CA2579394A1 - Method for increasing metal production in smelter operations - Google Patents
Method for increasing metal production in smelter operations Download PDFInfo
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- CA2579394A1 CA2579394A1 CA002579394A CA2579394A CA2579394A1 CA 2579394 A1 CA2579394 A1 CA 2579394A1 CA 002579394 A CA002579394 A CA 002579394A CA 2579394 A CA2579394 A CA 2579394A CA 2579394 A1 CA2579394 A1 CA 2579394A1
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- surfactant
- ore
- sulfidic
- ionic surfactant
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- 238000000034 method Methods 0.000 title claims abstract description 24
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 13
- 239000002184 metal Substances 0.000 title claims abstract description 13
- 238000004519 manufacturing process Methods 0.000 title description 7
- 230000008569 process Effects 0.000 claims abstract description 20
- 238000003723 Smelting Methods 0.000 claims abstract description 11
- 239000002736 nonionic surfactant Substances 0.000 claims abstract description 11
- 239000003945 anionic surfactant Substances 0.000 claims abstract description 7
- 239000000203 mixture Substances 0.000 claims abstract description 6
- 238000011084 recovery Methods 0.000 claims abstract 2
- 239000004094 surface-active agent Substances 0.000 claims description 19
- -1 alkyl phenol Chemical compound 0.000 claims description 18
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical group OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 9
- 239000006260 foam Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 229920000642 polymer Polymers 0.000 claims description 5
- ULUAUXLGCMPNKK-UHFFFAOYSA-N Sulfobutanedioic acid Chemical group OC(=O)CC(C(O)=O)S(O)(=O)=O ULUAUXLGCMPNKK-UHFFFAOYSA-N 0.000 claims description 3
- 239000006265 aqueous foam Substances 0.000 claims description 3
- 235000019329 dioctyl sodium sulphosuccinate Nutrition 0.000 claims description 2
- YHAIUSTWZPMYGG-UHFFFAOYSA-L disodium;2,2-dioctyl-3-sulfobutanedioate Chemical group [Na+].[Na+].CCCCCCCCC(C([O-])=O)(C(C([O-])=O)S(O)(=O)=O)CCCCCCCC YHAIUSTWZPMYGG-UHFFFAOYSA-L 0.000 claims description 2
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 claims description 2
- 125000000129 anionic group Chemical group 0.000 abstract 1
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- 239000007788 liquid Substances 0.000 description 5
- 229910052976 metal sulfide Inorganic materials 0.000 description 5
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 3
- 125000000217 alkyl group Chemical group 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 229940028356 diethylene glycol monobutyl ether Drugs 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N ethylene glycol Natural products OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- JCGNDDUYTRNOFT-UHFFFAOYSA-N oxolane-2,4-dione Chemical compound O=C1COC(=O)C1 JCGNDDUYTRNOFT-UHFFFAOYSA-N 0.000 description 3
- 150000003871 sulfonates Chemical class 0.000 description 3
- ZUHZGEOKBKGPSW-UHFFFAOYSA-N tetraglyme Chemical compound COCCOCCOCCOCCOC ZUHZGEOKBKGPSW-UHFFFAOYSA-N 0.000 description 3
- RRQYJINTUHWNHW-UHFFFAOYSA-N 1-ethoxy-2-(2-ethoxyethoxy)ethane Chemical compound CCOCCOCCOCC RRQYJINTUHWNHW-UHFFFAOYSA-N 0.000 description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- SBZXBUIDTXKZTM-UHFFFAOYSA-N diglyme Chemical compound COCCOCCOC SBZXBUIDTXKZTM-UHFFFAOYSA-N 0.000 description 2
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 239000011701 zinc Substances 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- OAYXUHPQHDHDDZ-UHFFFAOYSA-N 2-(2-butoxyethoxy)ethanol Chemical compound CCCCOCCOCCO OAYXUHPQHDHDDZ-UHFFFAOYSA-N 0.000 description 1
- VXQBJTKSVGFQOL-UHFFFAOYSA-N 2-(2-butoxyethoxy)ethyl acetate Chemical compound CCCCOCCOCCOC(C)=O VXQBJTKSVGFQOL-UHFFFAOYSA-N 0.000 description 1
- FPZWZCWUIYYYBU-UHFFFAOYSA-N 2-(2-ethoxyethoxy)ethyl acetate Chemical compound CCOCCOCCOC(C)=O FPZWZCWUIYYYBU-UHFFFAOYSA-N 0.000 description 1
- GZMAAYIALGURDQ-UHFFFAOYSA-N 2-(2-hexoxyethoxy)ethanol Chemical compound CCCCCCOCCOCCO GZMAAYIALGURDQ-UHFFFAOYSA-N 0.000 description 1
- SBASXUCJHJRPEV-UHFFFAOYSA-N 2-(2-methoxyethoxy)ethanol Chemical compound COCCOCCO SBASXUCJHJRPEV-UHFFFAOYSA-N 0.000 description 1
- BJINVQNEBGOMCR-UHFFFAOYSA-N 2-(2-methoxyethoxy)ethyl acetate Chemical compound COCCOCCOC(C)=O BJINVQNEBGOMCR-UHFFFAOYSA-N 0.000 description 1
- CRWNQZTZTZWPOF-UHFFFAOYSA-N 2-methyl-4-phenylpyridine Chemical compound C1=NC(C)=CC(C=2C=CC=CC=2)=C1 CRWNQZTZTZWPOF-UHFFFAOYSA-N 0.000 description 1
- DUIOKRXOKLLURE-UHFFFAOYSA-N 2-octylphenol Chemical compound CCCCCCCCC1=CC=CC=C1O DUIOKRXOKLLURE-UHFFFAOYSA-N 0.000 description 1
- IGFHQQFPSIBGKE-UHFFFAOYSA-N 4-nonylphenol Polymers CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 1
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 125000003342 alkenyl group Chemical class 0.000 description 1
- 150000005215 alkyl ethers Chemical class 0.000 description 1
- VEFXTGTZJOWDOF-UHFFFAOYSA-N benzene;hydrate Chemical compound O.C1=CC=CC=C1 VEFXTGTZJOWDOF-UHFFFAOYSA-N 0.000 description 1
- 229940077388 benzenesulfonate Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 229940019778 diethylene glycol diethyl ether Drugs 0.000 description 1
- XXJWXESWEXIICW-UHFFFAOYSA-N diethylene glycol monoethyl ether Chemical compound CCOCCOCCO XXJWXESWEXIICW-UHFFFAOYSA-N 0.000 description 1
- 229940075557 diethylene glycol monoethyl ether Drugs 0.000 description 1
- MOTZDAYCYVMXPC-UHFFFAOYSA-N dodecyl hydrogen sulfate Chemical class CCCCCCCCCCCCOS(O)(=O)=O MOTZDAYCYVMXPC-UHFFFAOYSA-N 0.000 description 1
- 229940043264 dodecyl sulfate Drugs 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 150000002194 fatty esters Chemical class 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000002334 glycols Chemical class 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 229910052750 molybdenum Inorganic materials 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Polymers CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 1
- 229920001281 polyalkylene Polymers 0.000 description 1
- 229920001515 polyalkylene glycol Polymers 0.000 description 1
- 229920001451 polypropylene glycol Polymers 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- RTVVXRKGQRRXFJ-UHFFFAOYSA-N sodium;2-sulfobutanedioic acid Chemical compound [Na].OC(=O)CC(C(O)=O)S(O)(=O)=O RTVVXRKGQRRXFJ-UHFFFAOYSA-N 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 150000003900 succinic acid esters Chemical class 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 125000000101 thioether group Chemical group 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0002—Preliminary treatment
- C22B15/0004—Preliminary treatment without modification of the copper constituent
- C22B15/0008—Preliminary treatment without modification of the copper constituent by wet processes
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0028—Smelting or converting
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B19/00—Obtaining zinc or zinc oxide
- C22B19/02—Preliminary treatment of ores; Preliminary refining of zinc oxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Abstract
A process for improving recovery of metal values in a smelting operation of the type wherein sulfidic ores are pyrometallurgically reduced. The process includes adding an anionic or non-ionic surfactant and blends thereof to the ore.
Description
METHOD FOR INCREASING METAL PRODUCTION IN SMELTER
OPERATIONS
FIELD OF THE INVENTION
The present disclosure pertains to methods for increasing production of metal values from sulfidic ores in smelting operations.
BACKGROUND OF THE INVENTION
Smelting is a common method for recovering the desired metal value from sulfidic ores. During the smelting process, the sulfur in the ore is oxidized, resulting in an exothermic reaction, whereby the heat generated is sufficient to melt the metal without the need for an external heat source. Typically, a carbonaceous reducing agent, such as coke, is employed in the reaction.
Reverberatory smelters, sometimes called "copolas" are commonly used. The fuel and metal ore charge are usually fed separately. In the first step, two liquids are formed: one is an oxide slag containing the impurities, and the other is a sulfide "matte" containing the valuable metal sulfide and some impurities. Fuel is burned at one end of the furnace, and the heat melts the dry sulfide concentrate (usually after partial roasting) which is fed through the openings in the roof of the furnace. The slag floats on the top of the heavier "matte" and is removed or rejected. The sulfide matte then is forwarded to a converter.
Metal production during the smelting operation is limited by the upper temperature limitations of the smelting furnace. Due to the exothermic nature of the pyrometallurgical reduction, adding additional metal sulfide has the same effect as adding more fuel. In order to increase production, smelters can benefit from smelting ores with increased surface moisture since the moisture will evaporate, reducing the temperature of the upper furnace, and thereby allowing more ore to be fed to the furnace, resulting in an increase in metal production.
While adding moisture to a sulfidic ore prior to smelting provides benefit, the amount of moisture added is limited due to problems that may be associated with increasing ore moisture content, such as caking and clogging of conveyor belts and other conventional ore transport means.
SUMMARY OF THE INVENTION
The present invention involves improvement of metal value yield in smelting processes of the type in which a sulfide containing metal ore is smelted. An aqueous solution or dispersion comprising a surfactant is brought into contact with the ore. In this manner, higher moisture content ores can enter the smelter, allowing for an increase in the amount of ore processed per given time period, and therefore an increase in metal production.
DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS
In accordance with one exemplary embodiment, an aqueous solution or dispersion comprising a surfactant is applied to the sulfidic ore prior to entry into the smelter.
Preferably, the surfactant may be applied in the form of an aqueous foam.
With respect to foam formation, air is preferred for use as the foam forming gas.
Details of the foam forming process are not critical to the invention.
Generally, foam may be produced as stated in U.S. Patent 4,700,200 (Cole), the disclosure of which is incorporated herein. Typically, the aqueous based surfactant is mixed with air at a ratio of about one gallon liquid with from about 1-100, preferably 1-10, scf air. The air and liquid may combine at a point immediately upstream from the mixing chamber. The mixing chamber may be a packed column, venturi, or static mixer.
The purpose of the mixing chamber is to induce the air in liquid dispersion that is defined as a"foam". Acceptable foam properties include expansion ratios (volume foam : volume liquid) on the order of about 10-100. Average bubble size is on the order of about 200 microns or less. Exemplary feed rates would range from about 0.1-1.0 pounds of active surfactant per ton of metal sulfide.
OPERATIONS
FIELD OF THE INVENTION
The present disclosure pertains to methods for increasing production of metal values from sulfidic ores in smelting operations.
BACKGROUND OF THE INVENTION
Smelting is a common method for recovering the desired metal value from sulfidic ores. During the smelting process, the sulfur in the ore is oxidized, resulting in an exothermic reaction, whereby the heat generated is sufficient to melt the metal without the need for an external heat source. Typically, a carbonaceous reducing agent, such as coke, is employed in the reaction.
Reverberatory smelters, sometimes called "copolas" are commonly used. The fuel and metal ore charge are usually fed separately. In the first step, two liquids are formed: one is an oxide slag containing the impurities, and the other is a sulfide "matte" containing the valuable metal sulfide and some impurities. Fuel is burned at one end of the furnace, and the heat melts the dry sulfide concentrate (usually after partial roasting) which is fed through the openings in the roof of the furnace. The slag floats on the top of the heavier "matte" and is removed or rejected. The sulfide matte then is forwarded to a converter.
Metal production during the smelting operation is limited by the upper temperature limitations of the smelting furnace. Due to the exothermic nature of the pyrometallurgical reduction, adding additional metal sulfide has the same effect as adding more fuel. In order to increase production, smelters can benefit from smelting ores with increased surface moisture since the moisture will evaporate, reducing the temperature of the upper furnace, and thereby allowing more ore to be fed to the furnace, resulting in an increase in metal production.
While adding moisture to a sulfidic ore prior to smelting provides benefit, the amount of moisture added is limited due to problems that may be associated with increasing ore moisture content, such as caking and clogging of conveyor belts and other conventional ore transport means.
SUMMARY OF THE INVENTION
The present invention involves improvement of metal value yield in smelting processes of the type in which a sulfide containing metal ore is smelted. An aqueous solution or dispersion comprising a surfactant is brought into contact with the ore. In this manner, higher moisture content ores can enter the smelter, allowing for an increase in the amount of ore processed per given time period, and therefore an increase in metal production.
DETAILED DESCRIPTION OF EXEMPLARY EMBODIMENTS
In accordance with one exemplary embodiment, an aqueous solution or dispersion comprising a surfactant is applied to the sulfidic ore prior to entry into the smelter.
Preferably, the surfactant may be applied in the form of an aqueous foam.
With respect to foam formation, air is preferred for use as the foam forming gas.
Details of the foam forming process are not critical to the invention.
Generally, foam may be produced as stated in U.S. Patent 4,700,200 (Cole), the disclosure of which is incorporated herein. Typically, the aqueous based surfactant is mixed with air at a ratio of about one gallon liquid with from about 1-100, preferably 1-10, scf air. The air and liquid may combine at a point immediately upstream from the mixing chamber. The mixing chamber may be a packed column, venturi, or static mixer.
The purpose of the mixing chamber is to induce the air in liquid dispersion that is defined as a"foam". Acceptable foam properties include expansion ratios (volume foam : volume liquid) on the order of about 10-100. Average bubble size is on the order of about 200 microns or less. Exemplary feed rates would range from about 0.1-1.0 pounds of active surfactant per ton of metal sulfide.
2 Exemplary surfactants that can be used include the anionic surfactants and non-ionic surfactants. Preferably, the non-ionic surfactants have an HLB of between about 10-15. Blends of the aforementioned surfactants can also be mentioned.
Suitable anionic surfactants include sulfates and sulfonates such as alkyl aryl sulfonic acids, alkyl sulfonic acids, alkenyl sulfonic acids, sulfonated alkyls, sulfonated alkyl ethers, sulfonated alkenyls, sulfated fatty esters, and the sulfosuccinates.
The term anionic surfactants should be broadly construed to include the anionic detergents such as the long chain alpha olefin sulfonates, water soluble salts of alkenyl sulfonic acid, such as the sodium salt of C14-C18 alpha olefin sulfonates, water soluble alkyl aryl sulfonic acid salts, such as sodium alkylnapthalene sulfonate and sodium alkyl benzene sulfonate and water soluble salts of lauryl sulfate.
Particularly preferred anionic surfactants are esters represented by the formula COOR' Cf7tlR'-wherein R is an aliphatic carbon chain containing at least one sulfonic group and Rl and R2 may be the same or different, but are chosen from alkyl groups having from 3 to about 18 carbon atoms. Most preferred are the succinic acid esters such as the dioctylester of sodium sulphosuccinic acid.
Exemplary non-ionic surfactants include alkyl phenols, such as the polyalkylene alkyl phenols; polyalkoxylated alkyl phenols; polyoxyalkylene polymers and block copolymers, glycol esters, glycol ethers including diethylene glycol esters, and diethylene glycol ethers, and polyalkylene glycols.
Specific non-ionic surfactants that may be mentioned include polyethylene nonyl phenol, polyethoxylated nonyl phenol, polyoxyethylene polymers and
Suitable anionic surfactants include sulfates and sulfonates such as alkyl aryl sulfonic acids, alkyl sulfonic acids, alkenyl sulfonic acids, sulfonated alkyls, sulfonated alkyl ethers, sulfonated alkenyls, sulfated fatty esters, and the sulfosuccinates.
The term anionic surfactants should be broadly construed to include the anionic detergents such as the long chain alpha olefin sulfonates, water soluble salts of alkenyl sulfonic acid, such as the sodium salt of C14-C18 alpha olefin sulfonates, water soluble alkyl aryl sulfonic acid salts, such as sodium alkylnapthalene sulfonate and sodium alkyl benzene sulfonate and water soluble salts of lauryl sulfate.
Particularly preferred anionic surfactants are esters represented by the formula COOR' Cf7tlR'-wherein R is an aliphatic carbon chain containing at least one sulfonic group and Rl and R2 may be the same or different, but are chosen from alkyl groups having from 3 to about 18 carbon atoms. Most preferred are the succinic acid esters such as the dioctylester of sodium sulphosuccinic acid.
Exemplary non-ionic surfactants include alkyl phenols, such as the polyalkylene alkyl phenols; polyalkoxylated alkyl phenols; polyoxyalkylene polymers and block copolymers, glycol esters, glycol ethers including diethylene glycol esters, and diethylene glycol ethers, and polyalkylene glycols.
Specific non-ionic surfactants that may be mentioned include polyethylene nonyl phenol, polyethoxylated nonyl phenol, polyoxyethylene polymers and
3 polyoxypropylene polymers, (EO) ethylene oxide (PO) propylene oxide polymers, polyethyene oxide octyl phenol ether, polyoxyethylene glycol dioleate, propylene glycol, and diethylene glycol ethers such as the "carbitol " series and diglymes.
Exemplary compounds falling within the classification of diethylene glycol ether compounds include diethylene glycol monobutyl ether, diethylene glycol monobutyl ether acetate, diethylene glycol monoethyl ether acetate, diethylene glycol monoethyl ether, diethylene glycol dibutyl ether, diethylene glycol monohexyl ether, diethylene glycol monomethyl ether, and diethylene glycol monomethyl ether acetate.
Additionally, diglyme (diethylene glycol dimethyl ether), ethyl diglyme (diethylene glycol diethyl ether), and tetraglyme (tetraethylene glycol dimethyl ether may also be mentioned.
Accordingly, the diethylene glycol ether compounds may be defined as having the formula:
(II) R3-(O-Et-O-Et-O)n R4 wherein R3 and R4 are independently selected from the group consisting of C1-lower alkyl, acyl and hydrogen; n is equal to 1 or 2. Of these, diethyleneglycol monobutyl ether (sometimes referred to as butyl carbitol) is preferred.
Preferably, the foam or other carrier containing the surfactant or surfactant blend is fed to the sulfidic ore in an amount of about 0.01 to about 5.0 pounds of active surfactant(s) per ton of metal sulfide. More preferably, from about 0.01 to 1.0 pounds of surfactant(s) is fed per ton of metal sulfide.
Any sulfidic ore that is to be smelted may benefit from the invention. For example, the surfactant treatment may be applied to sulfidic ores such as Au, Fe, Ag, Ni, Cu, Zn, Pb, and Mo ores.
Exemplary compounds falling within the classification of diethylene glycol ether compounds include diethylene glycol monobutyl ether, diethylene glycol monobutyl ether acetate, diethylene glycol monoethyl ether acetate, diethylene glycol monoethyl ether, diethylene glycol dibutyl ether, diethylene glycol monohexyl ether, diethylene glycol monomethyl ether, and diethylene glycol monomethyl ether acetate.
Additionally, diglyme (diethylene glycol dimethyl ether), ethyl diglyme (diethylene glycol diethyl ether), and tetraglyme (tetraethylene glycol dimethyl ether may also be mentioned.
Accordingly, the diethylene glycol ether compounds may be defined as having the formula:
(II) R3-(O-Et-O-Et-O)n R4 wherein R3 and R4 are independently selected from the group consisting of C1-lower alkyl, acyl and hydrogen; n is equal to 1 or 2. Of these, diethyleneglycol monobutyl ether (sometimes referred to as butyl carbitol) is preferred.
Preferably, the foam or other carrier containing the surfactant or surfactant blend is fed to the sulfidic ore in an amount of about 0.01 to about 5.0 pounds of active surfactant(s) per ton of metal sulfide. More preferably, from about 0.01 to 1.0 pounds of surfactant(s) is fed per ton of metal sulfide.
Any sulfidic ore that is to be smelted may benefit from the invention. For example, the surfactant treatment may be applied to sulfidic ores such as Au, Fe, Ag, Ni, Cu, Zn, Pb, and Mo ores.
4 Field Trial At one zinc smelting operation, ZnS ore was treated with a foamed surfactant formulation comprising on all actives bases 45 wt% sodium dioctyl sulfosuccinate 9.65 wt% propylene glycol 25.70 wt% diethylene glycol monobutyl ether remainder water.
Typically, the ZnS ore fed to the smelter had a moisture content of about 10%
as received. Normally, when the ore was sprayed with water to increase the moisture content to about 12.0 wt%, flow and plugging problems were encountered. When the above surfactant blend was foamed onto the ore, moisture contents of from 12.0 to about 14.0 wt% could be processed without significant hopper blockage, transport or plugging problems.
While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of this invention will be obvious to those skilled in the art. The appended claims and this invention generally should be construed to cover all such obvious forms and modifications which are within the true spirit and scope of the present invention.
Typically, the ZnS ore fed to the smelter had a moisture content of about 10%
as received. Normally, when the ore was sprayed with water to increase the moisture content to about 12.0 wt%, flow and plugging problems were encountered. When the above surfactant blend was foamed onto the ore, moisture contents of from 12.0 to about 14.0 wt% could be processed without significant hopper blockage, transport or plugging problems.
While this invention has been described with respect to particular embodiments thereof, it is apparent that numerous other forms and modifications of this invention will be obvious to those skilled in the art. The appended claims and this invention generally should be construed to cover all such obvious forms and modifications which are within the true spirit and scope of the present invention.
Claims (14)
1. A process for improving recovery of metal values in a smelting operation wherein sulfidic ores are pyrometallurgically reduced, said process comprising applying surfactant and water to said sulfidic ore.
2. A process as recited in claim 1 wherein said surfactant and water are applied to result in a moisture content of said sulfidic ore of about 12% and greater.
3. A process as recited in claim 1 wherein said ore is a ZnS ore.
4. A process as recited in claim 1 wherein said surfactant comprises a member selected from the group consisting of anionic surfactants and non-ionic surfactants and blends thereof.
5. A process as recited in claim 4 wherein said anionic surfactant is a sulfosuccinate or a sulfonate.
6. A process as recited in claim 5 wherein said sulfosuccinate is sodium dioctyl sulfosuccinate.
7. A process as recited in claim 4 wherein said non-ionic surfactant is a diethyleneglycol ether.
8. A process as recited in claim 4 wherein said non-ionic surfactant is an alkoxylated alkyl phenol.
9. A process as recited in claim 4 wherein said non-ionic surfactant is an alkyl phenol.
10. A process as recited in claim 4 wherein said non-ionic surfactant is a block EO-PO polymer.
11. A process as recited in claim 4 wherein said non-ionic surfactant is a glycol ether.
12. A process as recited in claim 4 wherein said surfactant is applied to said sulfidic ore in the form of an aqueous foam in an amount of about 0.01-5.0 pounds of surfactant per ton of said sulfidic ore.
13. A process as recited in claim 12 wherein, after application of said aqueous foam to said sulfidic ore, said sulfidic ore has a moisture content of about 12-14%.
14. A process as recited in claim 12 wherein said foam has an average bubble size of about 200 microns or less and an expansion ratio of between about 10 and about 100.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US11/655,649 | 2007-01-19 | ||
| US11/655,649 US7947327B2 (en) | 2007-01-19 | 2007-01-19 | Method for increasing metal production in smelter operations |
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| Publication Number | Publication Date |
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| CA2579394A1 true CA2579394A1 (en) | 2008-07-19 |
| CA2579394C CA2579394C (en) | 2014-09-16 |
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| CA2579394A Active CA2579394C (en) | 2007-01-19 | 2007-02-22 | Method for increasing metal production in smelter operations |
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| US (1) | US7947327B2 (en) |
| CA (1) | CA2579394C (en) |
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| WO2014134022A1 (en) * | 2013-02-28 | 2014-09-04 | Chemtreat, Inc. | Direct reduction of iron (dri) pellet treatments |
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|---|---|---|---|---|
| US3624019A (en) * | 1970-12-15 | 1971-11-30 | Nalco Chemical Co | Process for rapidly dissolving water-soluble polymers |
| US4088310A (en) * | 1971-09-17 | 1978-05-09 | Outokumpu Oy | Apparatus for suspension smelting of finely-grained oxide and/or sulfide ores and concentrates |
| GB1487411A (en) * | 1974-11-19 | 1977-09-28 | Allied Colloids Ltd | Materials and processes for flotation of mineral substances |
| CA1151430A (en) * | 1980-02-28 | 1983-08-09 | Charles E. O'neill | Reduction smelting process |
| DE3101369A1 (en) * | 1981-01-17 | 1982-08-26 | Klöckner-Humboldt-Deutz AG, 5000 Köln | METHOD AND DEVICE FOR PREVENTING FUSIBLE SUBSTANCES LIKE ORE CONCENTRATE |
| US4427568A (en) * | 1981-04-16 | 1984-01-24 | Betz Laboratories, Inc. | Composition for treating aqueous mediums |
| US4381066A (en) * | 1982-05-10 | 1983-04-26 | Page Edward H | Polymeric foam caulking compositions |
| US4511676A (en) * | 1983-08-08 | 1985-04-16 | Betz Laboratories, Inc. | Method for cleaning organically fouled anion exchange resins using diethylene glycol compound or derivative |
| JPS61217275A (en) * | 1985-03-25 | 1986-09-26 | Alps Electric Co Ltd | Thermal printer |
| US4605568A (en) * | 1985-05-02 | 1986-08-12 | Apollo Technologies Int'l Corp. | Application of foam to improve flow characteristics of water-insoluble products |
| US4751259A (en) * | 1987-08-05 | 1988-06-14 | Nalco Chemical Company | Compositions for iron ore agglomeration |
| US4780233A (en) * | 1987-09-04 | 1988-10-25 | Betz Laboratories, Inc. | Dust suppression methods and compositions |
| US5079036A (en) * | 1990-07-27 | 1992-01-07 | Betz Laboratories, Inc. | Method of inhibiting freezing and improving flow and handleability characteristics of solid, particulate materials |
| US6284077B1 (en) * | 1997-08-29 | 2001-09-04 | Dap Products Inc. | Stable, foamed caulk and sealant compounds and methods of use thereof |
| CA2352624A1 (en) * | 1998-12-21 | 2000-06-29 | The Procter & Gamble Company | Method of using steam ironing of fabrics as a way of causing reduction of physiological and/or subjective reactivity to stress in humans |
| US7097705B2 (en) * | 2000-09-11 | 2006-08-29 | Air Products And Chemicals, Inc. | Cationic-anionic blends for dynamic surface tension reduction |
| US6797180B2 (en) * | 2002-05-01 | 2004-09-28 | Ge Betz, Inc. | Dewatering sand with surfactants |
| AU2002951875A0 (en) * | 2002-10-04 | 2002-10-24 | Applied Australia Pty Ltd | Chemical formulations for treating self-heating metal ores |
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Also Published As
| Publication number | Publication date |
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| US7947327B2 (en) | 2011-05-24 |
| CA2579394C (en) | 2014-09-16 |
| US20080175771A1 (en) | 2008-07-24 |
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