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Kerboub, Wahiba, Atik, Zadjia (2009) Solubility and Liquid−Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa. Journal of Chemical & Engineering Data, 54 (7) 2132-2136 doi:10.1021/je900059e

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Reference TypeJournal (article/letter/editorial)
TitleSolubility and Liquid−Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa
JournalJournal of Chemical & Engineering Data
AuthorsKerboub, WahibaAuthor
Atik, ZadjiaAuthor
Year2009 (July 9)Volume54
Issue7
PublisherAmerican Chemical Society (ACS)
DOIdoi:10.1021/je900059eSearch in ResearchGate
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Mindat Ref. ID14559076Long-form Identifiermindat:1:5:14559076:7
GUID0
Full ReferenceKerboub, Wahiba, Atik, Zadjia (2009) Solubility and Liquid−Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa. Journal of Chemical & Engineering Data, 54 (7) 2132-2136 doi:10.1021/je900059e
Plain TextKerboub, Wahiba, Atik, Zadjia (2009) Solubility and Liquid−Liquid Equilibrium of Aqueous Systems of Iodoethane with Methanol, Ethanol, or 1-Propanol at Temperature 298.15 K and Pressure 101.2 kPa. Journal of Chemical & Engineering Data, 54 (7) 2132-2136 doi:10.1021/je900059e
In(2009, July) Journal of Chemical & Engineering Data Vol. 54 (7) American Chemical Society (ACS)

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Atik, Zadjia, Kerboub, Wahiba (2008) Liquid−Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K. Journal of Chemical & Engineering Data, 53 (7) 1669-1671 doi:10.1021/je8001688
Atik, Zadjia, Kerboub, Wahiba (2009) Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)†. Journal of Chemical & Engineering Data, 54 (2) 282-285 doi:10.1021/je8002964
Atik, Zadjia, Chaou, Malika (2007) Temperature Effect on Liquid-Liquid Phase Equilibria of Aqueous Solutions of Fluorobenzene in Ethanol at the Pressure 101.2 kPa. Journal of Solution Chemistry, 36 (3) 387-394 doi:10.1007/s10953-006-9111-4
Kerboub, Wahiba, Atik, Zadjia (2010) A thermodynamic study on solubility and liquid−liquid phase behaviour for 2,2,2-trifluoroethanol+cyclohexane+1-butanol at three temperatures and pressure 101.3kPa. The Journal of Chemical Thermodynamics, 42 (11) 1330-1334 doi:10.1016/j.jct.2010.05.010
Atik, Zadjia, Chaou, Malika (2007) Solubilities and Phase Equilibria for Ternary Solutions of α,α,α-Trifluorotoluene, Water, and 2-Propanol at Three Temperatures and Pressure of 101.2 kPa. Journal of Chemical & Engineering Data, 52 (3) 932-935 doi:10.1021/je600526x
Deenadayalu, Nirmala, Bahadur, Indra, Hofman, Tadeusz (2011) Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure. Journal of Chemical & Engineering Data, 56 (4) 1682-1686 doi:10.1021/je100830b
Kerboub, Wahiba, Atik, Zadjia (2009) Phase diagrams of (hexane+methanol+2,2,2-trifluoroethanol) at three temperatures: Measurement and correlation. The Journal of Chemical Thermodynamics, 41 (4) 549-552 doi:10.1016/j.jct.2008.10.017
Atik, Zadjia (2007) Study of Vapor−Liquid Equilibrium for Binary Mixtures (Chloroform + 2,2,2-Trifluoroethanol) and (α,α,α-Trifluorotoluene + 2,2,2-Trifluoroethanol) at Pressure 102 kPa. Journal of Chemical & Engineering Data, 52 (3) 1128-1130 doi:10.1021/je700103k
Atik, Zadjia, Kritli, Amina (2008) Liquid−Liquid Equilibrium for 2,2,2-Trifluoroethanol + Ethanol + Cyclohexane from (288.15 to 308.15) K. Journal of Chemical & Engineering Data, 53 (5) 1146-1150 doi:10.1021/je700741x
Chen, Yao, Cao, Chenyu (2009) Liquid−Liquid Equilibria for Three Quaternary Systems of Water, 2-Propanol, and Dimethyl Carbonate with Isooctane or Toluene or Heptane at 298.15 K. Journal of Chemical & Engineering Data, 54 (6) 1793-1798 doi:10.1021/je800753z
Atik, Zadjia (2007) Measurements and Calculation of Vapor−Liquid Equilibria for the Binary Mixtures of Fluorobenzene and Alkanes at a Pressure of 101.4 kPa. Journal of Chemical & Engineering Data, 52 (4) 1503-1505 doi:10.1021/je700207q
 
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