2011
DOI: 10.1016/j.jct.2011.01.011
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Measurement of (liquid+liquid) equilibria for ternary systems of (N-formylmorpholine+benzene+cyclohexane) at temperatures (303.15, 308.15, and 313.15)K

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Cited by 19 publications
(9 citation statements)
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“…Dimethylsulfoxide, Sulfolane, N-methylpyrrolidone, N-formylmorpholine and methylcarbonate are most widely used as extractants for aromatic compounds [10]. Studies had been carried out to establish the liquid-liquid equilibrium (LLE) data of the ternary systems involving the conventional solvents such as ethylene carbonate [11,12], dimethyl sulfone [13], ethylene glycol [3,14], and N-formylmorpholine [15]. Apart from ternary, the LLE data for quaternary systems had also been reported for N, N-dimethylformamide (DMF) + sodium thiocyanate (NaSCN) [16], and N,N-dimethylformamide + potassium thiocyanate [9].…”
Section: Introductionmentioning
confidence: 99%
“…Dimethylsulfoxide, Sulfolane, N-methylpyrrolidone, N-formylmorpholine and methylcarbonate are most widely used as extractants for aromatic compounds [10]. Studies had been carried out to establish the liquid-liquid equilibrium (LLE) data of the ternary systems involving the conventional solvents such as ethylene carbonate [11,12], dimethyl sulfone [13], ethylene glycol [3,14], and N-formylmorpholine [15]. Apart from ternary, the LLE data for quaternary systems had also been reported for N, N-dimethylformamide (DMF) + sodium thiocyanate (NaSCN) [16], and N,N-dimethylformamide + potassium thiocyanate [9].…”
Section: Introductionmentioning
confidence: 99%
“…The main solvents reported in the literature for aliphatic–aromatic liquid–liquid extraction, which have also been used in industrial separations, are sulfolane and glycols, ,, but many compounds have been tested for application in aliphatic–aromatic separations, including dimethyl sulfoxide, , ethylene and propylene carbonate, ,, N -methylpyrrolidone, N -formylmorpholine, ,, and dimethylformamide, among others. The ternary aliphatic + aromatic + solvent systems, with compositional analysis, distribution factors, and selectivities, are detailed in each study, which is useful for performance comparisons among different compound combinations.…”
Section: Introductionmentioning
confidence: 99%
“…The NRTL equation was used to model the liquid phases together with the Redlich–Kwong equation of state for the vapor phase. The NRTL model is able to successfully represent deviations at low pressure (LP) with numerous studies demonstrating the effectiveness of its representation of ternary phase equilibrium measurements consisting of aliphatic–aromatic solvent mixtures. The binary interaction parameters are automatically extracted from APV100 VLE-LIT and APV100 LLE-ASPEN databanks.…”
Section: Process Economicsmentioning
confidence: 99%
“…Since the early 1960s, the sulfolane process became more commonly used due to the observation that the solvent (sulfolane , ) demonstrated improved solvent characteristics. Other organic chemicals were then studied in the following decades as potential solvents such as 1-methylpyrrolidin-2-one (NMP), morpholine-4-carbaldehyde (NFM), N , N -dimethylmethanamide (DMF), dimethyl sulfoxide (DMSO), and propylene carbonate …”
Section: Introductionmentioning
confidence: 99%