CN106833027A - A kind of improved silica production technology - Google Patents
A kind of improved silica production technology Download PDFInfo
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- CN106833027A CN106833027A CN201710041357.8A CN201710041357A CN106833027A CN 106833027 A CN106833027 A CN 106833027A CN 201710041357 A CN201710041357 A CN 201710041357A CN 106833027 A CN106833027 A CN 106833027A
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- completion
- proportioning
- stirred tank
- hard charcoal
- charcoal black
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/28—Compounds of silicon
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/006—Combinations of treatments provided for in groups C09C3/04 - C09C3/12
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/04—Physical treatment, e.g. grinding, treatment with ultrasonic vibrations
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/04—Physical treatment, e.g. grinding, treatment with ultrasonic vibrations
- C09C3/043—Drying, calcination
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/12—Treatment with organosilicon compounds
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Silicon Compounds (AREA)
Abstract
A kind of production technology of improved silica, step is:White carbon is matched with water,The ratio of white carbon and water is 1: 5,Stirred after the completion of proportioning to being uniformly dispersed,High-speed stirred is carried out in white carbon after the completion of proportioning is sent into stirred tank,Stirred tank speed is set to 200 revs/min,Temperature setting is 60 DEG C~70 DEG C in stirred tank,Hard charcoal black wash is obtained after the completion of stirring,Hard charcoal black wash and silane coupler are matched,The ratio of hard charcoal black wash and silane coupler is 1: 0.015,It is fed again into carrying out high-speed stirred in stirred tank after the completion of proportioning,Stirred tank speed is set to 200 revs/min,Temperature setting is 60 DEG C~70 DEG C in stirred tank,Hard charcoal black wash after being matched after the completion of stirring,Hard charcoal black wash after proportioning is carried out into filtering means dehydration,Hard charcoal black wash dehydration 50% after proportioning,Starched in half tide after the completion of dehydration,Half tide slurry feeding pulper is carried out into slurrying,Dryer is re-fed into after slurrying to be dried,Improved silica is obtained after drying.
Description
Technical field
The present invention relates to a kind of improved silica production technology.
Background technology
Silica is a kind of acidic oxide, and correspondence hyrate is silicic acid.Silica is the most important compound of silicon.
Native silicon dioxide present on the earth accounts for the 12% of earth crustal mass, and its existing forms has crystal type and unformed two major class,
It is referred to as silica.Also known as white carbon on silica industry, and it is widely used in the reinforcement of rubber for tire as reinforcing agent.Due to two
There is aggregation when rubber organic matter disperses and be inclined in silica inorganic salts, be difficult dispersion, cause silica inorganic salt and rubber
Organic matter is difficult to mutually melt, and time of fusion is long.
The content of the invention
The technical problem to be solved in the present invention is to overcome existing defect, there is provided a kind of production work of improved silica
Skill, to improve dispersiveness of the silica inorganic salt in rubber inorganic matter.
In order to solve the problems, such as appeal, the invention provides following technical scheme:
A kind of production technology of improved silica, step is as follows:
White carbon is matched with water, the ratio of white carbon and water is 1: 5, is stirred after the completion of proportioning to being uniformly dispersed,
High-speed stirred is carried out in white carbon after the completion of proportioning is sent into stirred tank, stirred tank speed is set to 200 revs/min, stirring
Temperature in the kettle is set to 60 DEG C~70 DEG C, and hard charcoal black wash is obtained after the completion of stirring, and hard charcoal black wash and silane coupler are matched somebody with somebody
Than the ratio of hard charcoal black wash and silane coupler is 1: 0.015, is fed again into carrying out high-speed stirring in stirred tank after the completion of proportioning
Mix, stirred tank speed is set to 200 revs/min, temperature setting is 60 DEG C~70 DEG C in stirred tank, after being matched after the completion of stirring
Hard charcoal black wash, filtering means dehydration is carried out by the hard charcoal black wash after proportioning, the hard charcoal black wash dehydration 50% after proportioning, is in after the completion of dehydration
Half tide is starched, and half tide slurry feeding pulper is carried out into slurrying, dryer is re-fed into after slurrying and is dried, and modified two are obtained after drying
Silica.
Improved silica obtained by the present invention has good compatibility and dispersiveness with rubber, greatly reduces two
The time of fusion of silica and rubber.
Specific embodiment
With reference to specific embodiment, the present invention is expanded on further.
Embodiment
A kind of production technology of silica, production technology is divided into four-stage to be carried out.
Step one, white carbon and water are matched, the ratio of white carbon and water is 1: 5, after the completion of proportioning stirring to point
Dissipate uniform.
Step 2, high-speed stirred will be carried out in the white carbon feeding stirred tank after the completion of proportioning, stirred tank speed is set
It it is 200 revs/min, temperature setting is 60 DEG C~70 DEG C in stirred tank, and hard charcoal black wash is obtained after the completion of stirring.
Step 3, hard charcoal black wash and silane coupler are matched, the ratio of hard charcoal black wash and silane coupler is 1:
0.015, it is fed again into carrying out high-speed stirred in stirred tank after the completion of proportioning, stirred tank speed is set to 200 revs/min, in stirred tank
Temperature setting is 60 DEG C~70 DEG C, the hard charcoal black wash after being matched after the completion of stirring.
Step 4, the hard charcoal black wash after proportioning is carried out into filtering means dehydration, the hard charcoal black wash dehydration 50% after proportioning has been dehydrated
Cheng Houcheng half tides are starched, and half tide slurry feeding pulper is carried out into slurrying, dryer is re-fed into after slurrying and is dried, and are obtained after drying
Improved silica.
Claims (1)
1. a kind of production technology of improved silica, step is as follows:
(1) white carbon is matched with water, the ratio of white carbon and water is 1: 5, is stirred after the completion of proportioning to being uniformly dispersed, will
High-speed stirred is carried out in white carbon feeding stirred tank after the completion of proportioning, stirred tank speed is set to 200 revs/min, stirred tank
Interior temperature setting is 60 DEG C~70 DEG C, and hard charcoal black wash is obtained after the completion of stirring;
(2) hard charcoal black wash and silane coupler are matched, hard charcoal black wash is 1 with the ratio of silane coupler:
0.015, it is fed again into carrying out high-speed stirred in stirred tank after the completion of proportioning, stirred tank speed is set to 200 revs/min, in stirred tank
Temperature setting is 60 DEG C~70 DEG C, and the hard charcoal black wash after being matched after the completion of stirring carried out the hard charcoal black wash after proportioning
Filter dehydration, the hard charcoal black wash dehydration 50% after proportioning, starches after the completion of dehydration in half tide, by half tide slurry feeding pulper system
Slurry, is re-fed into dryer and is dried after slurrying, improved silica is obtained after drying.
Priority Applications (1)
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CN201710041357.8A CN106833027A (en) | 2017-01-12 | 2017-01-12 | A kind of improved silica production technology |
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CN201710041357.8A CN106833027A (en) | 2017-01-12 | 2017-01-12 | A kind of improved silica production technology |
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CN106833027A true CN106833027A (en) | 2017-06-13 |
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CN201710041357.8A Pending CN106833027A (en) | 2017-01-12 | 2017-01-12 | A kind of improved silica production technology |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110282633A (en) * | 2019-04-29 | 2019-09-27 | 江苏辉迈粉体科技有限公司 | A kind of method of modifying of nano oxidized silicon materials |
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CN105860588A (en) * | 2015-01-21 | 2016-08-17 | 中国石油天然气股份有限公司 | Preparation method of modified white carbon black |
KR20160145402A (en) * | 2015-06-10 | 2016-12-20 | 동우전기 주식회사 | Synthesizing method for micro-silica treated with epoxy-terminated silicone, the micro-silica and the micro-silica composite |
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2017
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CN101497752A (en) * | 2008-01-31 | 2009-08-05 | 上海麦登复合材料有限公司 | Method for coupling modified silicon white powder and silane coupling agent |
CN101514263A (en) * | 2009-04-01 | 2009-08-26 | 苏州大学 | Modified white carbon black and preparation method thereof |
CN101775157A (en) * | 2010-01-04 | 2010-07-14 | 江南大学 | Preparation method of nano white carbon black for high dispersing rubber ingredient |
CN101798473A (en) * | 2010-02-10 | 2010-08-11 | 广州吉必盛科技实业有限公司 | Silane-modified white carbon black-carbon black composite filling and preparation method thereof |
CN101914190A (en) * | 2010-08-17 | 2010-12-15 | 浙江理工大学 | Preparation method of modified nano-silica monomer dispersion liquid |
CN101974256A (en) * | 2010-10-12 | 2011-02-16 | 江南大学 | Method for preparing highly-dispersed modified nano-white carbon black for rubber compound ingredients |
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CN104650624A (en) * | 2013-11-19 | 2015-05-27 | 青岛欧美亚橡胶工业有限公司 | White carbon black modification method |
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