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    South African Journal of Chemistry

    On-line version ISSN 1996-840XPrint version ISSN 0379-4350

    S.Afr.j.chem. (Online) vol.65  Durban  2012

     

    RESEARCH ARICLE

     

    Utilization of ionic liquids for the separation of organic liquids from industrial effluents

     

     

    Mbongeni H. Mabaso; Gan G. Redhi*; Kandasamy G. Moodley

    Department of Chemistry, Durban University of Technology, P.O. Box 5400, Durban, 4000, South Africa

     

     


    ABSTRACT

    The recovery of aromatic organic solvents from mixtures containing aliphatic compounds has economic as well as environmental significance. This is so because viable methods have not been established for the recovery from mixtures in which the components of value are 20 % (v/v) or less. In the light of this, we investigated the efficacy of selected ionic liquids to recover aromatic solvents from prepared mixtures. We used 1-ethyl-3-methylimidazolium ethyl sulfate [EMIM][EtSO4] and 1-ethyl-3-methyl-pyridinium ethyl sulfate [EMpy][EtSO4] to separate and recover aromatic hydrocarbons (less than 10 % (v/v)) from aromatic/ aliphatic hydrocarbon mixtures, namely, benzene, toluene, ethyl benzene and o-xylene (BTEX) from «-heptane at 40 °C. The same aromatic components were used with «-hexane as an alkane and 1-ethyl-3-methylpyridinium ethyl sulfate [EMpy][EtSO4] as an ionic liquid. The concentrations of the aromatic components used were in the range of 2.5-10 % (v/v) for the following multi-systems at 40 °C:
    Benzene + toluene + ethyl benzene + o-xylene + n-heptane + [EMIM][EtSO4].
    Benzene + toluene + ethyl benzene + o-xylene + n-hexane + [EMIM][EtSO4].
    Benzene + toluene + ethyl benzene + o-xylene + n-hexane + [EMpy][EtSO4].
    The % removal of each aromatic, the ionic liquid selectivity trend, as well as its lifetime, and the distribution pattern of aromatic components in the ionic liquid obtained by gas chromatography were used to determine the capability of [EMIM][EtSO4] and [EMpy][EtSO4] as extracting solvents for low concentration BTEX.

    Keywords: Ionic liquids, solvent extraction, BTEX, aromatic hydrocarbons, aliphatic hydrocarbons


     

     

    Full text available only in PDF format.

     

    Acknowledgements

    Durban University of Technology (DUT) for financial support, and the University of KwaZulu-Natal for use of the NMR.

     

    References

    1 R.M. Maduro and M. Aznar, Fluid Phase Equilib., 2008, 265, 129-138.         [ Links ]

    2 E.J. Gonzalez, N. Calvar, B. Gonzalez and A. Dominguez, J. Chem. Thermodyn., 2009, 41, 1215-1221.         [ Links ]

    3 J. Chen, L. Duan, J. Mi, W. Fei and Z. Li, Fluid Phase Equilib, 2000, 173, 109-119.         [ Links ]

    4M. Mohsen-Nia and I. Paikar, J. Chem. Thermodyn., 2007, 39, 1085-1089.         [ Links ]

    5 R. Rappel, L.M. Nelson de Gois and S. Mattedi, Fluid Phase Equilib., 2002, 202, 273-276.         [ Links ]

    6 R.S. Santiago and M. Aznar, Fluid Phase Equilib., 2007, 253, 137-141.         [ Links ]

    7 R.S. Santiago and M. Aznar, Fluid Phase Equilib., 2007, 259, 71-76.         [ Links ]

    8 J. Mahmoudi and M.N. Lotfollahi, J. Chem. Thermodyn., 2010, 42, 466-471.         [ Links ]

    9 G.W. Meindersma, A.J.G. Podt and A.B. de Haan, Fuel Processing Tech, 2005, 87, 59-70.         [ Links ]

    10 G.W. Meindersma, A.J.G. Podt and A.B. de Haan, Fluid Phase Equilib., 2006, 247, 158-168.         [ Links ]

    11 G.W. Meiundersma and A.B. de Haan, Chem. Engin. Res. and Design, 2008, 86, 745-752.         [ Links ]

    12 T. Banerjee, M.K. Singh, R.K. Sahoo and A. Khanna, Fluid Phase Equilib, 2005, 234, 64-76.         [ Links ]

    13 M. Doeker and J. Gmehling Fluid Phase Equilib,, 2005, 227, 255-266.         [ Links ]

    14 B. Kirchner, Phys. Rep., 2007, 440, 1-111.         [ Links ]

    15 J.M. Gottfried, F. Maier,k, J. Rossa, D. Gerhard, P.S. Schulz, P Wasserscheid and H.P. Steinruck, Phys Chem , 2006, 220, 1439-1453.         [ Links ]

    16 C. Jork, C. Kristen, D. Pieraccini, A. Stark, C. Chiappe, Y.A. Beste and W. Arlt, J. Chem. Thermodyn., 2005, 37, 537-558.         [ Links ]

    17 M.J. Earle and K.R. Seddon, Pure Appl. Chem., 2000, 72, 1391-1398.         [ Links ]

    18 J. Garcia, A. Fernandez, J.S. Torrecilla, M. Oliet and F. Rodriguez, Fluid Phase Equilib., 2009, 282, 117-120.         [ Links ]

    19 E.J. Gonzalez, N. Calvar, B. Gonzalez and A. Dominguez, J. Chem. Thermodyn., 2010, 42, 104-109.         [ Links ]

    20 C.F. Poole and S.K. Poole, J. Chrom. A, 2010, 1217, 2268-2286.         [ Links ]

    21 A.R. Hansmeier, M. Jongmans, G.W. Meindersma and A.B. de Haan, J. Chem. Thermodyn., 2010, 42, 484-490.         [ Links ]

    22 E.J. Gonzalez, I. Dominguez, B. Gonzalez and J. Canosa, J. Chem. Thermodyn., 2010, 296, 213-218.         [ Links ]

    23 F. Onink, C. Drumm, G. W. Meiundersma, H. Bart and A.B. de Haan, Chem. Engin. J, 2010, 160, 511-521.         [ Links ]

    24 A.B. Pereiro and A. Rodriguez, J. Chem. Thermodyn., 2009, 41, 951-956.         [ Links ]

    25 J. Garcia, S, Garcia, J.S. Torrecilla, A. Fernandez, M. Oliet and F. Rodriguez, J. Chem. Thermodyn., 2010, 42, 144-150.         [ Links ]

    26 J. Garcia, J.S. Torrecilla, M. Oliet and F. Rodriguez, J. Chem. Thermodyn., 2010, 42, 1004-1008.         [ Links ]

    27 A. Arce, M.J. Earle, H. Rodriguez and K.R. Seddon, Green Chem., 2007, 9, 70-74.         [ Links ]

     

     

    Received 15 August 2011
    Revised 15 April 2012
    Accepted 29 June 2012

     

     

    * To whom correspondence should be addressed. E-mail: redhigg@dut.ac.za