CN1621374A - Process for preparing ultra-fine, high purity and high whiteness quartz powder - Google Patents

Process for preparing ultra-fine, high purity and high whiteness quartz powder Download PDF

Info

Publication number
CN1621374A
CN1621374A CN 200310110583 CN200310110583A CN1621374A CN 1621374 A CN1621374 A CN 1621374A CN 200310110583 CN200310110583 CN 200310110583 CN 200310110583 A CN200310110583 A CN 200310110583A CN 1621374 A CN1621374 A CN 1621374A
Authority
CN
China
Prior art keywords
carried out
add
kilogram
filter cake
handle
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.)
Granted
Application number
CN 200310110583
Other languages
Chinese (zh)
Other versions
CN1255346C (en
Inventor
尹荔松
周克省
黄生祥
周良玉
孔德明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Central South University
Original Assignee
Central South University
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Central South University filed Critical Central South University
Priority to CN 200310110583 priority Critical patent/CN1255346C/en
Publication of CN1621374A publication Critical patent/CN1621374A/en
Application granted granted Critical
Publication of CN1255346C publication Critical patent/CN1255346C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Silicon Compounds (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The present invention relates to chemical material, and is the preparation process of superfine high whiteness quartz powder. The preparation process includes the steps of: depurating quartz mineral; crushing and grinding in a SW-3000 wet grinding instrument for 1-1.5 hr while adding sodium dodecyl benzene sulfonate as surface modifier; filtering in a press filter; and drying and grading the filter cake in a XQ-4 powerful drying equipment at inlet temperature of 270 deg.c and outlet temperature of 160-180 deg.c to obtain the product powder with water content less than 1 %, size of 6000 mesh and whiteness of 97 %. The product may be used to replace expensive titanium dioxide powder as excellent stuffing for point, rubber and plastic and has also wide application in electronic and ceramic fields.

Description

The preparation method of the high whiteness silica powder of a kind of ultra-fine high purity
Technical field:
The present invention relates to chemical material field, is to utilize the flint mineral to prepare the method for the high whiteness silica powder of ultra-fine high purity.
Background technology:
The quartzy reserves of China are very abundant, but the quartzy product shortage of the high whiteness of high pure and ultra-fine, and industries such as coating, electronics, pottery are badly in need of in a large number.
Summary of the invention:
The objective of the invention is to make full use of abundant quartzy Mineral resources, a kind of method of utilizing quartzy raw ore for feedstock production ultra-fine high-brightness quartz is provided.Quartzy product pellet-2 μ the m of this method preparation is greater than 99%, whiteness reaches more than 97%, and is the same with the high-quality titanium dioxide, can replace expensive titanium dioxide, become fine paint filler, loading material of rubber, plastic filler, have a wide range of applications in fields such as electronics, potteries.
Technical scheme of the present invention:
At first quartzy raw ore is carried out removal of impurities and handle, promptly take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, adds 0.4~1 kilogram of vat powder and 1~4 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h~1.5h, realize the removal of impurities processing;
Then mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h~1.5h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, utilize filtering equipment that it is filtered as surface-modifying agent;
Then filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the content of the powder that obtains is less than 1%, and particle size is 6000 orders, and whiteness is greater than 97% product.
Advantage of the present invention and positively effect are embodied in:
The particle index of product reaches 99% for-2 μ m, and-1 μ m reaches 95%; The whiteness of product is higher than 97%, replaces expensive titanium dioxide, becomes fine paint filler, loading material of rubber, plastic filler, has a wide range of applications in fields such as electronics, potteries.
Embodiment:
Be described further below in conjunction with embodiment.
Embodiment 1
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
Embodiment 2
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 1 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
Embodiment 3
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 4 liters of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
Embodiment 4
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 180 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
Embodiment 5
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1.5h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
Embodiment 6
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 3 liters of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1.5h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.

Claims (7)

1. the preparation method of the high whiteness quartz of ultra-fine high purity is characterized in that:
At first quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, adding 0.4-1 kilogram vat powder and 1-4, to rise concentration be 98% sulfuric acid, at room temperature stirs 1-1.5h.
Then mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1-1.5h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, utilize filtering equipment that it is filtered as surface-modifying agent;
Then filter cake is carried out drying treatment, using XQ-4 type strong drying equipment that filter cake is carried out dry classification handles, the equipment entrance temperature is 270 ℃, and temperature out is 160-180 ℃, and the water content of the powder that obtains is 6000 order whiteness greater than 97% product less than 1% particle size.
2. the preparation method of the high whiteness quartz of ultra-fine high purity according to claim 1 is characterized in that:
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
3. the preparation method of the high whiteness quartz of ultra-fine high purity according to claim 2 is characterized in that:
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 1 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
4. the preparation method of the high whiteness quartz of ultra-fine high purity according to claim 3 is characterized in that:
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 4 liters of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
5. the preparation method of the high whiteness quartz of ultra-fine high purity according to claim 4 is characterized in that:
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 180 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
6. the preparation method of the high whiteness quartz of ultra-fine high purity according to claim 5 is characterized in that:
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 1 liter of concentration and be 98% sulfuric acid, at room temperature stir 1.5h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
7. the preparation method of the high whiteness quartz of ultra-fine high purity according to claim 6 is characterized in that:
1. quartzy raw ore is carried out removal of impurities and handle, take by weighing 1 ton in quartzy raw ore and add 1000 premium on currency and be made into slurries, add 0.4 kilogram of vat powder and 3 liters of concentration and be 98% sulfuric acid, at room temperature stir 1h, promptly realized the removal of impurities processing.
2. mineral are carried out pulverization process, use SW-3000 type wet grinding instrument, in above-mentioned slurries suction beveller, grind 1.5h, add 1 kilogram of ten disulfo acid sodium in the process of lapping, use filtering equipment that it is filtered as surface-modifying agent.
3. filter cake is carried out drying treatment, use XQ-4 type strong drying equipment that filter cake is carried out dry classification and handle, the equipment entrance temperature is 270 ℃, temperature out is 160 ℃, the water content of the powder that obtains is less than 1%, particle size 6000 orders, and whiteness is greater than 97% product.
CN 200310110583 2003-11-28 2003-11-28 Process for preparing ultra-fine, high purity and high whiteness quartz powder Expired - Fee Related CN1255346C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200310110583 CN1255346C (en) 2003-11-28 2003-11-28 Process for preparing ultra-fine, high purity and high whiteness quartz powder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200310110583 CN1255346C (en) 2003-11-28 2003-11-28 Process for preparing ultra-fine, high purity and high whiteness quartz powder

Publications (2)

Publication Number Publication Date
CN1621374A true CN1621374A (en) 2005-06-01
CN1255346C CN1255346C (en) 2006-05-10

Family

ID=34759168

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200310110583 Expired - Fee Related CN1255346C (en) 2003-11-28 2003-11-28 Process for preparing ultra-fine, high purity and high whiteness quartz powder

Country Status (1)

Country Link
CN (1) CN1255346C (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101215074B (en) * 2008-01-17 2010-12-15 徐传龙 Production technique for drawing crystal powder used for low-hydroxyl quartz glass soft pipe and pipe drawing method
CN101481203B (en) * 2009-02-19 2011-03-02 申士富 Preparation of fused silica material
CN103804958A (en) * 2013-06-27 2014-05-21 上海那博新材料科技有限公司 Active nanoscale monocrystal silicon dioxide

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101215074B (en) * 2008-01-17 2010-12-15 徐传龙 Production technique for drawing crystal powder used for low-hydroxyl quartz glass soft pipe and pipe drawing method
CN101481203B (en) * 2009-02-19 2011-03-02 申士富 Preparation of fused silica material
CN103804958A (en) * 2013-06-27 2014-05-21 上海那博新材料科技有限公司 Active nanoscale monocrystal silicon dioxide
CN103804958B (en) * 2013-06-27 2015-11-18 上海那博新材料科技有限公司 A kind of active nano level monocrystalline silicon-dioxide

Also Published As

Publication number Publication date
CN1255346C (en) 2006-05-10

Similar Documents

Publication Publication Date Title
CN1724595A (en) White minera powder TiO2 composite white pigment and its preparation method
CN1709985A (en) Method for producing iron oxide black
WO2010078821A1 (en) Method for preparing subsphaeroidal barium sulfate by sulfuric acid process and its use in copper foil substrate
WO2022057227A1 (en) Illite, preparation method therefor and use thereof
CN106395839B (en) A kind of technique preparing electrophoretic paint calcined kaolin with gangue
CN110451510A (en) A kind of silicon carbide processing method
CN1250654C (en) Nanometer kaolinite powder and preparing method thereof
CN112850761A (en) Preparation process of ultralow-sodium alumina and ultralow-sodium alumina
CN1151893C (en) Pollution-free gas-phase oxidation separation purification method for artificial diamond
CN1165488C (en) Continuous non-polluting liquid phase titanium dioxide process
CN108394903B (en) Preparation method of nano-scale silicon carbide micro powder
CN1255346C (en) Process for preparing ultra-fine, high purity and high whiteness quartz powder
CN1228247C (en) Process for producing super fine barium sulfate and calcium carbonate using chloralkali salt mud
CN109665536A (en) The method of purification of recessed soil
CN1522957A (en) Production method for ultra-fine silicon micronized quartz powder
CN1704374A (en) Process for preparing high-purity superthin high-whiteness kaolin
CN1231415C (en) Preparation method of boron carbide ultramicropowder
CN110921805B (en) Attapulgite clay reduction-magnetic separation coupling continuous iron removal whitening purification method
CN1657409A (en) Method for preparing high-purity ultrnfine silicone powder and aluminium sulphate using kadin as raw material
CN108793265A (en) A kind of new process of titanium powder industry waste acid concentration acid sludge production feed grade ferrous sulfate monohydrate
CN1022558C (en) Method for separating ultrafine iron oxide from waste mother liquor from rutile production by dilute hydrochloric acid
CN114162875A (en) Preparation method and preparation device of ferrous sulfate solution for iron oxide pigment and iron oxide pigment
CN112871434B (en) Method for sorting nano sepiolite
CN114031091B (en) Method for extracting kaolin by using machine-made sand tailings
CN114715949B (en) Processing technology of natural jarosite mineral pigment

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C19 Lapse of patent right due to non-payment of the annual fee
CF01 Termination of patent right due to non-payment of annual fee