CN102532404B - High-water-resistance acrylate emulsion and preparation method thereof - Google Patents
High-water-resistance acrylate emulsion and preparation method thereof Download PDFInfo
- Publication number
- CN102532404B CN102532404B CN201110457958XA CN201110457958A CN102532404B CN 102532404 B CN102532404 B CN 102532404B CN 201110457958X A CN201110457958X A CN 201110457958XA CN 201110457958 A CN201110457958 A CN 201110457958A CN 102532404 B CN102532404 B CN 102532404B
- Authority
- CN
- China
- Prior art keywords
- emulsion
- water
- initiator
- emulsifying agent
- initiator solution
- 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.)
- Active
Links
Landscapes
- Polymerisation Methods In General (AREA)
- Paints Or Removers (AREA)
Abstract
The invention provides a high-water-resistance acrylate emulsion. The emulsion comprises the following raw materials in percentage by weight: 20%-25% of styrene, 15%-20% of butyl acrylate, 3%-5% of methyl methacrylate, 1%-3% of acrylic acid, 1%-2% of organic silicon monomer, 1%-2% of mixed emulsifying agent, 0.5% of sodium bicarbonate, 0.5% of initiator and the balance of water. According to the invention, in the emulsion polymerization process, a reaction type emulsifying agent is adopted to carry out a polymerization reaction, and the emulsifying agent is polymerized to a large molecule chain in the polymerization process, thereby reducing the transfer of the emulsifying agent in a paint film, reducing the water adsorption rate of the paint film and improving water resistance; through adopting a nucleus-shell polymerization process, a shell polymerization part is subjected to copolymerization modification with organic silicon, so that a hydrophobic structure is formed on the surface of a latex particle, thereby improving the water resistance after film formation finally; and through the synergistic effect of the two methods, the water resistance of the prepared emulsion is greatly improved and the prepared emulsion can be widely applied to production and preparation of paints for inner and outer walls.
Description
Technical field
The present invention relates to the synthesis of polymer material field, be specially a kind of high-water-resistance acrylate emulsion that is mainly used in building coating, the present invention also comprises the preparation method of this acrylic ester emulsion.
Background technology
Building coating is very fast by the acrylic emulsion development in recent years, along with aqueous architectural coating is more and more applied in life, also more and more higher to the requirement of acrylic emulsion performance.By ordinary method, synthetic acrylic emulsion is made building coating and generally can be faced the poor problem of water resistance, and this is because emulsion can be applied to emulsifying agent and the hydrophilic monomer that some wetting abilities are stronger in preparation process.These hydrophilic component can show very strong water-absorbent at coating surface, more particularly at the small-molecular emulsifier of paint film inside, can be along with the time moves to surface, again with after water contact understanding absorption moisture, cause the paint film phenomenon such as even come off that occurs turning white, bubbles.Therefore, how improving the water resistance after emulsion film forming, be not only the important topic in the synthetic field of coating emulsion, is an important research direction of current emulsion polymerization technology.
Summary of the invention
Technical problem to be solved by this invention is to provide a kind of high-water-resistance acrylate emulsion and preparation method thereof, the water tolerance after raising coating emulsion film forming.
Technical problem of the present invention adopts following technical proposals to solve:
A kind of enhanced water resistance acrylate paint emulsion is characterized in that being prepared from by following raw material and proportioning:
Vinylbenzene: 20%~25%, butyl acrylate: 15%~20%, methyl methacrylate 3%~5%, vinylformic acid 1%~3%, organosilane monomer 1%~2%, blending emulsifiers 1%~2%, sodium bicarbonate 0.5%, initiator 0.5%, surplus is water.
Described initiator is ammonium persulphate or Sodium Persulfate.
Described organosilane monomer is γ-aminopropyl triethoxysilane (KH550) or γ-aminopropyltrimethoxysilane (KH551).
In described blending emulsifiers, the quality proportioning of each emulsifying agent is: nonionic emulsifying agent: anionic emulsifier: reactive emulsifier=1:2:1~2.
Described anionic emulsifier is sodium lauryl sulphate (K12); Described nonionic emulsifying agent is OP-10; Described reactive emulsifier is: allyloxy hydroxypropyl azochlorosulfonate acid sodium (AHPS) or hydroxyethyl methacrylate propyl sulfonic acid sodium (HMPS).
Preparation technology's flow process of aforesaid propylene acid esters coating emulsion is as follows:
(1) with 10% of water inventory in formula, initiator is dissolved, make initiator solution, standby;
(2) will fill a prescription in 60% and formula of blending emulsifiers total amount water inventory 40%, whole sodium bicarbonate, and vinylformic acid, butyl acrylate, vinylbenzene, the methyl methacrylate polymerization monomer carries out high speed dispersion, prepare pre-emulsion, pre-emulsion is divided into to A, two parts of B, the A:B weight ratio is 2:1, in B, add organosilane monomer to mix
(3) will fill a prescription in the blending emulsifiers total amount 40%, in formula, 50% of water inventory drops into reactor, be warmed up to 80-85 ℃, slowly add 6/10 of the pre-emulsion A configured and the initiator solution configured, then 3/10 of the initiator solution that drips pre-emulsion B and configure, all pre-emulsions added at 3-3.5 hour;
(4) add 1/10 of the initiator solution that configures after, keep temperature of reaction at 90 ℃, react 1 hour, be cooled to below 40 ℃, regulate emulsion viscosity, the packing discharging.
Technical characteristics of the present invention is as follows:
1, in the process of letex polymerization, adopt the emulsifying agent of response type to carry out polyreaction, emulsifying agent participates in being aggregated on macromolecular chain in polymerization process, has reduced the migration of emulsifying agent in paint film, has reduced the water-intake rate of paint film, has improved water tolerance.
2, by adopting the technique of nuclear-shell polymerization, at the shell polymeric part, adopt organosilicon to carry out modification by copolymerization, make the emulsion particle surface form a kind of hydrophobic structure, improved the water tolerance after final film forming.
By the synergy of these two kinds of methods, can make the water tolerance after prepared emulsion film forming obtain very large raising, can be widely used in the manufacture of coating for internal and external wall.
Embodiment
Embodiment 1
Vinylbenzene 20g, butyl acrylate 20g, methyl methacrylate 5g, vinylformic acid 1g, organosilane monomer KH550 1g, blending emulsifiers 2g(op-10 0.4g, K12 0.8g, AHPS 0.8g), sodium bicarbonate 0.5g, ammonium persulphate 0.5g, deionized water 50g.
(1) 0.5g ammonium persulphate and 5g water are mixed with to initiator solution.(5mL)
(2) in the 200mL four-hole bottle, the blending emulsifiers of 1.2g and 20g water, 0.5g sodium bicarbonate are mixed, then add the polymerization single polymerization monomers such as vinylformic acid 3g, butyl acrylate 20g, vinylbenzene 20g, methyl methacrylate 5g to carry out high speed dispersion, prepare the monomer pre-emulsion, pre-emulsion is divided into to A, two parts of B (the A:B weight ratio is 2:1) add organosilane monomer KH550 1g to mix in B.
(3) by the 0.8g blending emulsifiers, the water of 25g drops in the 200mL four-hole bottle, be warmed up to 80-85 ℃, successively slowly drip pre-emulsion A and the pre-emulsion B configured, drip simultaneously the total amount of initiator of initiator solution 4.5mL(90%) carry out polyreaction, whole process maintains the temperature at 80-85 ℃, and pre-emulsion and initiator all add about about 3-3.5 hour.
(4) add the total amount of initiator of initiator solution 0.5mL(10%), keep temperature of reaction at 90 ℃, react 1 hour, be cooled to below 40 ℃, regulate the emulsion pH value to 7-8 with ammoniacal liquor, filter, packing.
Embodiment 2
Vinylbenzene: 25g, butyl acrylate: 15g, methyl methacrylate 3g, vinylformic acid 3g, organosilane monomer KH551 2g, blending emulsifiers 1g(op-10 0.2g, K12 0.4g, HMPS 0.4g), sodium bicarbonate 0.5g, Sodium Persulfate 0.5g, deionized water 50g.
Reaction process is as follows:
(1) 0.5g ammonium persulphate and 5g water are mixed with to initiator solution (5mL).
(2) in the 200mL four-hole bottle, the blending emulsifiers of 0.8g and 20g water, 0.5g sodium bicarbonate are mixed, then the vinylformic acid that adds formula ratio, butyl acrylate, vinylbenzene, the polymerization single polymerization monomers such as methyl methacrylate carry out high speed dispersion, prepare the monomer pre-emulsion, and pre-emulsion is divided into to A, two parts of B (the A:B weight ratio is 2:1) add 1g KH-550 to mix in B.
(3) by the 1.2g blending emulsifiers, the water of 25g drops in the 200mL four-hole bottle, be warmed up to 80-85 ℃, successively slowly drip pre-emulsion A and the pre-emulsion B configured, drip simultaneously the total amount of initiator of initiator solution 4.32mL(90%) carry out polyreaction, whole process maintains the temperature at 80-85 ℃, and pre-emulsion and initiator all add about about 3-3.5 hour.
(4) add the total amount of initiator of initiator 0.5mL(10%), keep temperature of reaction at 90 ℃, react 1 hour, be cooled to below 40 ℃, regulate the emulsion pH value to 7-8 with ammoniacal liquor, filter, packing.
The foregoing is only and the present invention relates to the part example; other relate to example because length is limit the present invention; can not list one by one; in every case above example is done in composition and engineering given to this invention to equivalent modifications or proportioning variation according to know-why of the present invention, all within protection scope of the present invention.
Claims (1)
1. the preparation method of a high-water-resistance acrylate emulsion is characterized in that by following formula and technique preparation:
Vinylbenzene: 20%~25%, butyl acrylate: 15%~20%, methyl methacrylate 3%~5%, vinylformic acid 1%~3%, organosilane monomer 1%~2%, blending emulsifiers 1%~2%, sodium bicarbonate 0.5%, initiator 0.5%, surplus is water;
Described processing step is:
(1) with 10% of water inventory in formula, initiator is dissolved, make initiator solution, standby;
(2) will fill a prescription in 60% and formula of blending emulsifiers total amount water inventory 40%, whole sodium bicarbonate, and vinylformic acid, butyl acrylate, vinylbenzene, the methyl methacrylate polymerization monomer carries out high speed dispersion, prepares pre-emulsion, pre-emulsion is divided into to A, two parts of B, the A:B weight ratio is 2:1, in B, adds organosilane monomer to mix;
(3) will fill a prescription in the blending emulsifiers total amount 40%, in formula, 50% of water inventory drops into reactor, be warmed up to 80-85 ℃, slowly add 6/10 of the pre-emulsion A configured and the initiator solution configured, then 3/10 of the initiator solution that drips pre-emulsion B and configure, all pre-emulsions added at 3-3.5 hour;
(4) add 1/10 of the initiator solution that configures after, keep temperature of reaction at 90 ℃, react 1 hour, be cooled to below 40 ℃, regulate emulsion viscosity, the packing discharging.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110457958XA CN102532404B (en) | 2011-12-31 | 2011-12-31 | High-water-resistance acrylate emulsion and preparation method thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201110457958XA CN102532404B (en) | 2011-12-31 | 2011-12-31 | High-water-resistance acrylate emulsion and preparation method thereof |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102532404A CN102532404A (en) | 2012-07-04 |
CN102532404B true CN102532404B (en) | 2013-12-11 |
Family
ID=46340548
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201110457958XA Active CN102532404B (en) | 2011-12-31 | 2011-12-31 | High-water-resistance acrylate emulsion and preparation method thereof |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102532404B (en) |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102964502B (en) * | 2012-11-06 | 2015-01-21 | 海南必凯水性涂料有限公司 | Preparation method of water-resistant high-gloss water-based styrene-acrylic emulsion |
CN103193924B (en) * | 2013-04-03 | 2016-01-20 | 衡水新光化工有限责任公司 | Phased film forming styrene-acrylic coating emulsion and preparation method |
CN104693340A (en) * | 2013-12-06 | 2015-06-10 | 上海展辰涂料有限公司 | Carpentry paint emulsion with core-shell structure and preparation method thereof |
CN104193874B (en) * | 2014-08-27 | 2016-09-14 | 颐中(青岛)实业有限公司 | A kind of high glass transition temperature low film formation temperature modifying cinepazid emulsion |
CN104311739B (en) * | 2014-11-14 | 2017-11-24 | 杭州蓝励新材料有限公司 | Organic-silicon-modified styrene-butadiene latex and preparation method thereof |
CN105348973B (en) * | 2015-11-24 | 2017-08-15 | 三棵树涂料股份有限公司 | Silicon-acrylic lates outer wall coatings containing core shell structure and preparation method thereof |
CN105601799B (en) * | 2016-01-05 | 2018-03-16 | 广州中国科学院工业技术研究院 | Core/shell type organosilicon-modified acrylate emulsion and its preparation method and application |
CN106065044A (en) * | 2016-07-28 | 2016-11-02 | 苏州合志电子有限公司 | A kind of preparation method of woodcare paint styrene-acrylic emulsion |
CN107082851B (en) * | 2017-05-25 | 2019-04-19 | 广东工业大学 | A kind of preparation method of water repellent type acrylic acid ester emulsion |
CN110857370A (en) * | 2018-08-24 | 2020-03-03 | 佛山朗能建材科技有限公司 | Hydrophobic elastic waterproof coating and preparation method thereof |
CN112194750A (en) * | 2019-07-08 | 2021-01-08 | 安徽米兰士装饰材料有限公司 | Preparation method of environment-friendly acrylic emulsion transparent waterproof adhesive |
CN111171215B (en) * | 2020-02-25 | 2021-06-01 | 北京汉莫克化学技术有限公司 | Environment-friendly agricultural dispersant and preparation method thereof |
CN111793401A (en) * | 2020-07-09 | 2020-10-20 | 西卡(上海)管理有限公司 | Waterproof coating and preparation method thereof |
CN114479595A (en) * | 2021-07-13 | 2022-05-13 | 江苏膜可光学材料有限公司 | Novel water-based environment-friendly paint for enhancing surface adhesive performance of packaging box and process flow |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6005042A (en) * | 1996-03-11 | 1999-12-21 | Clariant Gmbh | Aqueous polymer dispersions as binders for elastic, nonblocking and scratch-resistant coatings |
CN101921360A (en) * | 2010-01-27 | 2010-12-22 | 陕西科技大学 | A kind of latex coating preparation method of nano silicone-acrylate core shell type composite emulsion |
CN101982477A (en) * | 2010-09-25 | 2011-03-02 | 西北工业大学 | Acrylic emulsion capable of simultaneously modifying two silane coupling agents and preparation method thereof |
-
2011
- 2011-12-31 CN CN201110457958XA patent/CN102532404B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6005042A (en) * | 1996-03-11 | 1999-12-21 | Clariant Gmbh | Aqueous polymer dispersions as binders for elastic, nonblocking and scratch-resistant coatings |
CN101921360A (en) * | 2010-01-27 | 2010-12-22 | 陕西科技大学 | A kind of latex coating preparation method of nano silicone-acrylate core shell type composite emulsion |
CN101982477A (en) * | 2010-09-25 | 2011-03-02 | 西北工业大学 | Acrylic emulsion capable of simultaneously modifying two silane coupling agents and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN102532404A (en) | 2012-07-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102532404B (en) | High-water-resistance acrylate emulsion and preparation method thereof | |
CN102585111B (en) | Modified epoxy emulsion and preparation method thereof | |
CN103483493B (en) | Organosilicon-modified acrylate emulsion and preparation method thereof | |
CN101280035A (en) | Wet-rub resistant styrene-acrylic emulsion and preparation thereof | |
CN102603960B (en) | Preparation method of acrylic emulsion with core-shell structure for redispersible emulsion powder | |
CN101781390B (en) | Preparation method of nuclear shell structure high-silicon silicone acrylic emulsion used for building exterior wall | |
CN103724520B (en) | Benzene emulsion of a kind of building coating and preparation method thereof | |
CN103570881B (en) | A kind of polyacrylate grafting vinyl chloride composite resin and preparation method thereof | |
CN104387521B (en) | A kind of montmorillonite and the preparation method of methacrylic acid compound modified acrylic ester core-shell emulsion | |
CN102603998A (en) | Preparation method of high solid content epoxy modified acrylic resin emulsion | |
CN105669910A (en) | Polycarboxylic cement grinding aid and preparation method thereof | |
CN101921360A (en) | A kind of latex coating preparation method of nano silicone-acrylate core shell type composite emulsion | |
CN105254802A (en) | Waterproof emulsion and preparation method thereof | |
CN101177516A (en) | High-wearing polytetrafluoroethylene composite material and method for making same | |
CN107602769A (en) | A kind of method of synthesis MBS resins | |
CN104356309B (en) | A kind of preparation method of unsaturated polyester resin shrinking agent | |
CN105315413A (en) | Novel modified acrylate emulsion adhesive and preparation method thereof | |
CN105255298A (en) | VAc/St/BA (vinyl acetate-styrene-butyl acrylate) stone paint emulsion and preparation method | |
CN104193215B (en) | Ternary block macromonomer graft copolymerization high-property polycarboxylic acid water-reducing agent and preparation method thereof | |
CN106632791B (en) | One kind resisting fresh cement accumulation of salt in the surface soil priming paint styrene-acrylic emulsion and preparation method thereof | |
CN111995708A (en) | Based on amphiphilic Janus SiO2Nano particle fluorine-containing polyacrylate finishing agent and preparation method thereof | |
CN103073670B (en) | impact modifier ACR resin and preparation method thereof | |
CN107418125A (en) | A kind of method that multiphase polymer material is prepared using segmented copolymer latex | |
CN103772593B (en) | A kind of acrylic acid or the like elastic emulsion and preparation method thereof | |
CN102050889A (en) | Preparation method of polybutadiene latex with super-large particle size |
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 |