GB1086438A - Concentration of phosphate ores - Google Patents
Concentration of phosphate oresInfo
- Publication number
- GB1086438A GB1086438A GB5226465A GB5226465A GB1086438A GB 1086438 A GB1086438 A GB 1086438A GB 5226465 A GB5226465 A GB 5226465A GB 5226465 A GB5226465 A GB 5226465A GB 1086438 A GB1086438 A GB 1086438A
- Authority
- GB
- United Kingdom
- Prior art keywords
- slurry
- flotation
- ore
- hydrophylic
- gum
- 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
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
- B03D1/02—Froth-flotation processes
- B03D1/021—Froth-flotation processes for treatment of phosphate ores
-
- 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
- B03D1/08—Subsequent treatment of concentrated product
- B03D1/085—Subsequent treatment of concentrated product of the feed, e.g. conditioning, de-sliming
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Geology (AREA)
- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Phosphate mineral, e.g. apatite, is separated from a phosphate-containing ore by conditioning an aqueous slurry of the ore with a hydrophylic gum of vegetable origin and separating the phosphate mineral from the slurry by froth flotation. The ore obtained from the mine is crushed and wet ground to liberate the apatite from the other minerals in the ore and to obtain the desired sizing for flotation. After slurrying with water removal of slime is effected, e.g. in a hydrocyclone. The de-slimed slurry is then conditioned at a pH of 7.5 to 10.0 by the addition of the hydrophylic gum which acts as a depressing agent for calcite, magnetite and silicate contained in the ore. A first froth flotation is carried out in the presence of a collecting agent, of which 80% may be added of the slurry enters the flotation circuit and the rest in subsequent flotation cells. The apatite particles adhere to the bubbles formed by the blowing of air or gas in the flotation cells and rise therewith to the surface of the slurry forming a froth which is recovered as a first concentrate which may be directly centrifuged and dried or refined. Alternatively, the first concentrate may be subjected to further froth flotation. The hydrophylic gum of vegetable origin may be a caustic soda-gelatinized starch obtained by agitating one volume of a 10% caustic soda solution with one to two volumes of an aqueous dispersion of about 10% of commercial starch. The suspension is then diluted to about 1% gelatinized starch content. The collecting agent is of an anionic character and may contain a major proportion of unsaturated fatty acids. A portion of the fatty acid may be saponified to maintain the required pH in the slurry. Alternatively, the fatty acid may be used with an olefin of a hydrocarbon oil, such as fuel oil, preferably with an emulsifier. Preferred collecting agents are linoleic and oleic acids and products rich in these compounds, e.g. distillate tall oil and red oil. Examples of the process are given.ALSO:Phosphate mineral, e.g. apatite, is separated from a phosphate-containing ore by conditioning an aqueous slurry of the ore with a hydrophylic gum of vegetable origin and separating the phosphate mineral from the slurry by froth flotation. The ore obtained from the mine is crushed and wet ground to liberate the apatite from the other minerals in the ore and to obtain the desired sizing for flotation. After slurrying with water removal of slime is effected, e.g. in a hydrocyclone. The de-slimed slurry is then conditioned at a pH of 7.5 to 10.0 by the addition of the hydrophylic gum which acts as a depressing agent for calcite, magnetite and silicate contained in the ore. A first froth flotation is carried out in the presence of a collecting agent, of which 80% may be added as the slurry enters the p flotation circuit and the rest in subsequent flotation cells. The apatite particles adhere to the bubbles formed by the blowing of air or gas in the flotation cells and rise therewith to the surface of the slurry forming a froth which is recovered as a first concentrate which may be directly centrifuged and dried or refined. Alternatively, the first concentrate may be subjected to further froth flotation. The hydrophylic gum of vegetable origin may be a caustic soda-gelatinised starch obtained by agitating one volume of a 10% caustic soda solution with one or two volumes of an aqueous dispersion of about 10% of commercial starch. The suspension is then diluted to about 1% gelatinised starch content. The collecting agent is of an anionic character and may contain a major proportion of unsaturated fatty acids. A portion of the fatty acid may be saponified to maintain the required pH in the slurry. Alternatively, the fatty acid may be used with an olefin or a hydrocarbon oil, such as fuel oil, preferably with an emulsifier. Preferred collecting agents are linoleic and oleic acids and products rich in these compounds, e.g. distillate tall oil and red oil. Examples of the process are given.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US509187A US3403783A (en) | 1965-11-22 | 1965-11-22 | Flotation of phosphate-containing materials |
GB5226465A GB1086438A (en) | 1965-12-09 | 1965-12-09 | Concentration of phosphate ores |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
GB5226465A GB1086438A (en) | 1965-12-09 | 1965-12-09 | Concentration of phosphate ores |
Publications (1)
Publication Number | Publication Date |
---|---|
GB1086438A true GB1086438A (en) | 1967-10-11 |
Family
ID=10463245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB5226465A Expired GB1086438A (en) | 1965-11-22 | 1965-12-09 | Concentration of phosphate ores |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB1086438A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102319634A (en) * | 2011-10-12 | 2012-01-18 | 湖南省矿产测试利用研究所 | Process for recovering fuel from collophanite |
CN107309093A (en) * | 2017-06-27 | 2017-11-03 | 湖北富邦科技股份有限公司 | It is a kind of to prevent gel and improve collecting agent of agent activity and preparation method thereof |
RU2737769C1 (en) * | 2020-04-16 | 2020-12-02 | федеральное государственное бюджетное образовательное учреждение высшего образования "Санкт-Петербургский горный университет" | Apatite ore dressing method |
CN113245064A (en) * | 2021-04-30 | 2021-08-13 | 瓮福(集团)有限责任公司 | Method for removing sesquioxide in complex refractory collophanite |
-
1965
- 1965-12-09 GB GB5226465A patent/GB1086438A/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102319634A (en) * | 2011-10-12 | 2012-01-18 | 湖南省矿产测试利用研究所 | Process for recovering fuel from collophanite |
CN107309093A (en) * | 2017-06-27 | 2017-11-03 | 湖北富邦科技股份有限公司 | It is a kind of to prevent gel and improve collecting agent of agent activity and preparation method thereof |
RU2737769C1 (en) * | 2020-04-16 | 2020-12-02 | федеральное государственное бюджетное образовательное учреждение высшего образования "Санкт-Петербургский горный университет" | Apatite ore dressing method |
CN113245064A (en) * | 2021-04-30 | 2021-08-13 | 瓮福(集团)有限责任公司 | Method for removing sesquioxide in complex refractory collophanite |
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