US1640218A - Concentration of ores - Google Patents
Concentration of ores Download PDFInfo
- Publication number
- US1640218A US1640218A US45704A US4570425A US1640218A US 1640218 A US1640218 A US 1640218A US 45704 A US45704 A US 45704A US 4570425 A US4570425 A US 4570425A US 1640218 A US1640218 A US 1640218A
- Authority
- US
- United States
- Prior art keywords
- flotation
- pulp
- concentration
- minerals
- mineral
- 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
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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
- B03D2203/00—Specified materials treated by the flotation agents; specified applications
- B03D2203/02—Ores
Definitions
- This invention relates to the concentration of ores, minerals, and the like, by flotation, and has for its object the provislon of oertain improvements in flotation processes, and more particularly the froth flotation process.
- the present invention is based upon the discovery that thiocarbaniic esters, thiourethanes) are effective flotation reagents.
- thiocarbamic esters and more particularly alkyl arylthiocarbamates such as methyl phenylthiocarbamate and ethyl phenylthiocarbamate, have a marked selective action on sulfide minerals, as distinguished from gangue minerals, and when used as flotation agents in the customary flotation processes cause the sulfide minerals to float readily with an attendant high recovery of the metal values.
- thiocarbamic esters are called thiourethanes, being urethanes (that is, esters of carbamic acids) in which one or both oxygen atoms have been replaced by sulfur. Since the two oxygen atoms of urethanes differ in function, distinctive names are required to indicate which one is replaced, in case sulfur has been substituted for only one. When the carbonyl oxygen is replaced by sulfur, the result is a thionurethane.
- the thionurethane compounds are ordinarily understood to-be embraced within the generic class of thiourethanes. Replacement of the other oxygen atom gives a thiolcarbamate or thiolurethane.
- the invention accordingly, contemplates the use, as flotation agents, of monoand dithiocarbamic esters (monoand dithiourethanes), and it is the intention throughout this specification and in the appended claims to include all these esters under the generic terms thiocarbamic esters or thiourethanes.
- the general method of preparing a thiourethane consists in treating an isotliiocyanate or mustard oil with an alcohol, under suitable conditions. For example, to prepare ethyl phenylthiocarbamate (C,,H,NHCSOC H or methyl phenylthiocarbamate (C H NHCSOCI-L),
- phenyl mustard oil is heated with ethyl alcohol, or with methyl alcohol, respectively, in an autoclave.
- an alkali such as caustic potash
- the resultin thiocarbamic esters crystallize readily, and may thus be removed from the re-. action mixture and obtained in a pure condition. If desired, the crude reaction mixture may be used in the flotation process without isolating the ester.
- Other methods of preparing the thiocarbamio esters may be uwd, as, for example, by alkylation of salts of dithiocarbamic acids.
- Thiourethanes are only sparingly soluble in water, but dissolve readily in aqueous solutions of alkalies,-such as caustic soda, as well as in various organic solvents. Hence, the thiourethane may be used in the flotation process either by adding it to the ore pulp prior to or during fine grinding, or it may be dissolved in aqueous, alkali or in an appropriate organic solvent and the resulting solution added to the ore pulp feed entering the flotation apparatus.
- thiourethanes are mineral collecting agentsonly, being substantially devoid of frothing power, they should be used, in practicing the present invention, in conjunction with an appropriate frothing agent, such as pine oil, or the like.
- the thio-urethanes exhibit marked mineral collecting power in acid, neutral and alkaline ore pulpsf My investigations indicate, however, that the thiourethanes give the best results on most ores in pulps made alkaline, as for example by the addition'of lime.
- thiourethanes as flotation agents in a neutral (that is nonacid) or alkaline ore pulp.
- Any alkali such as caustic soda, soda ash, or lime, may be added to the ore pulp to make the pulp neutral or alkaline. Lime, on the whole, is the most suitable and available alkali for this purpose.
- the alkali is preferably added to the ore pulp before the, final grinding, and before adding the thiourethane to the ore pulp.
- the quantity of the thiou-rethane to -be emplo ed in practicing the present invention depends to some extent upon the particular" ester being used and theparticular ore be ing treated. In general, l have found that one-fifth of a pound, and less, per ton of dry ore gives satisfactory results.
- T have given some typical flotation results obtained in the practice of the present invention.
- the thiourethane was added, in the proportion of 0.1 pound per ton of dry ore. together with the amount of hydrated lime indicated, to 500 grams of minus lO-mesh ore of the Utah Copper Com-- pany, which was then ground with 250 cc. of water in a laboratory pebble mill for 20 minutes.
- the ore pulp was transferred to a laboratory Gallow rougher flotation machine, diluted with about 2 liters of water, and floated after adding one drop of terpineol as a frothing agent immediately preceding flotation.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp to a flotation operation in' the presence of a thiourethane.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp to a flotation operation in the presence of an alkyl arylthiocarbamate.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp to a flotation operation in the presence of ethyl phenylthiocarbamate.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a nonacid pulp to a flotation operation in the presence of an alkyl arylthiocarbamate.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of an alkaline pulp to a flotation operation in the presence of a thiourethane.
- the improvement in the concentration of. minerals by flotation which comprises subjecting the mineral in the form of an alkaline pulp to a flotation operation in the presence of an alkyl arylthiocarbamate.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp made alkaline by the addition of lime to a flotation operation in the presence of a thiourethane.
- the improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp made alkaline by the addition of lime to afiotation operation in the presence of ethyl phenylthiocarbamate.
- step 12 which comprises subjecting the ore in the form of a pulp to a flotation operation in the pres 1 ence of aryl thiourethane.
Description
Patented Aug. 23, 1927.
UNITED STATES PATENT OFFICE.
' RALPH E. SAYRE, 02 NEW ROCHELLE, NEW YORK, ASSIGrNOR TO METALS RECOVERY COMPANY, OF NEW YORK, N. Y., A CORPORATION OF MAINE.
CONCENTRATION OF 03138.
No Drawing.
This invention relates to the concentration of ores, minerals, and the like, by flotation, and has for its object the provislon of oertain improvements in flotation processes, and more particularly the froth flotation process.
The present invention is based upon the discovery that thiocarbaniic esters, thiourethanes) are effective flotation reagents. I have found that the thiocarbamic esters, and more particularly alkyl arylthiocarbamates such as methyl phenylthiocarbamate and ethyl phenylthiocarbamate, have a marked selective action on sulfide minerals, as distinguished from gangue minerals, and when used as flotation agents in the customary flotation processes cause the sulfide minerals to float readily with an attendant high recovery of the metal values.
My investigations indicate that the thiocarbamic esters are substantially lacking in frothing power, so that an appropriate frothin agent, such as pine oil, terpineol, or the like, should be employed in conjunction therewith in carrying out the flotation operation.
In general, thiocarbamic esters are called thiourethanes, being urethanes (that is, esters of carbamic acids) in which one or both oxygen atoms have been replaced by sulfur. Since the two oxygen atoms of urethanes differ in function, distinctive names are required to indicate which one is replaced, in case sulfur has been substituted for only one. When the carbonyl oxygen is replaced by sulfur, the result is a thionurethane. The thionurethane compounds are ordinarily understood to-be embraced within the generic class of thiourethanes. Replacement of the other oxygen atom gives a thiolcarbamate or thiolurethane.
The derivation of the word urethane (from urea and ethane) implies an ethyl ester.' Accordingly, the rational but cumbersome nomenclature should be applied to other esters. For example, the compound represented by the chemiealhformula e AE HQ Q m Application filed July 23, 1925. Serial No. 45,704.
rethanes. The invention, accordingly, contemplates the use, as flotation agents, of monoand dithiocarbamic esters (monoand dithiourethanes), and it is the intention throughout this specification and in the appended claims to include all these esters under the generic terms thiocarbamic esters or thiourethanes.
The general method of preparing a thiourethane consists in treating an isotliiocyanate or mustard oil with an alcohol, under suitable conditions. For example, to prepare ethyl phenylthiocarbamate (C,,H,NHCSOC H or methyl phenylthiocarbamate (C H NHCSOCI-L),
phenyl mustard oil is heated with ethyl alcohol, or with methyl alcohol, respectively, in an autoclave. The addition of an alkali, such as caustic potash, promotes the reac-* tion, so that lower temperatures may thereby be employed. In the foregoing examples, the resultin thiocarbamic esters crystallize readily, and may thus be removed from the re-. action mixture and obtained in a pure condition. If desired, the crude reaction mixture may be used in the flotation process without isolating the ester. Other methods of preparing the thiocarbamio esters may be uwd, as, for example, by alkylation of salts of dithiocarbamic acids.
Thiourethanes are only sparingly soluble in water, but dissolve readily in aqueous solutions of alkalies,-such as caustic soda, as well as in various organic solvents. Hence, the thiourethane may be used in the flotation process either by adding it to the ore pulp prior to or during fine grinding, or it may be dissolved in aqueous, alkali or in an appropriate organic solvent and the resulting solution added to the ore pulp feed entering the flotation apparatus.
As thiourethanes are mineral collecting agentsonly, being substantially devoid of frothing power, they should be used, in practicing the present invention, in conjunction with an appropriate frothing agent, such as pine oil, or the like. The thio-urethanes exhibit marked mineral collecting power in acid, neutral and alkaline ore pulpsf My investigations indicate, however, that the thiourethanes give the best results on most ores in pulps made alkaline, as for example by the addition'of lime.
I prefer to employ the thiourethanes as flotation agents in a neutral (that is nonacid) or alkaline ore pulp. Any alkali, such as caustic soda, soda ash, or lime, may be added to the ore pulp to make the pulp neutral or alkaline. Lime, on the whole, is the most suitable and available alkali for this purpose. The alkali is preferably added to the ore pulp before the, final grinding, and before adding the thiourethane to the ore pulp.
The quantity of the thiou-rethane to -be emplo ed in practicing the present invention. depends to some extent upon the particular" ester being used and theparticular ore be ing treated. In general, l have found that one-fifth of a pound, and less, per ton of dry ore gives satisfactory results.
In the following table, T have given some typical flotation results obtained in the practice of the present invention. In each of the floats reported in this table, the thiourethane was added, in the proportion of 0.1 pound per ton of dry ore. together with the amount of hydrated lime indicated, to 500 grams of minus lO-mesh ore of the Utah Copper Com-- pany, which was then ground with 250 cc. of water in a laboratory pebble mill for 20 minutes. The ore pulp was transferred to a laboratory Gallow rougher flotation machine, diluted with about 2 liters of water, and floated after adding one drop of terpineol as a frothing agent immediately preceding flotation.
Lime lbs. per Heads Tails, Cone. cover Reagent. ton Cu. Cu. Cu. y
dry ore. v
Phenyl thloureth ane C0H5NHCSOC2H5 4 1.24 0.18 12. 5 86. 7 Methyl phenylthiocarbamate CeHrNHCSOCHJMa 5 l. 22 0. l4. 141 8 89. 5 otolyl thlourethano C1H7NHCSOC2H5 5 1'. 22 0.16 16. 7 87. 7. Phenyl dithiourethane CoHaNHCSSCsHa 5 1.22 0. 20 16. 1 84. 7
Satisfactor flotation results have also been obtaine using ethyl phenylthiocarbamate (phenyl thioureth'ane)v in acid and new tral pulp on the ore of the Magma Copper Co. Good results have likewise been obtained using ethyl .phenylthiolcarbamate the alkyl arylthiocarbamates, such as ethyl phenylthiocarbamate and methyl phenylthioea ers mineral and ore in a broad sense to inelude ores, mineral productsand all mate'- rials amenable to concentration or similar treatment by the flotation processes.
I claim: 5
l. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp to a flotation operation in' the presence of a thiourethane.
2. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp to a flotation operation in the presence of an alkyl arylthiocarbamate.
3 The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp to a flotation operation in the presence of ethyl phenylthiocarbamate.
4.. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a non-acid pulp to a flotation operation in the presence of a thiourethane.
5. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a nonacid pulp to a flotation operation in the presence of an alkyl arylthiocarbamate.
6. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of an alkaline pulp to a flotation operation in the presence of a thiourethane.
7. The improvement in the concentration of. minerals by flotation which comprises subjecting the mineral in the form of an alkaline pulp to a flotation operation in the presence of an alkyl arylthiocarbamate.
8. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of an alkaline pulp to a flotation operation in the presence of ethyl phenylthiocarbamate.
9. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp made alkaline by the addition of lime to a flotation operation in the presence of a thiourethane.
10. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form ofa pulp made alkaline by the addition of lime to a flotation operation in the presence of an alkyl arylthiocarbamate.
11. The improvement in the concentration of minerals by flotation which comprises subjecting the mineral in the form of a pulp made alkaline by the addition of lime to afiotation operation in the presence of ethyl phenylthiocarbamate.
12. 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 flotation operation in the pres 1 ence of aryl thiourethane.
13. 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 flotation operation in the presence
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US45704A US1640218A (en) | 1925-07-23 | 1925-07-23 | Concentration of ores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US45704A US1640218A (en) | 1925-07-23 | 1925-07-23 | Concentration of ores |
Publications (1)
Publication Number | Publication Date |
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US1640218A true US1640218A (en) | 1927-08-23 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US45704A Expired - Lifetime US1640218A (en) | 1925-07-23 | 1925-07-23 | Concentration of ores |
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US (1) | US1640218A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3590996A (en) * | 1969-02-03 | 1971-07-06 | Dow Chemical Co | Floatation of sulfide ores |
US3590998A (en) * | 1969-02-03 | 1971-07-06 | Dow Chemical Co | Flotation of sulfide ores |
US3975264A (en) * | 1973-07-13 | 1976-08-17 | Minerec Corporation | Flotation of copper sulfide ores with improved thionocarbamates |
US4136020A (en) * | 1976-11-11 | 1979-01-23 | Minerec Corporation | Flotation reagent and process |
US20040099836A1 (en) * | 2000-11-07 | 2004-05-27 | Heinrich Hesse | Collector for non iron metal sulphide preparation |
-
1925
- 1925-07-23 US US45704A patent/US1640218A/en not_active Expired - Lifetime
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3590996A (en) * | 1969-02-03 | 1971-07-06 | Dow Chemical Co | Floatation of sulfide ores |
US3590998A (en) * | 1969-02-03 | 1971-07-06 | Dow Chemical Co | Flotation of sulfide ores |
US3975264A (en) * | 1973-07-13 | 1976-08-17 | Minerec Corporation | Flotation of copper sulfide ores with improved thionocarbamates |
US4136020A (en) * | 1976-11-11 | 1979-01-23 | Minerec Corporation | Flotation reagent and process |
US20040099836A1 (en) * | 2000-11-07 | 2004-05-27 | Heinrich Hesse | Collector for non iron metal sulphide preparation |
US7051881B2 (en) * | 2000-11-07 | 2006-05-30 | Clariant International Ltd. | Collector for non iron metal sulphide preparation |
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