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Chemical Engineering & Technology | 2001

Determination of the Optimum Conditions for Leaching of Malachite Ore in H2SO4 Solutions

Osman Nuri Ata; Sabri Çolak; Zafer Ekinci; Mehmet Çopur

The Taguchi method has been used to determine the optimum conditions for the dissolution of malachite ore in H2SO4 solutions. The chosen experimental parameters and their range were (i) reaction temperature: 15 to 45 °C, (ii) solid-to-liquid ratio: 1/10 to 1/3 g cm–3, (iii) acid concentration (in weight): 2 % to 10 %, (iv) particle size: –40 to –3.5 mesh, (v) stirring speed: 240 to 720 rpm, and (vi) reaction time: 5 to 45 minutes. The optimum conditions were found to be reaction temperature: 40 °C, solid-to-liquid ratio: 1/3 g cm–3, acid concentration (in weight): 10 %, particle size: –30 mesh, stirring speed: 480 rpm, and reaction time: 45 minutes. Under these optimum working conditions, the dissolution of copper and iron in malachite ore was 100 % and 58 %, respectively. Besides, alternative working conditions reducing the total cost and dissolution of iron were found.


Chemical Engineering and Processing | 2003

Determination of the optimum conditions of dissolution of copper in converter slag with chlorine gas in aqueous media

Ayşe Vildan Beşe; Osman Nuri Ata; Cafer Çelik; Sabri Çolak

Abstract The Taguchi method has been used to determine the optimum conditions of dissolution of copper in converter slag with chlorine gas in aqueous media. After the parameters were determined to be efficient on the extraction efficiency, the experiments were begun. The chosen experimental parameters and their ranges were: (i) chlorine gas flow rate (ml min −1 ); 180–220, (ii) solid-to-liquid ratio (g ml −1 ); 0.1–0.166, (iii) stirring speed (rpm); 350–750, (vi) reaction time (min); 90–210. The optimum conditions were found to be as follows: chlorine gas flow rate (ml min −1 ); 220, solid-to-liquid ratio (g ml −1 ); 0.1, stirring speed (rpm); 550, reaction time (min); 90. Under these optimum conditions, copper, iron and zinc extraction efficiency from converter slag were 98.35, 8.97 and 25.17%, respectively.


Journal of Industrial and Engineering Chemistry | 2012

Ammonia removal by air stripping in a semi-batch jet loop reactor

Nejdet Değermenci; Osman Nuri Ata; Ergun Yildiz


Industrial & Engineering Chemistry Research | 2000

Determination of the optimum conditions for boric acid extraction with carbon dioxide gas in aqueous media from colemanite containing arsenic

Osman Nuri Ata; Sabri Çolak; Mehmet Copur; Cafer Çelik


Hydrometallurgy | 2005

Modelling of copper ion transport through supported liquid membrane containing LIX 984

Osman Nuri Ata


Chemical Engineering Journal | 2010

Optimization of dissolution of metals from Waelz sintering waste (WSW) by hydrochloric acid solutions

Ayşe Vildan Beşe; Nurcan Borulu; Mehmet Çopur; Sabri Çolak; Osman Nuri Ata


Chemical Engineering and Processing | 2004

Effect of parameters on the transport of zinc ion through supported liquid membrane

Osman Nuri Ata; Ayşe Vildan Beşe; Sabri Çolak; Bünyamin Dönmez; Avni Cakici


Canadian Journal of Chemical Engineering | 2008

Determination of the Optimum Conditions for Zinc Extraction from Ore Containing Sphalerite by HCL Solutions

Osman Nuri Ata; Murat Yeşilyurt; Sabri Çolak; Ayşe Vildan Beşe


Hydrometallurgy | 2005

Modelling of zinc transport through a supported liquid membrane

Osman Nuri Ata; Sabri Çolak


Hydrometallurgy | 2007

Mathematical modelling of unsteady-state transport of metal ions through supported liquid membrane

Osman Nuri Ata

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