Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere
Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2}...
Ausführliche Beschreibung
Autor*in: |
Yang, Weijiao [verfasserIn] |
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E-Artikel |
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Sprache: |
Englisch |
Erschienen: |
2022 |
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Schlagwörter: |
African cobalt-rich copper sulfide ore |
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Anmerkung: |
© Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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Übergeordnetes Werk: |
Enthalten in: Journal of thermal analysis and calorimetry - Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969, 147(2022), 23 vom: 08. Okt., Seite 13469-13481 |
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Übergeordnetes Werk: |
volume:147 ; year:2022 ; number:23 ; day:08 ; month:10 ; pages:13469-13481 |
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DOI / URN: |
10.1007/s10973-022-11628-6 |
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Katalog-ID: |
SPR048720690 |
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520 | |a Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. | ||
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700 | 1 | |a Wang, Hua |4 aut | |
700 | 1 | |a Jiang, Xingming |4 aut | |
700 | 1 | |a Wang, Chengyan |4 aut | |
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10.1007/s10973-022-11628-6 doi (DE-627)SPR048720690 (SPR)s10973-022-11628-6-e DE-627 ger DE-627 rakwb eng Yang, Weijiao verfasserin aut Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. African cobalt-rich copper sulfide ore (dpeaa)DE-He213 Thermal roasting kinetics (dpeaa)DE-He213 Roasting behavior (dpeaa)DE-He213 Deconvolution integral separation (dpeaa)DE-He213 Sulfating reaction (dpeaa)DE-He213 Li, Xiang aut Liu, Yubo aut Ma, Baozhong (orcid)0000-0003-3907-9097 aut Wang, Hua aut Jiang, Xingming aut Wang, Chengyan aut Enthalten in Journal of thermal analysis and calorimetry Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969 147(2022), 23 vom: 08. Okt., Seite 13469-13481 (DE-627)315295422 (DE-600)2017304-0 1572-8943 nnns volume:147 year:2022 number:23 day:08 month:10 pages:13469-13481 https://dx.doi.org/10.1007/s10973-022-11628-6 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 147 2022 23 08 10 13469-13481 |
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10.1007/s10973-022-11628-6 doi (DE-627)SPR048720690 (SPR)s10973-022-11628-6-e DE-627 ger DE-627 rakwb eng Yang, Weijiao verfasserin aut Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. African cobalt-rich copper sulfide ore (dpeaa)DE-He213 Thermal roasting kinetics (dpeaa)DE-He213 Roasting behavior (dpeaa)DE-He213 Deconvolution integral separation (dpeaa)DE-He213 Sulfating reaction (dpeaa)DE-He213 Li, Xiang aut Liu, Yubo aut Ma, Baozhong (orcid)0000-0003-3907-9097 aut Wang, Hua aut Jiang, Xingming aut Wang, Chengyan aut Enthalten in Journal of thermal analysis and calorimetry Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969 147(2022), 23 vom: 08. Okt., Seite 13469-13481 (DE-627)315295422 (DE-600)2017304-0 1572-8943 nnns volume:147 year:2022 number:23 day:08 month:10 pages:13469-13481 https://dx.doi.org/10.1007/s10973-022-11628-6 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 147 2022 23 08 10 13469-13481 |
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10.1007/s10973-022-11628-6 doi (DE-627)SPR048720690 (SPR)s10973-022-11628-6-e DE-627 ger DE-627 rakwb eng Yang, Weijiao verfasserin aut Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. African cobalt-rich copper sulfide ore (dpeaa)DE-He213 Thermal roasting kinetics (dpeaa)DE-He213 Roasting behavior (dpeaa)DE-He213 Deconvolution integral separation (dpeaa)DE-He213 Sulfating reaction (dpeaa)DE-He213 Li, Xiang aut Liu, Yubo aut Ma, Baozhong (orcid)0000-0003-3907-9097 aut Wang, Hua aut Jiang, Xingming aut Wang, Chengyan aut Enthalten in Journal of thermal analysis and calorimetry Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969 147(2022), 23 vom: 08. Okt., Seite 13469-13481 (DE-627)315295422 (DE-600)2017304-0 1572-8943 nnns volume:147 year:2022 number:23 day:08 month:10 pages:13469-13481 https://dx.doi.org/10.1007/s10973-022-11628-6 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 147 2022 23 08 10 13469-13481 |
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10.1007/s10973-022-11628-6 doi (DE-627)SPR048720690 (SPR)s10973-022-11628-6-e DE-627 ger DE-627 rakwb eng Yang, Weijiao verfasserin aut Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. African cobalt-rich copper sulfide ore (dpeaa)DE-He213 Thermal roasting kinetics (dpeaa)DE-He213 Roasting behavior (dpeaa)DE-He213 Deconvolution integral separation (dpeaa)DE-He213 Sulfating reaction (dpeaa)DE-He213 Li, Xiang aut Liu, Yubo aut Ma, Baozhong (orcid)0000-0003-3907-9097 aut Wang, Hua aut Jiang, Xingming aut Wang, Chengyan aut Enthalten in Journal of thermal analysis and calorimetry Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969 147(2022), 23 vom: 08. Okt., Seite 13469-13481 (DE-627)315295422 (DE-600)2017304-0 1572-8943 nnns volume:147 year:2022 number:23 day:08 month:10 pages:13469-13481 https://dx.doi.org/10.1007/s10973-022-11628-6 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 147 2022 23 08 10 13469-13481 |
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10.1007/s10973-022-11628-6 doi (DE-627)SPR048720690 (SPR)s10973-022-11628-6-e DE-627 ger DE-627 rakwb eng Yang, Weijiao verfasserin aut Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere 2022 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. African cobalt-rich copper sulfide ore (dpeaa)DE-He213 Thermal roasting kinetics (dpeaa)DE-He213 Roasting behavior (dpeaa)DE-He213 Deconvolution integral separation (dpeaa)DE-He213 Sulfating reaction (dpeaa)DE-He213 Li, Xiang aut Liu, Yubo aut Ma, Baozhong (orcid)0000-0003-3907-9097 aut Wang, Hua aut Jiang, Xingming aut Wang, Chengyan aut Enthalten in Journal of thermal analysis and calorimetry Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969 147(2022), 23 vom: 08. Okt., Seite 13469-13481 (DE-627)315295422 (DE-600)2017304-0 1572-8943 nnns volume:147 year:2022 number:23 day:08 month:10 pages:13469-13481 https://dx.doi.org/10.1007/s10973-022-11628-6 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER GBV_ILN_11 GBV_ILN_20 GBV_ILN_22 GBV_ILN_23 GBV_ILN_24 GBV_ILN_31 GBV_ILN_32 GBV_ILN_39 GBV_ILN_40 GBV_ILN_60 GBV_ILN_62 GBV_ILN_63 GBV_ILN_69 GBV_ILN_70 GBV_ILN_73 GBV_ILN_74 GBV_ILN_90 GBV_ILN_95 GBV_ILN_100 GBV_ILN_105 GBV_ILN_110 GBV_ILN_120 GBV_ILN_138 GBV_ILN_150 GBV_ILN_151 GBV_ILN_152 GBV_ILN_161 GBV_ILN_170 GBV_ILN_171 GBV_ILN_187 GBV_ILN_206 GBV_ILN_213 GBV_ILN_224 GBV_ILN_230 GBV_ILN_250 GBV_ILN_281 GBV_ILN_285 GBV_ILN_293 GBV_ILN_370 GBV_ILN_602 GBV_ILN_636 GBV_ILN_702 GBV_ILN_2001 GBV_ILN_2003 GBV_ILN_2004 GBV_ILN_2005 GBV_ILN_2006 GBV_ILN_2007 GBV_ILN_2008 GBV_ILN_2009 GBV_ILN_2010 GBV_ILN_2011 GBV_ILN_2014 GBV_ILN_2015 GBV_ILN_2020 GBV_ILN_2021 GBV_ILN_2025 GBV_ILN_2026 GBV_ILN_2027 GBV_ILN_2031 GBV_ILN_2034 GBV_ILN_2037 GBV_ILN_2038 GBV_ILN_2039 GBV_ILN_2044 GBV_ILN_2048 GBV_ILN_2049 GBV_ILN_2050 GBV_ILN_2055 GBV_ILN_2056 GBV_ILN_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2088 GBV_ILN_2093 GBV_ILN_2106 GBV_ILN_2107 GBV_ILN_2108 GBV_ILN_2110 GBV_ILN_2111 GBV_ILN_2112 GBV_ILN_2113 GBV_ILN_2118 GBV_ILN_2119 GBV_ILN_2122 GBV_ILN_2129 GBV_ILN_2143 GBV_ILN_2144 GBV_ILN_2147 GBV_ILN_2148 GBV_ILN_2152 GBV_ILN_2153 GBV_ILN_2188 GBV_ILN_2190 GBV_ILN_2232 GBV_ILN_2336 GBV_ILN_2446 GBV_ILN_2470 GBV_ILN_2472 GBV_ILN_2507 GBV_ILN_2522 GBV_ILN_2548 GBV_ILN_4035 GBV_ILN_4037 GBV_ILN_4046 GBV_ILN_4112 GBV_ILN_4125 GBV_ILN_4126 GBV_ILN_4242 GBV_ILN_4246 GBV_ILN_4249 GBV_ILN_4251 GBV_ILN_4305 GBV_ILN_4306 GBV_ILN_4307 GBV_ILN_4313 GBV_ILN_4322 GBV_ILN_4323 GBV_ILN_4324 GBV_ILN_4325 GBV_ILN_4326 GBV_ILN_4328 GBV_ILN_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 147 2022 23 08 10 13469-13481 |
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Yang, Weijiao @@aut@@ Li, Xiang @@aut@@ Liu, Yubo @@aut@@ Ma, Baozhong @@aut@@ Wang, Hua @@aut@@ Jiang, Xingming @@aut@@ Wang, Chengyan @@aut@@ |
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Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law.</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms.</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">African cobalt-rich copper sulfide ore</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Thermal roasting kinetics</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Roasting behavior</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Deconvolution integral separation</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="650" ind1=" " ind2="4"><subfield code="a">Sulfating reaction</subfield><subfield code="7">(dpeaa)DE-He213</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Li, Xiang</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Liu, Yubo</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Ma, Baozhong</subfield><subfield code="0">(orcid)0000-0003-3907-9097</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Wang, Hua</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Jiang, Xingming</subfield><subfield code="4">aut</subfield></datafield><datafield tag="700" ind1="1" ind2=" "><subfield code="a">Wang, Chengyan</subfield><subfield code="4">aut</subfield></datafield><datafield tag="773" ind1="0" ind2="8"><subfield code="i">Enthalten in</subfield><subfield code="t">Journal of thermal analysis and calorimetry</subfield><subfield code="d">Dordrecht [u.a.] : Springer Science + Business Media B.V., 1969</subfield><subfield code="g">147(2022), 23 vom: 08. 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|
author |
Yang, Weijiao |
spellingShingle |
Yang, Weijiao misc African cobalt-rich copper sulfide ore misc Thermal roasting kinetics misc Roasting behavior misc Deconvolution integral separation misc Sulfating reaction Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere |
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Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere African cobalt-rich copper sulfide ore (dpeaa)DE-He213 Thermal roasting kinetics (dpeaa)DE-He213 Roasting behavior (dpeaa)DE-He213 Deconvolution integral separation (dpeaa)DE-He213 Sulfating reaction (dpeaa)DE-He213 |
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misc African cobalt-rich copper sulfide ore misc Thermal roasting kinetics misc Roasting behavior misc Deconvolution integral separation misc Sulfating reaction |
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misc African cobalt-rich copper sulfide ore misc Thermal roasting kinetics misc Roasting behavior misc Deconvolution integral separation misc Sulfating reaction |
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Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere |
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Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere |
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Yang, Weijiao |
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Journal of thermal analysis and calorimetry |
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Yang, Weijiao Li, Xiang Liu, Yubo Ma, Baozhong Wang, Hua Jiang, Xingming Wang, Chengyan |
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Elektronische Aufsätze |
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Yang, Weijiao |
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title_sort |
thermal roasting behavior and kinetics of african cobalt-rich copper sulfide ore in air atmosphere |
title_auth |
Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere |
abstract |
Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
abstractGer |
Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
abstract_unstemmed |
Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. Therefore, it is of practical significance to explore the kinetics process in the activated roasting process of CRCS. In this study, thermal roasting kinetics of CRCS in the air atmosphere was studied by TG-DTG method at heating rates of 5, 10, 15, and 20 K $ min^{−1} $, respectively. Meanwhile, the phase transformation behavior of major minerals, pyrite, and carrollite during roasting was studied. The results show that the roasting process of CRCS mainly goes through three stages: Stage I: removal of free water and crystal water; Stage II: oxidation of sulfide minerals to sulfate; and Stage III: decomposition of sulfate to oxide. Given Stage II, the deconvolution separation method was used to separate overlapping reaction peaks of $ FeS_{2} $ and $ CuCo_{2} %$ S_{4} $. The kinetic parameters were evaluated by Friedman method, KAS method, FWO method, and CR method, respectively. The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. The oxidation processes of different ore in CRCS conform to different kinetic mechanisms. © Akadémiai Kiadó, Budapest, Hungary 2022. Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law. |
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container_issue |
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title_short |
Thermal roasting behavior and kinetics of African cobalt-rich copper sulfide ore in air atmosphere |
url |
https://dx.doi.org/10.1007/s10973-022-11628-6 |
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author2 |
Li, Xiang Liu, Yubo Ma, Baozhong Wang, Hua Jiang, Xingming Wang, Chengyan |
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Li, Xiang Liu, Yubo Ma, Baozhong Wang, Hua Jiang, Xingming Wang, Chengyan |
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doi_str |
10.1007/s10973-022-11628-6 |
up_date |
2024-07-03T21:03:19.982Z |
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Springer Nature or its licensor holds exclusive rights to this article under a publishing agreement with the author(s) or other rightsholder(s); author self-archiving of the accepted manuscript version of this article is solely governed by the terms of such publishing agreement and applicable law.</subfield></datafield><datafield tag="520" ind1=" " ind2=" "><subfield code="a">Abstract African cobalt-rich copper sulfide ore (CRCS) is an important copper-cobalt resource. The CRCS mainly contains chalcopyrite ($ CuFeS_{2} $), pyrite ($ FeS_{2} $), and carrollite ($ CuCo_{2} %$ S_{4} $). In our previous study, activated roasting was used to treat CRCS, converting $ CuCo_{2} %$ S_{4} $ into sulfate that is easy to leach Cu and Co. It was found that the kinetics of $ CuCo_{2} %$ S_{4} $ in CRCS transformation was slow during roasting, which is a key factor affecting the subsequent increase in cobalt leaching rate. 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The most probable mechanism function and activation energy (E) were determined by comparing the model-free method with the model-fitting method. Results showed that the oxidation of $ FeS_{2} $ in CRCS conforms to the 2-D diffusion model; the oxidation of $ CuCo_{2} %$ S_{4} $ in CRCS accords with the Avrami–Eroféev model. Finally, thermodynamic parameters of the reaction including enthalpy, entropy, and Gibbs free energy were calculated. Kinetic analysis shows that the heating rate has a significant influence on the ore phase transition during the oxidation process of CRCS. 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score |
7.3972845 |