[go: up one dir, main page]

US1997280A - Flotation of oxides - Google Patents

Flotation of oxides Download PDF

Info

Publication number
US1997280A
US1997280A US385472A US38547229A US1997280A US 1997280 A US1997280 A US 1997280A US 385472 A US385472 A US 385472A US 38547229 A US38547229 A US 38547229A US 1997280 A US1997280 A US 1997280A
Authority
US
United States
Prior art keywords
flotation
ore
reagent
oxidized
copper
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
Application number
US385472A
Inventor
Ludwig J Christmann
Stuart A Falconer
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wyeth Holdings LLC
Original Assignee
American Cyanamid Co
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by American Cyanamid Co filed Critical American Cyanamid Co
Priority to US385472A priority Critical patent/US1997280A/en
Application granted granted Critical
Publication of US1997280A publication Critical patent/US1997280A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D1/00Flotation
    • B03D1/001Flotation agents
    • B03D1/004Organic compounds
    • B03D1/014Organic compounds containing phosphorus
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B03SEPARATION 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
    • B03DFLOTATION; DIFFERENTIAL SEDIMENTATION
    • B03D2203/00Specified materials treated by the flotation agents; Specified applications
    • B03D2203/02Ores
    • B03D2203/04Non-sulfide ores
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S209/00Classifying, separating, and assorting solids
    • Y10S209/901Froth flotation; copper

Definitions

  • This invention relates to a process of recovering oxide ores as distinguished from those of the sulphide type by subjecting the same to a flotation operation.
  • oxide it is intended to designate ore comprising substantially non-sulphide compounds. While, of course, some oxide or oxidized ores contain as much as 5% sulphide, yet as far as this discovery and invention is concerned, such sulphide is present only incidentally, and though a part of the metals present as such may be recovered, yet it is primarily intended to float the oxides and particularly the definite chemical compounds such as oxides and carbonates of the heavy metals.
  • an ore comprising a copper carbonate such as malachite was ground to less than 200 mesh, and a sample thereof was subjected to a flotation operation with the following reagents in a mechanically agitated flotation machine:
  • Reagent A comprises the sodium salt of dicresyl dithiophosphoric acid.
  • Reagent B comprises di-isopropyl dithiophosphoric acid.
  • Reagent C comprises di-amyl dithiophosphoric acid.
  • a float was conducted using reagent C as being another substituted dithiophosphoric acid to the extent of 6.04 lbs. per ton with the result that 70.0% of the copper was floated.
  • the oxidized lead ores were also found to be amenable to the dithiophosphoric acids, as when a float was conducted using the lead carbonate cerussite, 1.44 lbs. of reagent A per ton floated 97.4% of the lead. 4
  • a method of ore flotation which includes the step of subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth 55 flotation operation in the presence of a dithiophosphate.
  • a method of ore flotation which includes the step of subjecting an oxidized ore to a froth flotation operation in the presence of a di-substitut'ed dithiophosphate.
  • a method of ore flotation which includes the step of subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth flotation operation in the presence of a salt of a substituted dithiophosphoric acid.
  • a method of ore flotation which includes the step of subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth flotation operation in the presence of a sodium salt of dicresyl dithiophosphoric acid.
  • a method of floating oxidized copper ores which consists in subjecting the same to a froth flotation operation in the presence of a di-substituted dithiophosphate.
  • a method of floating oxidized lead, ores which consists in subjecting the same to a flotation operation in the presence of a di-substituted dithiophosphate.
  • a method of ore flotation which comprises subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth flotation operation in the presence of a diaryl substituted dithiophosphate.
  • a method of ore flotation which includes the step of subjecting an oxidized copper ore to a froth flotation operation in the presence of a material havingthe probable formula:
  • R and R1 represent aryl or alkyl groups and X represents analkali metal group.

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Description

Patented Apr. 9, 1935 UNITED STATES FLOTATION OF OXIDES Ludwig J. Christmann,
A. Falconer, Elizabeth, N. J.,
American Cyanamid Jersey City, and Stuart assignors to Company, New York,
N. Y., a corporation of Maine No Drawing.' Application August 12, 1929,
Serial No. 385,472
8 Claims.
This invention relates to a process of recovering oxide ores as distinguished from those of the sulphide type by subjecting the same to a flotation operation.
Throughout this specification where the word oxide is used, it is intended to designate ore comprising substantially non-sulphide compounds. While, of course, some oxide or oxidized ores contain as much as 5% sulphide, yet as far as this discovery and invention is concerned, such sulphide is present only incidentally, and though a part of the metals present as such may be recovered, yet it is primarily intended to float the oxides and particularly the definite chemical compounds such as oxides and carbonates of the heavy metals.
Heretofore it has been a very common practice in the treatment of oxidized ores to first sulphidize the same in order to convert the non-sulphide compounds to sulphides to make them amenable to the flotation reagents, but this invention and discovery does not find such a procedure necessary as the oxides may be floated directly by the process hereinafter set forth.
Certain reagents specified in this application are well known in the recovery of sulphides, but it does not necessarily follow, and as a matter of fact, there is no theory of reasoning by which one would conclude that a sulphide flotation reagent may be efficiently used for the recovery of oxides. Actual flotation experience heretofore has distinctly shown the reverse to be true. According to prior practice in sulphide flotation, either the values present as non-sulphides were lost or they were given a preliminary treatment to convert them to a sulphide form. As an alternative, they were frequently given further and different treatment to recover them as such.
We have discovered that the substituted dithiophosphoric acids and their salts are particularly efficient as flotation reagents in the recovery of oxide minerals.
As demonstrating the invention, an ore comprising a copper carbonate such as malachite was ground to less than 200 mesh, and a sample thereof was subjected to a flotation operation with the following reagents in a mechanically agitated flotation machine:
Reagent A comprises the sodium salt of dicresyl dithiophosphoric acid.
Reagent B comprises di-isopropyl dithiophosphoric acid.
Reagent C comprises di-amyl dithiophosphoric acid.
Using 2.72 lbs. of reagent A per ton of ore with a 50 gram sample of malachite, a froth floated 74.8% of the copper. In this operation a very voluminous froth was obtained. Under the same conditions but using only 1.36 lb. per ton of reagent A only 30.8% of the copper was floated.
A further float was conducted with reagent A and as high as 93.6% of the copper was floated where 7.04 lbs. per ton of the reagent was used.
Using the same ore and reagent B to the extent of 3.84 lbs. per ton recovered 53.6% of the copper. m In this experiment no separate frother was used. When the same proportion of reagent B was used in connection with 0.54 lb. of pine oil per ton, a copper recovery of 87.0% was had. The same amount of pine oil used in connection with 15 5.76 lbs. per ton of reagent B floated 88.6% of the copper.
A float was conducted using reagent C as being another substituted dithiophosphoric acid to the extent of 6.04 lbs. per ton with the result that 70.0% of the copper was floated.
The above tests would appear to indicate that the dithiophosphoric acids were particularly applicable to the flotation of oxidized ores and specifically to that form of oxidized copper ore existing as malachite.
As a check on the amenability of oxidized ore to these reagents, a float was conducted using cuprite as the mineral, preliminarily treated as in the case of malachite, and 5.76 lbs. per ton of reagent A. This gave a recovery of 91.0% of the copper.
- A further experiment was conducted using azurite as the mineral, and 2.88 lbs. per ton of reagent A floated 94.5% of the copper.
The oxidized lead ores were also found to be amenable to the dithiophosphoric acids, as when a float was conducted using the lead carbonate cerussite, 1.44 lbs. of reagent A per ton floated 97.4% of the lead. 4
It is to be clearly understood that the results here set forth are merely indicative as to the types of reagents found eflicient in the flotation of oxidized ores. Obviously, the amounts of reagents used are not considered absolutely necessary and we therefore do not wish to be limited to the proportions indicated, as the discovery lies principally in the fact that certain reagents may be used with exceptional advantage in flotation processes for the recovery of heavy metals from non-sulphide or oxidized ores.
What We claim is:
1. A method of ore flotation which includes the step of subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth 55 flotation operation in the presence of a dithiophosphate.
2. A method of ore flotation which includes the step of subjecting an oxidized ore to a froth flotation operation in the presence of a di-substitut'ed dithiophosphate.
3. A method of ore flotation which includes the step of subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth flotation operation in the presence of a salt of a substituted dithiophosphoric acid.
4. A method of ore flotation which includes the step of subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth flotation operation in the presence of a sodium salt of dicresyl dithiophosphoric acid.
5. A method of floating oxidized copper ores which consists in subjecting the same to a froth flotation operation in the presence of a di-substituted dithiophosphate.
6. A method of floating oxidized lead, ores which consists in subjecting the same to a flotation operation in the presence of a di-substituted dithiophosphate.
'7. A method of ore flotation which comprises subjecting an oxidized ore containing oxides or carbonates of heavy metals to a froth flotation operation in the presence of a diaryl substituted dithiophosphate.
8. A method of ore flotation which includes the step of subjecting an oxidized copper ore to a froth flotation operation in the presence of a material havingthe probable formula:
where R and R1 represent aryl or alkyl groups and X represents analkali metal group.
LUDWIG J. CHRISTMANN; STUART A. FALCONER.
US385472A 1929-08-12 1929-08-12 Flotation of oxides Expired - Lifetime US1997280A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US385472A US1997280A (en) 1929-08-12 1929-08-12 Flotation of oxides

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US385472A US1997280A (en) 1929-08-12 1929-08-12 Flotation of oxides

Publications (1)

Publication Number Publication Date
US1997280A true US1997280A (en) 1935-04-09

Family

ID=23521508

Family Applications (1)

Application Number Title Priority Date Filing Date
US385472A Expired - Lifetime US1997280A (en) 1929-08-12 1929-08-12 Flotation of oxides

Country Status (1)

Country Link
US (1) US1997280A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4530758A (en) * 1982-05-17 1985-07-23 Thiotech, Inc. Ore flotation method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4530758A (en) * 1982-05-17 1985-07-23 Thiotech, Inc. Ore flotation method

Similar Documents

Publication Publication Date Title
US3438494A (en) Flotation method for the recovery of minerals
US2492936A (en) Differential froth flotation of sulfide ores
CA2075155C (en) Process for improved precious metals recovery from ores with the use of alkylhydroxamate collectors
US2074699A (en) Flotation process
US2327408A (en) Flotation
US3164549A (en) Flotation separation of phosphate ores
US1997280A (en) Flotation of oxides
US3037627A (en) Method of beneficiating sulfide and oxide ores of copper, manganese, lead and zinc
US2380698A (en) Beneficiation of acidic minerals
US3788467A (en) Flotation process for recovering molybdenum
US1801318A (en) Concentration of ores
US2316743A (en) Flotation of molybdenite
US2501269A (en) Froth flotation of sulfide ores
US1952907A (en) Method of flotation of oxidized ores
US1788331A (en) Concentration process for flotable substances as ores, coals, graphite, and the like
SU833326A1 (en) Collector for sulfide ore flotation
US3329266A (en) Flotation process involving depression of sulfide minerals previously activated
US1825501A (en) Method of floating ores
US1801319A (en) Flotation of minerals
US3834533A (en) Concentration of oxide copper ores by flotation separation
US2278020A (en) Process of separating chalcocite ore
US1972588A (en) Froth-flotation process
US2450720A (en) Froth flotation of silicious gangue from an alkaline magnetic iron ore pulp with an amine
US2287274A (en) Process of separating lead and zinc sulphides
US1839155A (en) Process of concentrating ores by flotation