US1364859A - Flotation of minerals - Google Patents
Flotation of minerals Download PDFInfo
- Publication number
- US1364859A US1364859A US395998A US39599820A US1364859A US 1364859 A US1364859 A US 1364859A US 395998 A US395998 A US 395998A US 39599820 A US39599820 A US 39599820A US 1364859 A US1364859 A US 1364859A
- Authority
- US
- United States
- Prior art keywords
- flotation
- frothing
- agent
- ore
- small amount
- 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
- 238000005188 flotation Methods 0.000 title description 28
- 229910052500 inorganic mineral Inorganic materials 0.000 title description 14
- 239000011707 mineral Substances 0.000 title description 14
- 239000003795 chemical substances by application Substances 0.000 description 35
- 235000010755 mineral Nutrition 0.000 description 13
- 238000000034 method Methods 0.000 description 11
- 239000000203 mixture Substances 0.000 description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 8
- FCSHMCFRCYZTRQ-UHFFFAOYSA-N N,N'-diphenylthiourea Chemical compound C=1C=CC=CC=1NC(=S)NC1=CC=CC=C1 FCSHMCFRCYZTRQ-UHFFFAOYSA-N 0.000 description 8
- 229910052802 copper Inorganic materials 0.000 description 8
- 239000010949 copper Substances 0.000 description 8
- PFRUBEOIWWEFOL-UHFFFAOYSA-N [N].[S] Chemical class [N].[S] PFRUBEOIWWEFOL-UHFFFAOYSA-N 0.000 description 7
- 239000003513 alkali Substances 0.000 description 7
- 238000011084 recovery Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 3
- 239000008396 flotation agent Substances 0.000 description 3
- -1 thiocarbanilid Chemical class 0.000 description 3
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 230000000051 modifying effect Effects 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000010665 pine oil Substances 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- 150000003585 thioureas Chemical class 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 241001092591 Flota Species 0.000 description 1
- 241001397173 Kali <angiosperm> Species 0.000 description 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- WUOACPNHFRMFPN-UHFFFAOYSA-N alpha-terpineol Chemical compound CC1=CCC(C(C)(C)O)CC1 WUOACPNHFRMFPN-UHFFFAOYSA-N 0.000 description 1
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 1
- 239000003518 caustics Substances 0.000 description 1
- 229910052947 chalcocite Inorganic materials 0.000 description 1
- DVRDHUBQLOKMHZ-UHFFFAOYSA-N chalcopyrite Chemical compound [S-2].[S-2].[Fe+2].[Cu+2] DVRDHUBQLOKMHZ-UHFFFAOYSA-N 0.000 description 1
- 229910052951 chalcopyrite Inorganic materials 0.000 description 1
- SQIFACVGCPWBQZ-UHFFFAOYSA-N delta-terpineol Natural products CC(C)(O)C1CCC(=C)CC1 SQIFACVGCPWBQZ-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 159000000011 group IA salts Chemical class 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 125000000449 nitro group Chemical group [O-][N+](*)=O 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 125000000446 sulfanediyl group Chemical group *S* 0.000 description 1
- 229940116411 terpineol Drugs 0.000 description 1
- 239000002023 wood Substances 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
- B03D1/012—Organic compounds containing sulfur
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/02—Collectors
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/04—Frothers
-
- 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
-
- 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
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S209/00—Classifying, separating, and assorting solids
- Y10S209/901—Froth flotation; copper
Definitions
- This invention relates to the concentration of minerals, such as sulfid ores and the like, by flotation.
- Thiocarbanilid, and other organic thio-urea compounds are non-oleaginous compounds which themselves have substantially no frothing properties, but which have valuable properties as selective or collecting or mineral-modifying agents. Such agents, although substantially non-frothing, neverthelessmaterially assist in the recovery of the minerals when used in connection with a suitable frothing agent.
- the substantially non-frothing nitrogen-sulfur compounds such as thiocarbanilid, etc.
- the collecting and frothing agents are successively incorporated with the ore pulp.
- the non-frothing collecting agent s incorporated with the ore in the tubemill or ball mill during the'grinding operation, and the frothing agent is of such a character that it can be subsequently incorporated, prior to or during the flotation operation.
- thiocarbanilid, etc. has substantially no frothing properties, but has valuable selective or collecting or mineral-modifying properties, and very materially assists in the recovery of the minerals when used in connec tion with a suitable frothingagent.
- the action of such agent appears to be a selective modifying action upon the mineral surface, rather than any action of importance upon the water itself, any modifying effect upon the water apparently being incidental and insufiicient to effect any frothing thereof.
- the collecting agents are substantially non-frothing, it is important to supplement their action byan agent which will provide an appropriate amount of froth, but the frothing agent used may be entirely inadequate to perform the flotation process by itself, inasmuch as its function appears to be merely to provide bubbles in sufficient quantity and of suflicient persistency to overflow into the launder of the flotation machine, thereby mechanically facilitating the removal of the mineral concentrate.
- the frothing agent may, however, have selective or collecting properties, as well as frothing properties.
- the frothing agent is, ac cording to the present invention, added at some time subsequent to the incorporation of the collecting agent. It may thus be added in the launder leading to the flotation cell, or even in the cell itself.
- Theflotation operation can be carried out in the'common forms of flotation. apparatus, such as an ordinary Callow cell, or appare tus where the air is incorporated in the ore.
- alkali may be caustic alkali, such as sodium hydrate, or an alkaline salt, such as sodium carbonate, or even lime or calcium oxid or hydrate can be user.
- nitrogen-sulfur compounds such as other thio-ureas
- other frothing agents or agents which may be both frothing and collecting agents, such as pine oil, etc.
- the nitrogen-sulfur compound can thus be used in conjunction with many. of the usual oil mixtures which are commonly employed in flotation, particularly those which are good frothing agents, such as pine oil and other wood distillation oils, inasmuch as they supplement the action of the collecting agent and are themselves supplemented in their ore floating properties by the. collecting or selective action of the collecting agents.
- the addition of the flotationagents successively has the advantage that the grinding of the ore pulp and the preliminary incorporation of the substantially non-frothing collecting agent can be effected without any objectionable froth formation, and the ore pulp can thus be kept free from objec-' tionable froth formation until the frothing agent is added, which addition may take place during or immediately preceding the flotation operation.
- the method of effecting the concentration of. minerals by flotation which comprises grinding the ore with the addition thereto of a small amount of a substantially non-frotliing, non-oleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding a'small amount of an agent having good frothing qualities, and subjecting the resulting mixture to a flotation operation; substantially as described.
- the method ofefl'ecting the concentration of copper ores by flotation which comprises intimately incorporating with the ore pulp asmall amount of alkali and a small amount of a substantially non-frothing, nonoleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding an agent having good frothing qualities, and subjecting the resulting mixture to a floatation operation; substantially as described.
- the method of effecting the concentration of copper ores by flotation which comprises grinding the ore in admixture with a small amount of alkali and a small amount of substantially non-frothing, non-oleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding a small amount of an agent having good frothing properties, and subjecting the resulting mixture to a flotation operation; substantially as described.
- the method of effecting the concentration of minerals by flotation which comprises adding to the mineral pulp a small amount of thiocarbanilid, subsequently adding an agent having good frothing properties, and subjecting the resulting mixture to a flotation operation; substantially as described.
- the method of effecting the concentration .of minerals by flotation which comprises grinding the ore with the addition thereto of a small amount of thio'carbanilid, subsequently adding a small amount of an agent having good frothing qualities, and subjecting the resulting mixture to a flotation operation; substantially as described.
Landscapes
- Paper (AREA)
Description
CLEMENT L. PERKINS AND RALPH E- SAYRE, 0F PITTSBURGH, PENNSYLVANIA,
ASSIQNQRS T0 METALS RECOVERY CQMPANY, OF NEW YORK, N. Y., A CORPO- FLOTA'IION 0F MINERALS.
increase.
No Drawing.
To all whom it may concern Be known that we, CLEMENT L. PERKINS and RALPH E. SAYRE, citizens of the United States, residing at Pittsburgh, Allegheny county, State of Pennsylvania, have invented certain new and useful Improvements in Flotation of Minerals; and we do hereby de-.
clare the following to be a full, clear, and exact description of the invention, suchas will enable others skilled in the art to which it appertains to make and use the same.
This invention relates to the concentration of minerals, such as sulfid ores and the like, by flotation.
In our prior applications I Serial hlo. 337,822, filed November 11, 1919, and Serial No. 284,981, filed March 25, 1919, we have described and claimed certain improvements in the flotation of minerals with the aid of nitro en-sulfur compounds, 6. 9., thio-amido and fhiomrea compounds. In the specific claims of said applications we have claimed a process in which mixtures of different agents are added simultaneously as flotation agents. The claims of the present application relate to an alternative and specifically different procedure in which the flotation agents are added in successive operations, instead of simultaneously.
Thiocarbanilid, and other organic thio-urea compounds are non-oleaginous compounds which themselves have substantially no frothing properties, but which have valuable properties as selective or collecting or mineral-modifying agents. Such agents, although substantially non-frothing, neverthelessmaterially assist in the recovery of the minerals when used in connection with a suitable frothing agent.
According to the present invention the substantially non-frothing nitrogen-sulfur compounds, such as thiocarbanilid, etc, are
used in conjunction with a frothing agent, and the collecting and frothing agents are successively incorporated with the ore pulp. In the preferred embodimentof the invention, the non-frothing collecting agent s incorporated with the ore in the tubemill or ball mill during the'grinding operation, and the frothing agent is of such a character that it can be subsequently incorporated, prior to or during the flotation operation.
Specification of Letters Patent.
Patented Jan. 4t, 1921.
Application filed July 13, 1920. SerieLNo. 395,998;
As pointed out in said prior applications, thiocarbanilid, etc., has substantially no frothing properties, but has valuable selective or collecting or mineral-modifying properties, and very materially assists in the recovery of the minerals when used in connec tion with a suitable frothingagent. The action of such agent appears to be a selective modifying action upon the mineral surface, rather than any action of importance upon the water itself, any modifying effect upon the water apparently being incidental and insufiicient to effect any frothing thereof.
Inasmuch as the collecting agents are substantially non-frothing, it is important to supplement their action byan agent which will provide an appropriate amount of froth, but the frothing agent used may be entirely inadequate to perform the flotation process by itself, inasmuch as its function appears to be merely to provide bubbles in sufficient quantity and of suflicient persistency to overflow into the launder of the flotation machine, thereby mechanically facilitating the removal of the mineral concentrate. The frothing agent, may, however, have selective or collecting properties, as well as frothing properties. The frothing agent is, ac cording to the present invention, added at some time subsequent to the incorporation of the collecting agent. It may thus be added in the launder leading to the flotation cell, or even in the cell itself.
Theflotation operation can be carried out in the'common forms of flotation. apparatus, such as an ordinary Callow cell, or appare tus where the air is incorporated in the ore.
pulp by mechanical agitation.
It is of advantage in many cases to add to the ore pulp a small amount of alkali, which may be suflicient in amount to give to the ore pulp a distinct alkaline reaction. kalis are used, it is desirable to give them an appreciable time of contact with the ore pulp before subjecting the latter to flotation. When possible, it appears preferable to add the alkalis in the grinding mill, so that they will be present during the grinding operation. The alkali may be caustic alkali, such as sodium hydrate, or an alkaline salt, such as sodium carbonate, or even lime or calcium oxid or hydrate can be user.
When al- 1 by the following specific examples of tests made upon a copper sulfidore having a silicious gangue containing its floatable or sulfld copper in the form of amixture of chalcocite and chalcopyrite, that is, so-called porphyry ores, such as those of the Utah Copper Com pany. In general, treatment of the ore with alkalis, as above noted, gives improved results, the alkalis themselves apparentlyhaving a valuable effect upon the ores in improving the flotation thereof.
500 parts by weight of the Utah Copper Companys ore was ground in a pebble mill with 250 parts of water, sodium hydroxid equivalent to two pounds per ton of dry ore, and thiocarbanilid equivalent to one-fifth pound per ton of dry ore. The ground pulp was then transferred to a Callow rougher cell, diluted with water, and floated with the addition of terpineol equivalent to about one-tenth pound per ton of dry ore. A satisfactory concentrate and high recovery were obtained.
Instead of thiocarbanilid, other substantially non-frothing nitrogen-sulfur compounds, such as other thio-ureas, can be similarly used, and also other frothing agents, or agents which may be both frothing and collecting agents, such as pine oil, etc. The nitrogen-sulfur compound can thus be used in conjunction with many. of the usual oil mixtures which are commonly employed in flotation, particularly those which are good frothing agents, such as pine oil and other wood distillation oils, inasmuch as they supplement the action of the collecting agent and are themselves supplemented in their ore floating properties by the. collecting or selective action of the collecting agents.
It is characteristic of the invention that the froth obtained is readily broken up, while a relatively clean concentrate and high recovery can nevertheless be obtained.
The addition of the flotationagents successively has the advantage that the grinding of the ore pulp and the preliminary incorporation of the substantially non-frothing collecting agent can be effected without any objectionable froth formation, and the ore pulp can thus be kept free from objec-' tionable froth formation until the frothing agent is added, which addition may take place during or immediately preceding the flotation operation.
We claim:
1. The method of effecting the concentration of m nerals by flotation, which com prises adding to the mineral pulp a small amount of a substantially non-frothing, nonoleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding an agent having-good frothing properties, andsubjecting the resulting mixture to a flotation operation; substantially as described.
2. The method of effecting the concentration of. minerals by flotation, which comprises grinding the ore with the addition thereto of a small amount of a substantially non-frotliing, non-oleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding a'small amount of an agent having good frothing qualities, and subjecting the resulting mixture to a flotation operation; substantially as described.
3. The method ofefl'ecting the concentration of copper ores by flotation, which comprises intimately incorporating with the ore pulp asmall amount of alkali and a small amount of a substantially non-frothing, nonoleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding an agent having good frothing qualities, and subjecting the resulting mixture to a floatation operation; substantially as described.
4. The method of effecting the concentration of copper ores by flotation, which comprises grinding the ore in admixture with a small amount of alkali and a small amount of substantially non-frothing, non-oleaginous organic nitrogen-sulfur compound as collecting agent, subsequently adding a small amount of an agent having good frothing properties, and subjecting the resulting mixture to a flotation operation; substantially as described.
The method of effecting the concentration of minerals by flotation, which comprises adding to the mineral pulp a small amount of thiocarbanilid, subsequently adding an agent having good frothing properties, and subjecting the resulting mixture to a flotation operation; substantially as described.
6. The method of effecting the concentration .of minerals by flotation, which comprises grinding the ore with the addition thereto of a small amount of thio'carbanilid, subsequently adding a small amount of an agent having good frothing qualities, and subjecting the resulting mixture to a flotation operation; substantially as described.
7 The method of effecting the concentration of copper ores by flotation, which comprises intimately incorporating with the ore pulp a small amount of alkali and a small amount of thiocarbanilid, subsequently adding an agent having good frothing qualities, and subjecting the resulting mixture to a flotation operation; substantially as described.
8. The method of eii'ecting the concentra .tion of. copper ores-by flotation, which commixture to a flotation operation; substanprises grinding the ore in admixture with tially as described.
a small amount of alkali and a small amount In testimony whereof We aflix our signaof thiocarbanilid, subsequently adding a tures. 5 small amount of an agent having good froth- CLEMENT L. PERKINS. ing properties, and subjecting the resulting- RALPH E. SAYRE.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US395998A US1364859A (en) | 1920-07-13 | 1920-07-13 | Flotation of minerals |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US395998A US1364859A (en) | 1920-07-13 | 1920-07-13 | Flotation of minerals |
Publications (1)
Publication Number | Publication Date |
---|---|
US1364859A true US1364859A (en) | 1921-01-04 |
Family
ID=23565425
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US395998A Expired - Lifetime US1364859A (en) | 1920-07-13 | 1920-07-13 | Flotation of minerals |
Country Status (1)
Country | Link |
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US (1) | US1364859A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2628716A (en) * | 1946-03-15 | 1953-02-17 | Koppers Co Inc | Flotation process |
-
1920
- 1920-07-13 US US395998A patent/US1364859A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2628716A (en) * | 1946-03-15 | 1953-02-17 | Koppers Co Inc | Flotation process |
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