CN106216103A - The method of purification of wollastonite - Google Patents
The method of purification of wollastonite Download PDFInfo
- Publication number
- CN106216103A CN106216103A CN201610684502.XA CN201610684502A CN106216103A CN 106216103 A CN106216103 A CN 106216103A CN 201610684502 A CN201610684502 A CN 201610684502A CN 106216103 A CN106216103 A CN 106216103A
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- CN
- China
- Prior art keywords
- wollastonite
- total amount
- purification
- addition
- powder total
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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
- B03D1/01—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
- B03C—MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03C1/00—Magnetic separation
- B03C1/02—Magnetic separation acting directly on the substance being separated
- B03C1/30—Combinations with other devices, not otherwise provided for
-
- 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
- B03D1/025—Froth-flotation processes adapted for the flotation of fines
-
- 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
-
- 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
- B03D1/082—Subsequent treatment of concentrated product of the froth product, e.g. washing
-
- 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
- B03D2201/005—Dispersants
-
- 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
- B03D2201/00—Specified effects produced by the flotation agents
- B03D2201/06—Depressants
-
- 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
Abstract
The invention discloses the method for purification of a kind of wollastonite, relate to mineral floating separation technology field.Impurity iron in wollastonite mine is removed by the present invention by magnetic separation, then by rosin amine, quartz is flotated, add collecting agent dodecyl salt acid amide and inhibitor tannic acid, wollastonite is flotated, the method is simple, and the grade of the wollastonite after purification reaches more than 90%.
Description
Technical field
The present invention relates to mineral floating technical field, the method for purification of a kind of wollastonite.
Background technology
Wollastonite mine based on wollastonite, the impure mineral multidigit quartz of association and diopside etc., impurity Ore many in
In the granular solution gap being distributed in wollastonite, wollastonite, quartz and diopside broadly fall into silicate mineral, have the most similar
Character, therefore FLOTATION SEPARATION wollastonite, diopside and quartz have suitable difficulty.
Summary of the invention
It is an object of the invention to provide the method for purification of a kind of wollastonite, the method for purification of this wollastonite can solve silicon
The problem that lime stone, diopside separate with quartz difficulty.
In order to solve the problems referred to above, the technical solution used in the present invention is:
The method of purification of this wollastonite is with wollastonite mine as raw material, and described wollastonite mine comprises wollastonite, quartz and saturating brightness
Stone, wherein, the content of wollastonite is 56.2%~60.4%, and method of purification is:
Being pulverized by wollastonite mine, cross 100 mesh~140 mesh molecular sieves, obtain wollastonite in powder, adding water and making mass percent is 12%
~first pulp slurry of 17%, adding dispersant, magnetic separation removes impurity iron, and regulation liquid pH value, to 6.2~6.8, adds Colophonium
Amine makees collecting agent, wollastonite and diopside is floatingly selected, and obtains the first flotation thing, then adds water in the first flotation thing, is modulated into
Mass percent is second pulp slurry of 20%~25%, adds dodecyl salt acid amide and tannic acid, is flotated by wollastonite,
Obtain the second flotation thing, washing, dry;Wherein, the addition of dispersant is the 0.2%~0.5% of wollastonite in powder total amount;Rosin amine
Addition is wollastonite in powder total amount 0.05%~0.1%, the addition of dodecyl salt acid amide be wollastonite in powder total amount
0.1%~0.5%, the addition of tannic acid is the 0.02%~0.05% of wollastonite in powder total amount.
In technique scheme, more specifically technical scheme is it may also is that dispersant is sodium dialkyl sulfate or methyl
Amylalcohol.
Owing to have employed technique scheme, the present invention compared with prior art has the advantages that
Impurity iron in wollastonite mine is removed by the present invention by magnetic separation, is then flotated by quartz by rosin amine, then
Adding collecting agent-dodecyl salt acid amide and inhibitor-tannic acid, flotated by wollastonite, the method is simple, carries
The grade of the wollastonite after pure reaches more than 90%.
Detailed description of the invention
Below in conjunction with embodiment, the invention will be further described:
Embodiment 1
The present embodiment with comprise wollastonite, quartz and diopside wollastonite as raw material, the content of wollastonite is 56.2%, carries
Pure method is: pulverized by wollastonite mine, crosses 120 mesh molecular sieves, obtains wollastonite in powder, and adding water and making mass percent is 12%
First pulp slurry, adds sodium dialkyl sulfate, and magnetic separation removes impurity iron, and regulation liquid pH value, to 6.2~6.8, adds rosin amine
Make collecting agent, wollastonite and diopside are floatingly selected, obtain the first flotation thing, then add water in the first flotation thing, be modulated into matter
Amount percentage ratio is second pulp slurry of 20%~25%, adds dodecyl salt acid amide and tannic acid, is flotated by wollastonite,
To the second flotation thing, washing, dry;Wherein, the addition of dispersant is the 0.2% of wollastonite in powder total amount;The addition of rosin amine
For 0.08%, addition is wollastonite in powder total amount the 0.1% of dodecyl salt acid amide of wollastonite in powder total amount, the interpolation of tannic acid
Amount is the 0.02% of wollastonite in powder total amount.
After the present embodiment purification, the grade of wollastonite is 91.6%.
Embodiment 2
The present embodiment with comprise wollastonite, quartz and diopside wollastonite as raw material, the content of wollastonite is 60.4%, carries
Pure method is: pulverized by wollastonite mine, crosses 100 mesh molecular sieves, obtains wollastonite in powder, and adding water and making mass percent is 15%
First pulp slurry, adds sodium dialkyl sulfate, and magnetic separation removes impurity iron, and regulation liquid pH value, to 6.2~6.8, adds rosin amine
Make collecting agent, wollastonite and diopside are floatingly selected, obtain the first flotation thing, then add water in the first flotation thing, be modulated into matter
Amount percentage ratio is second pulp slurry of 20%~25%, adds dodecyl salt acid amide and tannic acid, is flotated by wollastonite,
To the second flotation thing, washing, dry;Wherein, the addition of dispersant is the 0.5% of wollastonite in powder total amount;The addition of rosin amine
For 0.1%, addition is wollastonite in powder total amount the 0.3% of dodecyl salt acid amide of wollastonite in powder total amount, the interpolation of tannic acid
Amount is the 0.03% of wollastonite in powder total amount.
After the present embodiment purification, the grade of wollastonite is 91.2%.
Embodiment 3
The present embodiment with comprise wollastonite, quartz and diopside wollastonite as raw material, the content of wollastonite is 57.5%, carries
Pure method is: pulverized by wollastonite mine, crosses 140 mesh molecular sieves, obtains wollastonite in powder, and adding water and making mass percent is 17%
First pulp slurry, adds methyl anyl alcohol, and magnetic separation removes impurity iron, and regulation liquid pH value, to 6.2~6.8, adds rosin amine and catches
Receive agent, wollastonite and diopside are floatingly selected, obtains the first flotation thing, then add water in the first flotation thing, be modulated into quality hundred
Proportion by subtraction is second pulp slurry of 20%~25%, adds dodecyl salt acid amide and tannic acid, is flotated by wollastonite, obtains the
Two flotation things, washing, dry;Wherein, the addition of dispersant is the 0.4% of wollastonite in powder total amount;The addition of rosin amine is silicon
The 0.05% of limestone flour total amount, addition is wollastonite in powder total amount the 0.5% of dodecyl salt acid amide, the addition of tannic acid is
The 0.05% of wollastonite in powder total amount.
After the present embodiment purification, the grade of wollastonite is 92.3%.
Claims (2)
1. the method for purification of a wollastonite, it is characterised in that with wollastonite mine as raw material, described wollastonite mine comprise wollastonite,
Quartz and diopside, wherein, the content of wollastonite is 56.2%~60.4%, and method of purification is:
Described wollastonite mine is pulverized, crosses 100 mesh~140 mesh molecular sieves, obtain wollastonite in powder, add water and make mass percent and be
First pulp slurry of 12%~17%, adds dispersant, and magnetic separation removes impurity iron, and regulation liquid pH value, to 6.2~6.8, adds pine
Fragrant amine makees collecting agent, wollastonite and diopside is floatingly selected, obtains the first flotation thing, then add water in the first flotation thing, modulation
The second pulp slurry becoming mass percent to be 20%~25%, adds dodecyl salt acid amide and tannic acid, is floatingly selected by wollastonite
Come, obtain the second flotation thing, washing, dry;Wherein, the addition of dispersant is the 0.2%~0.5% of wollastonite in powder total amount;Pine
Perfume addition is wollastonite in powder total amount 0.05%~the 0.1% of amine, the addition of dodecyl salt acid amide are wollastonite in powder total amount
0.1%~0.5%, the addition of tannic acid is the 0.02%~0.05% of wollastonite in powder total amount.
The method of purification of wollastonite the most according to claim 1, it is characterised in that described dispersant is sodium dialkyl sulfate
Or methyl anyl alcohol.
Priority Applications (1)
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CN201610684502.XA CN106216103A (en) | 2016-08-18 | 2016-08-18 | The method of purification of wollastonite |
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CN201610684502.XA CN106216103A (en) | 2016-08-18 | 2016-08-18 | The method of purification of wollastonite |
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CN201610684502.XA Pending CN106216103A (en) | 2016-08-18 | 2016-08-18 | The method of purification of wollastonite |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110743697A (en) * | 2019-10-29 | 2020-02-04 | 广东五岭硅灰石有限公司 | Selection method for recovering needle-shaped wollastonite from mixed ore |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1085469A (en) * | 1993-07-07 | 1994-04-20 | 武汉工业大学 | The method that the wollastonite sorting is purified |
RU2142348C1 (en) * | 1999-07-01 | 1999-12-10 | Акционерное общество закрытого типа "НПМ" | Method of dry concentration of wollastonite ore |
CN1826187A (en) * | 2003-08-08 | 2006-08-30 | 福丁有限公司 | Recovery process for high aspect ratio materials |
CN102239014A (en) * | 2009-04-17 | 2011-11-09 | 阿莱克希·亚利桑德罗维奇·诺萨切夫 | Method for the dry beneficiation of wollastonite ores |
CN102671757A (en) * | 2012-05-10 | 2012-09-19 | 湖北冯家山硅灰石纤维有限公司 | Method for purifying aedelforsite by pure physical process |
CN103691563A (en) * | 2013-12-11 | 2014-04-02 | 广西大学 | Flotation separation method for aedelforsite and quartz |
-
2016
- 2016-08-18 CN CN201610684502.XA patent/CN106216103A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN1085469A (en) * | 1993-07-07 | 1994-04-20 | 武汉工业大学 | The method that the wollastonite sorting is purified |
RU2142348C1 (en) * | 1999-07-01 | 1999-12-10 | Акционерное общество закрытого типа "НПМ" | Method of dry concentration of wollastonite ore |
CN1826187A (en) * | 2003-08-08 | 2006-08-30 | 福丁有限公司 | Recovery process for high aspect ratio materials |
CN102239014A (en) * | 2009-04-17 | 2011-11-09 | 阿莱克希·亚利桑德罗维奇·诺萨切夫 | Method for the dry beneficiation of wollastonite ores |
CN102671757A (en) * | 2012-05-10 | 2012-09-19 | 湖北冯家山硅灰石纤维有限公司 | Method for purifying aedelforsite by pure physical process |
CN103691563A (en) * | 2013-12-11 | 2014-04-02 | 广西大学 | Flotation separation method for aedelforsite and quartz |
Non-Patent Citations (4)
Title |
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张泾生等: "《矿用药剂》", 30 November 2008, 冶金工业出版社 * |
张银年等: ""硅灰石矿提纯新工艺研究"", 《矿产保护与利用》 * |
曹明礼等: ""硅灰石与透辉石的浮选分离研究"", 《非金属矿》 * |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110743697A (en) * | 2019-10-29 | 2020-02-04 | 广东五岭硅灰石有限公司 | Selection method for recovering needle-shaped wollastonite from mixed ore |
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Application publication date: 20161214 |