Skip to main content
Log in

Extraction equilibrium of chromium(III) from sulphate medium by Cyanex 272 dissolved in kerosene

  • Original Paper
  • Published:
Chemical Papers Aims and scope Submit manuscript

Abstract

The solvent extraction of Cr(III) from SO42− medium by Cyanex 272 (bis 2,4,4-trimethyl pentyl phosphinic acid) dissolved in kerosene has been studied as a function of equilibration time, pH, [Cr(III)], [Cyanex 272], [SO42−] and temperature. Over 55% extraction occurs with the favourable parameters used. Experimental study of the pH variation shows that the hydrolysis of the extractant to a certain extent occurs during the phase contact period. One dimeric molecule of Cyanex 272 is required for each Cr(III) to form the extractable species. The co-existing anion (sulphate ion) suggests the formation of Cr(H2O)3SO4OH or Cr2(H2O)4(OH)2(SO4)2 in the aqueous phase. The positive ΔH value (~ 12.73 kJ/mol) indicates that the system under investigation is endothermic. The measured loading capacity is 4.40 g Cr(III)/100 g of Cyanex 272. The stripping is difficult, and after two stages, only 8.13% of Cr(III) is stripped by 3 mol/L H2SO4. Selectivity of Fe(III)/Cr(III) separation by Cyanex 272 is high.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Fig. 1
Fig. 2
Fig. 3
Fig. 4
Fig. 5
Fig. 6
Fig. 7
Fig. 8
Fig. 9
Fig. 10

Similar content being viewed by others

Abbreviations

D:

Extraction or distribution ratio of Cr(III) partitioned = [Cr(III)](o,eq)/[Cr(III)](aq,eq)

Cyanex 272:

BTMPPA, bis-(2,4,4-trimethylpentyl) phosphinic acid

HR:

Monomeric BTMPPA

H2R2 :

Dimeric BTMPPA

R:

Universal gas constant, 8.314 J/K mol

Cr(III) or Cr3 + :

Chromium(III)

D2EHPA:

Bis-(2-ethylhexyl)phosphoric acid

ΔH:

Apparent enthalpy changes for extraction reaction, kJ/mol

Kex :

The equilibrium constant from the equilibrium study

O:

Organic phase value

A:

Aqueous phase value

Suffix “eq”:

Equilibrium

Suffix “o”:

Organic phase

Suffix “A”, “aq” or without suffix:

Aqueous phase

Suffix “ini”:

Initial

References

  • Agrawal A, Kumar V, Pandey B (2006) Remediation options for the treatment of electroplating and leather tanning effluent containing chromium—a review. Miner Process Extr Metall Rev 27:99–130

    Article  CAS  Google Scholar 

  • Atkins PW, De Paula J, Keeler J (2018) Atkins’ physical chemistry. Oxford University Press, Oxford

    Google Scholar 

  • Attar K, Bouazza D, Miloudi H, Tayeb A, Boos A, Sastre AM, Demey H (2018) Cadmium removal by a low-cost magadiite-based material: characterization and sorption applications. J Environ Chem Eng 6:5351–5360

    Article  CAS  Google Scholar 

  • Biswas RK, Singha HP (2006) Purified Cyanex 272: Its interfacial adsorption and extraction characteristics towards iron(III). Hydrometallurgy 82:63–74

    Article  CAS  Google Scholar 

  • Biswas RK, Banu RA, Islam MN (2003) Some physico-chemical properties of D2EHPA: Part 2. Distribution, dimerization and acid dissociation constants in n-hexane/1 M (Na+, H+)SO42− system, interfacial adsorption and excess properties. Hydrometallurgy 69:157–168

  • Biswas RK, Habib MA, Singha HP (2005) Colorimetric estimation and some physicochemical properties of purified Cyanex 272. Hydrometallurgy 76:97–104

    Article  CAS  Google Scholar 

  • Biswas RK, Karmakar AK, Mottakin M (2017) Study of the solvent extraction of V (V) from nitrate medium by tri-n-octylamine dissolved in kerosene. JOM 69:1945–1949

    Article  CAS  Google Scholar 

  • Brooks C (1987) Application of solvent extraction in treatment of metal finishing wastes. Met Finish 85:55–60

    CAS  Google Scholar 

  • Charlot G (1964) Colorimetric determination of elements, principles and methods: By G. Charlot. Elsevier, Amsterdam

    Google Scholar 

  • Darvishi D, Haghshenas D, Alamdari EK, Sadrnezhaad S, Halali M (2005) Synergistic effect of Cyanex 272 and Cyanex 302 on separation of cobalt and nickel by D2EHPA. Hydrometallurgy 77:227–238

    Article  CAS  Google Scholar 

  • El-Hefny N, El-Nadi Y, Daoud J (2010) Equilibrium and mechanism of samarium extraction from chloride medium using sodium salt of CYANEX 272. Sep Purif Technol 75:310–315

    Article  CAS  Google Scholar 

  • Flett DS (2005) Solvent extraction in hydrometallurgy: the role of organophosphorus extractants. J Organomet Chem 690:2426–2438

    Article  CAS  Google Scholar 

  • Islam F, Biswas R (1979a) The solvent extraction of chromium (III) with bis-(2-ethyl hexyl) phosphoric acid in benzene and other solvents. J Inorg Nucl Chem 41:229–233

    Article  CAS  Google Scholar 

  • Islam MF, Biswas RK (1979b) Kinetics of solvent extraction of metal ions with HEDHP. III. The kinetics and mechanism of solvent extraction of Cr (III) from acidic aqueous solutions with bis-(2-ethyl hexyl) phosphoric acid in benzene. Can J Chem 57:3011–3016

    Article  CAS  Google Scholar 

  • Lanagan M, Ibana D (2003) The solvent extraction and stripping of chromium with Cyanex® 272. Miner Eng 16:237–245

    Article  CAS  Google Scholar 

  • Liu Y, Guo L, Zhu L, Sun X, Chen J (2010) Removal of Cr (III, VI) by quaternary ammonium and quaternary phosphonium ionic liquids functionalized silica materials. Chem Eng J 158:108–114

    Article  CAS  Google Scholar 

  • Lü L, Chen L, Shao W, Luo F (2010) Equilibrium and kinetic modeling of Pb (II) biosorption by a chemically modified orange peel containing Cyanex 272. J Chem Eng Data 55:4147–4153

    Article  Google Scholar 

  • Mellah A, Benachour D (2006) Solvent extraction of heavy metals contained in phosphoric acid solutions by 7-(4-ethyl-1-methyloctyl)-8-hydroxyquinoline in kerosene diluent. Hydrometallurgy 81:100–103

    Article  CAS  Google Scholar 

  • Ngomsik A-F, Bee A, Siaugue J-M, Talbot D, Cabuil V, Cote G (2009) Co (II) removal by magnetic alginate beads containing Cyanex 272®. J Hazard Mater 166:1043–1049

    Article  CAS  Google Scholar 

  • Owlad M, Aroua MK, Daud WAW, Baroutian S (2009) Removal of hexavalent chromium-contaminated water and wastewater: a review. Water Air Soil Pollut 200:59–77

    Article  CAS  Google Scholar 

  • Rakhunde R, Deshpande L, Juneja H (2012) Chemical speciation of chromium in water: a review. Crit Rev Environ Sci Technol 42:776–810

    Article  CAS  Google Scholar 

  • Rao V, Sastri M (1980) Solvent extraction of chromium: a review. Talanta 27:771–777

    Article  CAS  Google Scholar 

  • Richard FC, Bourg AC (1991) Aqueous geochemistry of chromium: a review. Water Res 25:807–816

    Article  CAS  Google Scholar 

  • Sahu S, Verma VK, Bagchi D, Kumar V, Pandey B (2008) Recovery of chromium (VI) from electroplating effluent by solvent extraction with tri-n-butyl phosphate. Indian J Chem Technol 15:397–402

    CAS  Google Scholar 

  • Treybal RE (1957) Liquid extraction. Ind Eng Chem 49:514–526

    Article  CAS  Google Scholar 

  • Urtiaga A, Bringas E, Mediavilla R, Ortiz I (2010) The role of liquid membranes in the selective separation and recovery of zinc for the regeneration of Cr (III) passivation baths. J Membr Sci 356:88–95

    Article  CAS  Google Scholar 

  • Wionczyk B, Apostoluk W, Charewicz WA (2006) Solvent extraction of chromium (III) from spent tanning liquors with Aliquat 336. Hydrometallurgy 82:83–92

    Article  CAS  Google Scholar 

  • Xing WD, Lee MS, Senanayake G (2018) Recovery of metals from chloride leach solutions of anode slimes by solvent extraction. Part I: recovery of gold with Cyanex 272. Hydrometallurgy 180:58–64

    Article  CAS  Google Scholar 

Download references

Acknowledgements

The authors are grateful to Cytec Canada Inc. for supplying Cyanex 272 as a gift.

Author information

Authors and Affiliations

Authors

Corresponding author

Correspondence to Aneek Krishna Karmakar.

Ethics declarations

Conflict of interest

On behalf of all authors, the corresponding author states that there is no conflict of interest.

Additional information

Publisher's Note

Springer Nature remains neutral with regard to jurisdictional claims in published maps and institutional affiliations.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Karmakar, A.K., Biswas, R.K. & Khatun, M.N. Extraction equilibrium of chromium(III) from sulphate medium by Cyanex 272 dissolved in kerosene. Chem. Pap. 75, 3739–3749 (2021). https://doi.org/10.1007/s11696-021-01575-1

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s11696-021-01575-1

Keywords

Navigation