidence: 99%