DE2602827

1481295 Recovery of precious metals NATIONAL INSTITUTE FOR METALLURGY 29 Jan 1976 [29 Jan 1975] 03495/76 Heading C1A [Also in Division C7] Precious metals (defined as Pt. group, Au and Ag) are recovered from a concentrate by alloying the concentrate with Al, and leaching the alloy to produce a solut...

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Hauptverfasser: EDWARDS, RODERICK IVAN, HONEYDEW, ZA, LOO, JOE POK, SANDTON, ZA, OSSIN, DAVID IAN, JOHANNESBURG, ZA
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LOO, JOE POK, SANDTON, ZA
OSSIN, DAVID IAN, JOHANNESBURG, ZA
description 1481295 Recovery of precious metals NATIONAL INSTITUTE FOR METALLURGY 29 Jan 1976 [29 Jan 1975] 03495/76 Heading C1A [Also in Division C7] Precious metals (defined as Pt. group, Au and Ag) are recovered from a concentrate by alloying the concentrate with Al, and leaching the alloy to produce a solution containing the precious metals. The alloy is preferably produced by melting the concentrate and Al powder at 1000‹ C or by an aluminothermic process by igniting a mixture of concentrate, Al powder and an oxide or sulphide (e.g. Fe 2 O 3 or FeS), at 1000‹ C (the oxide or sulphide may be omitted if already present in the concentrate). If the precious metal content of the concentrate is below 30 wt.%, the alloy may be formed by mixing the concentrate with C and CaO, roasting at 800‹ C, smelting with scrap iron in an arc furnace, removing the slag and adding Al scrap to form an Al-Fe-precious metal alloy. The alloy is initially leached with HCl or H 2 SO 4 to remove the Al and base metals, the residue being further leached under oxidizing conditions in HCl, using Cl 2 as the oxidant, to effect dissolution of the precious metals. If desired, the residue from the initial leaching step may be leached to dissolve Cu prior to the precious metal leach.
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The alloy is preferably produced by melting the concentrate and Al powder at 1000‹ C or by an aluminothermic process by igniting a mixture of concentrate, Al powder and an oxide or sulphide (e.g. Fe 2 O 3 or FeS), at 1000‹ C (the oxide or sulphide may be omitted if already present in the concentrate). If the precious metal content of the concentrate is below 30 wt.%, the alloy may be formed by mixing the concentrate with C and CaO, roasting at 800‹ C, smelting with scrap iron in an arc furnace, removing the slag and adding Al scrap to form an Al-Fe-precious metal alloy. The alloy is initially leached with HCl or H 2 SO 4 to remove the Al and base metals, the residue being further leached under oxidizing conditions in HCl, using Cl 2 as the oxidant, to effect dissolution of the precious metals. 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The alloy is preferably produced by melting the concentrate and Al powder at 1000‹ C or by an aluminothermic process by igniting a mixture of concentrate, Al powder and an oxide or sulphide (e.g. Fe 2 O 3 or FeS), at 1000‹ C (the oxide or sulphide may be omitted if already present in the concentrate). If the precious metal content of the concentrate is below 30 wt.%, the alloy may be formed by mixing the concentrate with C and CaO, roasting at 800‹ C, smelting with scrap iron in an arc furnace, removing the slag and adding Al scrap to form an Al-Fe-precious metal alloy. The alloy is initially leached with HCl or H 2 SO 4 to remove the Al and base metals, the residue being further leached under oxidizing conditions in HCl, using Cl 2 as the oxidant, to effect dissolution of the precious metals. 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subjects CHEMISTRY
COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSESC01D OR C01F
FERROUS OR NON-FERROUS ALLOYS
INORGANIC CHEMISTRY
METALLURGY
PRETREATMENT OF RAW MATERIALS
PRODUCTION AND REFINING OF METALS
TREATMENT OF ALLOYS OR NON-FERROUS METALS
title DE2602827
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