US1783207A - Concentration of ores - Google Patents
Concentration of ores Download PDFInfo
- Publication number
- US1783207A US1783207A US375892A US37589229A US1783207A US 1783207 A US1783207 A US 1783207A US 375892 A US375892 A US 375892A US 37589229 A US37589229 A US 37589229A US 1783207 A US1783207 A US 1783207A
- Authority
- US
- United States
- Prior art keywords
- flotation
- phosphorus
- ores
- pentasulfid
- ore
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- RUFPHBVGCFYCNW-UHFFFAOYSA-N 1-naphthylamine Chemical compound C1=CC=C2C(N)=CC=CC2=C1 RUFPHBVGCFYCNW-UHFFFAOYSA-N 0.000 description 14
- 239000007795 chemical reaction product Substances 0.000 description 12
- 238000005188 flotation Methods 0.000 description 12
- CYQAYERJWZKYML-UHFFFAOYSA-N phosphorus pentasulfide Chemical compound S1P(S2)(=S)SP3(=S)SP1(=S)SP2(=S)S3 CYQAYERJWZKYML-UHFFFAOYSA-N 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 7
- 239000007788 liquid Substances 0.000 description 6
- -1 amino compound Chemical class 0.000 description 5
- 229910052500 inorganic mineral Inorganic materials 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 239000011707 mineral Substances 0.000 description 5
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000003153 chemical reaction reagent Substances 0.000 description 4
- 150000001875 compounds Chemical class 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 description 2
- 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 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 238000009291 froth flotation Methods 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 239000011133 lead Substances 0.000 description 2
- RNVCVTLRINQCPJ-UHFFFAOYSA-N o-toluidine Chemical compound CC1=CC=CC=C1N RNVCVTLRINQCPJ-UHFFFAOYSA-N 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 229910052709 silver Inorganic materials 0.000 description 2
- 239000004332 silver Substances 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 229910052708 sodium Inorganic materials 0.000 description 2
- 150000004992 toluidines Chemical class 0.000 description 2
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- RZVAJINKPMORJF-UHFFFAOYSA-N Acetaminophen Chemical compound CC(=O)NC1=CC=C(O)C=C1 RZVAJINKPMORJF-UHFFFAOYSA-N 0.000 description 1
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 description 1
- 238000003556 assay Methods 0.000 description 1
- 239000010953 base metal Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000008396 flotation agent Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- 239000012263 liquid product Substances 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/014—Organic compounds containing phosphorus
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03D—FLOTATION; DIFFERENTIAL SEDIMENTATION
- B03D2203/00—Specified materials treated by the flotation agents; Specified applications
- B03D2203/02—Ores
- B03D2203/025—Precious metal ores
Definitions
- This invention relates to the concentration of ores by flotation and is particularly applicable to the treatment of'those ores in which the valuable minerals occur entirely or-in a ores, becausejtheytend to reduce silver ex traction if enough sulfidizing agent is added to insure high. recovery of the base metals and a clean concentrate. Also, the consump-' tionof the sulfidizing agent on ores containing very much hydrated iron oxide is very high. Efiorts to float the oxidized minerals without sulfidizing, by using a reagent with a strong collecting action, like oleic acid, re-
- the presentinve-ntion is. based on the discovery that a class of compounds formed by the reaction ⁇ of amino compoundswith phosphorus pentasulfid are effective flotation agents, not only for the sulfid ,.minerals, but also for the oxidized minerals of gold, silver, lead and copper. While all the reconstructed amino compounds tried have shown the ability to float oxidized minerals, I have found the reaction products of phosphorus pentasulfid with aniline, orthotoluidinc and alpha naphthylamine, respectively, to give most 40 satisfactory results. T v
- reaction products of amino compounds with phosphorus pentasulfid are solids.
- flotation operations it is advantageous to have-the reagents in a liquid condition in h order that they may easily and accurately be Application filed July 3,5192%). ,Serial, No. 375,892.
- reaction product of phosphoruspentasulfid with a solution of alpha naphthylamine in ortho, toluidine gives particularly good results on the ore,with which I have been working, 'It may be prepared in the following manner: 7,
- Reagents were added in four stages. Sodium'silicate solution was added to properly condition the pulp and to prevent excess frothing in the later stages? The compound "referred to above acted .both as collecting per ton added at each stage, stage covered a period of five minutes.
- An agent for use in flotation comprising the reaction product of alpha naphthylamine with phosphorus pentasulfid.
- An agent for-use in flotation comprising the reaction product of hosphorus pentasulfid with a solution 0? .alpha naphthylamine in ortho'toluidine.
- An agent for use in flotation compris -i ing the reactionproduct of an oxygen free aromatic amino compound with sulfur and phosphorus.
- An agent for use in flotation comprising v the reaction product of an oxygen free aro-
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
Patented Dec. 2,1930
enonenn. wieron, or Erma; UTAH PATENT OFFI E) concnncrna'rron or onns 80 Drawing.
This invention relates to the concentration of ores by flotation and is particularly applicable to the treatment of'those ores in which the valuable minerals occur entirely or-in a ores, becausejtheytend to reduce silver ex traction if enough sulfidizing agent is added to insure high. recovery of the base metals and a clean concentrate. Also, the consump-' tionof the sulfidizing agent on ores containing very much hydrated iron oxide is very high. Efiorts to float the oxidized minerals without sulfidizing, by using a reagent with a strong collecting action, like oleic acid, re-
' sult inflotation so non-selective that good A extraction and high grade concentrate are impossible to produce simultaneously.
This application is a continuation in part my application, Serial No. 287 ,349, led June 21,1928. 1 a
The presentinve-ntion is. based on the discovery that a class of compounds formed by the reaction} of amino compoundswith phosphorus pentasulfid are effective flotation agents, not only for the sulfid ,.minerals, but also for the oxidized minerals of gold, silver, lead and copper. While all the reconstructed amino compounds tried have shown the ability to float oxidized minerals, I have found the reaction products of phosphorus pentasulfid with aniline, orthotoluidinc and alpha naphthylamine, respectively, to give most 40 satisfactory results. T v
The reaction products of amino compounds with phosphorus pentasulfid are solids. In flotation operations it is advantageous to have-the reagents in a liquid condition in h order that they may easily and accurately be Application filed July 3,5192%). ,Serial, No. 375,892.
of the efiorts to float oxidized ores have in-' added to the flotation pulp. Consequently it becomes desirable to dissolve these solid reaction products in an inert solvent, such as benzol, for example. In some cases it may be preferable to dissolve the amino compound in an inert liquid hydrocarbon before reacting, it with phosphorus pentasulfid. .A liquid product may also be obtained byr acting a large excess of a liquid amino co pound" vwlth phosphorus pentasuliid or by reacting a solution of a' solid amino compound in a liquid amino compound with phosphorus pentasulfid. s p
The reaction product of phosphoruspentasulfid with a solution of alpha naphthylamine in ortho, toluidine gives particularly good results on the ore,with which I have been working, 'It may be prepared in the following manner: 7,
10 grams pulverized phosphorus, pentasulfid was slowly added to a solution of 40 grams alpha naphthylamine in 20 grams ortho toluidine, with constant stirringa Stirring was continued occasionally for one hour, at v the end of which time a brown translucent liquid resulted. The liquid was viscous but not enough so to prevent'satisfactory feeding of such a reagent in mill operations.
To illustrate the action of this compound, I results are iven of a test on oxidized ore from-the ureka Lilly mine. This ore is highly oxidized, containing only 0.2% sulfur. The ore was ground with water in a laboratory ball mill until it passed a 100' mesh screen. The pulp was then placed in a laboratory flotation cell and subjected to flotation operations. i
Reagents were added in four stages. Sodium'silicate solution was added to properly condition the pulp and to prevent excess frothing in the later stages? The compound "referred to above acted .both as collecting per ton added at each stage, stage covered a period of five minutes.
. Recc nstrucfied Sodium a apap BM time? dine.
matic amino compound with phosphorus pentasulfid.
8. An agent for use in flotation comprising the reaction product of alpha naphthylamine with phosphorus pentasulfid.
9; An agent for-use in flotation comprising the reaction product of hosphorus pentasulfid with a solution 0? .alpha naphthylamine in ortho'toluidine.
In testimony whereof, I have signed my name to this specification this 27th day of June, 1929.
GEORGE H. WIGTON.
The results of the testwere as follows:
LPer cent l p Assay recoveries cent wt. y A u Ag Pb Ins- Au Ag Pb Ore 100.00 .217 3.22 13.50 69.4 Concentrate-.- 27.64 .42 8.0 41.5 32.4 53.38 6863 84.96 Tailing 72.36 ..14 L4 2.8 46.62 31.37 15.04
It will be understood that the foregoing is only a single example of procedure, and I do not wish the invention to be limited to this specific agent or method; Q a
I claim:
1. The process of concentrating ores by froth iflotation which comprises subjecting the ore in the form of a pulp to. a flotation operation in the presence of the react-ion product of an oxygen free aromatic amino flotation operation in the presence of the reaction product of alpha naphthylamine and phosphorus pentasulfid.
4. The process of concentrating oxidized ores by froth flotation which comprises subr I v jecting the ore in the form of a pulp to a flotationvoperation in the presence of the reaction product of phosphorus pentasulfid with a solution of'alpha naphthylamine in ortho tolui-dine. I
v 5. The process of concentrating oxidized ores by froth flotation which comprises subjecting the ore in the form of a pulp to a flotation operation in the presence ofv the reaction product of an oxygen free aromatic amino. compound with sulfur and phosphorus.
6. An agent for use in flotation compris -i ing the reactionproduct of an oxygen free aromatic amino compound with sulfur and phosphorus.
7. An agent for use in flotation comprising v the reaction product of an oxygen free aro-
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US375892A US1783207A (en) | 1929-07-03 | 1929-07-03 | Concentration of ores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US375892A US1783207A (en) | 1929-07-03 | 1929-07-03 | Concentration of ores |
Publications (1)
Publication Number | Publication Date |
---|---|
US1783207A true US1783207A (en) | 1930-12-02 |
Family
ID=23482796
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US375892A Expired - Lifetime US1783207A (en) | 1929-07-03 | 1929-07-03 | Concentration of ores |
Country Status (1)
Country | Link |
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US (1) | US1783207A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4540484A (en) * | 1977-12-15 | 1985-09-10 | Mccarthy James R | Method and apparatus for separating selected particulate materials from a mixture of liquids and solids |
US20050263442A1 (en) * | 2002-08-03 | 2005-12-01 | Tobias Rau | Collecting agent for sulphidic ores, the production and use thereof |
-
1929
- 1929-07-03 US US375892A patent/US1783207A/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4540484A (en) * | 1977-12-15 | 1985-09-10 | Mccarthy James R | Method and apparatus for separating selected particulate materials from a mixture of liquids and solids |
US20050263442A1 (en) * | 2002-08-03 | 2005-12-01 | Tobias Rau | Collecting agent for sulphidic ores, the production and use thereof |
US7104404B2 (en) * | 2002-08-03 | 2006-09-12 | Clariant Gmbh | Collecting agent for sulphidic ores, the production and use thereof |
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