1. Field of the Invention
The present invention relates to a vinyl acetate-ethylene copolymer emulsion and a paper coating composition based on the same. More specifically, the present invention relates to a vinyl acetate-ethylene copolymer emulsion based paper coating composition with low odor. The present invention also relates to processes for preparing the vinyl acetate-ethylene copolymer emulsion and the paper coating composition, and uses thereof.
2. Description of the Related Art
Aqueous emulsions, such as styrene-butadiene copolymer emulsion, styrene-acrylate copolymer emulsion, acrylate copolymer emulsion, vinyl acetate homopolymer emulsion, vinyl acetate-ethylene copolymer emulsion, etc., are commonly used as binder for paper surface coating in paper industry, and styrene-butadiene copolymer emulsion are the most widely used aqueous emulsion among others. With the advancement in modern printing package techniques, the requirements to the papers for using in printing and packing are also enhancing, in particular to those printing packages with high qualities such as cigarette package and food package which require that the package material per se has a low odor. Especially as the application of Ultra-Violet (UV) curable ink and electron beam radiation curable ink printing techniques recently, a higher requirement to the odor of the package material and therefore to the odor of the emulsion for surface coating has raised. However, traditional aqueous emulsions tend to be odorous and cannot meet the requirement of low odor paper coating, especially printing packages with high qualities such as cigarette package and food package.
Although a low odor aqueous emulsion is required in the art, few researches have been done to lower the odor of the aqueous emulsion used in paper making industry, and the factors which directly influence the odor of the emulsion are still unknown up to now. Furthermore, the odors of various kinds of emulsion polymers which have already cured under UV and electron beam radiation are still unpredictable respectively to the technicians in the art based on their past experiences.
Therefore, a need still exists for low odor aqueous emulsion and paper coating composition based on the same for application in printing packages with high qualities.
It has been surprisingly found by the present inventors that, by using a specific vinyl acetate-ethylene copolymer emulsion according to the present invention instead of commonly used aqueous emulsion such as styrene-butadiene emulsion as binder for paper coating compositions, especially high qualities paper coating compositions used in UV curable ink and electron beam radiation curable ink, such as those used in cigarette package and food package, a vinyl acetate-ethylene copolymer emulsion and a paper coating composition based on the same with extraordinary low odor are obtained.
The vinyl acetate-ethylene copolymer emulsion according to the present invention is obtained through aqueous emulsion polymerization of vinyl acetate and ethylene. It has been surprisingly found by the present inventors that the package paper made by using the inventive vinyl acetate-ethylene copolymer emulsion as binder for paper surface coating exhibits a extremely low odor after application of Ultra-Violet (UV) curable ink and electron beam radiation curable ink printing techniques, which can meet the low odor requirement sufficiently as needed by the market. Without wishing to be bound by any theory, but the applicant believes that the low odor performances as provided by the vinyl acetate-ethylene copolymer emulsion according to the present invention is partially attributed to following factors, such as the structure/composition properties of the vinyl acetate-ethylene copolymer emulsion and/or its advantages over commonly used styrene-butadiene copolymer emulsion, which could include: the vinyl acetate-ethylene copolymer emulsion is free of organic phenylic monomer, and the polymerization process is carried out without addition of phenylic derived monomer, therefore the residue of volatile phenylic derivative which has special odor such as 4-phenyl cyclohexene is avoided; ethylene, one of the monomers, is gas, thus can hardly retained in the emulsion; the vinyl acetate monomer and other possible volatile organic residues can be further reduced by chemical and physical process during or after the end of the polymerization, whereby the content of residue vinyl acetate monomer can be reduced to less than about 800 ppm, preferably less than about 600 ppm, more preferably less than about 400 ppm; furthermore, vinyl acetate ethylene copolymer will not release odorous substances by further chemical reaction under exposure to UV or electron beam radiation.
Thus, one object of the present invention is to provide a low odor vinyl acetate-ethylene copolymer emulsion.
Another object of the present invention is to provide a process for preparing said vinyl acetate-ethylene copolymer emulsion.
Still another object of the present invention is to provide a use of the vinyl acetate-ethylene copolymer emulsion for low odor paper coating composition.
Furthermore, one object of the present invention is to provide a low odor paper coating composition.
Another object of the present invention is to provide a process for preparing said low odor paper coating composition.
Still another object of the present invention is to provide a use of the low odor paper coating composition in printing packages with high qualities, such as cigarette package and food package.
For the purposes of this description, unless otherwise indicated, all numbers expressing quantities of ingredients, reaction conditions, and so forth used in the description and claims are to be understood as being modified in all instances by the term “about”. Accordingly, unless indicated to the contrary, the numerical parameters set forth in the following description and attached claims are approximations that may vary depending upon the desired properties sought to be obtained by the present invention. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter should at least be construed in light of the number of reported significant digits and by applying ordinary rounding techniques.
Notwithstanding that the numerical ranges and parameters setting forth the broad scope of the invention are approximations, the numerical values set forth in the specific Examples are reported as precisely as possible. Any numerical value, however, inherently contain certain errors necessarily resulting from the standard deviation found in their respective testing measurements.
It is noted that, as used in this description and the appended claims, the singular forms “a”, “an” and “the” include plural referents unless expressly and unequivocally limited to one referent.
According to one aspect of the present invention, a vinyl acetate-ethylene copolymer-based emulsion for low odor paper coating composition is provided, wherein the copolymer comprises, based on the total weight of the copolymer:
In some non-limiting embodiments of the present invention, the monomers used in emulsion polymerization can be composed of about 65-95 pphm of vinyl acetate, about 5-35 pphm of ethylene and about 0-10 pphm of other comonomers or functional monomers. Examples of other comonomers or functional monomers suitable for the present invention include, but not limited to, one or more selected from the group of:
wherein each of R1 and R2 is hydrogen or alkyl group, provided that the total carbon atom number of R1 and R2 is from 1 to 14;
wherein R3 is hydrogen or alkyl group with 1 to 16 carbon atom(s);
wherein R4 is hydrogen or alkyl group with 1 to 16 carbon atom(s);
wherein each of R5 and R6 is alkyl group with 1 to 16 carbon atom(s);
In some non-limiting embodiments of the present invention, said surfactant can be selected from anionic surfactants, nonionic surfactants or combination thereof.
Examples of anionic surfactants suitable for the present invention include, but not limited to: alkylsulfates, alkylsulfonates, alkyl benzenesulfonates, alkyl polyoxyethylene ether sulfates, alkylpolyoxyethylene-propylene ether sulfates, sodium fatty alcohol succinic acid mono ester sulfonates, disodium fatty alcohol polyoxyethylene ether sulfosuccinates, disodium fatty alcohol polyoxyethylene-propylene ether sulfosuccinates, alkylpolyoxyethylene phosphates, alkylpolyoxyethylene-propylene phosphates and alkali metal salts of fatty acids. Specific examples of anionic surfactants suitable for the present invention include, but not limited to: sodium dodecylbenzene sulfonate, sodium dodecylsulfonate, sodium dodecylsulfate, disodium dodecyldiphenylether sulfonate, octadecyl sulfosuccinic acid and sodium dioctylsulfosuccinate. In some non-limiting embodiments of the present invention, the anionic surfactants as mentioned above can be used in the form of aqueous solution.
Examples of nonionic surfactants suitable for the present invention include, but not limited to: linear alkyl alcohol polyoxyethylene ethers, linear alkyl alcohol polyoxyethylene-propylene ethers, branched alkyl alcohol polyoxyethylene ethers, branched alkyl alcohol polyoxyethylene-propylene ethers, fatty acid polyoxyethylenemonoesters, fatty acid polyoxyethylene-propylenemonoesters. Specific examples of nonionic surfactants suitable for the present invention include, but not limited to: isometric tridecyl alcohol polyoxyethylene monoether, cetyl alcohol polyoxyethylenemonoether, octadecyl alcohol polyoxyethylenemonoether lauroylhydroxylpolyoxyethylene, etc., wherein the EO numbers of polyoxyethylene section are chosen according to the desired HLB value of the surfactant, typically in the range of about 20 to 40. In some non-limiting embodiments of the present invention, the nonionic surfactants as mentioned above can be used in the form of aqueous solution.
In some non-limiting embodiments of the present invention, the surfactant can be used in an amount of about 1-5 pphm, preferably about 2-5 pphm, more preferably about 2-4 pphm.
In some non-limiting embodiments of the present invention, the polymeric protective colloid can be selected from partially hydrolyzed polyvinyl alcohols, cellulose ethers and polyvinyl pyrrolidone. Specific examples of polymeric protective colloids suitable for the present invention include, but not limited to: polyvinyl alcohols having a degree of alcoholysis of about 75 to 95%, more preferably about 70 to 92% and a degree of polymerization of about 200 to 4000, more preferably polyvinyl alcohols having a degree of alcoholysis of about 80 to 90% and a degree of polymerization of about 200 to 4000. Cellulose ethers as polymeric protective colloid suitable for the present invention include, but not limited to, hydroxymethyl cellulose ether, hydroxyl ethylcellulose ether and hydroxypropyl cellulose ether. In some non-limiting embodiments of the present invention, the polymeric protective colloid can be used in an amount of about 0-10 pphm, preferably about 0-5 pphm.
According to one aspect of the present invention, a low odor paper coating composition, comprising a solid component and a binder, characterized in that said binder comprises:
The low odor paper coating composition comprises the solid component and the binder. In some non-limiting embodiments of the present invention, the weight ratio of solid component to binder is about 100:6 to 100:19, preferably about 100:8 to 100:16.
The solid component used in low odor paper coating composition can comprise, but not limited to, kaolin, calcium carbonate or a mixture thereof.
The binder used in low odor paper coating composition comprises mainly vinyl acetate-ethylene copolymer-based emulsion and additional water. In some non-limiting embodiments of the present invention, the binder can have a solid content of about 40 to 70%, more commonly about 50 to 60% by weight.
In some non-limiting embodiments of the present invention, the binder used in low odor paper coating composition essentially consists of vinyl acetate-ethylene copolymer-based emulsion, additional water and other conventional additives.
The conventional additives added to the aqueous phase of the binder may include those known in the art which are useful in the emulsion polymerization system or improve the stability or pot life of the final emulsion. For example, those additives can be redox reaction promoter, pH adjusting agents, ion intensity regulators, molecular weight modifiers, defoamers, fungicides, chelating agents, and the like.
In some non-limiting embodiments of the present invention, the emulsion polymerization is conducted in the presence of a redox initiator. The oxidizing agent and reducing agent used to make up of the redox initiator include, but not limited to water soluble oxidizing agents and reducing agents known in the art. Examples of oxidizing agents and reducing agents suitable for the present invention may include, but not limited to, ammonium persulfate, sodium persulfate, hydrogen peroxide, tert-butyl peroxide, sodium formaldehyde-sulfoxylate, disodium 2-hydroxyl-2-sulfinatoacetate, ascorbic acid, erythorbic acid, alkali metal salts of ascorbic acid, alkali metal salts of erythorbic acid, sodium bisulfite, sodium sulfite, sodium metabisulfite, sodium thiosulfate, etc. Typically, the oxidizing agent and reducing agent can be each added in an amount of about 0.05 to 5 pphm.
According to another aspect of the present invention, a process for preparing the vinyl acetate-ethylene copolymer-based emulsion is provided. Said process comprises emulsion polymerizing a monomeric composition comprising:
According to another aspect of the present invention, a process for preparing the low odor paper coating composition is provided, said process comprises
In a preferable embodiment of the present invention, the emulsion may be obtained by the following steps: forming an aqueous phase by adding surfactant and protective colloid, as emulsifier, and other additives such as defoamers, pH adjusting agents, ion intensity regulators, molecular weight modifiers, etc. into water under stirring; feeding the aqueous phase to a reactor under slow stirring; evacuating the reactor under vacuum and purging with nitrogen several times for removing any air; raising the temperature of the reactor to about 40-70° C., then increasing the speed of stirring, adding to the reactor part of the vinyl acetate monomer or mixture of the vinyl acetate monomer and the other comonomers or functional monomers, together with part of ethylene gas; after the temperature and pressure of the reactor becomes stable, adding dropwise oxidizing agent and reducing agent, as polymerization initiator, so that polymerization takes place, with increasing of temperature; adding remaining monomers when the temperature of the reactor reaches a predetermined value, about 50-90° C., until the consumption of the monomers. The temperature of the reactor was controlled at about 50-90° C. during the emulsion polymerization process. After completion of polymerization, the reactor is cooled to selected temperature, about 50-70° C., and the polymerization product therein was transferred to a post-treatment reactor, while the unreacted ethylene gas was discharged as exhaust gas. Subsequently, certain amount of oxidizing agent and reducing agent were added to the post-treatment reactor, to reduce the amount of residual monomers by further initiating the polymerization of residual monomers. Alternatively, the amount of residual monomers can be further reduced by extraction of water vapor. Finally, the emulsion parameters of the copolymer-based emulsion thus obtained can be adjusted by feeding with additional water and/or other conventional additives, such as fungicides, pH adjusting agents, etc. The emulsion thus obtained can have a solid content of about 40 to 70%, most commonly about 50 to 60% by weight, and can be used as binder for the low odor paper coating composition according to the present invention.
In some non-limiting embodiments of the present invention, a vinyl acetate-ethylene copolymer-based emulsion was obtained according to the above mentioned formulation and process, and the vinyl acetate-ethylene copolymer-based emulsion thus obtained can be used to formulate the low odor paper coating composition.
In a preferable embodiment of the present invention, the low odor paper coating composition may be obtained by the following steps: forming an slurry by mixing the solid component with water, dispersing agents, defoamers and the like; the slurry thus obtained is added with the binder derived from the vinyl acetate-ethylene copolymer-based emulsion and co-adjuvants such as fluorescent whiteners, rheology modifiers, etc., and mixed under stirring to obtain a homogeneous paper coating composition.
In some non-limiting embodiments of the present invention, the low odor paper coating composition according to the present invention comprises:
According to the concept of the present invention, the present invention comprises the following items:
1. A low odor paper coating composition, comprising a solid component and a binder, characterized in that said binder comprises:
wherein each of R1 and R2 is hydrogen or alkyl group, provided that the total carbon atom number of R1 and R2 is from 1 to 14;
wherein R3 is hydrogen or alkyl group with 1 to 16 carbon atom(s);
wherein R4 is hydrogen or alkyl group with 1 to 16 carbon atom(s);
wherein each of R5 and R6 is alkyl group with 1 to 16 carbon atom(s);
wherein each of R1 and R2 is hydrogen or alkyl group, provided that the total carbon atom number of R1 and R2 is from 1 to 14;
wherein R3 is hydrogen or alkyl group with 1 to 16 carbon atom(s);
wherein R4 is hydrogen or alkyl group with 1 to 16 carbon atom(s);
wherein each of R5 and R6 is alkyl group with 1 to 16 carbon atom(s);
The inventive paper coating composition has extraordinary low odor, even after application of Ultra-Violet (UV) curable ink and electron beam radiation curable ink printing techniques. In the context of this application, the term “low odor” means that the inventive paper coating composition pass the odor evaluation test as described hereinafter.
The odor evaluation test can be carried out as follows:
In some non-limiting embodiments of the present invention, the inventive low odor paper coating composition made from vinyl acetate-ethylene copolymer-based emulsion produce by aqueous emulsion polymerization as described above exhibits a final score of greater than 30, more preferably greater than 40 when compared with other paper coating composition made from traditional aqueous emulsions, such as styrene-butadiene copolymer emulsion, styrene-acrylate copolymer emulsion, acrylate copolymer emulsion, vinyl acetate homopolymer emulsion, vinyl acetate-ethylene copolymer emulsion, etc.
The following Examples are included to demonstrate preferred embodiments of the invention. It should be appreciated by those of skill in the art that the techniques disclosed in the Examples which follow represent techniques discovered by the inventor to function well in the practice of the invention, and thus can be considered to constitute preferred modes for its practice. However, those of skill in the art should, in light of the present disclosure, appreciate that many changes can be made in the specific embodiments which are disclosed and still obtain a like or similar result without departing from the spirit and scope of the invention.
Unless indicated to the contrary, all parts and percentages are by weight.
The odor of the inventive paper coating composition and other comparative paper coating compositions are tested according to the odor evaluation test as described above.
To a 10 L reactor was added 2.4 kg deionized water, 116 g polyvinyl alcohol having an alcoholysis degree of 88% and a viscosity of 5 mPa·s in 4% aqueous solution at 20° C. and 120 g polyvinyl alcohol having an alcoholysis degree of 88% and a viscosity of 23 mPa·s in 4% aqueous solution at 20° C. with stirring (300 rpm). The reactor was heated to 99° C. and maintained for 1 hour to obtain a sufficiently dissolved solution. The reactor was then cooled to 55° C. 33 g Disponil A3065 (Cognis, with a concentration of 65%), 3 g sodium acetate and 6 g 85% phosphoric acid solution (which were used to adjust the pH of the solution), 2 g silicone defoamer and 0.2 g 40% ferric chloride solution were added sequentially into the reactore to provide a catalyst for the polymerization reaction. The reactor was evacuated and purged with nitrogen for three times to remove residual air. The stirring speed was then increased to 600 rpm. 2.9 kg vinyl acetates were added into the reactor by feeding pump, and 550 g ethylene gases were fed into the reactor at the same time. The pressure of the reactor was equilibrated for 5 mins, and then the reactor was charged with 35 g of 1.7 wt % aqueous solution of disodium 2-hydroxy-2-sulfinatoacetate. The reactor was kept under 55° C. and equilibrated for 5 mins. The polymerization reaction was initiated by feeding into the reactor with the following initiators: 1.5 wt % aqueous solution of t-butyl peroxide with a starting feeding rate of 94.5 g/h, 1.7 wt % aqueous solution of disodium 2-hydroxy-2-sulfinatoacetate with a starting feeding rate of 94.5 g/h. When the temperature of the reactor reached 57° C., the reaction temperature was controlled by adjusting the flow rates of the initiators so that the reaction temperature increased to 85° C. in 20 mins and then was maintained under 85° C. When temperature of the reactor reached 72° C., 230 g ethylene gases were added, and the maximum pressure inside the reactor was maintained below 60bar. When temperature of the reactor reached 80° C., 1.24 kg vinyl acetates were added into the reactor with a feeding rate of 1.26 kg/h.
After completion of adding the initiators, the reactor was cooled to 55° C. The obtained emulsion was transferred to post-treatment reactor.
The post-treatment reactor was stirred at a speed of 200 rpm and charged with 90 g of 3.1 wt % aqueous solution of disodium 2-hydroxy-2-sulfinatoacetate in 30 mins, then 90 g of mixture of 1 wt % aqueous solution of t-butyl peroxide and 1 wt % aqueous solution of hydrogen peroxide in 30 mins. The post-treatment reactor was kept under a vacuum degree of −0.3 bar. When the temperature of the post-treatment reactor reached 65° C., a total amount of 105 g water vapor was charged in to the post-treatment reactor for extraction. Finally, the post-treatment reactor was cooled to 40° C. 30 g 1.5% CIT/MIT fungicides were added into the post-treatment reactor.
The properties of the obtained vinyl acetate-ethylene copolymer-based emulsion (Emulsion 1) are listed in Table 1.
A vinyl acetate-ethylene copolymer-based emulsion (Emulsion 2) was prepared according to the procedure in Example 1, except that the post-treatment reactor has not subjected to water vapor extraction. The obtained vinyl acetate-ethylene copolymer-based emulsion (Emulsion 2) has a residual monomer content of 685 ppm.
A commercial available styrene-butadiene copolymer emulsion (Comparative Emulsion 1) for paper coating was obtained, which has a residual monomer content of 60 ppm.
A commercial available styrene-acrylate copolymer emulsion (Comparative Emulsion 2) for paper coating was obtained, which has a residual monomer content of 550 ppm.
The emulsions as obtained in Example 1-2 and Comparative Example 1-2 were used to prepare paper coating compositions respectively according to the formulation as listed in Table 2.
The paper coating compositions thus obtained were tested according to the odor evaluation test as described above respectively and the results are summarized in Table 3.
According to results of Table 3, although the residual monomer content of Emulsion 1 (291 ppm) is higher than that of Comparative Emulsion 1 (60 ppm), the paper coating composition prepared from Emulsion 1 according to the present invention exhibits a much higher score than that of the paper coating composition prepared from Comparative Emulsion 1. The paper coating composition prepared from Emulsion 2 with a high residual monomer content of 685 ppm also passes the odor evaluation test with a value of greater than 30, which suggests that the vinyl acetate-ethylene copolymer-based emulsion according to the present invention can provide low odor to the paper coating composition prepared therefrom, especially after exposure to UV drier according to the procedure of odor evaluation test, therefore is useful as binder for printing packages with high qualities, such as cigarette package, food package and the like.
All of the methods disclosed and claimed herein can be made and executed without undue experimentation in light of the present disclosure. While the products and methods of this invention have been described in terms of preferred embodiments, it will be apparent to those of skill in the art that variations may be applied to the methods and in the steps or in the sequence of steps of the method described herein without departing from the concept, spirit and scope of the invention.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/CN2012/075432 | 5/14/2012 | WO | 00 | 11/12/2014 |