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Extraction

Salting-out effect of sodium carbonate on the liquid–liquid equilibrium of (Water + Dichloromethane + N,N-Dimethylacetamide) system at temperature T=(298.15 and 308.15) K

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Pages 1194-1203 | Received 14 Nov 2017, Accepted 24 Sep 2018, Published online: 10 Oct 2018

References

  • Young Jeong, A.; Cho, J.A.; Kim, Y.; Cho, H.-K.; Choi, K.Y.; Lim, J.S. (2018) Liquid-liquid equilibria for water+2,3-butanediol+1-pentanol ternary system at different temperatures of 298.2, 308.2, and 318.2 K. Korean Journal Chemical Engineering, 35: 1328–1334. doi:10.1007/s11814-018-0036-6
  • Yang, X.; Zhang, X.; Dong, H.; Yue, G.; Liu, J. (2015) (Liquid+liquid) equilibria for (benzene+cyclohexane+dimethyl sulfoxide) system at T=(298.15 or 303.15)K: experimental data and correlation. Journal Chemical Thermodynics, 84: 14–17. doi:10.1016/j.jct.2014.12.014
  • Zhang, H.; Wang, T. (2009) Measurement and correlation of liquid−liquid equilibrium data for Water + Acetic acid + Methyltert-Butyl ether + NaCl. Journal Chemical Engineering Data, 54: 945–949. doi:10.1021/je800724g
  • Vakili-Nezhaad, G.R.; Mohsen-Nia, M.; Taghikhani, V.; Behpoor, M.; Aghahosseini, M. (2004) Salting-out effect of NaCl and KCl on the ternary LLE data for the systems of (water+propionic acid+isopropyl methyl ketone) and of (water+propionic acid+isobutyl methyl ketone). Journal Chemical Thermodynics, 36: 341–348. doi:10.1016/j.jct.2003.11.011
  • Salabat, A.;. (2007) Liquid–liquid equilibria for the MTBE+water+salts systems at 298.15K. Fluid Phase Equilibria, 257: 1–5. doi:10.1016/j.fluid.2007.04.026
  • Kunthakudee, N.; Pancharoen, U.; Fulajtárová, K.; Soták, T.; Hronec, M.; Ramakul, P. (2017) Salt effect on the liquid-liquid equilibrium of water-furfuryl alcohol-furfural system at 298.15 K. Korean Journal Chemical Engineering, 34: 2293–2300. doi:10.1007/s11814-017-0136-8
  • Saien, J.; Norouzi, M. (2011) Salting-out effect of NaCl and KCl on the liquid–liquid equilibrium of Water + 2-Methylpropanoic Acid + (1-Methylethyl)-benzene system at several temperatures. Journal Chemical Engineering Data, 56: 2892–2898. doi:10.1021/je200083a
  • Saien, J.; Fattahi, M.; Mozafarvandi, M. (2014) The impact of uni-univalent electrolytes on (water+acetic acid+toluene) equilibria: representation with electrolyte-NRTL model. Journal Chemical Thermodynics, 74: 238–246. doi:10.1016/j.jct.2014.02.005
  • Bahrpaima, K.H.; Ebrahimi, M.; Madani, H.; Shekarriz, S. (2014) RETRACTED: salting-out effect on the (liquid+liquid) equilibrium for the ternary systems (water+phosphoric acid+dichloromethane or 1,2-dichloroethane). Journal Chemical Thermodynics, 71: 118–125. doi:10.1016/j.jct.2013.11.034
  • Chen, Jui-Tang; Chen, Ming-Chung. (2008) Liquid–liquid equilibria for the quaternary systems of Water +N-Methyl-2-pyrrolidone + 1-Hexanol + NaCl, + KCl, or + KAc. Journal Chemical Engineering Data, 53: 217–222. doi:10.1021/je700561p
  • Wang, C.; Liu, X.; Wang, P.; Yang, P. (2014) Determination and correlation of liquid–liquid equilibrium data for the Ternary Dichloromethane + Water +N,N-Dimethylacetamide System. Journal Chemical Engineering Data, 59: 1733–1736. doi:10.1021/je401001z
  • Taylor, B.N.; Kuyatt, C.E. (1994) Guidelines for Evaluating and Expressing the Uncertainty of NIST Measurement Results. National Institute Standards and Technology: Gaithersburg.
  • BIPM, IEC, IFCC, ILAC, ISO, IUPAC, IUPAP and OIML. (2008) Joint Committee for Guides in Metrology. 100
  • Renon, H.; Prausnitz, J.M. (1968) Local compositions in thermodynamic excess functions for liquid mixtures. AIChE Journal, 14: 135–144. doi:10.1002/aic.690140124
  • Gilani, H.G.; Noury, S.; Asan, S. (2013) Phase equilibrium data for aqueous solutions of formic acid with 2-ethyl-1-hexanol at T=(298.2, 308.2, 318.2, and 328.2) K. Korean Journal Chemical Engineering, 30: 1289–1294. doi:10.1007/s11814-013-0050-7
  • Marcilla, A.; Reyes-Labarta, J.A.; Olaya, M.M. (2017) Should we trust all the published LLE correlation parameters in phase equilibria? Necessity of their assessment prior to publication. Fluid Phase Equilibria, 433: 243–252. doi:10.1016/j.fluid.2016.11.009
  • Treybal, R.E.;. (1963) Liquid Extraction, 2. New York: McGraw-Hill.
  • Reyes-Labarta, J.A. Graphical User Interface (GUI) for the Representation of GM Surfaces and Curves, Including Tie-Lines. Institutional Repository of the University of Alicante(RUA) http://hdl.handle.net/10045/51725
  • Wasylkiewicz, S.K.; Sridhar, L.N.; Doherty, M.F.; Malone, M.F. (1996) Global stability analysis and calculation of liquid−liquid equilibrium in multicomponent mixtures. Industrial Engineering Chemical Researcher, 35: 1395–1408. doi:10.1021/ie950049r
  • Iglesias-Silva, G.A.; Bonilla-Petriciolet, A.; Eubank, P.T.; Holste, J.C.; Hall, K.R. (2003) An algebraic method that includes Gibbs minimization for performing phase equilibrium calculations for any number of components or phases. Fluid Phase Equilibria, 210: 229–245. doi:10.1016/S0378-3812(03)00171-7
  • Reyes-Labarta, J.A.; Olaya, M.M.; Velasco, R.; Serrano, M.D.; Marcilla, A. (2009) Correlation of the liquid–liquid equilibrium data for specific ternary systems with one or two partially miscible binary subsystems. Fluid Phase Equilibria, 278: 9–14. doi:10.1016/j.fluid.2008.12.002
  • Marcilla, A.; Reyes-Labarta, J.A.; Olaya, M.D.M.; Serrano, M.D. (2008) Simultaneous correlation of liquid−liquid, liquid−solid, and liquid−liquid−solid equilibrium data for Water + Organic Solvent + Salt Ternary Systems:  Hydrated Solid Phase Formation. Industrial Engineering Chemical Researcher, 47: 2100–2108. doi:10.1021/ie071290w
  • Karaboga, D.; Akay, B. (2011) A modified Artificial Bee Colony (ABC) algorithm for constrained optimization problems. Applications Soft Computation, 11: 3021–3031. doi:10.1016/j.asoc.2010.12.001
  • Karaboga, D.; Ozturk, C. (2011) A novel clustering approach: Artificial Bee Colony (ABC) algorithm. Applications Soft Computation, 11: 652–657. doi:10.1016/j.asoc.2009.12.025
  • Kim, H.D.; Hwang, I.C.; Park, S. J.; Lee, K.W. (2010) (Liquid + Liquid) equilibrium for (N,N-Dimethylformamide (DMF) + Hexadecane) at Temperatures between (293.15 and 313.15) K and Ternary Mixtures of (DMF + Hexadecane) with Either Quinoline, or Pyridine, or Pyrrole, or Aniline, or Indole at T= 298.15 K. Journal Chemical Engineering Data, 55: 1266–1270. doi:10.1021/je9006234

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