Zobrazeno 1 - 10
of 43
pro vyhledávání: '"Yun Chen"'
Publikováno v:
Journal of Chemical & Engineering Data. 64:5497-5509
The extraction efficiency of the solvent on the polyphenols greatly determines whether the phenol-containing wastewater can be handled well. In this work, liquid–liquid equilibrium (LLE) data for t...
Publikováno v:
Journal of Chemical & Engineering Data. 64:4454-4464
Octan-2-one is a promising extraction solvent with low solubility in water. The experimental solubility behavior of benzene-1,2-diol, benzene-1,3-diol, or benzene-1,4-diol in mixtures of octan-2-on...
Publikováno v:
Journal of Chemical & Engineering Data. 64:3521-3534
Methyl isobutyl ketone (MIBK) had been successfully employed to extract phenols from coal gasification wastewater since 2009, and it has been proved to be an excellent extraction solvent. In this w...
Publikováno v:
Journal of Chemical & Engineering Data. 64:2801-2808
1-Dodecanol with low solubility in water is a potential solvent to extract phenol from wastewater. The liquid–liquid equilibrium data of the ternary system (1-dodecanol–phenol–water) were measured at 298.15, 313.15, 323.15, 333.15, and 343.15 K
Publikováno v:
Journal of Chemical & Engineering Data. 64:1349-1356
Isobaric vapor–liquid equilibrium (VLE) data for the dimethyl oxalate + methanol and methanol + 1,2-butanediol binary systems, as well as the VLE for the dimethyl oxalate + methanol + 1,2-butanedio...
Publikováno v:
Journal of Chemical & Engineering Data. 63:2376-2383
The phenols recovery process is a significant part of treating coal chemical wastewater with highly concentrated phenols and ammonia. Solvent extraction is an important unit for phenol recovery section. The accurate measurement of liquid–liquid equ
Publikováno v:
Journal of Chemical & Engineering Data. 62:1929-1936
Liquid–liquid equilibrium (LLE) for the methyl tert-butyl ketone (MTBK) + o-, m-, and p-cresol + water ternary systems, at temperatures of (298.2, 313.2, and 323.2) K and 101 kPa, were determined in this work. High distribution coefficient and sele
Publikováno v:
Journal of Chemical & Engineering Data. 62:141-147
The tie-line data for the {4-methylpentan-2-one + 3-methylphenol, 4-methylphenol + water} ternary systems at 298.2, 313.2, and 323.2 K were measured under 101.3 kPa. The partition coefficient and separation factor were computed in order to estimate t
Publikováno v:
Journal of Chemical & Engineering Data. 61:2493-2498
In this work, liquid–liquid equilibria (LLE) data for the ternary system {mesityl oxide (1) + phenol (2) + water (3)} were measured at 298.15, 313.15, and 323.15 K under atmospheric pressure. The experimental LLE data were proven to be highly relia
Publikováno v:
Journal of Chemical & Engineering Data. 61:2221-2225
Liquid–liquid equilibria (LLE) data for the ternary system, methyl isopropyl ketone (MIPK) + phenol + water, were measured at 298.15 K, 313.15 and 323.15 K under atmospheric pressure by gas chromatography. Distribution coefficients and separation f