CN106269273A - A kind of PPM level low ferrum glass sand floating agent - Google Patents
A kind of PPM level low ferrum glass sand floating agent Download PDFInfo
- Publication number
- CN106269273A CN106269273A CN201610639529.7A CN201610639529A CN106269273A CN 106269273 A CN106269273 A CN 106269273A CN 201610639529 A CN201610639529 A CN 201610639529A CN 106269273 A CN106269273 A CN 106269273A
- Authority
- CN
- China
- Prior art keywords
- floating agent
- quartz
- glass
- base
- quartz sand
- 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.)
- Pending
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
- B03D1/001—Flotation agents
- B03D1/004—Organic compounds
- B03D1/012—Organic compounds containing sulfur
Landscapes
- Glass Compositions (AREA)
Abstract
The present invention relates to a kind of PPM level low ferrum glass sand floating agent, it is characterised in that be made up of the raw material of following percentage by weight: mixed amine 20 55%, fatty acid 5 30%, diesel oil 20 50%.The floating agent that the present invention relates to, apply in flotation production line, particular/special requirement is not had to using temperature, need not original production line and production technology are improved, original quality according to purity quartzite raw material and production scene situation, grope through practice in process of production, find out the best-fit amount using this medicament, just can fast and effeciently realize the flotation of quartz sand, and then improve the output capacity of high-quality quartz sand, and the production cost of high-quality quartz sand can be substantially reduced, also reduce the labor intensity of operator.
Description
Technical field
The present invention relates to low iron-stone sand and purify field, generally refer to quartz sand in floatation process with the use of floating
Select medicament.It is specifically related to a kind of PPM level low ferrum glass sand floating agent.
Background technology
Glass sand generally refers to Si02Content 99.5%~99.999% silica flour, glass sand has fabulous
Chemical stability, high insulation voltage endurance capability and the extremely low coefficient of volume expansion, be photovoltaic glass, quartz glass, silica crucible, system
Make the primary raw material of silicon single crystal rod container.
China is one of country of enriching the most of quartz reserves, and exploitation utilizes quartz mine preferably to have Donghai Area, Jiangsu, Anhui
The ground such as Fengyang, Hong'an, Hubei, xiushui, Inner Mongol Wuhai, these quartz mine reserves are big, of high grade, easily exploit, but exploit at present
Most of quartz mines both function as and produce low-grade quartz ware: such as silicon powder, glass, refractory material, carborundum, ferrosilicon, molten
Melt quartz, quartz glass tube etc..
The domestic mineral resources that can be used for glass sand is a lot, but owing to processed means fall behind, product can not reach
The requirement of glass sand raw material, so that high grade ore is used as low-grade product, causes the serious waste of resource.
The domestic quartz raw material consumed that produces for quartz glass product of China, what the overwhelming majority produced is low and middle-grade products
Product, its medium-to-high grade electric light source quartz sand, silica crucible (polycrystalline, monocrystal silicon) quartz sand, quasiconductor and optical-fibre communications are used
Quartz raw material is still based on import quartz raw material.
In recent years, along with China's electronics and IT industry, the developing rapidly of electric light source industry, particularly solar photovoltaic industry
Growth, along with the fast development of domestic solar cell industry, it is contemplated that in the coming five years China's quartz glass industry will keep
The speed sustainable growth of more than 15-20%.
Producing high-quality quartz products, not only Technology wants advanced person, requires the highest to material purity.Present stage China
Produce the raw material Duo Shi import U.S. UNIMIN(You Niming of high purity quartz) glass sand of company, although its raw materials quality
Good, but price goes up again and again.Therefore improve quartz products quality and yield, promote the industrial development of HIGH-PURITY SILICON material, reach
High-end quartz raw material domesticizes, and is the instant thing of high purity quartz raw material production enterprise of China.
The prescription of PPM level low ferrum glass sand is the strictest, it is desirable to chemical analysis: SiO2(99.5%~
99.999%) , Fe2O3(1PPM~100PPM).In order to high efficiency, low cost produces satisfactory PPM level low ferrum high purity quartz
Sand, needs to set up floatation process production line, and with the use of the floating wash agent of high-efficiency low-pollution.
Glass sand is the primary raw material of quartz glass.Quartz glass is become " glass king " by people, because it has
A series of special physics, chemical property.It has excellent resistance to elevated temperatures, and temperature tolerance is up to 1100 ~ 1200 DEG C, and ratio is commonly
Glass is high 800 DEG C, and its fusing point is close with the fusing point of platinum (platinum).Coefficient of thermal expansion is minimum, and the evenly heat between 0~1000c is swollen
Swollen coefficient a-5.4 × 10-7, is equivalent to the 1/6 of pottery, is equivalent to the 1/20 of simple glass, mixes a certain amount of in quartz glass
Titanium, quartz glass have splendid spectral characteristic ' be possible not only to through visible ray, and infrared ray, ultraviolet can be passed through.Stone
English glass is good acid resisting material, is equivalent to 30 times of acid-proof ceramics, is equivalent to 150 times of rustless steel (nichrome).Stone
English glass is fabulous electrically insulating material, and its resistance is equivalent to 10,000 times of simple glass, and when 20 DEG C, resistivity is 1018 Q.
Cm, dielectric strength is 250KV/cm, and vacuum is up to (10-6Mpa).Because it is high temperature resistant, light transmission is good, good leak tightness, it is novel
The optimal material of electric light source, is also the optimal material manufacturing integrated circuit.
The major product of quartz glass includes: large scale integrated circuit high-purity high temperature resistant quartz glass tube, arc process stone
English crucible (solar level and semiconductor grade), optical communication quartz glass, electric light source quartz glass.All trades and professions are nearly all used
To quartz glass, but because of quartz glass product complex process, cost of material is expensive, and the price causing quartz glass is the most expensive, constrains
Being widely used of quartz glass.
Summary of the invention
It is an object of the invention to provide the floating agent of a kind of quartz, use in flotation produces, can significantly carry
Rise the quality of quartz sand, produce the low ferrum glass sand of high-quality, low cost, meet the demand in market.
In order to achieve the above object, in research process, select suitable chemical substance, through appropriate proportioning, allow it
Biochemical reaction, obtains the floating agent containing all kinds of materials, and these materials react with ore pulp, reaches to be greatly reduced refined
Iron content in quartz sand, final production goes out PPM level low ferrum glass sand, Fe2O3(1PPM~100PPM).
Main component and content after the appropriate application proportioning of the component of floating agent, each component, proportioning, in detail
As follows:
1, the material of producing of floating agent is constituted and application proportioning:
Sequence number | Component | Each component application proportioning (percentage by weight) |
1 | Mixed amine | 20 - 55% |
2 | Fatty acid | 5 - 30% |
3 | Diesel oil | 20 - 50% |
2, the final material composition of the floating agent (percentage by weight) obtained after proportioning:
Sequence number | Material title | Content (%) |
1 | Dodecane-1-amine | 4.2~5.5 |
2 | Azophenlyene-2,3-diamidogen | 55~60 |
3 | Heptadecane | 0.02~0.04 |
4 | Stearmide | 0.07~0.09 |
5 | (E)-5-((5-benzofurane-2-base) methylene) furan-2 (5H)-one | 14~18 |
6 | Two (4-isocyanatophenyl) methane | 2~2.4 |
7 | (E)-N-(4-(3-carbonyl-3-(pyridine-2-base) acrylate-1-thiazolinyl) phenyl) acetamide | 3~4.5 |
8 | N-(1-isopropyl-1H-pyrazoles-4-base)-2-(4-nitro-1H-pyrazol-1-yl) acetamide | 2.5~4.5 |
9 | (13R,14S)-13-ethyl-3-methoxyl group-12,13,15,16-tetrahydrochysene-11H-cyclopenta [a] luxuriant and rich with fragrance-17 (14H)-one | 0.3~0.6 |
10 | Naphtho-[7,8,1,2,3-nopqr] four sweet smell-6,12-diketone | 2.2~3.2 |
11 | 7,7'-methylene two (2-methyl-4H-benzo [d] [1,3] piperazine-4-ketone) | 4~7 |
12 | Docosyl amine | 1.3~1.9 |
13 | 8-(acrylate-1-alkene-2-base)-2H-furo [2,3-h] chromen-2-one | 0.5~0.8 |
Beneficial effects of the present invention: the floating agent that the present invention relates to, applies in flotation production line, does not has spy to using temperature
Different requirement, it is not necessary to original production line and production technology are improved, according to original quality and the life of purity quartzite raw material
Produce field condition, grope through practice in process of production, find out the best-fit amount using this medicament, it becomes possible to fast and effeciently
Realize the flotation of quartz sand, and then the output capacity of raising high-quality quartz sand, and the life of high-quality quartz sand can be substantially reduced
Produce cost, also reduce the labor intensity of operator.
Detailed description of the invention
Embodiment 1
1, preparation floating agent
The PPM level low ferrum glass sand floating agent that the present invention relates to, is made into by following percentage by weight: mixed amine 20%,
Fatty acid 30%, diesel oil 50%, after mix homogeneously, preparation obtains floating agent, and the finished product after preparation is by following percentage by weight structure
Become:
Dodecane-1-amine 5.5%,
Azophenlyene-2,3-diamidogen 60%,
Heptadecane 0.02%,
Stearmide 0.07%,
(E)-5-((5-benzofurane-2-base) methylene) furan-2 (5H)-one 16.5%,
Two (4-isocyanatophenyl) methane 2.25%,
(E)-N-(4-(3-carbonyl-3-(pyridine-2-base) acrylate-1-thiazolinyl) phenyl) acetamide 4.25%,
N-(1-isopropyl-1H-pyrazoles-4-base)-2-(4-nitro-1H-pyrazol-1-yl) acetamide 2.65%,
(13R,14S)-13-ethyl-3-methoxyl group-12,13,15,16-tetrahydrochysene-11H-cyclopenta [a] luxuriant and rich with fragrance-17 (14H)-
Ketone 0.3%,
Naphtho-[7,8,1,2,3-nopqr] four sweet smell-6,12-diketone 2.2%,
7,7'-methylene two (2-methyl-4H-benzo [d] [1,3] piperazine-4-ketone) 4.25%,
Docosyl amine 1.45%,
8-(acrylate-1-alkene-2-base)-2H-furo [2,3-h] chromen-2-one 0.56%.
2, flow process is used
Through the batcher of measuring fixed amount, quartz sand is input to agitator, floating agent is added by quartz sand per ton the amount of 2kg
Joining in agitator, export and be inflated flotation in flotation device after stirring two minutes, impurity, with form of foam emersion, purifies
After quartz sand export warehouse and be dehydrated, the medicament water containing floating agent enters tank precipitation Posterior circle and makes in the process
With.
3, the quartz sand composition after flotation
Quartz sand output capacity reaches 96%, after testing the composition of quartz sand: SiO2 99.8%,FeO3 30PPM。
Embodiment 2
1, preparation floating agent
The PPM level low ferrum glass sand floating agent that the present invention relates to, is made into by following percentage by weight: mixed amine 40%,
Fatty acid 30%, diesel oil 30%, after mix homogeneously, preparation obtains floating agent,
Finished product after preparation is made up of following percentage by weight:
Dodecane-1-amine 5.225%,
Azophenlyene-2,3-diamidogen 57.031%,
Heptadecane 0.037%,
Stearmide 0.079%,
(E)-5-((5-benzofurane-2-base) methylene) furan-2 (5H)-one 16.095%,
Two (4-isocyanatophenyl) methane 2.252%,
(E)-N-(4-(3-carbonyl-3-(pyridine-2-base) acrylate-1-thiazolinyl) phenyl) acetamide 4.069%,
N-(1-isopropyl-1H-pyrazoles-4-base)-2-(4-nitro-1H-pyrazol-1-yl) acetamide 3.912%,
(13R,14S)-13-ethyl-3-methoxyl group-12,13,15,16-tetrahydrochysene-11H-cyclopenta [a] luxuriant and rich with fragrance-17 (14H)-
Ketone 0.496%,
Naphtho-[7,8,1,2,3-nopqr] four sweet smell-6,12-diketone 2.723%,
7,7'-methylene two (2-methyl-4H-benzo [d] [1,3] piperazine-4-ketone) 5.785%,
Docosyl amine 1.624%,
8-(acrylate-1-alkene-2-base)-2H-furo [2,3-h] chromen-2-one 0.672%.
2, flow process is used
Through the batcher of measuring fixed amount, quartz sand is input to agitator, floating agent is added 2.5kg's by quartz sand per ton
Amount joins in agitator, exports and be inflated flotation in flotation device after stirring two minutes, and impurity, with form of foam emersion, carries
Quartz sand after pure exports warehouse and is dehydrated, and the medicament water entrance tank precipitation Posterior circle containing floating agent makes in the process
With.
3, the quartz sand composition after flotation
Quartz sand output capacity reaches 95%, after testing the composition of quartz sand: SiO2 99.97%,FeO3 5PPM。
Embodiment 3
1, preparation floating agent
The PPM level low ferrum glass sand floating agent that the present invention relates to, is made into by following percentage by weight: mixed amine 55%,
Fatty acid 5%, diesel oil 40%, after mix homogeneously, preparation obtains floating agent,
Finished product after preparation is made up of following percentage by weight:
Dodecane-1-amine 4.22%,
Azophenlyene-2,3-diamidogen 57.5%,
Heptadecane 0.04%,
Stearmide 0.09%,
(E)-5-((5-benzofurane-2-base) methylene) furan-2 (5H)-one 14.52%,
Two (4-isocyanatophenyl) methane 2.38%,
(E)-N-(4-(3-carbonyl-3-(pyridine-2-base) acrylate-1-thiazolinyl) phenyl) acetamide 3.27%,
N-(1-isopropyl-1H-pyrazoles-4-base)-2-(4-nitro-1H-pyrazol-1-yl) acetamide 4.5%,
(13R,14S)-13-ethyl-3-methoxyl group-12,13,15,16-tetrahydrochysene-11H-cyclopenta [a] luxuriant and rich with fragrance-17 (14H)-
Ketone 0.6%,
Naphtho-[7,8,1,2,3-nopqr] four sweet smell-6,12-diketone 3.2%,
7,7'-methylene two (2-methyl-4H-benzo [d] [1,3] piperazine-4-ketone) 6.98%,
Docosyl amine 1.9%,
8-(acrylate-1-alkene-2-base)-2H-furo [2,3-h] chromen-2-one 0.8%.
2, flow process is used
Through the batcher of measuring fixed amount, quartz sand is input to agitator, floating agent is added 3kg's by quartz fine sand per ton
Amount joins in agitator, exports and be inflated flotation in flotation device after stirring two minutes, and impurity, with form of foam emersion, carries
Quartz sand after pure exports warehouse and is dehydrated, and the medicament water entrance tank precipitation Posterior circle containing floating agent makes in the process
With.
3, the quartz sand composition after flotation
Quartz sand output capacity reaches 91%, after testing the composition of quartz sand: SiO2 99.95%,FeO3 1PPM。
Claims (2)
1. a PPM level low ferrum glass sand floating agent, it is characterised in that be made up of the raw material of following percentage by weight:
Mixed amine 20-55%
Fatty acid 5-30%
Diesel oil 20-50%.
A kind of PPM level low ferrum glass sand floating agent the most according to claim 1, it is characterised in that manufactured goods by
The material composition of following percentage by weight is constituted:
Dodecane-1-amine 4.2 ~ 5.5%,
Azophenlyene-2,3-diamidogen 55 ~ 60%,
Heptadecane 0.02 ~ 0.04%,
Stearmide 0.07 ~ 0.09%,
(E)-5-((5-benzofurane-2-base) methylene) furan-2 (5H)-one 14 ~ 18%,
Two (4-isocyanatophenyl) methane 2 ~ 2.4%,
(E)-N-(4-(3-carbonyl-3-(pyridine-2-base) acrylate-1-thiazolinyl) phenyl) acetamide 3 ~ 4.5%,
N-(1-isopropyl-1H-pyrazoles-4-base)-2-(4-nitro-1H-pyrazol-1-yl) acetamide 2.5 ~ 4.5%,
(13R,14S)-13-ethyl-3-methoxyl group-12,13,15,16-tetrahydrochysene-11H-cyclopenta [a] luxuriant and rich with fragrance-17 (14H)-
Ketone 0.3 ~ 0.6%,
Naphtho-[7,8,1,2,3-nopqr] four sweet smell-6,12-diketone 2.2 ~ 3.2%,
7,7'-methylene two (2-methyl-4H-benzo [d] [1,3] piperazine-4-ketone) 4 ~ 7%,
Docosyl amine 1.3 ~ 1.9%,
8-(acrylate-1-alkene-2-base)-2H-furo [2,3-h] chromen-2-one 0.5 ~ 0.8%.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610639529.7A CN106269273A (en) | 2016-08-08 | 2016-08-08 | A kind of PPM level low ferrum glass sand floating agent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201610639529.7A CN106269273A (en) | 2016-08-08 | 2016-08-08 | A kind of PPM level low ferrum glass sand floating agent |
Publications (1)
Publication Number | Publication Date |
---|---|
CN106269273A true CN106269273A (en) | 2017-01-04 |
Family
ID=57666121
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201610639529.7A Pending CN106269273A (en) | 2016-08-08 | 2016-08-08 | A kind of PPM level low ferrum glass sand floating agent |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN106269273A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107377229A (en) * | 2017-09-29 | 2017-11-24 | 江苏闽江矿业有限公司 | A kind of silica sand method for floating |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4136020A (en) * | 1976-11-11 | 1979-01-23 | Minerec Corporation | Flotation reagent and process |
CN1027141C (en) * | 1991-11-21 | 1994-12-28 | 山东省栖霞县选矿药剂厂 | Production process of bar or granular xanthate |
JP2015010246A (en) * | 2013-06-27 | 2015-01-19 | 株式会社神戸製鋼所 | Production method of low sulfur iron ore |
CN104923385A (en) * | 2015-05-21 | 2015-09-23 | 河北钢铁股份有限公司承德分公司 | Production method of low-silicon low-sulfur titanium concentrates |
CN105327785A (en) * | 2015-11-16 | 2016-02-17 | 合肥万泉非金属矿科技有限公司 | Flotation technology of PPM level low-iron high-purity quartz sand |
-
2016
- 2016-08-08 CN CN201610639529.7A patent/CN106269273A/en active Pending
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4136020A (en) * | 1976-11-11 | 1979-01-23 | Minerec Corporation | Flotation reagent and process |
CN1027141C (en) * | 1991-11-21 | 1994-12-28 | 山东省栖霞县选矿药剂厂 | Production process of bar or granular xanthate |
JP2015010246A (en) * | 2013-06-27 | 2015-01-19 | 株式会社神戸製鋼所 | Production method of low sulfur iron ore |
CN104923385A (en) * | 2015-05-21 | 2015-09-23 | 河北钢铁股份有限公司承德分公司 | Production method of low-silicon low-sulfur titanium concentrates |
CN105327785A (en) * | 2015-11-16 | 2016-02-17 | 合肥万泉非金属矿科技有限公司 | Flotation technology of PPM level low-iron high-purity quartz sand |
Non-Patent Citations (1)
Title |
---|
张闿: "《浮选药剂的组合使用》", 31 August 1994, 北京:冶金工业出版社 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107377229A (en) * | 2017-09-29 | 2017-11-24 | 江苏闽江矿业有限公司 | A kind of silica sand method for floating |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101948235B (en) | Method for preparing high-purity quartz sand | |
CN101759364B (en) | Manufacturing method of medical high white material molded glass bottle | |
CN102897993A (en) | Method for preparing high-purity quartz sands by using natural vein quartz ores | |
CN101696087A (en) | Black micro-crystalline glass plate made of gold ore tailings and manufacturing method thereof | |
CN104692808B (en) | A kind of additive and method for reducing ceramic firing temperature | |
CN102180584A (en) | Method for removing gas-liquid inclusion and impurity during high-purity quartz sand production | |
CN109020523A (en) | A kind of low iron ultrawhite fused quartz ceramic crucible preparation method | |
CN106746637A (en) | A kind of production method of low oxyhydroxide and rear-earth-doped quartz ampoule | |
CN106269273A (en) | A kind of PPM level low ferrum glass sand floating agent | |
CN107759229A (en) | A kind of preparation method for the high-purity anaerobic crucible of polycrystalline cast ingot | |
CN106316134B (en) | A kind of diopside and feldspar principal crystalline phase devitrified glass and preparation method thereof | |
CN103232164A (en) | Coffee microcrystal glass plate and production method thereof | |
CN105399330B (en) | A kind of titanium white fritted glaze and preparation method thereof | |
CN103359918A (en) | Crucible and preparation method thereof | |
CN103030405B (en) | Control method for firing high-performance quartz ceramic | |
CN105502937A (en) | Preparation method of high-purity chalcogenide infrared glass | |
CN107601861A (en) | A kind of high transmittance photovoltaic rolled glass formula | |
CN102964063B (en) | Semi-opaque material skyblue winebottle and technology for producing same | |
CN102951841A (en) | Preparation method of high borosilicate glass for solar photovoltaic batteries | |
CN104445963A (en) | Method for preparing glass fiber from smelting blast furnace slag | |
CN102351403B (en) | Method for preparing ultrafine glass powder used for solar battery slurry | |
CN101823902B (en) | Environmental-protection green enamel and production method thereof | |
CN105236741B (en) | A kind of boron split-phase zirconium white frit high and preparation method thereof | |
CN105417956B (en) | The method that microlite is manufactured with tailings of high silicon iron | |
CN103950943B (en) | Molybdic tailing is utilized to prepare fluorophlogopite and method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170104 |
|
RJ01 | Rejection of invention patent application after publication |