2003
DOI: 10.1021/je0255271
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Solubility of Ethane in N-Formyl Morpholine

Abstract: Measurements of the solubility of ethane in N-formyl morpholine have been made over a range of temperatures from (298 to 403) K. Pressures varied between (0.1 and 20.3) MPa. The data were correlated with the Peng−Robinson equation of state.

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Cited by 12 publications
(16 citation statements)
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References 5 publications
(10 reference statements)
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“…The literature data appear a little dispersed, but close to the new data except those measured by Stephenson [9] which are significantly different (see figure 2). In fact, a minimum in toluene Nomenclature A, B, C, D, E adjustable parameters, equations (4) and (6 Greek letters c activity coefficient U fugacity coefficient solubility vs. temperature occurs around 300 K. This minimum is confirmed by Jou and Mather [12]. Moreover, the extrapolation of the tendency curve determined on our experimental data indicates the existence of a minimum too.…”
Section: Solubility In Watersupporting
confidence: 76%
See 1 more Smart Citation
“…The literature data appear a little dispersed, but close to the new data except those measured by Stephenson [9] which are significantly different (see figure 2). In fact, a minimum in toluene Nomenclature A, B, C, D, E adjustable parameters, equations (4) and (6 Greek letters c activity coefficient U fugacity coefficient solubility vs. temperature occurs around 300 K. This minimum is confirmed by Jou and Mather [12]. Moreover, the extrapolation of the tendency curve determined on our experimental data indicates the existence of a minimum too.…”
Section: Solubility In Watersupporting
confidence: 76%
“…In fact, up to 0.5 MPa, methane has a very small influence on toluene solubility (deviation is less than 1% between benzene mole fraction measured at 0.5 MPa and benzene mole fraction calculated by extrapolation to zero methane partial pressure as described in ref [2] and [5]). Several authors have studied the solubility of toluene in pure water [6,[8][9][10][11][12]. Corresponding data are presented in table 3.…”
Section: Solubility In Watermentioning
confidence: 99%
“…We have extrapolated these to 298K through plots of log γ ∞ against 1/T(K) or plots of log Vg o against 1/T(K) for each solute and obtained values of log K s and log P s for 50 solutes. In addition, there are data for a few more gases, 90, 91 making 55 solutes in all as given in Table S4. Application of eqn (3) yielded eqn (11).…”
Section: Resultsmentioning
confidence: 99%
“…Recently, solubilities of aqueous systems at high temperatures have been paid much attention. These data are required for pollution assessment of high-temperature water discharged from laboratories and industrial plants, [9][10][11][12][13] and moreover, for designing an environment protecting technology that uses high-temperature water in the sub-to supercritical condition as a reaction medium for destruction of toxic waste chemicals. 14 -17 In addition, the high-temperature solubility data are indispensable to designs, operations and maintenance of plants for oil refineries and petrochemical industry.…”
Section: Introductionmentioning
confidence: 99%
“…The transferring of a sample without disturbing equilibrium and/or without composition change is rather difficult, particularly at high temperatures and pressures. 10,21 Therefore most of the solubility data of the water-benzene system have been limited at the three-phase equilibrium pressures, 9,10,13,21 and a few other pressures at higher temperatures. [22][23][24][25] In addition, effect of pressure on the mutual solubilities has not been fully understood, in contrast to the temperature effect, namely the significant increase in the mutual solubilities with increasing temperature.…”
Section: Introductionmentioning
confidence: 99%