Optimization of continuous air-assisted solvent extraction for treating dilute Cu leach solutions using response surface methodology

Abstract A newly designed air-assisted solvent extraction (AASX) system was used to extract Cu from dilute solutions in a continuous-mode at pilot scale. The effects of some operational and chemical parameters including aqueous phase flowrate, extractant concentration, organic phase level in an organic coating cylinder (OCC level), Cu concentration, and silicone oil dosage on the efficiency of AASX process were investigated using a response surface methodology. The main and interaction effects of the variables on Cu recovery (26–85%), organic phase recycling (the portion of entered organic phase transferred to the column overflow for stripping, 7–56%), and aqueous/organic phase ratio (A/O, 59–435) were evaluated by the analysis of variance (ANOVA). The results showed that the addition of silicone oil increased Cu recovery and reduced organic phase recycling. Also, increasing OCC level caused to reduce A/O ratio and increase Cu recovery. Increasing extractant concentration and reducing the Cu concentration increased Cu recovery. The results were interpreted by their effects on bubble size, organic coating of air bubbles and A/O ratio. Varying the aqueous phase flowrate changed the A/O ratio in a curved mode which was related to the venturi tube suction force. Results showed that maximum efficiency of the AASX process (78% Cu recovery and 38% organic phase recycling, predicted by the ANOVA model), occurred at the aqueous flowrate of 24 L/min, extractant concentration of 40%, OCC level of 28 cm, Cu concentration of 50 mg/L without using silicone oil with an A/O ratio of 83. It can be concluded that AASX process could be used as an efficient and promising method for treating dilute solutions such as AMDs and wastewaters.

[1]  G. Stevens,et al.  Innovations in separations technology for the recycling and re-use of liquid waste streams , 2001 .

[2]  B. Bowerman Statistical Design and Analysis of Experiments, with Applications to Engineering and Science , 1989 .

[3]  J. A. Finch,et al.  AIR ASSISTED SOLVENT EXTRACTION , 2003 .

[4]  Chi-Wang Li,et al.  Integration of ceramic membrane and compressed air-assisted solvent extraction (CASX) for metal recovery. , 2010, Water science and technology : a journal of the International Association on Water Pollution Research.

[5]  Ashfaq Shaikh,et al.  A Review on Flow Regime Transition in Bubble Columns , 2007 .

[6]  H. Dong,et al.  The recent progress of solvent sublation. , 2010, Journal of chromatography. A.

[7]  M. Ranjbar,et al.  Response surface methodology (RSM) analysis of organic acid production for Kaolin beneficiation by Aspergillus niger , 2009 .

[8]  J. Finch,et al.  Air-assisted solvent extraction: towards a novel extraction process , 2005 .

[9]  H. Sohn,et al.  The kinetics of extraction in a novel solvent extraction process with bottom gas injection without moving parts , 1998 .

[10]  Fathi Habashi,et al.  Textbook of Hydrometallurgy , 1999 .

[11]  Ahmet Baylar,et al.  Experimental investigations of air and liquid injection by venturi tubes , 2006 .

[12]  A. Adamson Physical chemistry of surfaces , 1960 .

[13]  W. D. Harkins A General Thermodynamic Theory of the Spreading of Liquids to Form Duplex Films and of Liquids or Solids to Form Monolayers , 1941 .

[14]  H. Sohn,et al.  A novel solvent extraction process with bottom gas injection without moving parts , 1998 .

[15]  Khairul Anwar Mohamad Said,et al.  Overview on the Response Surface Methodology (RSM) in Extraction Processes , 2016 .

[16]  T. Chmielewski,et al.  Growing role of solvent extraction in copper ores processing , 2008 .

[17]  R. Pugh Foaming, foam films, antifoaming and defoaming , 1996 .

[18]  Ahmet Baylar,et al.  Applications of Venturi Principle to Water Aeration Systems , 2006 .

[19]  D. Fletcher,et al.  Particle Aerosolisation and Break-up in Dry Powder Inhalers 1: Evaluation and Modelling of Venturi Effects for Agglomerated Systems , 2010, Pharmaceutical Research.

[20]  Lawrence L. Tavlarides,et al.  Solvent Extraction, Membranes, and Ion Exchange in Hydrometallurgical Dilute Metals Separation , 1987 .

[21]  M. Hosseini,et al.  Surface phenomena in air-assisted solvent extraction , 2018 .

[22]  J. Finch,et al.  Foaming properties of solvents for use in air-assisted solvent extraction , 2005 .

[23]  Shiao‐Shing Chen,et al.  Compressed Air-Assisted Solvent Extraction (CASX) for Chromate Removal: Regeneration and Recovery , 2009 .

[24]  Chi-Wang Li,et al.  Compressed air-assisted solvent extraction (CASX) for metal removal. , 2008, Chemosphere.

[25]  Fenglian Fu,et al.  Removal of heavy metal ions from wastewaters: a review. , 2011, Journal of environmental management.

[26]  K. Valsaraj,et al.  Solvent sublation for the removal of hydrophobic chlorinated compounds from aqueous solutions , 1986 .

[27]  P. Garrett Preliminary considerations concerning the stability of a liquid heterogeneity in a plane-parallel liquid film , 1980 .