GB961194A - Talc beneficiation - Google Patents
Talc beneficiationInfo
- Publication number
- GB961194A GB961194A GB32013/60A GB3201360A GB961194A GB 961194 A GB961194 A GB 961194A GB 32013/60 A GB32013/60 A GB 32013/60A GB 3201360 A GB3201360 A GB 3201360A GB 961194 A GB961194 A GB 961194A
- Authority
- GB
- United Kingdom
- Prior art keywords
- talc
- slurry
- ore
- froth flotation
- froth
- 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
Links
- 239000000454 talc Substances 0.000 title abstract 17
- 229910052623 talc Inorganic materials 0.000 title abstract 17
- 238000009291 froth flotation Methods 0.000 abstract 10
- 239000002002 slurry Substances 0.000 abstract 8
- 241000276425 Xiphophorus maculatus Species 0.000 abstract 6
- 239000002245 particle Substances 0.000 abstract 6
- 239000007787 solid Substances 0.000 abstract 6
- XNWFRZJHXBZDAG-UHFFFAOYSA-N 2-METHOXYETHANOL Chemical compound COCCO XNWFRZJHXBZDAG-UHFFFAOYSA-N 0.000 abstract 2
- 229920001353 Dextrin Polymers 0.000 abstract 2
- 239000004375 Dextrin Substances 0.000 abstract 2
- 229920002907 Guar gum Polymers 0.000 abstract 2
- 229920002472 Starch Polymers 0.000 abstract 2
- 239000002253 acid Substances 0.000 abstract 2
- 230000000994 depressogenic effect Effects 0.000 abstract 2
- 235000019425 dextrin Nutrition 0.000 abstract 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 abstract 2
- 239000003292 glue Substances 0.000 abstract 2
- 235000010417 guar gum Nutrition 0.000 abstract 2
- 239000000665 guar gum Substances 0.000 abstract 2
- 229960002154 guar gum Drugs 0.000 abstract 2
- 239000000463 material Substances 0.000 abstract 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 abstract 2
- -1 n-butyl alcohols Chemical class 0.000 abstract 2
- 229920001451 polypropylene glycol Polymers 0.000 abstract 2
- 235000019698 starch Nutrition 0.000 abstract 2
- 239000008107 starch Substances 0.000 abstract 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/22—Magnesium silicates
-
- 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
-
- 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
- B03D2203/04—Non-sulfide ores
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Abstract
The platy talc content of natural talc is increased by grinding a talc ore to liberate the platy talc from the other forms of talc and other materials present, optionally removing from the ground ore most of the fines of particle size of less than 10 microns, forming a slurry of the remaining talc with a solids content determined as follows: .- 10 Microns.Platy con-.Per cent solids .fines removed..tent of ore..content of slurry .No.\sF 80%.\sO 80% .No.< 80%.\sO 15% .Yes.Any.\sE 25% subjecting the slurry to froth flotation, removing froth formed during the froth flotation and separating the talc contained in the floated froth. The talc ore is preferably ground to a particle size of about - 100 Tyler mesh although froth flotation can be obtained with particles ground only to - 20 mesh. The froth flotation may be effected in the presence of a depressant, e.g. dextrin, starch, glue or guar gum, and a water soluble frother, e.g. polypropylene glycol methyl ether, and methyl, ethyl and n-butyl alcohols, in an amount not exceeding 0.1 lb. per ton of solids. The pH of the slurry is preferably maintained within the range of 6.8 to 8.0 during froth flotation, e.g. by the addition of an acid.ALSO:The platy talc content of natural talc is increased by grinding a talc ore to liberate the platy talc from the other forms of talc and other materials present, optionally removing from the ground ore most of the fines of particle size of less than 10 microns, forming a slurry of the remaining talc with a solids content determined as follows:- .-10 Micron Fines.Platy Content.Percent Solids .Removed.of Ore.Content of Slurry .No. 80%.\sO 8% .No.<80%.\sO 15% .Yes.any.\yP 25% subjecting the slurry to froth flotation, removing froth formed during the froth flotation and separating the talc contained in the floated froth. The talc ore is preferably ground to a particle size of -100 Tyler mesh although froth flotation can be obtained with particles ground only to -20 mesh. The froth flotation may be effected in the presence of a depressant, e.g. dextrin, starch, glue or guar gum, and a water-soluble frother, e.g. polypropylene glycol methyl ether, and methyl, ethyl, and n-butyl alcohols, in an amount not exceeding 0,1 lb. per ton of solids. The pH of the slurry is preferably maintained within the range of 6,8-8,0 during froth flotation, e.g. by the addition of an acid.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US840941A US3102855A (en) | 1959-09-18 | 1959-09-18 | Talc beneficiation |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| GB961194A true GB961194A (en) | 1964-06-17 |
Family
ID=25283622
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB32013/60A Expired GB961194A (en) | 1959-09-18 | 1960-09-16 | Talc beneficiation |
Country Status (2)
| Country | Link |
|---|---|
| US (1) | US3102855A (en) |
| GB (1) | GB961194A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115818655A (en) * | 2022-11-01 | 2023-03-21 | 江西广源化工有限责任公司 | Flaky talcum powder, preparation method thereof and application of flaky talcum powder in preparation of laminating base paper |
Families Citing this family (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3269667A (en) * | 1963-04-29 | 1966-08-30 | Microcyclomat Co | Extraction method |
| US3424308A (en) * | 1965-11-09 | 1969-01-28 | Dresser Ind | Recovery of clay and sand from an ore |
| US3528915A (en) * | 1969-02-28 | 1970-09-15 | Titan Products Co | Titaniferous biotite lubricant |
| US5167375A (en) * | 1988-04-04 | 1992-12-01 | Datta Rabinder S | Apparatus for mineral matter separation |
| US5849333A (en) * | 1995-04-04 | 1998-12-15 | American Westmin, Inc. | Delaminated transparent talc |
| CN104085895B (en) * | 2014-07-03 | 2015-11-11 | 湖南尔康制药股份有限公司 | A kind of preparation method of medicinal talcum powder |
| CN104148172B (en) * | 2014-07-28 | 2016-05-04 | 鞍钢集团矿业公司 | A kind of bloodstone mine tailing is ore grinding, strong magnetic-reverse flotation recovery process respectively |
| CN115155791B (en) * | 2022-07-11 | 2024-05-10 | 辽宁艾海滑石有限公司 | Preparation method of talcum powder special for DPF of tail gas purifier of diesel truck |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US1250216A (en) * | 1916-11-28 | 1917-12-18 | Bridgewater Chemical Company | Process of extracting magnesium compounds from magnesium-bearing rocks. |
-
1959
- 1959-09-18 US US840941A patent/US3102855A/en not_active Expired - Lifetime
-
1960
- 1960-09-16 GB GB32013/60A patent/GB961194A/en not_active Expired
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115818655A (en) * | 2022-11-01 | 2023-03-21 | 江西广源化工有限责任公司 | Flaky talcum powder, preparation method thereof and application of flaky talcum powder in preparation of laminating base paper |
| CN115818655B (en) * | 2022-11-01 | 2024-03-26 | 江西广源化工有限责任公司 | Flaky talcum powder and preparation method thereof and application of flaky talcum powder in preparation of laminating base paper |
Also Published As
| Publication number | Publication date |
|---|---|
| US3102855A (en) | 1963-09-03 |
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