Development of the processing technology of a gold-containing sulfide concentrate
Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its s...
Ausführliche Beschreibung
Gespeichert in:
| Autor*in: |
Neta, V. [verfasserIn] Strizhko, L. S. [verfasserIn] |
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| Format: |
E-Artikel |
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| Sprache: |
Englisch |
| Erschienen: |
2008 |
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| Schlagwörter: |
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| Übergeordnetes Werk: |
Enthalten in: Russian journal of non-ferrous metals - New York, NY : Allerton Press, 2007, 49(2008), 2 vom: Apr., Seite 104-109 |
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| Übergeordnetes Werk: |
volume:49 ; year:2008 ; number:2 ; month:04 ; pages:104-109 |
| Links: |
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| DOI / URN: |
10.3103/S1067821208020077 |
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| Katalog-ID: |
SPR023424761 |
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| 245 | 1 | 0 | |a Development of the processing technology of a gold-containing sulfide concentrate |
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| 520 | |a Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. | ||
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| 650 | 4 | |a Copper Carbon |7 (dpeaa)DE-He213 | |
| 700 | 1 | |a Strizhko, L. S. |e verfasserin |4 aut | |
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10.3103/S1067821208020077 doi (DE-627)SPR023424761 (SPR)S1067821208020077-e DE-627 ger DE-627 rakwb eng 620 660 ASE Neta, V. verfasserin aut Development of the processing technology of a gold-containing sulfide concentrate 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. Noble Metal (dpeaa)DE-He213 Desulfurization (dpeaa)DE-He213 Metal Iron (dpeaa)DE-He213 Blister Copper (dpeaa)DE-He213 Copper Carbon (dpeaa)DE-He213 Strizhko, L. S. verfasserin aut Enthalten in Russian journal of non-ferrous metals New York, NY : Allerton Press, 2007 49(2008), 2 vom: Apr., Seite 104-109 (DE-627)531202909 (DE-600)2323641-3 1934-970X nnns volume:49 year:2008 number:2 month:04 pages:104-109 https://dx.doi.org/10.3103/S1067821208020077 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_65 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 49 2008 2 04 104-109 |
| spelling |
10.3103/S1067821208020077 doi (DE-627)SPR023424761 (SPR)S1067821208020077-e DE-627 ger DE-627 rakwb eng 620 660 ASE Neta, V. verfasserin aut Development of the processing technology of a gold-containing sulfide concentrate 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. Noble Metal (dpeaa)DE-He213 Desulfurization (dpeaa)DE-He213 Metal Iron (dpeaa)DE-He213 Blister Copper (dpeaa)DE-He213 Copper Carbon (dpeaa)DE-He213 Strizhko, L. S. verfasserin aut Enthalten in Russian journal of non-ferrous metals New York, NY : Allerton Press, 2007 49(2008), 2 vom: Apr., Seite 104-109 (DE-627)531202909 (DE-600)2323641-3 1934-970X nnns volume:49 year:2008 number:2 month:04 pages:104-109 https://dx.doi.org/10.3103/S1067821208020077 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_65 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 49 2008 2 04 104-109 |
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10.3103/S1067821208020077 doi (DE-627)SPR023424761 (SPR)S1067821208020077-e DE-627 ger DE-627 rakwb eng 620 660 ASE Neta, V. verfasserin aut Development of the processing technology of a gold-containing sulfide concentrate 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. Noble Metal (dpeaa)DE-He213 Desulfurization (dpeaa)DE-He213 Metal Iron (dpeaa)DE-He213 Blister Copper (dpeaa)DE-He213 Copper Carbon (dpeaa)DE-He213 Strizhko, L. S. verfasserin aut Enthalten in Russian journal of non-ferrous metals New York, NY : Allerton Press, 2007 49(2008), 2 vom: Apr., Seite 104-109 (DE-627)531202909 (DE-600)2323641-3 1934-970X nnns volume:49 year:2008 number:2 month:04 pages:104-109 https://dx.doi.org/10.3103/S1067821208020077 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_65 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 49 2008 2 04 104-109 |
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10.3103/S1067821208020077 doi (DE-627)SPR023424761 (SPR)S1067821208020077-e DE-627 ger DE-627 rakwb eng 620 660 ASE Neta, V. verfasserin aut Development of the processing technology of a gold-containing sulfide concentrate 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. Noble Metal (dpeaa)DE-He213 Desulfurization (dpeaa)DE-He213 Metal Iron (dpeaa)DE-He213 Blister Copper (dpeaa)DE-He213 Copper Carbon (dpeaa)DE-He213 Strizhko, L. S. verfasserin aut Enthalten in Russian journal of non-ferrous metals New York, NY : Allerton Press, 2007 49(2008), 2 vom: Apr., Seite 104-109 (DE-627)531202909 (DE-600)2323641-3 1934-970X nnns volume:49 year:2008 number:2 month:04 pages:104-109 https://dx.doi.org/10.3103/S1067821208020077 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_65 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 49 2008 2 04 104-109 |
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10.3103/S1067821208020077 doi (DE-627)SPR023424761 (SPR)S1067821208020077-e DE-627 ger DE-627 rakwb eng 620 660 ASE Neta, V. verfasserin aut Development of the processing technology of a gold-containing sulfide concentrate 2008 Text txt rdacontent Computermedien c rdamedia Online-Ressource cr rdacarrier Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. Noble Metal (dpeaa)DE-He213 Desulfurization (dpeaa)DE-He213 Metal Iron (dpeaa)DE-He213 Blister Copper (dpeaa)DE-He213 Copper Carbon (dpeaa)DE-He213 Strizhko, L. S. verfasserin aut Enthalten in Russian journal of non-ferrous metals New York, NY : Allerton Press, 2007 49(2008), 2 vom: Apr., Seite 104-109 (DE-627)531202909 (DE-600)2323641-3 1934-970X nnns volume:49 year:2008 number:2 month:04 pages:104-109 https://dx.doi.org/10.3103/S1067821208020077 lizenzpflichtig Volltext GBV_USEFLAG_A SYSFLAG_A GBV_SPRINGER SSG-OLC-PHA 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_65 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_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_2057 GBV_ILN_2059 GBV_ILN_2061 GBV_ILN_2064 GBV_ILN_2065 GBV_ILN_2068 GBV_ILN_2070 GBV_ILN_2086 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_2116 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_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_4333 GBV_ILN_4334 GBV_ILN_4335 GBV_ILN_4336 GBV_ILN_4338 GBV_ILN_4393 GBV_ILN_4700 AR 49 2008 2 04 104-109 |
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Enthalten in Russian journal of non-ferrous metals 49(2008), 2 vom: Apr., Seite 104-109 volume:49 year:2008 number:2 month:04 pages:104-109 |
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Neta, V. @@aut@@ Strizhko, L. S. @@aut@@ |
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|
| author |
Neta, V. |
| spellingShingle |
Neta, V. ddc 620 misc Noble Metal misc Desulfurization misc Metal Iron misc Blister Copper misc Copper Carbon Development of the processing technology of a gold-containing sulfide concentrate |
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620 660 ASE Development of the processing technology of a gold-containing sulfide concentrate Noble Metal (dpeaa)DE-He213 Desulfurization (dpeaa)DE-He213 Metal Iron (dpeaa)DE-He213 Blister Copper (dpeaa)DE-He213 Copper Carbon (dpeaa)DE-He213 |
| topic |
ddc 620 misc Noble Metal misc Desulfurization misc Metal Iron misc Blister Copper misc Copper Carbon |
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ddc 620 misc Noble Metal misc Desulfurization misc Metal Iron misc Blister Copper misc Copper Carbon |
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ddc 620 misc Noble Metal misc Desulfurization misc Metal Iron misc Blister Copper misc Copper Carbon |
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Elektronische Aufsätze Aufsätze Elektronische Ressource |
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Russian journal of non-ferrous metals |
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Russian journal of non-ferrous metals |
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Development of the processing technology of a gold-containing sulfide concentrate |
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| title_full |
Development of the processing technology of a gold-containing sulfide concentrate |
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Neta, V. |
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Russian journal of non-ferrous metals |
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Russian journal of non-ferrous metals |
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Neta, V. Strizhko, L. S. |
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Elektronische Aufsätze |
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Neta, V. |
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10.3103/S1067821208020077 |
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620 660 |
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verfasserin |
| title_sort |
development of the processing technology of a gold-containing sulfide concentrate |
| title_auth |
Development of the processing technology of a gold-containing sulfide concentrate |
| abstract |
Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. |
| abstractGer |
Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. |
| abstract_unstemmed |
Abstract Smelting of a flotation gold-containing concentrate with the use of a copper collector and slag of the four-component system $ SiO_{2} $-FeO-$ Na_{2} $O-CaO is studied. Optimum parameters are determined for the preliminary roasting of the concentrate (t = 750–800°C, τ = 45–60 min) and its smelting (t = 1200–1250°C, τ = 50–60 min, time of metal-slag stratification is 45 min, concentrate-to-carbon ratio is 10: 1). It is shown that as the last parameter decreases (below 10: 1), reduction of hematite and magnetite to metal iron starts with the subsequent transfer of iron into copper. For a fourfold recycling of the copper collector, the extraction of gold was 99.5% and that of silver was 77.7%. |
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Development of the processing technology of a gold-containing sulfide concentrate |
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https://dx.doi.org/10.3103/S1067821208020077 |
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Strizhko, L. S. |
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Strizhko, L. S. |
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| doi_str |
10.3103/S1067821208020077 |
| up_date |
2024-07-03T18:50:42.183Z |
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