Submerged combustion in molten materials

Claim 2

A process for heating a molten material by oxygen and a fluid fuel comprising the steps of: (a) providing a bath containing molten material at a bath temperature at or above the spontaneous combustion temperature of said fuel, said molten material having at least the same resistance to oxidation by carbon dioxide and water at bath temperature as nickel; (b) injecting oxygen and said fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fuel to no greater than about 150% of that required for complete combustion of said fuel; and (d) combusting said fuel to provide heat to said molten material.

Claim 3

The process of claim 1 wherein all of said fluid fuel forms a shroud surrounding the injected oxygen.

Claim 4

The process of claim 1 wherein a portion of said fluid fuel forms a shroud surrounding both the injected oxygen and the remaining portion of said fuel.

Claim 5

The process of claim 3 wherein the shroud-forming fluid fuel is from about 10% to about 50% of the total fuel injected through said tuyere.

Claim 6

The process of claim 3 wherein the injected oxygen forms a shroud surrounding the remaining portion of said fuel.

Claim 7

The process of claim 1 wherein said material is a metal is selected from the group consisting of copper, nickel, lead, palladium, osmium, gold, and silver.

Claim 8

The process of claim 1 wherein said material is a non-metallic material selected from the group consisting of silica, alumina, and slags containing silicates, metallic oxides, and lime.

Claim 9

The process of claim 6 wherein said metal is copper.

Claim 10

The process of claim 8 additionally comprising, during any of steps (b) through (d), the steps of: (i) adding solid copper to said molten copper; (ii) melting said solid copper in said bath primarily by the heat generated in step (d); and (iii) maintaining said bath temperature no lower than about 2000° F. (1090° C.) without additional external heat input.

Claim 11

The process of claim 9 wherein said scrap copper after melting comprises at least 5% of said molten copper.

Claim 12

The process of claim 1 wherein during step (c) the amount of oxygen injected is from about 75% to about 150% of that required for complete combustion with said fuel.

Claim 13

The process of claim 1 wherein the injected oxygen is at least 70% pure.

Claim 14

The process of claim 1 wherein said fluid fuel is selected from the group consisting of hydrogen, natural gas, methane, ethane, propane, butane and combinations thereof.

Claim 15

A process for refining copper comprising the steps of: (a) providing a bath of impure molten copper having oxygen containing impurities, including dissolved oxygen: (b) injecting oxygen and a fluid fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fluid fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fluid fuel to less than that required for complete combustion of said fuel; and (d) reacting said injected oxygen, fuel and oxygen-containing impurities in said bath to remove said oxygen-containing impurities.

Claim 16

A process for refining copper comprising the steps of: (a) providing a bath of impure molten copper having oxygen containing impurities, including dissolved oxygen: (b) injecting oxygen and a fluid fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fluid fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fluid fuel to less than that required for complete combustion of said fuel; and (d) reacting said injected oxygen, fuel and oxygen-containing impurities in said bath to remove said oxygen-containing impurities.

Claim 17

The process of claim 14 wherein all of said fluid fuel forms a shroud surrounding the injected oxygen.

Claim 18

The process of claim 14 wherein a portion of said fluid fuel forms a shroud surrounding both the injected oxygen and the remaining portion of said fuel.

Claim 19

The process of claim 16 wherein the shroud-forming fluid fuel is from about 10% to about 50% of the total fuel injected through said tuyere.

Claim 20

The process of claim 16 wherein the injected oxygen forms a shroud surrounding the remaining portion of said fuel.

Claim 21

The process of claim 14 additionally comprising, during any of steps (b) through (d), the steps of: (i) adding solid copper to said molten copper; (ii) melting said solid copper in said bath primarily by the heat generated in step (d); and (iii) maintaining said bath temperature no lower than about 2000° F. (1090° C.) without additional external heat input.

Claim 22

The process of claim 19 wherein said solid copper after melting comprises at least 5% of said molten copper.

Claim 23

The process of claim 14 wherein the amount of said oxygen injected is from about 25% to less than 100% of that required for complete combustion with said fluid fuel.

Claim 24

The process of claim 14 wherein the amount of said oxygen injected is from about 33% to less than 100% of that required for complete combustion with said fluid fuel.

Claim 25

The process of claim 14 wherein the injected oxygen is at least 70% pure.

Claim 26

The process of claim 14 wherein said fluid fuel is selected from the group consisting of hydrogen, natural gas, methane, ethane, propane, butane and combinations thereof.

Claim 27

The process of claim 14 wherein during step (c) the amount of said oxygen injected is from about 25% to about 33% of that required for complete combustion with said fuel, and during step (d) reaction products form which are emitted from said bath as off-gas, and the opacity of said off-gas is no greater than 20%.

Claim 28

The process of claim 14 wherein said impure molten copper is desulfurized crude or blister copper.

Claim 29

A process for refining copper comprising the steps of: (a) providing a bath of impure molten copper having oxidizable impurities, including sulfur, and oxygen-containing impurities, including dissolved oxygen; (b) injecting oxygen and a fluid fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fluid fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fluid fuel to no less than that required for complete combustion of said fuel; (d) reacting said injected oxygen, fuel and oxidizable impurities in said bath to remove said oxidizable impurities; (e) adjusting the amount of said oxygen injected relative to said fluid fuel to less than that required for complete combustion of said fuel; and (f) reacting said injected oxygen, fuel and oxygen-containing impurities in said bath to remove said oxygen-containing impurities.

Claim 30

A process for refining copper comprising the steps of: (a) providing a bath of impure molten copper having oxidizable impurities, including sulfur, and oxygen-containing impurities, including dissolved oxygen; (b) injecting oxygen and a fluid fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fluid fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fluid fuel to no less than that required for complete combustion of said fuel; (d) reacting said injected oxygen, fuel and oxidizable impurities in said bath to remove said oxidizable impurities; (e) adjusting the amount of said oxygen injected relative to said fluid fuel to less than that required for complete combustion of said fuel; and (f) reacting said injected oxygen, fuel and oxygen-containing impurities in said bath to remove said oxygen-containing impurities.

Claim 31

The process of claim 27 wherein all of said fluid fuel forms a shroud surrounding the injected oxygen.

Claim 32

The process of claim 27 wherein a portion of said fluid fuel forms a shroud surrounding both the injected oxygen and the remaining portion of said fuel.

Claim 33

The process of claim 29 wherein the shroud forming fluid fuel is from about 10% to about 50% of the total fuel injected through said tuyere.

Claim 34

The process of claim 29 wherein the injected oxygen forms a shroud surrounding the remaining portion of said fluid fuel.

Claim 35

The process of claim 27 additionally comprising, during any of steps (b) through (f), the steps of: (i) adding solid copper to said molten copper; (ii) melting said solid copper in said bath primarily by the heat generated in steps (d) or (f); and (iii) maintaining said bath temperature no lower than about 2000° F. (1090° C.) without additional external heat input.

Claim 36

The process of claim 32 wherein said solid copper after melting comprises at least 5% of said molten copper.

Claim 37

The process of claim 27 wherein the amount of said oxygen injected in step (c) is from 100% to about 450% of that required for complete combustion with said fluid fuel.

Claim 38

The process of claim 27 wherein the amount of said oxygen injected in step (c) is from 100% to about 300% of that required for complete combustion with said fluid fuel.

Claim 39

The process of claim 27 wherein the amount of said oxygen injected in step (e) is from 25% to less than 100% of that required for complete combustion with said fluid fuel.

Claim 40

The process of claim 27 wherein the amount of said oxygen injected in step (e) is from 33% to less than 100% of that required for complete combustion with said fluid fuel.

Claim 41

The process of claim 27 wherein the injected oxygen is at least 70% pure.

Claim 42

The process of claim 27 wherein said fluid fuel is selected from the group consisting of hydrogen, natural gas, methane, ethane, propane, butane, and combinations thereof.

Claim 43

The process of claim 27 wherein during step (e) the amount of said oxygen injected is from about 25% to about 33% of that re quired for complete combustion with said fuel, and during step (f) reaction products form which are emitted from said bath as off-gas, and the opacity of said off-gas is no greater than 20%.

Claim 44

The process of claim 27 wherein said impure molten copper is crude or blister copper.

Claim 45

A process for refining copper comprising the steps of: (a) providing a bath of impure molten crude or blister copper having oxidizable impurities, including sulfur, and oxygen-containing impurities, including dissolved oxygen; (b) injecting oxygen and a fluid fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fluid fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fluid fuel to no less than that required for complete combustion of said fuel; (d) reacting said injected oxygen, fuel and oxidizable impurities in said bath to remove said oxidizable impurities; (e) adjusting the amount of said oxygen injected relative to said fluid fuel to less than that required for complete combustion of said fuel; and (f) reacting said injected oxygen, fuel and oxygen-containing impurities in said bath to remove said oxygen-containing impurities; and (g) during any one or more of steps b) through (f), the steps of: (i) adding solid copper to said molten copper; (ii) melting said solid copper in said bath primarily by the heat generated in steps (d) or (f); and (iii) maintaining said bath temperature no lower than about 2000° F. (1090° C. ) without additional external heat input.

Claim 46

A process for refining copper comprising the steps of: (a) providing a bath of impure molten crude or blister copper having oxidizable impurities, including sulfur, and oxygen-containing impurities, including dissolved oxygen; (b) injecting oxygen and a fluid fuel into said bath through a tuyere below the surface of said bath, at least a portion of said fluid fuel forming a shroud surrounding the injected oxygen; (c) controlling the amount of said oxygen injected relative to said fluid fuel to no less than that required for complete combustion of said fuel; (d) reacting said injected oxygen, fuel and oxidizable impurities in said bath to remove said oxidizable impurities; (e) adjusting the amount of said oxygen injected relative to said fluid fuel to less than that required for complete combustion of said fuel; and (f) reacting said injected oxygen, fuel and oxygen-containing impurities in said bath to remove said oxygen-containing impurities; and (g) during any one or more of steps b) through (f), the steps of: (i) adding solid copper to said molten copper; (ii) melting said solid copper in said bath primarily by the heat generated in steps (d) or (f); and (iii) maintaining said bath temperature no lower than about 2000° F. (1090° C. ) without additional external heat input.

Claim 47

The process of claim 42 wherein the shroud-forming fluid fuel is from about 10% to about 50% of the total fuel injected through said tuyere.

Claim 48

The process of claim 42 wherein the injected oxygen forms a shroud surrounding the remaining portion of said fuel.

Claim 49

The process of claim 42 wherein said solid copper a fter melting comprises at least 5% of said molten copper.

Claim 50

The process of claim 42 wherein the amount of said oxygen injected in step (c) is from 100% to about 450% of that required for complete combustion with said fluid fuel.

Claim 51

The process of claim 42 wherein the amount of said oxygen injected in step (c) is from 100% to about 300% of that required for complete combustion with said fluid fuel.

Claim 52

The process of claim 42 wherein the amount of said oxygen injected in step (e) is from 25% to less than 100% of that required for complete combustion with said fluid fuel.

Claim 53

The process of claim 42 wherein the amount of said oxygen injected in step (e) is from 33% to less than 100% of that required for complete combustion with said fluid fuel.

Claim 54

The process of claim 42 wherein the injected oxygen is at least 90% pure.

Claim 55

The process of claim 42 wherein said fluid fuel is selected from the group consisting of hydrogen, natural gas, methane, ethane, propane, butane, and combinations thereof.

Claim 56

The process of claim 42 wherein during step (e) the amount of said oxygen injected is from about 25% to about 33% of that required for complete combustion with said fuel, and during step (f) reaction products form which are emitted from said bath as off-gas, and the opacity of said off-gas is no greater than 20%.

Claim 57

The process of claim 1 wherein during step (c) the amount of oxygen injected is less than that required for complete combustion with said fuel.