Ternary liquid-liquid equilibria for mixtures of an N-alkane plus an aromatic hydrocarbon plus N-methyl-2-pyrrolidone at 298.2 K and 1 atm

被引:52
作者
Letcher, TM [1 ]
Naicker, PK [1 ]
机构
[1] Univ Natal, Dept Chem & Appl Chem, ZA-4041 Durban, South Africa
关键词
D O I
10.1021/je980114e
中图分类号
O414.1 [热力学];
学科分类号
摘要
Tie lines and liquid-liquid equilibrium data are presented for mixtures of an n-alkane + toluene + N-methyl-2-pyrrolidone and. mixtures of n-hexadecane + an aromatic hydrocarbon + N-methyl-2-pyrrolidone at 298.2 K and 1 atm pressure, n-Alkane refers to n-hexane or n-nonane or n-tetradecane or n-hexadecane, and an aromatic hydrocarbon refers toluene or o-xylene or m-xylene or p-xylene or mesitylene or ethylbenzene. N-methyl-2-pyrrolidone is an important solvent used in the extraction of aromatic compounds from alkane-aromatic mixtures. The data presented here complements data in the literature and gives a broader description of the phase equilibrium properties of the mixtures generated by an n-alkane + an aromatic hydrocarbon and N-methyl-2-pyrrolidone.
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页码:1034 / 1038
页数:5
相关论文
共 10 条
[1]   MEASUREMENT OF PHASE-EQUILIBRIUM IN MULTICOMPONENT SYSTEMS OF AROMATICS WITH N-METHYLPYRROLIDONE AND PREDICTIONS WITH UNIFAC [J].
ALZAYIED, TA ;
ALSAHHAF, TA ;
FAHIM, MA .
FLUID PHASE EQUILIBRIA, 1990, 61 (1-2) :131-144
[2]   Effect of temperature on liquid-liquid equilibrium - Benzene-acetone-water system and docosane-1,6-diphenylhexane-furfural system [J].
Briggs, SW ;
Comings, EW .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1943, 35 :411-417
[3]   LIQUID LIQUID EQUILIBRIA FOR THE SYSTEM N-METHYLPYRROLIDONE + TOLUENE + N-HEPTANE - UNIFAC INTERACTION PARAMETERS FOR N-METHYLPYRROLIDONE [J].
FERREIRA, PO ;
FERREIRA, JB ;
MEDINA, AG .
FLUID PHASE EQUILIBRIA, 1984, 16 (03) :369-379
[4]   PHASE-EQUILIBRIA FOR THE SEPARATION OF AROMATIC AND NONAROMATIC COMPOUNDS USING MIXED-SOLVENTS .1. THE SYSTEM NORMAL-HEPTANE-TOLUENE-N-METHYLPYRROLIDONE MONOETHYLENEGLYCOL [J].
FERREIRA, PO ;
BARBOSA, D ;
MEDINA, AG .
FLUID PHASE EQUILIBRIA, 1984, 15 (03) :309-322
[5]   CORRELATION OF BINODAL CURVE IN A TERNARY LIQUID MIXTURE WITH ONE PAIR OF IMMISCIBLE LIQUIDS [J].
HLAVATY, K .
COLLECTION OF CZECHOSLOVAK CHEMICAL COMMUNICATIONS, 1972, 37 (12) :4005-4007
[6]   LIQUID LIQUID EQUILIBRIA FOR MIXTURES OF AN ALKANOL PLUS WATER PLUS A METHYL-SUBSTITUTED BENZENE AT 25-DEGREES-C [J].
LETCHER, TM ;
SISWANA, PM .
FLUID PHASE EQUILIBRIA, 1992, 74 :203-217
[7]   LIQUID LIQUID EQUILIBRIA FOR MIXTURES OF AN ALKANOL + DIISOPROPYL ETHER + WATER AT 25-DEGREES-C [J].
LETCHER, TM ;
RAVINDRAN, S ;
RADLOFF, S .
FLUID PHASE EQUILIBRIA, 1992, 71 (1-2) :177-188
[8]  
MULLER JM, 1967, 7 WORLD PET C, V4, P13
[9]  
Riddick JA., 1986, Organic Solvents. Physical Properties and Methods of Purification, V4
[10]   THE SYSTEM ACETONE WATER 1,1,2-TRICHLOROETHANE - TERNARY LIQUID AND BINARY VAPOR EQUILIBRIA [J].
TREYBAL, RE ;
WEBER, LD ;
DALEY, JF .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1946, 38 (08) :817-821