[go: up one dir, main page]

US1659396A - Process of concentrating ores and minerals by flotation - Google Patents

Process of concentrating ores and minerals by flotation Download PDF

Info

Publication number
US1659396A
US1659396A US144193A US14419326A US1659396A US 1659396 A US1659396 A US 1659396A US 144193 A US144193 A US 144193A US 14419326 A US14419326 A US 14419326A US 1659396 A US1659396 A US 1659396A
Authority
US
United States
Prior art keywords
flotation
minerals
trithio
ores
carbonate
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
US144193A
Inventor
William A Douglass
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.)
EIDP Inc
Original Assignee
EI Du Pont de Nemours and 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 EI Du Pont de Nemours and Co filed Critical EI Du Pont de Nemours and Co
Priority to US144193A priority Critical patent/US1659396A/en
Application granted granted Critical
Publication of US1659396A publication Critical patent/US1659396A/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
    • B03D1/012Organic compounds containing sulfur
    • 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
    • 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 the recovery of valuable ores and minerals by flotation, and comprises more particularly the concentration of such ores and minerals by means of a certain class of organic flotation agents.
  • R and R are orgamc groups.
  • R and B may represent the same or different organic groups.
  • a specific example of a derivative in which R and R are alkyl groups is diethyl ester of trithio carbonic acid having the following formula:
  • SCHgCOO 02115 is an example of a derivative in which R and R are acyl groups. Diethyl thiol ester Application filed October 25, 1926. Serial No. 144,193.
  • diethyl trithio carbonate can be made by dissolving 150 grams of potassium hydroxide in 250 cc. water, and saturating this solution with hydrogen sulfide. To this solution is added 150 grams of potasslum hydroxideand, when all is dissolved. 250 grams of carbon bisulfide are added and the mixture agitated vigorously until all of the carbon disulfide goes into solution. The solution is washed once with 300 cc. of alcohol.
  • This compound may loo-used as a flotation reagent in the following manner: 500 grams of minus 29 mesh Phelps-Dodge Corporation Copper Queen ore are ground for 20 minutes in a pebble mill with 500 cc. of water, 0.6 grams of lime and 0.025 grams of diethyl trithio carbonate. The lime and diethyl trithio carbonate are in the proportions of 2,4 lbs. and 0.10 lb. respectively per ton of ore.
  • the pulp from the pebble mill is transferred to a J anney laboratory flotation machine and a frothing agent (terpineol or pine oil) added. The pulp is diluted to about two liters and a rougher concentrate removed for 10 minutes, water being added as needed. The following results were obtained:
  • the flotation reagents forming part of the present invention do not decompose in an acid solution, and are therefore suitable for use in acid flotation circuits. .
  • diethyl trithio carbonate in the proportion of 0.15 lbs. per ton of ore in a circuit containing 7.0 lbs. of sulfuric acid per ton of ore, the following results were obtained:
  • Dibenzoyl trithio carbonate can be made conveniently by treating potassium trithio carbonate in benzene suspension with benzoyl chloride, removing the heat of reaction by cooling. After filtration from the potassium chloride and evaporation of the solvent, dibenzoyl trithio carbonate is obtained as a yellowish orange oil.
  • Diethyl thiol ester of thioncarbonyl disulfide may be made by treating the mono ethyl ester of trithio carbonic acid (Chancelpreferably bericht fiir Chemie 1851, p. 513) with iodine. The orange brown oil which is formed, is washed with water and then dried with calcium chloride.
  • the present process is not limit- 7 ed to the specific substances or details of procedure mentioned, but includes generally processes of recovering values from ores by flotation in which the flotation agents are members of the class of compounds described. For instance, it has been pointed out as being desirable to add a frothing agent in the specific examples noted. However, where the flotation agent itself has sutficient frothing power, the frothing agent may be omitted.
  • R and R are organic groups.

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Description

Patented Feb. 14, 1928.
UNITED STATES PATENT OFFICE;
WILLIAM A. DOUGLASS, OF PENNS GROVE, NEW JERSEY, ASSIGNOR TO E. I. DU IONl- DE NEMOURS & COMPANY, OF WILMINGTON, DELAWARE, A CORPORATION OF DEL- AWARE.
PROCESS OIE GONCENTRATING ORES AND MINERALS BY FLOTA'IION.
N Drawing.
This invention relates to the recovery of valuable ores and minerals by flotation, and comprises more particularly the concentration of such ores and minerals by means of a certain class of organic flotation agents.
It is one of the objects of the present invention to carry out flotation processes in an eficient manner by using as the flotation agent one of a class of organic compounds having highly selective properties when so used. It is-a further object to carry out the flotation processes by using flotation agents which are suitable for use in neutral, alkaline or acid flotation circuits without decoinplosition of the flotation agents.
ave discovered that these and other ob jects may be accomplished by using in a flotation process organic derivatives of trithio carbonic acid as the flotation agents. These compounds are characterized by having the following general structural formula:
where R and R are orgamc groups. R and B may represent the same or different organic groups.
A specific example of a derivative in which R and R are alkyl groups is diethyl ester of trithio carbonic acid having the following formula:
' s,-o,n
SCaHt somooocm.
Dibenzoyl trithio carbonate having the formula:
SCHgCOO 02115 is an example of a derivative in which R and R are acyl groups. Diethyl thiol ester Application filed October 25, 1926. Serial No. 144,193.
of thion carbonyl disulfide having the following formula:
S=(l]-SOgH5 18 still another type of derivative of trithio carbonate, wherein Ris an alkyl group and R is another trithio carbonate group having the following formula:
S- SJ in which X represents an organic group such as an alkyl.
The various derivatives of trithio carbonic acid may be made in any suitable manner. For instance, diethyl trithio carbonate can be made by dissolving 150 grams of potassium hydroxide in 250 cc. water, and saturating this solution with hydrogen sulfide. To this solution is added 150 grams of potasslum hydroxideand, when all is dissolved. 250 grams of carbon bisulfide are added and the mixture agitated vigorously until all of the carbon disulfide goes into solution. The solution is washed once with 300 cc. of alcohol. To the water layer containing potassium trithio carbonate, 300 grams of ethyl bromide are slowly added with agitation and coolin The reaction product is washed with water and the excess ethyl bromide removed by bubbling a current of air through the liquid. The resulting orange red liquid is pure diethyl trithio carbonate.
This compound may loo-used as a flotation reagent in the following manner: 500 grams of minus 29 mesh Phelps-Dodge Corporation Copper Queen ore are ground for 20 minutes in a pebble mill with 500 cc. of water, 0.6 grams of lime and 0.025 grams of diethyl trithio carbonate. The lime and diethyl trithio carbonate are in the proportions of 2,4 lbs. and 0.10 lb. respectively per ton of ore. The pulp from the pebble mill is transferred to a J anney laboratory flotation machine and a frothing agent (terpineol or pine oil) added. The pulp is diluted to about two liters and a rougher concentrate removed for 10 minutes, water being added as needed. The following results were obtained:
% Cu in concentrate=7 .25.
% Cu in tailings=.22.
Extraction 87.6
Using Anaconda Table Tailings in a neutral circuit with diethyl trithio carbonate as the flotation reagent in the proportion of 0.15 lbs. per ton of ore, the following results were obtained:
% Cu in heads=1.88.
% Cu in concentrate 8.84:.
% Cu in tailings=0.18.
Total Cu recovered=92.3%.
The flotation reagents forming part of the present invention do not decompose in an acid solution, and are therefore suitable for use in acid flotation circuits. .Using as the flotation reagent diethyl trithio carbonate in the proportion of 0.15 lbs. per ton of ore in a circuit containing 7.0 lbs. of sulfuric acid per ton of ore, the following results were obtained:
% Cu in heads=l.88.
% Cu in concentrate=9.68.
% Cu in tailings=0.085.
Total Cu recovered=96.3%.
Dibenzoyl trithio carbonate can be made conveniently by treating potassium trithio carbonate in benzene suspension with benzoyl chloride, removing the heat of reaction by cooling. After filtration from the potassium chloride and evaporation of the solvent, dibenzoyl trithio carbonate is obtained as a yellowish orange oil.
When tested as a flotation reagent using an alkaline circuit according to the process described, the following results were obtained:
% Cu in concentrate=6.67.
% Cu in tailings=.20.
Extraction=89.2%.
Diethyl thiol ester of thioncarbonyl disulfide may be made by treating the mono ethyl ester of trithio carbonic acid (Chancel Jahres bericht fiir Chemie 1851, p. 513) with iodine. The orange brown oil which is formed, is washed with water and then dried with calcium chloride.
When tested as a flotation reagent using an alkaline circuit according to the process described, the following results were obtained:
% Cu in concentrate=6.60.
% Cu in tailings=0.24.
E xtraction=86.9%.
In illustrating the present process, reference has been made specifically to certain ores and reagents, and to various specific conditions of operation. It will be understood that the present process is not limit- 7 ed to the specific substances or details of procedure mentioned, but includes generally processes of recovering values from ores by flotation in which the flotation agents are members of the class of compounds described. For instance, it has been pointed out as being desirable to add a frothing agent in the specific examples noted. However, where the flotation agent itself has sutficient frothing power, the frothing agent may be omitted.
Any suitable modifications and changes may be made without departing from the spirit and scope of the invention.
I claim:
1. In the process of concentratin ores and minerals by flotation the step which comprises subjecting the ore in the form of a pulp to a froth flotation operation in the presence of an organic derivative of trithio carbonate.
2. In the process of concentrating ores and minerals by flotation, the step which comprises subjecting the ore in the form of a pulp to a froth flotation operation in the presence of an organic derivative of trithio carbonate having the following structural formula:
where R and R are organic groups.
3. In the process of concentrating ores and minerals by flotation, the step which comprises subjecting the ore in the form of 1 a pulp to a froth flotation operation in the presence of an organic derivative of trithio carbonate having the following structural formula:
SR =C/ in which R is an alkyl group and R is an
US144193A 1926-10-25 1926-10-25 Process of concentrating ores and minerals by flotation Expired - Lifetime US1659396A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US144193A US1659396A (en) 1926-10-25 1926-10-25 Process of concentrating ores and minerals by flotation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US144193A US1659396A (en) 1926-10-25 1926-10-25 Process of concentrating ores and minerals by flotation

Publications (1)

Publication Number Publication Date
US1659396A true US1659396A (en) 1928-02-14

Family

ID=22507496

Family Applications (1)

Application Number Title Priority Date Filing Date
US144193A Expired - Lifetime US1659396A (en) 1926-10-25 1926-10-25 Process of concentrating ores and minerals by flotation

Country Status (1)

Country Link
US (1) US1659396A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2634291A (en) * 1951-11-13 1953-04-07 Phillips Petroleum Co Primary and secondary alkyl sulfenyl trithiocarbonates
US2676129A (en) * 1951-06-12 1954-04-20 Stauffer Chemical Co Aliphatic trithiocarbonate nematocides
US3901450A (en) * 1969-11-03 1975-08-26 David Weston Flotation with xanthate
US4316797A (en) * 1980-09-10 1982-02-23 Phillips Petroleum Company Flotation agent and process
US4341715A (en) * 1980-10-06 1982-07-27 Phillips Petroleum Company S-Allyl-S'-n-butyl-trithiocarbonate
US4425230A (en) 1982-02-16 1984-01-10 Oreprep Chemicals, Inc. Separation of molybdenite from its mixture with other sulfide ores
US4518492A (en) * 1984-06-15 1985-05-21 Phillips Petroleum Company Ore flotation with combined collectors
US4594151A (en) * 1982-10-13 1986-06-10 Societe Nationale Elf Aquitaine (Production) Flotation of minerals

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2676129A (en) * 1951-06-12 1954-04-20 Stauffer Chemical Co Aliphatic trithiocarbonate nematocides
US2634291A (en) * 1951-11-13 1953-04-07 Phillips Petroleum Co Primary and secondary alkyl sulfenyl trithiocarbonates
US3901450A (en) * 1969-11-03 1975-08-26 David Weston Flotation with xanthate
US4316797A (en) * 1980-09-10 1982-02-23 Phillips Petroleum Company Flotation agent and process
US4341715A (en) * 1980-10-06 1982-07-27 Phillips Petroleum Company S-Allyl-S'-n-butyl-trithiocarbonate
US4425230A (en) 1982-02-16 1984-01-10 Oreprep Chemicals, Inc. Separation of molybdenite from its mixture with other sulfide ores
US4594151A (en) * 1982-10-13 1986-06-10 Societe Nationale Elf Aquitaine (Production) Flotation of minerals
US4518492A (en) * 1984-06-15 1985-05-21 Phillips Petroleum Company Ore flotation with combined collectors

Similar Documents

Publication Publication Date Title
US1659396A (en) Process of concentrating ores and minerals by flotation
US4908125A (en) Froth flotation process for the recovery of minerals and a collector composition for use therein
US1652099A (en) Process of concentrating ores and minerals by flotation
US2074699A (en) Flotation process
US1833740A (en) Process of ore flotation
US2011176A (en) Ore concentration
US1364307A (en) Flotation of minerals
US2501269A (en) Froth flotation of sulfide ores
US1497699A (en) Concentration of ores
US1640218A (en) Concentration of ores
US1674166A (en) Process of concentrating ores and minerals by flotation
US1819112A (en) Froth flotation of minerals
GB498450A (en) Improvements in or relating to processes of concentrating minerals from their ores
US1554220A (en) Concentration of ores
US1554216A (en) Froth-flotation concentration of ores
US2222332A (en) Treatment of sylvinite ore
US1364304A (en) Flotation of minerals
US2901107A (en) Froth flotation of copper sulfide ores
US1773787A (en) Art of concentration of ores
US1847367A (en) Concentration of ores, minerals, and the like
US1819113A (en) Flotation reagent and process of froth flotation
US2289996A (en) Process of separating chalcopyrite ores
US1364858A (en) Flotation of minerals
US1763851A (en) Concentration of ores
US2044851A (en) Froth flotation concentration of ores