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Recovery of Au and Ag from the roasted calcine of a copper-rich pyritic refractory gold ore using ion exchange resins. / Msumange, Deus Albert; Yazici, Ersin Yener; Celep, Oktay и др.
в: Minerals Engineering, Том 195, 108017, 2023.

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Msumange DA, Yazici EY, Celep O, Deveci H, Kritskii A, Karimov K. Recovery of Au and Ag from the roasted calcine of a copper-rich pyritic refractory gold ore using ion exchange resins. Minerals Engineering. 2023;195:108017. doi: 10.1016/j.mineng.2023.108017

Author

Msumange, Deus Albert ; Yazici, Ersin Yener ; Celep, Oktay и др. / Recovery of Au and Ag from the roasted calcine of a copper-rich pyritic refractory gold ore using ion exchange resins. в: Minerals Engineering. 2023 ; Том 195.

BibTeX

@article{c60bef635b3b4a59a10d2bbe4588a8ec,
title = "Recovery of Au and Ag from the roasted calcine of a copper-rich pyritic refractory gold ore using ion exchange resins",
abstract = "The recovery of Au and Ag from a roasted copper-rich pyritic refractory gold ore (78 g/t Au, 6.8 g/t Ag, 1.38 % Cu and 3.09 % Fe was investigated. Cyanide leaching and adsorption tests were performed at different concentrations of cyanide (1.5 g/L and 5 g/L NaCN) and the adsorbent dosages ranged from 2 g/L to 10 g/L. In the cyanide leaching tests, those performed at a high cyanide level (i.e., 5 g/L) produced high gold and silver extractions from the roasted ore apparently due to the increased availability of cyanide for gold leaching. Adsorption tests (CIL/CIP, RIL/RIP) were performed to investigate the selective recovery of gold and silver from copper-laden pregnant leach solutions obtained from cyanide leaching of the roasted ore. Activated carbon (NORIT GAC 1240), strong base resin (Purogold A194) and weak base resin (Purogold S992) were tested as adsorbents in these tests. The practical importance of increasing cyanide concentration on the selectivity (gold/silver vs copper) of resins as well as activated carbon was demonstrated. Each adsorbent offered good selectivity for gold over copper, particularly at a high concentration of cyanide (5 g/L NaCN). Purogold S992 appeared to be the most selective adsorbent with the highest gold and the lowest copper loadings. This distinctive trait makes the resin preferable for gold recovery from cyanide solutions containing significant levels of copper. Comparative pore size distribution analysis of the adsorbents has shown that Purogold S992 has the smallest pores with uniform size distribution among the adsorbents used. This was concomitant with its superior selectivity for gold at high cyanide concentration, which is linked with the small-size and linear gold-cyanide complexes c.f. large size and non-linear copper–cyanide complexes (Cu(CN)32– and Cu(CN)43-).",
author = "Msumange, {Deus Albert} and Yazici, {Ersin Yener} and Oktay Celep and Haci Deveci and Aleksei Kritskii and Kirill Karimov",
note = "The authors would like to extend their gratitude to Mastra Gold Mine (Koza Gold Operations) for kindly providing the ore sample, Dr. Fatih {\"O}zkalaycı (Department of Metallurgical & Materials Engineering, KTU) for performing XRD analysis, Assoc. Prof. Dr. Ferdi Cihangir and Research Assistant Erc{\"u}ment Ko{\c c} (Department of Mining Engineering, KTU) for their help in porosimetry analysis and PUROLITE Co. for providing the resin samples. This work was supported by Office of Scientific Research Projects of Karadeniz Technical University (Project number: FBA-2018-7399).",
year = "2023",
doi = "10.1016/j.mineng.2023.108017",
language = "English",
volume = "195",
journal = "Minerals Engineering",
issn = "0892-6875",
publisher = "Elsevier BV",

}

RIS

TY - JOUR

T1 - Recovery of Au and Ag from the roasted calcine of a copper-rich pyritic refractory gold ore using ion exchange resins

AU - Msumange, Deus Albert

AU - Yazici, Ersin Yener

AU - Celep, Oktay

AU - Deveci, Haci

AU - Kritskii, Aleksei

AU - Karimov, Kirill

N1 - The authors would like to extend their gratitude to Mastra Gold Mine (Koza Gold Operations) for kindly providing the ore sample, Dr. Fatih Özkalaycı (Department of Metallurgical & Materials Engineering, KTU) for performing XRD analysis, Assoc. Prof. Dr. Ferdi Cihangir and Research Assistant Ercüment Koç (Department of Mining Engineering, KTU) for their help in porosimetry analysis and PUROLITE Co. for providing the resin samples. This work was supported by Office of Scientific Research Projects of Karadeniz Technical University (Project number: FBA-2018-7399).

PY - 2023

Y1 - 2023

N2 - The recovery of Au and Ag from a roasted copper-rich pyritic refractory gold ore (78 g/t Au, 6.8 g/t Ag, 1.38 % Cu and 3.09 % Fe was investigated. Cyanide leaching and adsorption tests were performed at different concentrations of cyanide (1.5 g/L and 5 g/L NaCN) and the adsorbent dosages ranged from 2 g/L to 10 g/L. In the cyanide leaching tests, those performed at a high cyanide level (i.e., 5 g/L) produced high gold and silver extractions from the roasted ore apparently due to the increased availability of cyanide for gold leaching. Adsorption tests (CIL/CIP, RIL/RIP) were performed to investigate the selective recovery of gold and silver from copper-laden pregnant leach solutions obtained from cyanide leaching of the roasted ore. Activated carbon (NORIT GAC 1240), strong base resin (Purogold A194) and weak base resin (Purogold S992) were tested as adsorbents in these tests. The practical importance of increasing cyanide concentration on the selectivity (gold/silver vs copper) of resins as well as activated carbon was demonstrated. Each adsorbent offered good selectivity for gold over copper, particularly at a high concentration of cyanide (5 g/L NaCN). Purogold S992 appeared to be the most selective adsorbent with the highest gold and the lowest copper loadings. This distinctive trait makes the resin preferable for gold recovery from cyanide solutions containing significant levels of copper. Comparative pore size distribution analysis of the adsorbents has shown that Purogold S992 has the smallest pores with uniform size distribution among the adsorbents used. This was concomitant with its superior selectivity for gold at high cyanide concentration, which is linked with the small-size and linear gold-cyanide complexes c.f. large size and non-linear copper–cyanide complexes (Cu(CN)32– and Cu(CN)43-).

AB - The recovery of Au and Ag from a roasted copper-rich pyritic refractory gold ore (78 g/t Au, 6.8 g/t Ag, 1.38 % Cu and 3.09 % Fe was investigated. Cyanide leaching and adsorption tests were performed at different concentrations of cyanide (1.5 g/L and 5 g/L NaCN) and the adsorbent dosages ranged from 2 g/L to 10 g/L. In the cyanide leaching tests, those performed at a high cyanide level (i.e., 5 g/L) produced high gold and silver extractions from the roasted ore apparently due to the increased availability of cyanide for gold leaching. Adsorption tests (CIL/CIP, RIL/RIP) were performed to investigate the selective recovery of gold and silver from copper-laden pregnant leach solutions obtained from cyanide leaching of the roasted ore. Activated carbon (NORIT GAC 1240), strong base resin (Purogold A194) and weak base resin (Purogold S992) were tested as adsorbents in these tests. The practical importance of increasing cyanide concentration on the selectivity (gold/silver vs copper) of resins as well as activated carbon was demonstrated. Each adsorbent offered good selectivity for gold over copper, particularly at a high concentration of cyanide (5 g/L NaCN). Purogold S992 appeared to be the most selective adsorbent with the highest gold and the lowest copper loadings. This distinctive trait makes the resin preferable for gold recovery from cyanide solutions containing significant levels of copper. Comparative pore size distribution analysis of the adsorbents has shown that Purogold S992 has the smallest pores with uniform size distribution among the adsorbents used. This was concomitant with its superior selectivity for gold at high cyanide concentration, which is linked with the small-size and linear gold-cyanide complexes c.f. large size and non-linear copper–cyanide complexes (Cu(CN)32– and Cu(CN)43-).

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UR - https://gateway.webofknowledge.com/gateway/Gateway.cgi?GWVersion=2&SrcAuth=tsmetrics&SrcApp=tsm_test&DestApp=WOS_CPL&DestLinkType=FullRecord&KeyUT=000951458300001

U2 - 10.1016/j.mineng.2023.108017

DO - 10.1016/j.mineng.2023.108017

M3 - Article

VL - 195

JO - Minerals Engineering

JF - Minerals Engineering

SN - 0892-6875

M1 - 108017

ER -

ID: 35501278