US1683569A - Selective flota l iqsr osi minerals - Google Patents
Selective flota l iqsr osi minerals Download PDFInfo
- Publication number
- US1683569A US1683569A US1683569DA US1683569A US 1683569 A US1683569 A US 1683569A US 1683569D A US1683569D A US 1683569DA US 1683569 A US1683569 A US 1683569A
- Authority
- US
- United States
- Prior art keywords
- thio
- carbanilid
- ortho
- selective
- toluidine
- 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
- 229910052500 inorganic mineral Inorganic materials 0.000 title description 6
- 239000011707 mineral Substances 0.000 title description 6
- 241001092591 Flota Species 0.000 title 2
- QWVGKYWNOKOFNN-UHFFFAOYSA-N O-Cresol Chemical compound CC1=CC=CC=C1O QWVGKYWNOKOFNN-UHFFFAOYSA-N 0.000 description 32
- RNVCVTLRINQCPJ-UHFFFAOYSA-N o-toluidine Chemical compound CC1=CC=CC=C1N RNVCVTLRINQCPJ-UHFFFAOYSA-N 0.000 description 32
- 239000003795 chemical substances by application Substances 0.000 description 24
- 239000000203 mixture Substances 0.000 description 22
- 238000005188 flotation Methods 0.000 description 18
- 239000002904 solvent Substances 0.000 description 14
- 239000008396 flotation agent Substances 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- HCHKCACWOHOZIP-UHFFFAOYSA-N zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 10
- 239000011701 zinc Substances 0.000 description 10
- 229910052725 zinc Inorganic materials 0.000 description 10
- 239000012141 concentrate Substances 0.000 description 8
- 229910052742 iron Inorganic materials 0.000 description 6
- 230000000153 supplemental Effects 0.000 description 6
- 239000002253 acid Substances 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 231100000614 Poison Toxicity 0.000 description 2
- 238000004166 bioassay Methods 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 239000003960 organic solvent Substances 0.000 description 2
- 230000000717 retained Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- -1 zinc lead Chemical compound 0.000 description 2
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
- B03D1/00—Flotation
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/008—Organic compounds containing oxygen
-
- 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
- B03D1/01—Organic compounds containing nitrogen
-
- 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 selective flotation of minerals, especially the suliid ores and is based upon the useoit cresylic acid as a solvent for and as a: supplemental flotative agent with thio-carbanilid.
- the use of thio-carbanilid in the concentration of sulfid ores by the iiotation process is well known.
- the solvent may have selective flotation qualities or it may be a frothing agent or both.
- the most commonly .used solvent for thio-carbanilid is ortho-toluidine, the usual mixture or solution used containing about 80 percent of the ortho-toluidine and 20 percent of thio-earbanilid.
- this comparatively dilute solution it is necessary to heat and maintain its temperature at about 45 C. in order to hold the thio-carbanilid in solution. This temperature requirement is highly objectionable due to the volatility of the ortho-toluidine which is lostby volatilization and the vapors of which moreover are highly inflammable.
- ortho-toluidine itself is etl'ective only as Y .a frothing agent, and when used in excess gives a spongy 'l'roth which is not desirable for the best flotation results since it tends to contaminate the concentrate with insolublc material.
- Another objection to the use of ortho-toluidine is its cost, the available supply being fairly limited.
- cresylic acid is an excellent solvent for and supplemental flotation agent with thio-carbanilid.
- Cresylic acid is a well-known flotation agent having desirable selective flotation properties as well as some frothing Value, and is moreover a relatively inexpensive agent in that it is effective when used in very small amounts in a flotation circuit.
- thio-carbanilid is more effective when used as a wet agent, that is, in solution than when used as a dry agent, that is, added to the ore pulp in its dry state in the ball mill. Due to the increased amount of thio-carbanilid which may be retained in solution in cresylic acid or in a mixture of cresylic acid and ortho-toluidine and due to the less violent :trothing characteristics of cresylic acid or a mixture of cresylic acid and ortho-toluidine as compared to ortho-toluidine alone, it is possible to use all of the thio-carbanilid required for the flotation in the form of a solution, thus entirely dispensing with the customary supplemental addition of dry thio-carbanilid to the ore pulp in the ball mill. This results in a direct saving of thiocarbanilid.
- a flotation agent a mixture of about 20 parts by weight of: ortho-toluidine, 20 parts by weight of thio-carbanilid and 60 parts by weight of cresylic acid.
Description
Patented Sept. l, 1928.
UNITED srAres BAYARD S. MORROW AND KLETEETKO, O]? ANACOIIDA, MdNTANA SELECTIVE FLOTJ BELEZON E MINERALS.
Io Drawing.
This invention relates to the selective flotation of minerals, especially the suliid ores and is based upon the useoit cresylic acid as a solvent for and as a: supplemental flotative agent with thio-carbanilid. The use of thio-carbanilid in the concentration of sulfid ores by the iiotation process is well known. It has been used with marked success on copper ores as wellas complex lead-zinc-iron 1 ores, both as a dry agent, that is, according to the common practice by feeding the dry thio-carbanilid to the ore grinding mill and also asa Wet agent, that is, in combination with an organic solvent such as the common flotation oils andoil mixtures Due to its low solubility in water, it ismueh more eli'ective as a wet agent than as .a dry agent. In the use of thio-carbanilid as a wet agent, the solvent used may be either one which will directly assist the flotation operation or it may be one which itself has no flotation properties. Thus the solvent may have selective flotation qualities or it may be a frothing agent or both. The most commonly .used solvent for thio-carbanilid is ortho-toluidine, the usual mixture or solution used containing about 80 percent of the ortho-toluidine and 20 percent of thio-earbanilid. However even 'with this comparatively dilute solution it is necessary to heat and maintain its temperature at about 45 C. in order to hold the thio-carbanilid in solution. This temperature requirement is highly objectionable due to the volatility of the ortho-toluidine which is lostby volatilization and the vapors of which moreover are highly inflammable. The ortho-toluidine itself is etl'ective only as Y .a frothing agent, and when used in excess gives a spongy 'l'roth which is not desirable for the best flotation results since it tends to contaminate the concentrate with insolublc material. Another objection to the use of ortho-toluidine is its cost, the available supply being fairly limited.
WVe have now found that cresylic acid is an excellent solvent for and supplemental flotation agent with thio-carbanilid. Cresylic acid is a well-known flotation agent having desirable selective flotation properties as well as some frothing Value, and is moreover a relatively inexpensive agent in that it is effective when used in very small amounts in a flotation circuit.
We have found that thio-carbanilid is soluble in cresylic acid and that the result- Application filed Gctober 21, 1925. Serial No. 63,992.
ing solution is very effective as a fiotation' agent. Owing to its highly selective qualifamount of ortho-toluidine. to the, mixture.
Thus, a mixture or solution of 20 parts by weight of ortho-toluidine and parts by weight of cresylic acid and 20 parts by weight of thio-carbanilid will hold the thiocarbanilid in solution indefinitely at 30 0., and for 24 hours at 20 C. In general, both 'cresylic acid alone and a mixture of oresylic acid and ortho-toluidine have the advantage over ortho-toluidine aloneas solvents for thio-carbanilid in that they will hold more ot the thio-carbanilid in solution at a given temperature. This greater solubility of the thio-carbanilid in cresylic acid or in a mixture of cresylic acid and ortho-toluidine makes possible the employment of lower temperatures which in turn reduces the fire hazard and the danger to the health of work men due to poisonous fumes, and further more avoids the loss of solvent by volitization and thus insures the retention of the thio-carbanilid in solution. The lower cost of the cresylic acid as compared with orthotoluidine also is a direct economic advantage.
As previously stated, thio-carbanilid is more effective when used as a wet agent, that is, in solution than when used as a dry agent, that is, added to the ore pulp in its dry state in the ball mill. Due to the increased amount of thio-carbanilid which may be retained in solution in cresylic acid or in a mixture of cresylic acid and ortho-toluidine and due to the less violent :trothing characteristics of cresylic acid or a mixture of cresylic acid and ortho-toluidine as compared to ortho-toluidine alone, it is possible to use all of the thio-carbanilid required for the flotation in the form of a solution, thus entirely dispensing with the customary supplemental addition of dry thio-carbanilid to the ore pulp in the ball mill. This results in a direct saving of thiocarbanilid.
The principal advantage in the use of The improved metallurgical results are illustrated by the following tables:
1. Using a solution of parts of thiocarhanilid in a mixture of 60 parts of cresylic acid and 20 parts of ortho-toluidine.
Assays Weight Per For For Per Per cent cent gi r 3d cent cent zinc lead p 5 e g iron 11130] per 0T0 A a. 100 10. 8 i 2. (i 0. 29 5. 5 009 3. l Zinc COIICL. 18. 9 53. 3 5. 8 0. 75 18. 8 030 3. 9 5. 2 Lead CODCIJ. l. 6 (i. 5 (i8: 0 3. 10 66. l 050 2. 1 0. 5 'l illllngflin 79. 3 0. 7 0. O. 07 1.0 003 2. 5
II. Using thio-carbanilid in its natural state added to the ball mill with thio-earhanilid in solution in ortho-tolulcline.
reeasee The metallurgical advantages indicated by the foregoing tables are as follows:
(a) A decrease in the loss of zinc and lead in the tailings or in the discard.
(6) Increased recovery of zinc and lead in the concentrates.
(0) Increased concentration of zinc and lead in the concentrates. I
((Z) Increased recovery of zinc in the subsequent treatment ofthe concentrate due to the lower iron content thereof.
The scope of the invention is indicated in the appended claims.
We claim:
1. As a flotation agent a solution comprisinq' cresylic acid and thio-carbanilid.
As a flotation agent a solution comprising cresylie acid, thio-carhanilid and 0rthotoluidine.
3. As a flotation agent a mixture of about 20 parts by weight of: ortho-toluidine, 20 parts by weight of thio-carbanilid and 60 parts by weight of cresylic acid.
In testimony whereof, we afiix our signatures.
BAYARD S. MORROW ERNEST KLEPETKQ.
Publications (1)
Publication Number | Publication Date |
---|---|
US1683569A true US1683569A (en) | 1928-09-04 |
Family
ID=3416165
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US1683569D Expired - Lifetime US1683569A (en) | Selective flota l iqsr osi minerals |
Country Status (1)
Country | Link |
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US (1) | US1683569A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3414128A (en) * | 1965-09-24 | 1968-12-03 | Armour Ind Chem Co | Nitrogenous material fractions obtained from gilsonite in froth flotation |
-
0
- US US1683569D patent/US1683569A/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3414128A (en) * | 1965-09-24 | 1968-12-03 | Armour Ind Chem Co | Nitrogenous material fractions obtained from gilsonite in froth flotation |
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