Araştırma Makalesi
BibTex RIS Kaynak Göster

Sülfürik Asit Liçi ile Çinko Oksit Cevherinden Çinko Geri Kazanımı

Yıl 2019, Cilt: 40 Sayı: 1, 179 - 185, 22.03.2019
https://doi.org/10.17776/csj.463775

Öz

Bu çalışmada sülfürik
asit kullanılarak liç ile çinko oksit cevherinin kazanımı araştırılmıştır. Liç
süresi, asit konsantrasyonu, liç sıcaklığı, partikül boyutu ve katı/sıvı oranı
gibi bazı parametrelerin etkileri maksimum çinko ekstraksiyonu ve minimum asit tüketimi
için araştırılmıştır. Optimum liç koşulları 120 dakika liç süresi, 55 g/L H2SO4
asit konsantrasyonu, 25 ˚C liç sıcaklığı, -780 µm partikül boyutu ve 1/10
katı/sıvı oranı olarak belirlenmiştir. Bu optimum koşullarda, %93.42 çinko
ekstraksiyonu ve 1.58 (ton H2SO4/ çözünen ton Zn) asit
tüketimi elde edilmiştir.

Kaynakça

  • [1]. Abdel-Aal E.A., Kinetics of Sulfuric Acid Leaching of Low-Grade Zinc Silicate Ore, Hydrometallurgy, 55 (2000) 247-254.
  • [2]. Havlik T., Turzakova M., Stopic S., Friedrich B., Atmospheric Leaching of EAF Dust with Diluted Sulphuric Acid, Hydrometallurgy, 77 (2005) 41-50.
  • [3]. Xu H., Wei C., Li C., Fan G., Deng Z., Li M., Li X., Sulfuric Acid Leaching of Zinc Silicate Ore Under Pressure, Hydrometallurgy, 105 (2010) 186-190.
  • [4]. Bodas M.G., Hydrometallurgical Treatment of Zinc Silicate Ore from Thailand, Hydrometallurgy, 40 (1996) 37-49.
  • [5]. Canbazoğlu M., Kaya Ö., Kulaksız M.I., Nizamoğlu Y.S., Sulphuric Acid Leaching of Zinc from Low Grade Lead&Zinc Ores, Proceedings of the XIII Balkan Mineral Processing Congress, 2 (2009) 587-593.
  • [6]. Uysal G., The Evaluation of Low Grade Zinc Oxide Ore of Niğde Öküzgönü Tepe Using Sulfuric Acid Leaching and Solvent Extraction, MSc thesis, Cumhuriyet University, Department of Mining Engineering, (2011) Sivas, Turkey.
  • [7]. Souza A.D., Pina P.S., Lima E.V.O., Silva C.A., Leão V.A., Kinetics of Sulfuric Acid Leaching of a Zinc Silicate Calcine, Hydrometallurgy, 89 (2007) 337-345.
  • [8]. Wang R.X., Tang M.T, Yang S.H, Zhagn W.H, Tang C.B., He J. Yang J.G., Leaching Kinetics of Low-Grade Zinc Oxide Ore in NH3-NH4Cl-H2O System, J. Cent. South Univ. Technol., 15 (2008) 679-683.
  • [9]. Bayrak B., Laçin O., Saraç H., Kinetic Study on the Leaching of Calcined Magnesite in Gluconic Acid Solutions, J. Ind. and Eng. Chem., 16 (2010) 479-484.
  • [10]. Espiari S., Rashchi F., Sadrnezhaad S.K., Hydrometallurgical Treatment of Tailings with High Zinc Content, Hydrometallurgy 82 (2006) 54-62.

Recovery of Zinc from Zinc Oxide Ore by Sulfuric Acid Leaching

Yıl 2019, Cilt: 40 Sayı: 1, 179 - 185, 22.03.2019
https://doi.org/10.17776/csj.463775

Öz



This study investigates the extraction from zinc
oxide ore by leaching using sulfuric acid. Effects of some parameters such as
leaching time, acid concentration, leaching temperature, particle size and
solid/liquid ratio were studied for maximum zinc extraction and minimum acid
consumption. Optimum leaching conditions were determined to be 120 minutes of
leaching time, 55 g/L H2SO4 of acid concentration, 25 ˚C
of leaching temperature, -780 µm of particle size and a solid/liquid ratio of
1/10. In these optimum conditions, 93.42% of zinc extraction and 1.58 (ton H2SO4/dissolved
ton Zn) of acid consumption were achieved.



Kaynakça

  • [1]. Abdel-Aal E.A., Kinetics of Sulfuric Acid Leaching of Low-Grade Zinc Silicate Ore, Hydrometallurgy, 55 (2000) 247-254.
  • [2]. Havlik T., Turzakova M., Stopic S., Friedrich B., Atmospheric Leaching of EAF Dust with Diluted Sulphuric Acid, Hydrometallurgy, 77 (2005) 41-50.
  • [3]. Xu H., Wei C., Li C., Fan G., Deng Z., Li M., Li X., Sulfuric Acid Leaching of Zinc Silicate Ore Under Pressure, Hydrometallurgy, 105 (2010) 186-190.
  • [4]. Bodas M.G., Hydrometallurgical Treatment of Zinc Silicate Ore from Thailand, Hydrometallurgy, 40 (1996) 37-49.
  • [5]. Canbazoğlu M., Kaya Ö., Kulaksız M.I., Nizamoğlu Y.S., Sulphuric Acid Leaching of Zinc from Low Grade Lead&Zinc Ores, Proceedings of the XIII Balkan Mineral Processing Congress, 2 (2009) 587-593.
  • [6]. Uysal G., The Evaluation of Low Grade Zinc Oxide Ore of Niğde Öküzgönü Tepe Using Sulfuric Acid Leaching and Solvent Extraction, MSc thesis, Cumhuriyet University, Department of Mining Engineering, (2011) Sivas, Turkey.
  • [7]. Souza A.D., Pina P.S., Lima E.V.O., Silva C.A., Leão V.A., Kinetics of Sulfuric Acid Leaching of a Zinc Silicate Calcine, Hydrometallurgy, 89 (2007) 337-345.
  • [8]. Wang R.X., Tang M.T, Yang S.H, Zhagn W.H, Tang C.B., He J. Yang J.G., Leaching Kinetics of Low-Grade Zinc Oxide Ore in NH3-NH4Cl-H2O System, J. Cent. South Univ. Technol., 15 (2008) 679-683.
  • [9]. Bayrak B., Laçin O., Saraç H., Kinetic Study on the Leaching of Calcined Magnesite in Gluconic Acid Solutions, J. Ind. and Eng. Chem., 16 (2010) 479-484.
  • [10]. Espiari S., Rashchi F., Sadrnezhaad S.K., Hydrometallurgical Treatment of Tailings with High Zinc Content, Hydrometallurgy 82 (2006) 54-62.
Toplam 10 adet kaynakça vardır.

Ayrıntılar

Birincil Dil İngilizce
Bölüm Engineering Sciences
Yazarlar

Özlem Kaya 0000-0001-7613-3609

Funda Serin Çakır 0000-0002-4337-2993

Yayımlanma Tarihi 22 Mart 2019
Gönderilme Tarihi 25 Eylül 2018
Kabul Tarihi 29 Ocak 2019
Yayımlandığı Sayı Yıl 2019Cilt: 40 Sayı: 1

Kaynak Göster

APA Kaya, Ö., & Serin Çakır, F. (2019). Recovery of Zinc from Zinc Oxide Ore by Sulfuric Acid Leaching. Cumhuriyet Science Journal, 40(1), 179-185. https://doi.org/10.17776/csj.463775