Patent Grant
10975273
The present invention relates to an aqueous polymer emulsion. The present invention also relates to an aqueous adhesive composition containing such aqueous polymer emulsion which is used in laminates, textile and non-woven fabrics.
Aqueous vinyl acetate polymer emulsions are widely used as binders in the adhesive industry because they are relatively inexpensive compared to acrylic emulsions. Vinyl acetate has high water solubility, a high monomer-polymer swelling ratio, and a high chain transfer constant. However, the use of vinyl acetate monomers in adhesives may hurt the emulsion storage stability of polymer emulsions. Usually, this problem can be solved by increasing the amount of surfactants added or by adding protective colloids such as polyvinyl alcohol (“PVOH”) and hydroxyethyl cellulose (“HEC”) to the vinyl acetate polymer emulsions to provide required stability. However, adding high levels of surfactants is not economical and may have negative effect on emulsion water-sensitivity, which may cause foaming in the adhesives as well as deteriorating adhesive performance such as bond strength. The addition of protective colloid may also lead to high emulsion viscosity.
It is therefore desired to provide an aqueous vinyl acetate polymer emulsion with low viscosity and acceptable emulsion storage stability, and an aqueous adhesive composition containing such aqueous vinyl acetate polymer emulsion with acceptable adhesive performance, such as bond strength and heat seal strength.
The present invention provides a novel aqueous vinyl acetate polymer emulsion with low viscosity and acceptable emulsion storage stability, and an aqueous adhesive composition containing such aqueous vinyl acetate polymer emulsion with acceptable adhesive performance, such as bond strength and heat seal strength.
In a first aspect of the present invention there is provided an aqueous polymer emulsion comprising: i) as polymerized units, from 20% to 80% by dry weight, based on total dry weight of the polymer, of vinyl acetate; ii) as polymerized units, from 20% to 80% by dry weight, based on total dry weight of the polymer, of an α,β-ethylenically unsaturated carboxylic ester monomer; iii) as polymerized units, from 0.1% to 5% by dry weight, based on total dry weight of the polymer, of a stabilizer monomer; iv) from 0.05% to 1% by dry weight, based on total dry weight of the polymer, of a surfactant, wherein said aqueous polymer emulsion has a viscosity of less than 100 cps.
In a second aspect of the present invention there is provided an aqueous adhesive composition comprising the aqueous polymer emulsion.
An aqueous polymer emulsion comprising, as polymerized units, from 20% to 80%, preferably from 30% to 55%, and more preferably from 35% to 50%, by dry weight, based on total dry weight of the polymer, of vinyl acetate.
The aqueous polymer emulsion further comprises, as polymerized units, from 20% to 80%, preferably from 45% to 70%, and more preferably from 50% to 65%, by dry weight, based on total dry weight of the polymer, of an α,β-ethylenically unsaturated carboxylic ester monomer.
Suitable examples of the α,β-ethylenically unsaturated carboxylic ester monomers include (meth)acrylic ester monomers, i.e., methacrylic ester or acrylic ester monomers such as methyl acrylate, ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate, decyl acrylate, lauryl acrylate, methyl methacrylate, butyl methacrylate, isodecyl methacrylate, lauryl methacrylate, 2-hydroxybutyl acrylate, 2-hydroxyethyl methacrylate, and 2-hydroxypropyl methacrylate; itaconic ester monomers such as dimethyl itaconate, dibutyl itaconate; and maleic ester such as dioctyl maleate; Preferably, the α,β-ethylenically unsaturated carboxylic ester monomers are ethyl acrylate, methyl methacrylate, butyl acrylate, 2-ethylhexyl acrylate, and any combinations thereof. More preferably, the α,β-ethylenically unsaturated carboxylic ester monomer are butyl acrylate, 2-ethylhexyl acrylate, and any combinations thereof.
The aqueous polymer emulsion further comprises, as polymerized units, from 0.1% to 5%, preferably from 0.1% to 2.5%, and more preferably from 0.1% to 1.5% by dry weight, based on total dry weight of the polymer, of a stabilizer monomer.
Suitable examples of the stabilizer monomers include sodium styrene sulfonate, sodium vinyl sulfonate, 2-acrylamido-2-methylpropanesulfonic acid, acrylamide, acrylic acid, methacrylic acid, itaconic acid, and any combinations thereof.
The aqueous polymer emulsion may further comprise a vinyl ester monomer other than vinyl acetate. Suitable examples of the vinyl ester monomers include vinyl propionate, vinyl neononanoate, vinyl neodecanoate, vinyl 2-ethylhexanoate, vinyl pivalate, vinyl versatate and any combinations thereof.
The glass transition temperature (“Tg”) of the aqueous polymer emulsion is from 8° C. to −43° C., preferably from −14° C. to −32° C., and more preferably from −23° C. to −30° C. Tgs herein are calculated using the Fox Equation (T. G. Fox, Bull. Am. Physics Soc., Volume 1, Issue 3, page 123 (1956)).
The solids content of the aqueous polymer emulsion is from 30% to 60%. It is preferably from 35% to 50%, and more preferably from 41% to 45%.
The viscosity of the aqueous polymer emulsion is less than 100 cps, preferably less than 50 cps, and more preferably less than 30 cps, as measured by a Brookfield LVT Dial-Reading Viscometer (Spindle #2 at 60 rpm).
The particle size of the aqueous polymer emulsion is from 150 nm to 500 nm, and preferably from 250 nm to 350 nm.
Preferably, the aqueous polymer emulsion has a grit of less than 0.2%, preferably less than 0.02%, and more preferably less than 0.01% by weight, based on total weight of the polymer. The grit is determined by filtering 200 g of the aqueous polymer emulsion through a 325 mesh filter, and subsequently drying and weighing the dried grit.
The polymerization process used herein can be carried out using known method for preparing an aqueous emulsion polymer.
The aqueous polymer emulsion further comprises, as emulsifier, from 0.05% to 1%, preferably from 0.05% to 0.5%, and more preferably from 0.05% to 0.3% by dry weight, based on total dry weight of the polymer, a surfactant.
The surfactant is preferably a combination of anionic surfactant and non-ionic surfactant with a mole ratio of the ionic surfactant to that of the non-ionic surfactant being 0.5 to 20, preferably being 1 to 10, and more preferably being 2 to 5.
Suitable examples of the anionic surfactants include sulfates, sulfonates, phosphates, carboxylates, and any combinations thereof. Preferably, the anionic surfactant is sulfonate such as sodium dodecyl benzene sulfonate, sodium dodecyl sulfonate, sodium dodecyl diphenyl oxide disulfonate, sodium n-decyl diphenyl oxide disulfonate, isopropylamine dodecylbenzenesulfonate, and sodium hexyl diphenyl oxide disulfonate. More preferably, the anionic surfactant is sodium dodecyl benzene sulfonate.
Suitable examples of non-ionic surfactants include polyoxyethylenated alkylphenols, polyoxyethylenated alcohols, ethylene oxide-propylene oxide block copolymers, polyoxyethylenated fatty acid esters. Preferably, the non-ionic surfactant is polyoxyethylenated alcohols with general molecule as RO—(CH2CH2O)nH, wherein R is alkyl group. More preferably, alkyl group R is C12-C18 and oxyethylene group —(CH2CH2O)— is greater than 20. Commercially available non-ionic surfactant includes TERGITOL™ 15-S-40 from The Dow Chemical Company.
Preferably, protective colloid is excluded from the aqueous polymer emulsion of the present invention. Protective colloid can be (1) natural or modified-natural products such as gum agar, gum arabic, gum tragacanth, water soluble starch, pectin, gelatin, and aliginate, and modified cellulose such as hydroxylethyl cellulose and carboxymethyl cellulose; or (2) synthetic products such as polyvinyl alcohol with a hydrolysis degree of from 70 to 100 mol %.
An aqueous adhesive composition comprising said aqueous polymer emulsion is prepared by techniques which are well known in the adhesives art. Optionally, such adhesive composition may comprise additional water, latex binder, crosslinker, and additives such as rheology modifiers, biocides, wetting and defoaming agents. Preferably, the aqueous adhesive composition excludes further addition of any surfactants during the preparation of the aqueous adhesive composition.
The aqueous adhesive composition is applied onto the surface of ordinary substrates such as biaxially oriented polypropylene film, polyester film, or nylon film, and dried to form a dry layer. The applied adhesive composition is considered to be dry when the remainder of water is less than 10% of the applied adhesive composition.
The surface of a vacuum metallized casted polypropylene film, casted polypropylene film or polyethylene film is covered on the dry layer of applied adhesive composition so that a biaxially oriented polypropylene film/adhesive/vacuum metallized casted polypropylene film composite (composite films, and also known as the laminate) is formed. The laminate is preferably subjected to mechanical force to press the films even more closely. Such mechanical force is preferably applied by passing the laminate between rollers. Preferably, the rollers are heated.
In the present disclosure, the technical features in each preferred technical solution and more preferred technical solution can be combined with each other to form new technical solutions unless indicated otherwise. For briefness, the specification omits the descriptions for these combinations. However, all the technical solutions obtained by combining these technical features should be deemed as being literally described in the present specification in an explicit manner.
1. Emulsion Storage Stability (Stability)
The pH value, solid content, viscosity and grit of the fresh polymer emulsion samples were recorded. Then, each of the fresh polymer emulsion samples was poured into a 250 ml glass bottle leaving no free space on the top of the emulsion surface. Bottles were then sealed up appropriately with additional tape around the cover. The sealed bottles were put in a 50° C. oven and aged for a period of time, then taken out and cooled down in room temperature. The pH value, solid content (top & bottom), and viscosity of aged polymer emulsion samples were measured again, and they were further observed for gel, grit or separation. The time aged in the oven was also recorded.
2. Bond Strength
Laminates prepared from adhesive compositions were cut into 15 mm width strips for T-peel test under 250 mm/min crosshead speed using a 5940 Series Single Column Table Top System available from Instron Corporation. During the test, the tail of each strip was pulled slightly by fingers to make sure the tail remained 90 degree to the peeling direction. Three strips for each sample were tested and the average value was calculated. Results were in the unit of N/15 mm. The higher the value is, the better the bond strength is.
3. Heat Seal Strength
Laminates prepared from adhesive compositions were heat-sealed in a HSG-C Heat-Sealing Machine available from Brugger Company under 140° C. seal temperature and 300N pressure for 1 second, then cooled down and cut into 15 mm width strips for heat seal strength test under 250 mm/min crosshead speed using a 5940 Series Single Column Table Top System available from Instron Corporation. Three strips for each sample were tested and the average value was calculated. Results were in the unit of N/15 mm. The higher the value is, the better the heat seal strength is.
1. Preparation of Aqueous Polymer Emulsions
Monomer Emulsion Preparation: An emulsified monomer mixture was prepared by adding 435.0 g of DI water, 9.6 g of DS-4, 11.5 g of V3525, 854.5 g of BA, 36.0 g of AA and 548.0 g of VA slowly to the agitated solution before polymerization.
Polymerization: A solution containing 0.9 g of sodium bicarbonate and 730.0 g of DI water were placed in a 5-necked, 5-liter round bottom flask equipped with a thermocouple, a cooling condenser and an agitator, and heated to 74° C. under nitrogen. 0.01 g FeSO4, 0.01 g EDTA tetrasodium salt, 3.2 g of APS and 28.7 g of perform seed in 51.0 g of DI water were charged into the flask. When the temperature was at 74° C., monomer mixture and a co-feed solution of 3.2 g of APS solved in 148.0 g DI water and 0.7 g of IAA solved in 148.0 g DI water were fed in 210 minutes. The polymerization reaction temperature was maintained at 73-75° C. Upon completion of the additions, the reaction mixture was cooled to 70° C. before gradual addition of a solution of 3.0 g t-BHP (70% active content) in 28.2 g DI water and 2.3 g SBS solved in 28.2 g DI water in 45 minutes with stirring. Upon completion of the feeds, the reaction was cooled to room temperature. 6.8 g Na2CO3 in 78.2 g DI water was then drop added in 30 minutes to adjust pH value to 6.0-8.0. Then, 0.11 g of KATHON™ LX biocide was added with stirring in 30 minutes. Proper amount of DI water was added to adjust final solids to 42-45%.
Polymer emulsions were prepared by using the procedure outlined for Inventive Example 1. The weights for the monomer emulsions are detailed in Table 1.
Monomer Emulsion Preparation: An emulsified mixture was prepared by adding 435.0 g of DI water, 9.6 g of DS-4, 0.9 g of 15-S-40, 11.5 g of V3535, 883.1 g of BA, 14.4 g of AA and 540.8 g of VA slowly to the agitated solution before polymerization.
Polymerization: A solution containing 0.9 g of sodium bicarbonate and 587.3 g of DI water were placed in a 5-necked, 5 liter round bottom flask equipped with a thermocouple, a cooling condenser and an agitator, and heated to 74° C. under nitrogen. Charge 7.18 g HEC A dispersed in 143.6 g hot water. Charge 0.01 g FeSO4, 0.01 g EDTA tetrasodium salt, 3.2 g of APS and 28.7 g of perform seed in 51.0 g of DI Water into the kettle. When the temperature was at 74° C., monomer emulsion and a co-feed solution of 3.2 g of APS solved in 148.0 g of DI water and 0.7 g of IAA solved in 148.0 g of DI water were fed in 210 minutes. The polymerization reaction temperature was maintained at 73-75° C. Upon completion of the additions the reaction mixture was cooled to 70° C. before gradual addition of solution of 3.0 g t-BHP (70% active content) in 28.2 g DI water and 2.3 g SBS solved in 28.2 g DI water in 45 minutes with stirring. Upon completion of the feeds, the reaction was cooled to room temperature. Add 6.8 g Na2CO3 in 78.2 g water solution drop adding in 30 minutes to adjust pH value to 6.0˜8.0. Then add 0.11 g of KATHON™ LX biocide with stirring 30 minutes. Add proper amount of DI water to adjust final solids to 42-45%.
Monomer Emulsion Preparation: An emulsified monomer mixture was prepared by adding 435.0 g of DI water, 9.6 g of DS-4, 0.9 g of 15-S-40, 11.5 g of V3535, 883.1 g of BA, 14.4 g of AA and 540.8 g of VA slowly to the agitated solution before polymerization.
Polymerization: A solution containing 0.9 g of sodium bicarbonate and 605.0 g of DI water were placed in a 5-necked, 5 liter round bottom flask equipped with a thermocouple, a cooling condenser and an agitator, and heated to 74° C. under nitrogen. Charge 14.6 g PVOH A dispersed in 125.0 g hot water. Charge 0.01 g FeSO4, 0.01 g EDTA tetrasodium salt, 3.2 g of APS and 28.7 g of perform seed in 51.0 g of DI Water into the kettle. When the temperature was at 74° C., monomer emulsion and a co-feed solution of 3.2 g of APS solved in 148.0 g of DI water and 0.7 g of IAA solved in 148.0 g of DI water were fed in 210 minutes. The polymerization reaction temperature was maintained at 73-75° C. Upon completion of the additions the reaction mixture was cooled to 70° C. before gradual addition of solution of 3.0 g t-BHP (70% active content) in 28.2 g DI water and 2.3 g SBS solved in 28.2 g DI in 45 minutes with stirring. Upon completion of the feeds, the reaction was cooled to room temperature. Add 6.8 g Na2CO3 in 78.2 g water solution drop adding in 30 minutes to adjust pH value to 6.0˜8.0. Then add 0.11 g of KATHON™ LX biocide with stirring 30 minutes. Add proper amount of DI water to adjust final solids to 42-45%.
Monomer Emulsion Preparation: An emulsified monomer mixture was prepared by adding 435.0 g of DI water, 51.2 g of DS-4, 15.8 g of 15-S-40, 11.5 g of V3535, 789.8 g of BA, 14.4 g of AA and 634.5 g of VA slowly to the agitated solution before polymerization.
Polymerization: A solution containing 0.9 g of sodium bicarbonate and 730.0 g of DI water were placed in a 5-necked, 5 liter round bottom flask equipped with a thermocouple, a cooling condenser and an agitator, and heated to 74° C. under nitrogen. Charge 0.01 g FeSO4, 0.01 g EDTA tetrasodium salt, 3.2 g of APS and 28.7 g of perform seed in 51.0 g of DI Water into the kettle. When the temperature was at 74° C., monomer emulsion and a co-feed solution of 3.2 g of APS solved in 148.0 g of DI water and 0.7 g of IAA solved in 148.0 g of DI water were fed in 210 minutes. The polymerization reaction temperature was maintained at 73-75° C. Upon completion of the additions the reaction mixture was cooled to 70° C. before gradual addition of solution of 3.0 g t-BHP (70% active content) in 28.2 g DI water and 2.3 g SBS solved in 28.2 g DI water in 45 minutes with stirring. Upon completion of the feeds, the reaction was cooled to room temperature. Add 6.8 g Na2CO3 in 78.2 g water solution drop adding in 30 minutes to adjust pH value to 6.0˜8.0. Then add 0.11 g of KATHON™ LX biocide with stirring 30 minutes. Add proper amount of DI water to adjust final solids to 42-45%.
The weight percent of the surfactant, protective colloid, stabilizer monomer, vinyl acetate and α,β-ethylenically unsaturated carboxylic ester monomer in Inventive Examples 1 to 8 and Comparative Examples 1 to 3 are detailed in Table 2.
2. Preparation of Aqueous Adhesive Compositions
The above aqueous polymer emulsions are used as aqueous adhesive compositions without further formulations.
3. Preparation for Laminates
BOPP and VMCPP films were used without any pre-treatment. The adhesive was coated on BOPP, dried and combined with VMCPP films to obtain BOPP/adhesive/VMCPP film composite with adhesive coating weight of 1.8 g/m2 on dry weight basis. Then the combined BOPP/adhesive/VMCPP film composite was curing on 50° C. for 1 day.
As Table 3 illustrates, all aqueous polymer emulsions of Inventive Examples 1 to 8 meet performance requirement, and exhibit good emulsion storage stability (greater than 1 month) and low viscosity (less than 100 cps). Both aqueous polymer emulsions of Comparative Example 1 and Comparative Example 2, which use HEC or PVOH respectively as protective colloid, exhibit high viscosity (greater than 300 cps) and poor emulsion storage stability (grit greater than 1%). Although Comparative Example 4 (Rovace™ Binder 662) exhibits good emulsion storage stability, the viscosity (greater than 300 cps) is higher than the desired performance requirement of less than 100 cps, due to the high surfactant level and added protective colloid.
As Table 4 illustrates, laminates prepared from the aqueous adhesive composition comprising aqueous polymer emulsions of Inventive Examples 3 to 5 exhibit good bond strength (greater than 1.0N/15 nm) and heat seal strength (greater than 10N/15 nm) adhesive performances. Especially, Inventive Example 5 shows optimized performance comparable to Comparative Example 5 (Robond™ Binder L-70D prepared from styrene-acrylic emulsion) which is used as a benchmark for performance goals. Although aqueous polymer emulsion of Comparative Example 3 exhibits good stability and low viscosity, the bond strength (less than 0.5N/nm) of the laminate prepared from the aqueous adhesive composition comprising aqueous polymer emulsion of Comparative Example 3 is much lower than Inventive Example 3 to 5 due to the high surfactant level.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/CN2015/096614 | 12/8/2015 | WO | 00 |
| Publishing Document | Publishing Date | Country | Kind |
|---|---|---|---|
| WO2017/096514 | 6/15/2017 | WO | A |
| Number | Name | Date | Kind |
|---|---|---|---|
| 3365410 | Wesslau | Jan 1968 | A |
| 5037700 | Davis | Aug 1991 | A |
| 5201948 | Fasano et al. | Apr 1993 | A |
| 6201062 | Weitzel et al. | Mar 2001 | B1 |
| 6203916 | Eisenhart et al. | Mar 2001 | B1 |
| 6251213 | Bartman et al. | Jun 2001 | B1 |
| 8067513 | Davis | Nov 2011 | B2 |
| 20120121921 | Cosyns et al. | May 2012 | A1 |
| 20120130035 | Schliwka et al. | May 2012 | A1 |
| Number | Date | Country |
|---|---|---|
| 101585894 | Nov 2009 | CN |
| 102559104 | Jul 2012 | CN |
| 103059211 | Apr 2013 | CN |
| 103435736 | Dec 2013 | CN |
| 105086886 | Nov 2015 | CN |
| 2011009800 | Jan 2011 | WO |
| 2015155157 | Oct 2015 | WO |
| 2015155159 | Oct 2015 | WO |
| 2016007313 | Jan 2016 | WO |
| Entry |
|---|
| Online translation of Detailed Description of CN 103059211 A; publication date: Apr. 2013 (Year: 2013). |
| T. G. Fox, Bull. Am. Physics Soc., vol. 1, Issue 3, p. 123 (1956). |
| PCT/CN2015/096614, International Search Report and Written Opinion dated Aug. 17, 2016. |
| Number | Date | Country | |
|---|---|---|---|
| 20180298247 A1 | Oct 2018 | US |
