CN100489047C - Process for preparing acrylic acid emulsion adhesive for rubber - Google Patents
Process for preparing acrylic acid emulsion adhesive for rubber Download PDFInfo
- Publication number
- CN100489047C CN100489047C CNB2006101237467A CN200610123746A CN100489047C CN 100489047 C CN100489047 C CN 100489047C CN B2006101237467 A CNB2006101237467 A CN B2006101237467A CN 200610123746 A CN200610123746 A CN 200610123746A CN 100489047 C CN100489047 C CN 100489047C
- Authority
- CN
- China
- Prior art keywords
- emulsion
- monomer
- monomers
- initiator
- emulsifying agent
- 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.)
- Expired - Fee Related
Links
Landscapes
- Polymerisation Methods In General (AREA)
- Adhesives Or Adhesive Processes (AREA)
Abstract
The invention discloses a preparing method of acroleic acid emulsion adhesive for rubber, which comprises the following steps: pre-emulsifying partial monomer in the core component, partial deionized water and partial emulsion to obtain the pre-emulsion; transmitting the pre-emulsion into autoclave; adding partial initiator in the core component to produce seed emulsion; dripping residual monomer of core component in the seed emulsion slowly; supplementing residual emulsion, deionized water and initiator to obtain the core part of emulsion; dripping the monomer of case component in the core part of emulsion; supplementing emulsion of case component, deionized water and initiator; reinforcing the bonding strength and stripping strength and cutting strength; fitting for metal, aluminizing metal and PE; replacing solvent-typed adhesive.
Description
Technical field:
The invention belongs to elastomeric material emulsion adhesive technology, relate in particular to a kind of preparation method of acrylic acid emulsion adhesive for rubber.
Background technology:
ACRYLIC EMULSION is widely used in fields such as coating, tackiness agent with its excellent performance and cheap price.With water to replace organic solvent, promptly prevented the pollution that solvent evaporates caused, avoid using expensive organic solvents again, saved the energy, reduced cost, can solve environmental protection and problem of energy saving simultaneously, have good application prospects.But the application of aqueous adhesive is also very limited at present, and its major cause is all too late solvent-based adhesives sticking power, bonding strength and the time of drying etc. of aqueous adhesive.The bonding force and the set time of therefore how to improve emulsion adhesive are the subject matter that will solve at present.The research in this field is had the history of decades abroad, and obtained very big achievement, a lot of products have carried out industrialization; Domesticly then start to walk to want evening a lot of in this field, only have a spot of water-borne coatings to put goods on the market at present, a lot of products all also are in the research trial stage.Especially report is seen still less at present in the aqueous adhesive field, and all is be applied to the very strong material of surfactivity bonding, to the bonding report of also not seen at present of the very strong material of surface inertness such as rubber, plastics.
Summary of the invention:
The preparation method who the purpose of this invention is to provide a kind of acrylic acid emulsion adhesive for rubber, prepare the method for the nucleocapsid structure acrylic acid emulsion adhesive of adhesiveproperties excellence by adding the modification acrylate monomer, can be widely used in the bonding of material such as rubber.
The preparation of a kind of acrylic acid emulsion adhesive for rubber of the present invention is to have added the monomers such as tetrahydrofuran (THF) acrylate that contain polar group to carry out modification in the shell component, has well improved the adhesiveproperties of acrylic acid emulsion adhesive to adhesives; In addition, the emulsion of preparation has nuclear-shell bilayer structure, and guarantees that the second-order transition temperature of emulsion shell will be far below the second-order transition temperature of nuclear, makes the performances such as sticking power of under force of cohesion and the condition that is not affected set time raising emulsion.
Particularly, preparation method of the present invention comprises the steps:
(1) earlier the partial monosomy in the nuclear consitution, part deionized water, partial emulsifier are carried out pre-emulsification and obtain pre-emulsion;
(2) pre-emulsion is moved in the reactor, under 100-150 rev/mins the rotating speed, be warming up to 70-80 ℃, add the part initiator in the nuclear consitution, reaction obtains seed emulsion;
(3) residual monomer of nuclear consitution is added dropwise to slowly in the seed emulsion that step (2) obtains, adds residual emulsifier, deionized water and the initiator of nuclear consitution in the reaction process, reaction obtains the nuclear part of emulsion;
(4) monomer of shell component slowly is added dropwise in the nuclear part of emulsion of step (3) preparation again, adds emulsifying agent, deionized water, the initiator of shell component in the reaction process, reaction finishes, and transfers pH value to 7-8 promptly to obtain acrylic acid emulsion adhesive for rubber;
Wherein the composition and the parts by weight thereof of nuclear consitution and shell component are as follows:
Shell component: Butyl Acrylate Monomer 30-50 Hydroxyethyl acrylate monomers 0.5-2.5 methacrylic acid monomers 1-5
Styrene monomer 5-15 methyl methacrylate lists 10-20 modified monomers 3-10
Body
Initiator 0.1-0.4 emulsifying agent 0.3-3.5
Nuclear consitution: Butyl Acrylate Monomer 25-45 methyl methacrylate lists 10-30 styrene monomers 5-15
Body
Methacrylic acid monomer 1-3 Hydroxyethyl acrylate monomers 0.5-2.0 sodium bicarbonates 0.1-0.25
Emulsifying agent 0.3-3.5 initiators 0.1-0.4
Preferred version is as follows:
Shell component: Butyl Acrylate Monomer 30-50 Hydroxyethyl acrylate monomers 0.5-2.5 methacrylic acid monomers 1-5
Styrene monomer 5-15 methyl methacrylate monomers 10-20 modified monomers 3-10
Ammonium persulfate 0.1-0.4 Sodium dodecylbenzene sulfonate 0.5-2.0 OP-10 0.25-15
Nuclear consitution: Butyl Acrylate Monomer 25-45 methyl methacrylate monomers 10-30 styrene monomers 5-15
Methacrylic acid monomer 1-3 Hydroxyethyl acrylate monomers 0.5-2.0 sodium bicarbonates 0.1-0.25
OP-10 0.25-1.5 Sodium dodecylbenzene sulfonate 0.5-2.0 ammonium persulfates 0.1-0.4
The summation of said components consumption is 100.
Described initiator preferred anionic initiator potassium persulfate and/or ammonium persulfate, triggering mechanism are that free radical causes.
The compound emulsifying agent of described emulsifying agent preferred anionic emulsifying agent and nonionic emulsifier.
In the preferred Sodium dodecylbenzene sulfonate of anionic emulsifier, sodium laurylsulfonate, the sodium lauryl sulphate one or more;
Nonionic emulsifying agent comprises OP-10 and/or XP-10 etc.
The main foundation that emulsifying agent is selected is the HLB value of polymerization single polymerization monomer group, and the HLB value of emulsifying agent and the HLB value of monomeric groups are good more near its emulsive effect more.According to mentioned above principle, the present invention explores by creativeness and draws the compound emulsifying agent of Sodium dodecylbenzene sulfonate and OP-10 emulsifying effectiveness the best to Acrylic Acid Monomer, and the ratio of selecting for use is 1:2-1:1, and its consumption is 1.0-3.0% of an emulsion weight.
Monomer of the present invention mainly comprises hard monomer, soft monomer, functional monomer and modified monomer.
Hard monomer comprises: the monomer that second-order transition temperatures such as methyl methacrylate, vinylbenzene are higher, the increase of hard monomer amount can improve force of cohesion, bonding strength and the set time etc. of emulsion glue;
Soft monomer comprises the lower monomers of second-order transition temperature such as butyl acrylate, Isooctyl acrylate monomer, the raising of its add-on can increase the initial bonding strength of emulsion glue and hold viscous force, but the higher problems such as the reduction of emulsion glue force of cohesion, prolongation time of drying that occur easily of soft monomer amount;
Functional monomer comprises vinylformic acid, Hydroxyethyl acrylate etc., it mainly acts on is that groups such as hydroxyl by on the functional monomer are coupled to each other the acrylate copolymer chain, the cohesive strength of ACRYLIC EMULSION is greatly improved, simultaneously because the mutual connection of polymer chain also causes problems such as emulsion viscosity increase easily;
Modified monomer mainly comprises the fluorine-containing and/or the tetrahydrofuran (THF) acrylate of polar functionalities, the polar group that adds all has certain corrosive nature to the surface of a lot of base materials, thereby makes the latex ion can well infiltrate the sticking power that substrate surface has improved acrylic acid emulsion adhesive greatly.Experimental result of the present invention shows that the effect of the emulsion adhesive that the stronger tetrahydrofuran (THF) of polarity is acrylate modified is better than the modification of fluorine-containing, and, used the surface corrosion vestige of the acrylate modified bonding base material of emulsion adhesive of tetrahydrofuran (THF) obviously more a lot of than other latex gluing of surfaces from also as can be seen by the surface of sticking base material.
The consumption of soft monomer preferably is higher than the consumption of soft monomer in the nuclear consitution monomer in the described shell constituent monomers, make prepared emulsion have the strong adhesion of shell part, the strong characteristics of force of cohesion of nuclear part, this structure has solved when increasing sticking power, and force of cohesion is descended and elongated problem set time.The second-order transition temperature of the prepared emulsion shell of the present invention is 0--30 ℃, and the second-order transition temperature of nuclear is 20--10 ℃.
The acrylic acid emulsion adhesive of the present invention preparation, its solid content is 42-60%, can be used in rubber, metal, materials such as the metal of aluminizing, PE, can replace solvents type tackiness agent in a lot of occasions, have advantages such as low VOC, low cost.
Embodiment:
Embodiment 1 prescription following (g):
Nuclear consitution: shell component:
Butyl acrylate: 45 butyl acrylates: 60
Methyl methacrylate: 35 methyl methacrylates: 15
Vinylbenzene: 20 vinylbenzene: 15
Methacrylic acid: 3 methacrylic acids: 5
Hydroxyethyl methylacrylate: 1.5 hydroxyethyl methylacrylates: 2.5
OP-10:1.0 tetrahydrofuran methyl vinylformic acid 8
Ester:
Sodium dodecylbenzene sulfonate: 1.5 Sodium dodecylbenzene sulfonatees: 0.5
Ammonium persulfate: 0.6 OP-10:0.5
Sodium bicarbonate: 0.5 ammonium persulfate: 0.3
Deionized water: 130 deionized waters: 70
Synthesis step:
(1) will mix in 0.5g sodium bicarbonate, 0.5g OP-10 and 1.0g Sodium dodecylbenzene sulfonate and the adding 70g deionized water, and then add 20g nuclear consitution mix monomer, high-speed stirring 20min gets pre-emulsion;
(2) pre-emulsion is moved in the four-hole boiling flask, under the condition of 100-150r/min, be warming up to about 70 ℃, add 0.4g ammonium persulfate initiator, reacting refluxes to the flask walls monomer-free promptly gets seed emulsion;
(3) remaining nuclear consitution is added dropwise in the seed emulsion slowly, dropwised in 1.5 hours, remaining emulsifying agent, initiator and deionized water in the nuclear consitution are added in the centre, and monomer adds afterreaction promptly gets emulsion to the monomer-free backflow nuclear part;
(4) again shell component mixed solution slowly is added dropwise in the emulsion of step (3) preparation, but emulsifying agent, initiator and deionized water in the component are added in the centre, monomer dropwised in 2 hours, be warming up to 90 ℃ of reactions 1 hour after dropwising, transfer Ph value to 7-8 promptly to obtain acrylic acid emulsion adhesive.
With the emulsion adhesive adhesive rubber sample that makes, record location and set time, on the electron detachment trier, carry out peel strength test after the completely solidified according to GB/T2791-1995 standard, carry out the tensile shear strength test according to USS ASTM D 4501 simultaneously, test result sees Table 1.
Embodiment 2 is changed to fluorine-containing with the tetrahydrofuran (THF) acrylate among the embodiment 1, and other prescriptions are constant with preparation process.
According to embodiment 1 same testing method the performance of emulsion adhesive is tested, its test result sees Table 1
The tetrahydrofuran (THF) acrylate that embodiment 3 removes among the embodiment 1, other prescriptions are constant with preparation process.
According to embodiment 1 same testing method the performance of emulsion adhesive is tested equally, its test result sees Table 1
Every performance data contrast of the emulsion adhesive that table 1 embodiment 1, embodiment 2 and embodiment 3 make
| Embodiment 1 | Embodiment 2 | Embodiment 3 | |
| Setting time | 8h | 8h | 6h |
| Set time | 4 days | 4 days | 3 days |
| Stripping strength | 3N/15mm | 2.5N/15mm | 0.4N/15mm |
| Shearing resistance | 5Mpa | 4.6Mpa | 3.0Mpa |
As can be seen from the above table, the adding of modification acrylate all improves a lot to the stripping strength and the shearing resistance of emulsion glue, and its adding will be much larger than the influence to shearing resistance to the influence of strength of glass; It can also be seen that the stripping strength of the emulsion glue that adds the stronger tetrahydrofuran methyl acrylate of polarity and the emulsion glue that shearing resistance all is better than the fluorine-containing modification by contrasting us; The adding of modification acrylate is to the location of emulsion glue and exist certain influence set time, but influence is not very big, in the acceptable scope.
Embodiment 4 prescriptions following (g):
Nuclear consitution: shell component:
Butyl acrylate: 40 butyl acrylates: 65
Methyl methacrylate: 35 methyl methacrylates: 15
Vinylbenzene: 25 vinylbenzene: 10
Methacrylic acid: 3 methacrylic acids: 5
Hydroxyethyl methylacrylate: 1.5 hydroxyethyl methylacrylates: 2.5
OP-10:1.0 tetrahydrofuran methyl vinylformic acid 5
Ester:
Sodium dodecylbenzene sulfonate: 2.0 Sodium dodecylbenzene sulfonatees: 2.0
Ammonium persulfate: 1.0 OP-10:1.0
Sodium bicarbonate: 0.5 ammonium persulfate: 0.6
Deionized water: 130 deionized waters: 70
Synthesis step:
(1) will mix in 0.5g sodium bicarbonate, 0.5g OP-10 and 1.0g Sodium dodecylbenzene sulfonate and the adding 70g deionized water, and then add 20g nuclear consitution mix monomer, high-speed stirring 20min gets pre-emulsion;
(2) pre-emulsion is moved in the four-hole boiling flask, under the condition of 100-150r/min, be warming up to about 80 ℃, add 0.6g ammonium persulfate initiator, reacting refluxes to the flask walls monomer-free promptly gets seed emulsion;
(3) remaining nuclear consitution is added dropwise in the seed emulsion slowly, dropwised in 1.5 hours, remaining emulsifying agent, initiator and deionized water in the nuclear consitution are added in the centre, and monomer adds afterreaction promptly gets emulsion to the monomer-free backflow nuclear part;
(4) again shell component mixed solution slowly is added dropwise in the emulsion of step (3) preparation, but emulsifying agent, initiator and deionized water in the component are added in the centre, monomer dropwised in 2 hours, be warming up to 90 ℃ of reactions 1 hour after dropwising, transfer Ph value to 7-8 promptly to obtain acrylic acid emulsion adhesive.
Embodiment 5 prescriptions following (g):
Nuclear consitution: shell component:
Butyl acrylate: 40 butyl acrylates: 65
Methyl methacrylate: 35 methyl methacrylates: 15
Vinylbenzene: 25 vinylbenzene: 15
Methacrylic acid: 3.0 methacrylic acids: 1.0
Hydroxyethyl methylacrylate: 2.0 hydroxyethyl methylacrylates: 1.0
OP-10:2.5 tetrahydrofuran methyl vinylformic acid 3
Ester:
Sodium dodecylbenzene sulfonate: 4.0 Sodium dodecylbenzene sulfonatees: 3.5
Ammonium persulfate: 0.3 OP-10:2.0
Sodium bicarbonate: 0.2 ammonium persulfate: 0.1
Deionized water: 130 deionized waters: 70
Synthesis step:
(1) will mix in 0.2g sodium bicarbonate, 1.5g OP-10 and 2.0g Sodium dodecylbenzene sulfonate and the adding 70g deionized water, and then add 20g nuclear consitution mix monomer, high-speed stirring 20min gets pre-emulsion;
(2) pre-emulsion is moved in the four-hole boiling flask, under the condition of 100-150r/min, be warming up to about 78 ℃, add 0.2g ammonium persulfate initiator, reacting refluxes to the flask walls monomer-free promptly gets seed emulsion;
(3) remaining nuclear consitution is added dropwise in the seed emulsion slowly, dropwised in 1.5 hours, remaining emulsifying agent, initiator and deionized water in the nuclear consitution are added in the centre, and monomer adds afterreaction promptly gets emulsion to the monomer-free backflow nuclear part;
(4) again shell component mixed solution slowly is added dropwise in the emulsion of step (3) preparation, but emulsifying agent, initiator and deionized water in the component are added in the centre, monomer dropwised in 2 hours, be warming up to 90 ℃ of reactions 1 hour after dropwising, transfer Ph value to 7-8 promptly to obtain acrylic acid emulsion adhesive.
Embodiment 6 prescriptions following (g):
Nuclear consitution: shell component:
Butyl acrylate: 25 butyl acrylates: 65
Methyl methacrylate: 40 methyl methacrylates: 15
Vinylbenzene: 30 vinylbenzene: 15
Methacrylic acid: 3.0 methacrylic acids: 1.0
Hydroxyethyl methylacrylate: 2.0 hydroxyethyl methylacrylates: 1.0
OP-10:1.5 tetrahydrofuran methyl vinylformic acid 10
Ester:
Sodium dodecylbenzene sulfonate: 3.0 Sodium dodecylbenzene sulfonatees: 3.0
Ammonium persulfate: 0.3 OP-10:2.0
Sodium bicarbonate: 0.4 ammonium persulfate: 0.2
Deionized water: 140 deionized waters: 80
Synthesis step:
(1) will mix in 0.4g sodium bicarbonate, 1.0g OP-10 and 2.0g Sodium dodecylbenzene sulfonate and the adding 70g deionized water, and then add 20g nuclear consitution mix monomer, high-speed stirring 20min gets pre-emulsion;
(2) pre-emulsion is moved in the four-hole boiling flask, under the condition of 100-150r/min, be warming up to about 78 ℃, add 0.2g ammonium persulfate initiator, reacting refluxes to the flask walls monomer-free promptly gets seed emulsion;
(3) remaining nuclear consitution is added dropwise in the seed emulsion slowly, dropwised in 1.5 hours, remaining emulsifying agent, initiator and deionized water in the nuclear consitution are added in the centre, and monomer adds afterreaction promptly gets emulsion to the monomer-free backflow nuclear part;
(4) again shell component mixed solution slowly is added dropwise in the emulsion of step (3) preparation, but emulsifying agent, initiator and deionized water in the component are added in the centre, monomer dropwised in 2 hours, be warming up to 90 ℃ of reactions 1 hour after dropwising, transfer Ph value to 7-8 promptly to obtain acrylic acid emulsion adhesive.
Embodiment 7 prescriptions following (g):
Nuclear consitution: shell component:
Butyl acrylate: 50 butyl acrylates: 65
Methyl methacrylate: 30 methyl methacrylates: 10
Vinylbenzene: 20 vinylbenzene: 15
Methacrylic acid: 3.0 methacrylic acids: 1.0
Hydroxyethyl methylacrylate: 2.0 hydroxyethyl methylacrylates: 1.0
OP-10:2.5 fluorine-containing: 5
Sodium dodecylbenzene sulfonate: 4.0 Sodium dodecylbenzene sulfonatees: 3.5
Ammonium persulfate: 0.6 OP-10:2.0
Sodium bicarbonate: 0.5 ammonium persulfate: 0.3
Deionized water: 150 deionized waters: 80
Synthesis step:
(1) will mix in 0.5g sodium bicarbonate, 1.5g OP-10 and 2.0g Sodium dodecylbenzene sulfonate and the adding 70g deionized water, and then add 20g nuclear consitution mix monomer, high-speed stirring 20min gets pre-emulsion;
(2) pre-emulsion is moved in the four-hole boiling flask, under the condition of 100-150r/min, be warming up to about 78 ℃, add 0.2g ammonium persulfate initiator, reacting refluxes to the flask walls monomer-free promptly gets seed emulsion;
(3) remaining nuclear consitution is added dropwise in the seed emulsion slowly, dropwised in 1.5 hours, remaining emulsifying agent, initiator and deionized water in the nuclear consitution are added in the centre, and monomer adds afterreaction promptly gets emulsion to the monomer-free backflow nuclear part;
(4) again shell component mixed solution slowly is added dropwise in the emulsion of step (3) preparation, but emulsifying agent, initiator and deionized water in the component are added in the centre, monomer dropwised in 2 hours, be warming up to 90 ℃ of reactions 1 hour after dropwising, transfer Ph value to 7-8 promptly to obtain acrylic acid emulsion adhesive.
Claims (6)
1, a kind of preparation method of acrylic acid emulsion adhesive for rubber is characterized in that comprising the steps:
(1) earlier the partial monosomy in the nuclear consitution, part deionized water, partial emulsifier are carried out pre-emulsification and obtain pre-emulsion;
(2) pre-emulsion is moved in the reactor, under 100-150 rev/mins the rotating speed, be warming up to 70-80 ℃, add the part initiator in the nuclear consitution, reaction obtains seed emulsion;
(3) residual monomer of nuclear consitution is added dropwise to slowly in the seed emulsion that step (2) obtains, adds residual emulsifier, deionized water and the initiator of nuclear consitution in the reaction process, reaction obtains the nuclear part of emulsion;
(4) monomer of shell component slowly is added dropwise in the nuclear part of emulsion of step (3) preparation again, adds emulsifying agent, deionized water, the initiator of shell component in the reaction process, reaction finishes, and transfers pH value to 7-8 promptly to obtain acrylic acid emulsion adhesive for rubber;
Wherein the composition and the parts by weight thereof of nuclear consitution and shell component are as follows:
Shell component: Butyl Acrylate Monomer 30-50 Hydroxyethyl acrylate monomers 0.5-2.5 methacrylic acid monomers 1-5
Styrene monomer 5-15 methyl methacrylate lists 10-20 modified monomers 3-10
Body
Initiator 0.1-0.4 emulsifying agent 0.3-3.5
Nuclear consitution: Butyl Acrylate Monomer 25-45 methyl methacrylate lists 10-30 styrene monomers 5-15
Body
Methacrylic acid monomer 1-3 Hydroxyethyl acrylate monomers 0.5-2.0 sodium bicarbonates 0.1-0.25
Emulsifying agent 0.3-3.5 initiators 0.1-0.4
The summation of said components consumption is 100, and described modified monomer is selected the fluorine-containing and/or the tetrahydrofuran (THF) acrylate of polar functionalities for use.
2, method according to claim 1 is characterized in that described initiator selects anionic initiator Potassium Persulphate and/or ammonium persulfate for use.
3, method according to claim 1 and 2 is characterized in that described emulsifying agent selects the compound emulsifying agent of anionic emulsifier and nonionic emulsifier for use.
4, method according to claim 3 is characterized in that anionic emulsifier comprises one or more in Sodium dodecylbenzene sulfonate, sodium laurylsulfonate, the sodium lauryl sulphate; Nonionic emulsifying agent comprises OP-10 and/or XP-10.
5, method according to claim 3 is characterized in that it is 1:2-1:1 that described emulsifying agent is selected its mass ratio of compound emulsifying agent of Sodium dodecylbenzene sulfonate and OP-10 for use.
6, method according to claim 1 is characterized in that the composition and the parts by weight thereof of nuclear consitution and shell component are as follows:
Shell component: Butyl Acrylate Monomer 30-50 Hydroxyethyl acrylate monomers 0.5-2.5 methacrylic acid monomers 1-5
Styrene monomer 5-15 methyl methacrylate monomers 10-20 modified monomers 3-10
Ammonium persulfate 0.1-0.4 Sodium dodecylbenzene sulfonate 0.5-2.0 OP-10 0.25-15
Nuclear consitution: Butyl Acrylate Monomer 25-45 methyl methacrylate monomers 10-30 styrene monomers 5-15
Methacrylic acid monomer 1-3 Hydroxyethyl acrylate monomers 0.5-2.0 sodium bicarbonate 0.1-0.25
OP-10 0.25-1.5 Sodium dodecylbenzene sulfonate 0.5-2.0 ammonium persulfates 0.1-0.4
The summation of said components consumption is 100.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101237467A CN100489047C (en) | 2006-11-24 | 2006-11-24 | Process for preparing acrylic acid emulsion adhesive for rubber |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006101237467A CN100489047C (en) | 2006-11-24 | 2006-11-24 | Process for preparing acrylic acid emulsion adhesive for rubber |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1962793A CN1962793A (en) | 2007-05-16 |
| CN100489047C true CN100489047C (en) | 2009-05-20 |
Family
ID=38082028
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006101237467A Expired - Fee Related CN100489047C (en) | 2006-11-24 | 2006-11-24 | Process for preparing acrylic acid emulsion adhesive for rubber |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100489047C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104910838A (en) * | 2015-06-05 | 2015-09-16 | 华南理工大学 | Emulsion-type polyacrylate pressure-sensitive adhesive, and preparation method and application thereof |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101205449B (en) * | 2007-12-05 | 2012-02-22 | 东莞市英科水墨有限公司 | Leather binder and preparation thereof |
| CN101376796B (en) * | 2008-09-08 | 2010-09-08 | 河北华夏实业有限公司 | Aqueous bottom glue for soft polychloroethylene contact adhesive tape and manufacturing method thereof |
| JP6001241B2 (en) * | 2010-05-18 | 2016-10-05 | 日東電工株式会社 | Optical film adhesive composition, optical film adhesive layer, adhesive optical film, and image display device |
| CN102492379B (en) * | 2011-11-29 | 2013-06-19 | 广东达美新材料有限公司 | Fog-resistant aqueous pressure-sensitive adhesive and polyethylene protection film containing same |
| CN102533179B (en) * | 2011-12-16 | 2014-04-16 | 广东达美新材料有限公司 | Acrylate emulsion pressure-sensitive adhesive and preparation method thereof |
| CN103172786A (en) * | 2012-03-26 | 2013-06-26 | 唐述华 | Polyacrylic emulsion with good binding resistance, water resistance, smoothness and adhesive force and low-temperature film-forming property at same time |
| CN103626912A (en) * | 2013-05-17 | 2014-03-12 | 佛山市三水灏诚合成树脂有限公司 | Aqueous acrylate emulsion adhesive for colorful metallic tiles and preparation method thereof |
| CN105602490B (en) * | 2016-01-25 | 2017-06-06 | 华南理工大学 | A kind of double-component emulsion-type polyacrylate pressure-sensitive and preparation method and application |
| CN107163179B (en) * | 2017-04-11 | 2019-11-19 | 河北晨阳工贸集团有限公司 | Hud typed acrylic emulsion and the environment-friendly water-based bloom finishing coat of zero VOC and preparation method thereof |
| CN110467899B (en) * | 2019-08-23 | 2021-05-18 | 武汉双键开姆密封材料有限公司 | Double-component aqueous polyurethane adhesive with high bonding strength |
| CN110746903B (en) * | 2019-10-25 | 2021-08-06 | 江苏国胶新材料有限公司 | Water-based acrylate pressure-sensitive adhesive for automobile protective film and preparation method thereof |
| CN112029040A (en) * | 2020-08-24 | 2020-12-04 | 上海东升新材料有限公司 | Preparation method of acrylate core-shell structure emulsion for insect-trapping board glue |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1546541A (en) * | 2003-12-12 | 2004-11-17 | 华东理工大学 | Shell-core type fluoride containing emulsion |
-
2006
- 2006-11-24 CN CNB2006101237467A patent/CN100489047C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1546541A (en) * | 2003-12-12 | 2004-11-17 | 华东理工大学 | Shell-core type fluoride containing emulsion |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104910838A (en) * | 2015-06-05 | 2015-09-16 | 华南理工大学 | Emulsion-type polyacrylate pressure-sensitive adhesive, and preparation method and application thereof |
| CN104910838B (en) * | 2015-06-05 | 2017-03-01 | 华南理工大学 | A kind of emulsion-type polyacrylate pressure-sensitive and preparation method and application |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1962793A (en) | 2007-05-16 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100489047C (en) | Process for preparing acrylic acid emulsion adhesive for rubber | |
| CN101362929B (en) | Emulsion type adhesive for paper and plastics and preparation method thereof | |
| CN107573469A (en) | A kind of preparation method of the Acrylate pressure-sensitive adhesive emulsion of block structure | |
| CN103059212B (en) | Hydrogenated rosin modified acrylic ester hybridization emulsion and preparation method and application thereof | |
| CN101597355B (en) | Water-based room temperature crosslinking acrylic acid emulsion and preparation method thereof | |
| CN1384169A (en) | Two-component structure adhesive with long service life | |
| CN105531340A (en) | Acrylic emulsion adhesive, and production method for same | |
| CN1622987A (en) | Rubber-acrylic adhesive formulation | |
| CN106753087B (en) | A kind of aqueous, environmental protective all-purpose adhesive and preparation method thereof | |
| CN104004477A (en) | Room temperature self-crosslinking polyacrylate pressure-sensitive adhesive and preparation method and application thereof | |
| CN101818034B (en) | Alcohol-soluble decorative adhesive and preparation method thereof | |
| CN102504091B (en) | Method for preparing emulsion acrylic pressure-sensitive adhesive for high-speed coating machine | |
| CN102532403A (en) | Shell-structure acrylic emulsion for dispersible glue powder and preparation method of shell-structure acrylic emulsion | |
| KR20180064482A (en) | Repellency - Adhesive composition having reworkability | |
| CN105408437B (en) | Pressure-sensitive adhesive agent dispersion for protective film is prepared by multistage emulsion polymerization | |
| CN103946253B (en) | The manufacture method of acrylic acid series polymeric compounds, acrylic acid series polymeric compounds and acrylic sol composition | |
| CN110734718A (en) | high-strength low-odor double-component acrylate structural adhesive and preparation method thereof | |
| CN100447170C (en) | Method for promoting grafting efficiency of acrylate core/shell structure latex particle | |
| CN108192024A (en) | Liquid coumarone resin and preparation method thereof | |
| CN104449457B (en) | For primer accelerator that inert material is bonding and preparation method thereof | |
| JP5533406B2 (en) | UV curable adhesive composition | |
| CN108659752A (en) | A kind of label water-soluble polyacrylate pressure sensitive adhesive, preparation method and application | |
| CN1823150A (en) | Water-whitening resistant latex emulsion pressure sensitive adhesive and its production | |
| CN1216113C (en) | Method for preparing pressure-sensitive hybridization compound latex adhesive | |
| CN110157360B (en) | Acrylate emulsion adhesive for bonding low-surface-energy base material and preparation 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 | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| EE01 | Entry into force of recordation of patent licensing contract |
Assignee: ZHUHAI YUTIAN CHEMICAL PRODUCTS CO., LTD. Assignor: South China University of Technology Contract record no.: 2010440000924 Denomination of invention: Process for preparing acrylic acid emulsion adhesive for rubber Granted publication date: 20090520 License type: Exclusive License Open date: 20070516 Record date: 20100708 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20090520 Termination date: 20141124 |
|
| EXPY | Termination of patent right or utility model |