CN107021495A - A kind of preparation method of the rubber high reinforcing silica of high oil absorption - Google Patents

A kind of preparation method of the rubber high reinforcing silica of high oil absorption Download PDF

Info

Publication number
CN107021495A
CN107021495A CN201710287776.XA CN201710287776A CN107021495A CN 107021495 A CN107021495 A CN 107021495A CN 201710287776 A CN201710287776 A CN 201710287776A CN 107021495 A CN107021495 A CN 107021495A
Authority
CN
China
Prior art keywords
preparation
oil absorption
rubber
stirring
reinforcing silica
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
Application number
CN201710287776.XA
Other languages
Chinese (zh)
Inventor
万火平
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.)
FUJIAN SANMING JUFENG CHEMICAL Co Ltd
Original Assignee
FUJIAN SANMING JUFENG CHEMICAL Co Ltd
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 FUJIAN SANMING JUFENG CHEMICAL Co Ltd filed Critical FUJIAN SANMING JUFENG CHEMICAL Co Ltd
Priority to CN201710287776.XA priority Critical patent/CN107021495A/en
Publication of CN107021495A publication Critical patent/CN107021495A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B33/00Silicon; Compounds thereof
    • C01B33/113Silicon oxides; Hydrates thereof
    • C01B33/12Silica; Hydrates thereof, e.g. lepidoic silicic acid
    • C01B33/14Colloidal silica, e.g. dispersions, gels, sols
    • C01B33/141Preparation of hydrosols or aqueous dispersions
    • C01B33/142Preparation of hydrosols or aqueous dispersions by acidic treatment of silicates
    • C01B33/143Preparation of hydrosols or aqueous dispersions by acidic treatment of silicates of aqueous solutions of silicates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08KUse of inorganic or non-macromolecular organic substances as compounding ingredients
    • C08K3/00Use of inorganic substances as compounding ingredients
    • C08K3/34Silicon-containing compounds
    • C08K3/36Silica
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01PINDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
    • C01P2006/00Physical properties of inorganic compounds
    • C01P2006/12Surface area

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Dispersion Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Silicon Compounds (AREA)

Abstract

The invention discloses a kind of preparation method of rubber with the high reinforcing silica of high oil absorption, the first accurate formulation waterglass in make-up tank;Enter reactor from change a job skill hot water, the glass that adds water from refinery pit of warm water tank again, be warming up to 60 DEG C;While stirred on one side toward sulfuric acid and dilution water is added in reactor, stop stirring and be aged 30 minutes after pH is controlled between 6.5 ~ 7.0;Start stirring, while starting cocurrent when being warming up to 85 DEG C;First adduction flowing water glass then adds between sulfuric acid, control ph 9.5 ~ 10.5 at 9 ~ 10 to pH value;Cocurrent does not stop stirring after terminating, be acidified after adding sulfuric acid and dilution water progress, between terminal point control pH value 4.8 5.3;Ageing stirring reaction in 20 minutes terminates.The characteristics of there is Gao Bibiao, high oil absorption by silica made from the preparation method, and burning decrement is low, pH value is high, the cure time of rubber is shortened more than 50%, greatly improves processing efficiency.

Description

A kind of preparation method of the rubber high reinforcing silica of high oil absorption
Technical field
The invention belongs to chemical field, and in particular to a kind of preparation side of rubber high reinforcing silica of high oil absorption Method.
Background technology
Precipitated silica is commonly called as white carbon, also known as silicate hydrate, light silicon dioxide, and chemical expression can be written generally as MSiO2nH2O, outward appearance is amorphous powder, the microballon of white high degree of dispersion.Precipitated silica is widely used in rubber system All multirows such as product, tire, feed addictive, food additives, paint delustering agent, papermaking, silicon rubber, toothpaste abrasives, ink Industry.
Silica is used in rubber applications as excellent reinforcing agent and filler, can greatly improve the physics of sizing material Performance, reduces sizing material delayed.Silica can reduce tire drag in tire industry, while it is anti-slippery not lose its Property, silica-filled sizing material is compared with the sizing material that ordinary carbon black is filled, and rolling resistance can reduce by 30%.
But it is single in terms of the reinforcing rubber effect for, the reinforcement ability of silica needs raising badly.
The content of the invention
The present invention is intended to provide a kind of preparation method of the rubber silica with high reinforcing property.
The preparation method of the high reinforcing silica of rubber high oil absorption comprises the following steps:
S1, accurate formulation concentration of sodium silicate is to 0.995 ~ 1.005 mol/l in make-up tank, and temperature control is in 25 ~ 50 DEG C of degree;
S2, the skill hot water 30m3 that changes a job from warm water tank, the glass 3.5m3 that adds water from refinery pit enter reactor, 60 DEG C are warming up to, by bottom liquid Concentration is adjusted between 0.100 ~ 0.105 mol/l;
S3, step acidifying:While toward addition sulfuric acid and dilution water in reactor while stirring, pH is controlled between 6.5 ~ 7.0 After stop stirring and be aged 30 minutes;
S4, start stirring, while starting cocurrent when being warming up to 85 DEG C;First adduction flowing water glass then adds sulphur at 9 ~ 10 to pH value Between acid, control ph 9.5 ~ 10.5;
S5, rear acidifying:Cocurrent does not stop stirring after terminating, be acidified after adding sulfuric acid and dilution water progress, terminal point control pH value 4.8- 5.3 between;
S6, ageing stirring reaction in 20 minutes terminate.
Further, first reactor is cleaned before step S2, makes it without wall dirt.
Preferably, step S3 is into step S5, and sour flow rate is 0.50 m3/h, and dilution water flow rate is 3.5 m3/h.
Preferably, in step S4, waterglass flow rate is 12.6 m3/h, stirring and 50 minutes cocurrent used times.
In step S3, jelly must occur after stopping stirring.
In step S4, the heating-up time is controlled at 30 minutes or so.
Preferably, concentration >=98% of sulfuric acid.
Pass through dioxide-containing silica made from the preparation method(w%) ≥ 98.5%;Burning decrement(w%)For 3.2 ~ 4.2; Specific surface area(BET)(m2/g) it is 230 ~ 260;Loss on drying(w%)For 5.0 ~ 7.0;Oil factor(DBP absorption values)(ml/g)For 3.2~3.8;The characteristics of having Gao Bibiao, high oil absorption because of it, makes it have in rubber high reinforcing, and other physical property are also Do not reduce;Meanwhile, the characteristics of its burning decrement is low, pH value is high make its apply rubber or tire cure time shorten 50% with On, it is greatly improved processing efficiency.
Embodiment
To make the object, technical solutions and advantages of the present invention clearer, further is made to embodiment of the present invention below It is described in detail on ground.
The present invention provides a kind of preparation method of the high reinforcing silica of rubber high oil absorption and comprised the following steps:
S1, accurate formulation concentration of sodium silicate is to 0.995 ~ 1.005 mol/l in make-up tank, and temperature control is in 25 ~ 50 DEG C of degree;
S2, the skill hot water 30m3 that changes a job from warm water tank, the glass 3.5m3 that adds water from refinery pit enter reactor, 60 DEG C are warming up to, by bottom liquid Concentration is adjusted between 0.100 ~ 0.105 mol/l;
S3, step acidifying:While toward addition sulfuric acid and dilution water in reactor while stirring, sour flow rate is 0.50 m3/h, dilution Rate of flow of water is 3.5 m3/h, by pH controls between 6.5 ~ 7.0 after stop stirring and be aged 30 minutes, glue must occur after stopping stirring Freeze;
S4, start stirring, while start cocurrent when being warming up to 85 DEG C, the heating-up time is controlled at 30 minutes or so;First adduction flowing water Glass, flow rate is 12.6 m3/h, then adds sulfuric acid at 9 ~ 10 to pH value, and sour flow rate is 0.50 m3/h, and cocurrent waterglass is total Measure as 10.0m3, between control ph 9.5 ~ 10.5;
S5, rear acidifying:Cocurrent does not stop stirring after terminating, be acidified after adding sulfuric acid and dilution water progress, sour flow rate is 0.50 m3/ H, dilution water flow rate is between 3.5 m3/h, terminal point control pH value 4.8-5.3;
S6, ageing stirring reaction in 20 minutes terminate.
First reactor is cleaned before step S2, makes it without wall dirt.
In step S4, waterglass is stirred and 50 minutes cocurrent used times.
In the preparation method, concentration >=98% of sulfuric acid.
Pass through dioxide-containing silica made from the preparation method(w%) ≥ 98.5%;Burning decrement(w%)For 3.2 ~ 4.2; Specific surface area(BET)(m2/g) it is 230 ~ 260;Loss on drying(w%)For 5.0 ~ 7.0;Oil factor(DBP absorption values)(ml/g)For 3.2~3.8;The characteristics of having Gao Bibiao, high oil absorption because of it, makes it have in rubber high reinforcing, and other physical property are also Do not reduce;Meanwhile, the characteristics of its burning decrement is low, pH value is high make its apply rubber or tire cure time shorten 50% with On, it is greatly improved processing efficiency.
The foregoing is only presently preferred embodiments of the present invention, be not intended to limit the invention, it is all the present invention spirit and Within principle, any modification, equivalent substitution and improvements made etc. should be included in the scope of the protection.

Claims (7)

1. a kind of rubber preparation method of the high reinforcing silica of high oil absorption, it is characterised in that comprise the following steps:
S1, accurate formulation concentration of sodium silicate is to 0.995 ~ 1.005 mol/l in make-up tank, and temperature control is in 25 ~ 50 DEG C of degree;
S2, the skill hot water 30m3 that changes a job from warm water tank, the glass 3.5m3 that adds water from refinery pit enter reactor, 60 DEG C are warming up to, by bottom liquid Concentration is adjusted between 0.100 ~ 0.105 mol/l;
S3, step acidifying:While toward addition sulfuric acid and dilution water in reactor while stirring, pH is controlled between 6.5 ~ 7.0 After stop stirring and be aged 30 minutes;
S4, start stirring, while starting cocurrent when being warming up to 85 DEG C;First adduction flowing water glass then adds sulphur at 9 ~ 10 to pH value Between acid, control ph 9.5 ~ 10.5;
S5, rear acidifying:Cocurrent does not stop stirring after terminating, be acidified after adding sulfuric acid and dilution water progress, terminal point control pH value 4.8- 5.3 between;
S6, ageing stirring reaction in 20 minutes terminate.
2. a kind of preparation method of rubber high reinforcing silica of high oil absorption according to claim 1, its feature It is, first reactor is cleaned before step S2, makes it without wall dirt.
3. a kind of preparation method of rubber high reinforcing silica of high oil absorption according to claim 1, its feature It is, step S3 is into step S5, and sour flow rate is 0.50 m3/h, and dilution water flow rate is 3.5 m3/h.
4. a kind of preparation method of rubber high reinforcing silica of high oil absorption according to claim 1, its feature It is, in step S4, waterglass flow rate is 12.6 m3/h, stirring and 50 minutes cocurrent used times.
5. a kind of preparation method of rubber high reinforcing silica of high oil absorption according to claim 1, its feature It is in step S3, jelly must occur after stopping stirring.
6. a kind of preparation method of rubber high reinforcing silica of high oil absorption according to claim 1, its feature It is, in step S4, the heating-up time is controlled at 30 minutes or so.
7. a kind of preparation method of rubber high reinforcing silica of high oil absorption according to claim 1, its feature It is, concentration >=98% of sulfuric acid.
CN201710287776.XA 2017-04-27 2017-04-27 A kind of preparation method of the rubber high reinforcing silica of high oil absorption Pending CN107021495A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710287776.XA CN107021495A (en) 2017-04-27 2017-04-27 A kind of preparation method of the rubber high reinforcing silica of high oil absorption

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710287776.XA CN107021495A (en) 2017-04-27 2017-04-27 A kind of preparation method of the rubber high reinforcing silica of high oil absorption

Publications (1)

Publication Number Publication Date
CN107021495A true CN107021495A (en) 2017-08-08

Family

ID=59528200

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710287776.XA Pending CN107021495A (en) 2017-04-27 2017-04-27 A kind of preparation method of the rubber high reinforcing silica of high oil absorption

Country Status (1)

Country Link
CN (1) CN107021495A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108516559A (en) * 2018-05-25 2018-09-11 广州市飞雪材料科技有限公司 A kind of preparation method of low viscosity high oil absorption value Silica Using for Toothpaste
CN110835110A (en) * 2019-12-12 2020-02-25 通化双龙硅材料科技有限公司 Preparation method of precipitated hydrated silicon dioxide
CN111039298A (en) * 2020-01-13 2020-04-21 福建省三明正元化工有限公司 Preparation method of high-dispersion silicon dioxide
CN111153411A (en) * 2020-01-13 2020-05-15 福建省三明正元化工有限公司 Preparation method of silicon dioxide with excellent physical application performance

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008136019A2 (en) * 2007-05-03 2008-11-13 Council Of Scientific & Industrial Research A process for the preparation of finely divided precipitated silica
CN101597065A (en) * 2009-07-28 2009-12-09 通化双龙化工股份有限公司 PE dividing plate Preparative Method of White Carbon Black
CN101618876A (en) * 2009-08-18 2010-01-06 通化双龙化工股份有限公司 Method for preparing precipitated white carbon black with controllable specific surface area
CN106185956A (en) * 2016-07-12 2016-12-07 通化双龙化工股份有限公司 A kind of preparation method of toothpaste precipitated silica thickening agent
CN106185957A (en) * 2016-07-20 2016-12-07 福建远翔新材料股份有限公司 The preparation method of tire silica reinforcing agent

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2008136019A2 (en) * 2007-05-03 2008-11-13 Council Of Scientific & Industrial Research A process for the preparation of finely divided precipitated silica
CN101597065A (en) * 2009-07-28 2009-12-09 通化双龙化工股份有限公司 PE dividing plate Preparative Method of White Carbon Black
CN101618876A (en) * 2009-08-18 2010-01-06 通化双龙化工股份有限公司 Method for preparing precipitated white carbon black with controllable specific surface area
CN106185956A (en) * 2016-07-12 2016-12-07 通化双龙化工股份有限公司 A kind of preparation method of toothpaste precipitated silica thickening agent
CN106185957A (en) * 2016-07-20 2016-12-07 福建远翔新材料股份有限公司 The preparation method of tire silica reinforcing agent

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
全国部分高校铸造专业《铸造化学》编写组: "《铸造化学》", 31 December 1976 *
本书编委: "《辞海 数学物理化学分册》", 31 December 1987, 上海辞书出版社 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108516559A (en) * 2018-05-25 2018-09-11 广州市飞雪材料科技有限公司 A kind of preparation method of low viscosity high oil absorption value Silica Using for Toothpaste
CN110835110A (en) * 2019-12-12 2020-02-25 通化双龙硅材料科技有限公司 Preparation method of precipitated hydrated silicon dioxide
CN111039298A (en) * 2020-01-13 2020-04-21 福建省三明正元化工有限公司 Preparation method of high-dispersion silicon dioxide
CN111153411A (en) * 2020-01-13 2020-05-15 福建省三明正元化工有限公司 Preparation method of silicon dioxide with excellent physical application performance
CN111153411B (en) * 2020-01-13 2023-10-24 福建省三明正元化工有限公司 Preparation method of silicon dioxide
CN111039298B (en) * 2020-01-13 2023-10-24 福建省三明正元化工有限公司 Preparation method of high-dispersion silicon dioxide

Similar Documents

Publication Publication Date Title
CN107021495A (en) A kind of preparation method of the rubber high reinforcing silica of high oil absorption
CN101139096B (en) Precipitated silica with a specific pore size distribution
US4463108A (en) Precipitated silica pigment for silicone rubber
CN106044790B (en) A kind of method of preparing white carbon black by precipitation method
US8840719B2 (en) Titanium dioxide pigments and manufacturing method
CN106554643B (en) The preparation method of high temperature resistant bismuth vanadium pigments
BR112014015235B1 (en) silica preparation process
BR112014018044B1 (en) process for preparing precipitated silicas
CN107353673A (en) Titanium dioxide that surface is modified and preparation method thereof
US20110179970A1 (en) Stable aqueous dispersions of precipitated silica
JP2015519442A (en) Paint dispersion
CN108033453A (en) A kind of preparation method of modified precipitated silica
NO177230B (en) Process for preparing an acid-resistant coating on calcium carbonate particles and using the particles
CN106315596B (en) A kind of production technology of low CTAB specific surface areas low-heat-generation white carbon
CN108408732A (en) A kind of preparation method of especially big specific surface area silica flatting silica
CN106752099A (en) A kind of nano-calcium carbonate powder of Chitosan Phosphate cross-linked polymer coating modification and preparation method thereof
CN103848427A (en) Highly dispersive precipitated white carbon black and preparation method thereof
CN108047795A (en) A kind of zinc silicate anti-corrosion paint with warning function
CN106752098A (en) A kind of nano-calcium carbonate powder of ferrocene polyethyleneimine cross-linked polymer coating modification and preparation method thereof
AU6436300A (en) Precipitated silica, a process to make it, and its use
CN107055560A (en) A kind of preparation method of high-purity lithium metasilicate solution
CN109319793A (en) A kind of preparation method of Gao Bibiao, high oil absorption white carbon black
CN105504108A (en) Preparation method for high-chlorinated polyethylene
CN111533951B (en) Preparation method of aluminum silicate-white carbon black composite filler
CN104109260A (en) Preparation method of transparent padding functional calcium carbonate specially used for TPR shoe material

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170808