In situ alloying of Cu—Cr—Nb alloys using selective laser melting
US-11859272-B1 · Jan 2, 2024 · US
US2023078641A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2023078641-A1 |
| Application number | US-202017904172-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 21, 2020 |
| Priority date | Feb 18, 2020 |
| Publication date | Mar 16, 2023 |
| Grant date | — |
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A method for producing a collector alloy comprising 25 to 100 wt % precious metal in total, comprising 0 to <97 wt % of the precious metal silver, 0 to 75 wt % of at least one precious metal selected from gold, platinum, rhodium and palladium, and 0 to 75 wt % of at least one non-precious metal selected from copper, iron, tin and nickel, or for producing pure silver, comprising the steps of:(1) providing precious metal sweeps;(2) providing a flux which, during collective melting with the refractory inorganic material from the precious metal sweeps provided in step (1);(3) collective melting of the materials provided in steps (1) and (2) at a temperature in the range of from 1300 to 1600° C., forming a melt comprising at least two phases of different densities arranged one above the other; and.(4) separating the upper phase and the lower phase.
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1 . A method for producing a collector alloy comprising 25 to 100 wt % precious metal in total, comprising 0 to <97 wt % of the precious metal silver, 0 to 75 wt % of at least one precious metal selected from the group consisting of gold, platinum, rhodium and palladium, and 0 to 75 wt % of at least one non-precious metal selected from the group consisting of copper, iron, tin and nickel, comprising the steps of: (1) providing precious metal sweeps comprising 4 to 30 wt % precious metal in total, comprising 0 to 30 wt % of the precious metal silver, 0 to 10 wt % of at least one precious metal selected from the group consisting of gold, platinum, rhodium and palladium, 0 to 10 wt % of at least one non-precious metal selected from the group consisting of copper, iron, tin and nickel, and 70 to 96 wt % of at least one refractory inorganic material, (2) providing a flux which, during collective melting with the refractory inorganic material from the precious metal sweeps provided in step (1), is capable of forming a molten slag consisting of >35 to 45 wt % calcium oxide, 35 to 45 wt % silicon dioxide, 15 to <20 wt % aluminum oxide, and 0 to <15 wt % of one or more refractory inorganic compounds other than calcium oxide, silicon dioxide and aluminum oxide, (3) collective melting of the materials provided in steps (1) and (2) at a temperature in the range from 1300 to 1600° C., forming a melt comprising at least two phases of different densities arranged one above the other, and (4) separating the low-density upper phase and the high-density lower phase, wherein the upper phase comprises a slag phase consisting of >35 to 45 wt % calcium oxide, 35 to 45 wt % silicon dioxide, 15 to <20 wt % aluminum oxide, and 0 to <15 wt % of one or more refractory inorganic compounds other than calcium oxide, silicon dioxide and aluminum oxide, and the lower phase comprises the collector alloy, wherein none of the materials used in the method comprises copper oxide, except for copper oxide optionally present as an outer copper oxide layer on metallic copper. 2 . A method for producing pure silver, comprising the steps of: (1) providing silver sweeps consisting of 4 to 30 wt % silver and 70 to 96 wt % of at least one refractory inorganic material, (2) providing a flux which, during collective melting with the refractory inorganic material from the silver sweeps provided in step (1), is capable of forming a molten slag consisting of >35 to 45 wt % calcium oxide, 35 to 45 wt % silicon dioxide, 15 to <20 wt % aluminum oxide, and 0 to <15 wt % of one or more refractory inorganic compounds other than calcium oxide, silicon dioxide and aluminum oxide, (3) collective melting of the materials provided in steps (1) and (2) at a temperature in the range of from 1300 to 1600° C., forming a melt comprising at least two phases of different densities arranged one above the other, and (4) separating the low-density upper phase and the high-density lower phase, wherein the upper phase comprises a slag phase consisting of >35 to 45 wt % calcium oxide, 35 to 45 wt % silicon dioxide, 15 to <20 wt % aluminum oxide, and 0 to <15 wt % of one or more refractory inorganic compounds other than calcium oxide, silicon dioxide and aluminum oxide, and the lower phase comprises pure silver, wherein none of the materials used in the method comprises copper oxide. 3 . The method according to claim 1 , wherein the precious metal sweeps comprise 3.5 to 29.5 wt % of the precious metal silver, 0.5 to 10 wt % of at least one precious metal selected from the group consisting of gold, platinum, rhodium and palladium, 0 to 10 wt % of at least one non-precious metal selected from the group consisting of copper, iron, tin and nickel, and 70 to 96 wt % of at least one refractory inorganic material. 4 . The method according to claim 1 , wherein the precious metal sweeps and/or the flux are crushed prior to the collective melting in step (3). 5 . The method according to claim 2 , wherein the silver sweeps and/or the flux are crushed prior to the collective melting in step (3). 6 . The method according to claim 1 , wherein work is carried out so as to produce a ratio of the upper and lower phases, adding up to 100 parts by weight, in the range of 5 to 60 parts by weight of collector alloy: 40 to 95 parts by weight of slag. 7 . The method according to claim 2 , wherein work is carried out so as to produce a ratio of the upper and lower phases, adding up to 100 parts by weight, in the range of 5 to 60 parts by weight of silver: 40 to 95 parts by weight of slag. 8 . The method according to claim 1 , wherein reducing agent is supplied or added during step (3). 9 . The method according to claim 1 , wherein the melting process takes place in a rotating and/or tiltable melting furnace. 10 . The method according to claim 1 , wherein step (4) is a separation of said phases from one another by exploiting the density difference. 11 . The method according to claim 1 , wherein step (4) is conducted in such a way that the two-phase or multiphase melt is poured out and allowed to cool and solidify without separation measures, followed by mechanical separation of the solidified phases.
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