AN AQUEOUS POLYMER DISPERSION COMPOSITION USEFUL AS A GLAZING COAT FOR PAPERS

Abstract: There is provided an aqueous polymer dispersion composition obtained by dispersing a vinyl monomer in which nitrocellulose has been dissolved and thereafter polymerizing the monomer. The dispersion also contains a film-forming assistant and is useful as a glazing coat for papers. The invention reduces environmental pollution.

Description: DESCRIPTION "AN AQUEOUS POLYMER DLSPERSION COMPOSITION USEFUL AS A GIAZiN COAT FOR PAPEENi". The present invention relates to an aqueous polymer dispersion composition useful as a glazing coat for papers comprising an aqueous acrylic polymer dispersion containing nitrocellulose and having excellent blocking resistance and gloss. For glazing treatment or printed papers, a glazing varnish in the form of a solution containing a resin and an organic solvent has been used heretofore. As the resin, a vinyl chloride resin has exclusively been used. However, the vinyl chloride resin has demerits in that surface gloss and strength of the finished surface are insufficient due to softness thereof and blocking is easily caused. Other demerits are that the organic solvent used harms the health of workers and that there is a risk of fire. Under circumstances as above, the utilization of said varnish is now limited for the prevention of environmental pollution. Other techniques of the glazing treatment are press working and lamination working. However, they have a demerit of inviting an increase in the number of steps, though efficiencies are increased. lacquers containing nitrocellulose as a base have been used so as to improve abrasion resistance and to impart gloss and blocking resistance. However, those lacquers are also unfavourable, since they are harmful due to solvents contained therein as described above. Recently, glazing treatment of paper with an aqueous dispersion of acrylic polymers containing methyl methacrylate and styrene as principal components has been effected extensively. However, this technique has problems with the film-forming property of the dispersion and blocking caused at a high temperature and a high humidity. After intensive investigations for the purpose of developing an aqueous polymer dispersion as a glazing coat for papers having excellent gloss and surface properties such as blocking resistance, the inventors have found that an aqueous polymer dispersion composition obtained by dispersing a vinyl monomer in which nitrocellulose has been dissolved and thereafter polymerizing the monomer does not cause environmental pollution and that a coating film obtained by applying the composition to a paper and drying the same has excellent physical properties (which could not be attained by using conventional aqueous dispersions) such as blocking resistance and also a high adhesion to the paper and an excellent gloss. The present invention has been attained on the basis of this finding. The present invention relates to an aqueous polymer dispersion composition useful ás a-glazing¯coat for papers in which 100 parts by weight of the polymer comprise 3-35 parts by weight of nitrocellulose and 97-65 parts by weight of a vinyl polymer in which nitrocellulose is soluble or with which nitrocellulose is compatible irrespective of the state (monomer or polymer) of the vinyl polymer and which vinyl polymer satisfies the following two formulae for second-order transition temnerature (2 EMI2.1 wherein NO represents parts by weight of nitrocellulose and P represents parts by weight of the vinyl polymer; said composition being obtained by adding a filmforming assistant to an aqueous polymer dispersion formed by dissolving nitrocellulose in said vinyl polymerforming monomer (hereinafter referred to as vinyl monomer), dispersing the solution in the form of oil particles in water and polymerizing the monomer. As nitrocelluloses used in the present invention those used generally for lacquers can be used without any particular limitation. The nitrocellulose content of the polymer composition is 3-35 parts by weight, preferably 10-30 parts by weight. If the nitrocellulose content is insufficient, the gloss obtained is poor and blocking cannot be prevented. On the other hand, if the nitrocellulose content is excessive, the gloss, adhesion and film-forming property at room temperature are all reduced. As the vinyl monomers, there may be used those containing at least one monomer in which nitrocellulose is soluble. The vinyl monomers in which nitrocellulose is soluble include acrylic monomers of the general formula: EMI3.1 wherein R represents hydrogen or a methyl group and R1 represents an alkyl group having 1-20 carbon atoms, a cyclo-alkyl group in which the alkyl group has 5 or 6 carbon atoms, -CH2CH2OCH2CH3, -C6H5 or -CH2C6H5. As the acrylic monomers, there may be mentioned ethyl acrylate, butyl acrylate, 2-ethylhexyl acrylate and methyl methacrylate. Those compounds may be used either alone or in the form of a mixture. Other useful monomers include the following compounds: (1) Styrene and substituted styrenes of the general formula: EMI3.2 wherein X represents hydrogen, C3, a halogen such as C1 Br, NO2, m of an N(alkyl)2 in which the alkyl group has one or two carbon atoms; as well as combina tions of them with acrylic comonomers. Preferably, X represents hydrogen or QH. (2) Vinyl acetate: and vinyl esters of a higher aliphatic acid, such' as propionic vinyl ester and butyric vinyl ester, preferably vinyl acetate as well as vinyl acetate/acrylic acid ester comonomers. (3) Combinatis of, vinyl chloride or vinylidene chloride with an acrylic comonomer. As a monomer which enhances stabilization of the aqueous polymer dispersion and adhesion thereof to the paper, there may be used a small proportion (based on the whole of the monemers) of at least one as of the monomers of the general formula: EMI4.1 wherein R represents hydrogen or a methyl group, R3 represents hydrogen or a 2-sulfoethyl group or a hydroxy alkyl group in which the alkyl group has 1-4 carbon atoms, such acrylic acid or methacrylic acid, and monomers of the general formula: EMI4.2 wherein R represents hydrogen or a methyl group and R4 represents NH2, SHCk or or an NHCII0-a1kyl group in which the alkyl group has 1-4 carbon atoms. Further, up to about 200%, based on the total monomers, of unsaturated carbocylic ester having an epoxy group such as acrylonitrile methacrylonitrile, glycidyl acrylate or glycidyl methacrylate may be contained therein as a minor monomer component. It is preferred to use a surfactant in the preparation of the aqueous polymer dispersion according to the present invention. As the surfactants, there may be used anionic surfactants, nonionic surfactants and combinations of the anionic and nonionic surfactants. As the anionic surfactants, there may be mentioned aikyl- and aThyl-arlsulfonic acid salts and sulfuric acid salts, diai?r,lsulfosuccinic acid salts, s , sulfuric acid salts of nonionic surfactants and complex phosphate esters. As the nonionic surfactants, there may be mentioned polyoethylene carboxyllc esters, polyoxyethylene nonylphenyl ether, polyoxyethylene alkyl ethers, polyoxyethylene sorbitan monocarboxylic esters and ethylene oxidepropylene oxide block copolymers. Colloids and high molecular weight stabilizers may be used either alone or in combination with the above mentioned surfactants. As the stabilizers, there may be mentioned;complicated polysaccharides, amylopectins, water-soluble derivatives of cellulose, polvinyl alcohols, alginic acid salts of polyvinyl alcohols and carraghe enin The dispersion in water can be attained by completely dissolving nitrocellulose in the monomer and then directly dispersing a mixture of nitrocellulose, the vinyl monomer and other additives in water. The polymerization is effected by using a radical initiator to obtain an aqueous polymer dispersion in which generally at least two polymers are present substantially homogeneously in the aqueous polymer dispersion, i.e. in the dispersed particles. The polymerization temperature ranges from 000 to 2000C, preferably from room temperature to 10000. The reaction is carried out for from several minutes to several hours, generally for from 30 minutes to about 6 hours. As the polymerization initiators, known watersoluble or oil-soluble polymerization initiators can be used in the presence or absence of a reducing agent. Typically, the initiators are used in an amount of 0.01 1.0 part by weight per 100 parts by weight of the polyinerizable monomer, Additives generally used for aqueous polymer dispersions such as a solvent, plasticizer, pigment, thickening agent, an antifoaming agent, a blockingpreventing agent and an agent for preventing yellowing can be used, if necessary. Purthert a resin compatible therewith such as a water-soluble acrylic resin and a water-soluble aLkrd resin may also be added thereto. y forming assistants are used for Improving the film-forming properties or physical properties of the coating film according to the present invention. As the film-forming assistants, glycol ether acetates are preferred. There may be used, for example, etho=éthy- lene glycol acetate, n-butcryethylene glycol acetate, diethylene glycol n-butyl acetate and ethylene glycol n-butyl ether acetate'(butyl cellosolve acetate) Of these, butyl cellosolve acetate is preferred. It is used preferably in an amount of 5-25 parts by weight per 100 parts by weight of the aqueous polymer dispersion. In carrying out the present invention, generally up to 15 parts by weight of a co-solvent such as a ketone, for example, methyl isobutyl ketone or isophorone or an acetic ester, for example, n-butyl acetate or n-amylacetate or a plasticizer such as a glycol, for example, ethylene glycol or propylene glycol may be added to the aqueous polymer dispersion. -The film-forming assistant, plasticizer and co- solvent may be introduced into the reaction system at any time during the dispersion step. For coating papers with the aqueous polymer dispersion of the present invention, any of the known methods such as the size press coating method, the calendar coating method, tbe roll coater method, the air doctor method and the blade coater method can be employed. The amount of the aqueous polymer dispersion which varies depending on the properties of a paper to be coated is substantially the same as that of ordinary glazing varnish to cause a satisfactory glaze. The usual amount is preferably in the range between about 4 and about 10 im2 expressed as the solid content. In the drying step, a drying temperature which varies depending on the Tg of the resin and the amounts of plasticizer and solvent contained therein is generally in the range of from room temperature to 1500Ct preferably 50-130 C. The drying time which varies depending on the quality of the paper and the temperature is in the range of from 5 seconds to 5 minutes. A sufficient gloss can be obtained even if a hot press is not utilized. The following examples further illustrate the present invention, in which parts and percentages are given by weight unless otherwise stated. Gloss, scratch test, adhesion, blocking resistance and abrasion resistance were determined for assessing properties of the coating films by the following methods: Gloss: 60 Mirror plane reflectivity: Values above 70 stood the test. Scratch test: The coating films were scratched with a nail and degrees of peeling were examined. Those showing no peeling stood the test. Adhesion: A cellophane tape was pressed against the samples five times with the fingers and then peeled off forcibly. Degrees of peeling were examined. Those showing no peeling stood the test. Blocking resistance test: The samples were placed face to face one over the other at 4000 and 90,'; RH under a load of 300 t/cm2 for 24 hours. 30 minutes after removal of the load, degrees of separation of the faces from each other were examined. Samples of which the natural separation was achieved stood the test. Abrasion resistance test: The samples placed face to face were rubbed with the fingers. Those which were not peeled off after 50 times stood the test. Monomers used are shown as given below: Methyl methacrylate MAA: Methacrylic acid St: Styrene Ethyl acrylate 2-Ethylhexyl acrylate BA : Butyl acrylate A Acrylic acid Example 1. Into an ice-cooled vessel, nitrocellulose, vinyl monomers and other additives were charged so that the NC/P would be 30/70 and the monomer ratio would be (MMA/ 2-EHA)/MAA=(70/30)/1.5 (Tg=18.6 C)+ More particularly, in a one-liter four neck flask, there were charged 161.1 g of nitrocellulose (RS-1/8) of a water content of 46.4' (a product of Daicel Rabushiki Eaisha), 11.8 g of anionic composite phosphate ester emulsifier, 19.7 g of anionic alkylaryl sulfonate, 4.1 g of sodium hydrogencarbonate, 0.8 g of antifoaming agent and 233 g of distilled water. Then, a monomer phase comprising 140 g of IDS, 60 g of 2-EBA, 3 g of MPLA and 0.2 g of chain transfer agent was added thereto. The mixture was mixed arith a Homomixer, type M (a product of Tokushu Kiki Kogyo-Sha) for 45 minutes. Then, a condenser, a stirrer and a nitrogen-introducing pipe were attached to the flask and nitrogen replacement was effected sufficiently. The contents of the flask were heated to 0 65 C. Then, an aliquot of 28.3 g of a solution of 0.41 g of potassium persulfate in 40 g of distilled water was added thereto to initiate the reaction. After generation of heat ceased, the mixture was kept at 650C for 60 minutes. Then the remainder of the aqueous potassium persulfate solution, 5 g of distilled water and 0.08 g of sodium hydroSensulfire were added thereto. The temperature was elevated to 8000 and the whole was kept at this temperature for 90 minutes to obtain an aqueous polymer dispersion having a pli of 6.7, a viscosity of 14 cps (3L viscometer, rotor No.1, 60 rpm; 300C) and a solids content of 45%. 15 parts of butylcellosolve acetate (hereinafter referred to as BCeA) were added to 100 parts of the aqueous polymer dispersion and the whole was mixed thoroughly. The mixture was allowed to stand for one day, applied to a hiding rate test paper with a No.10 bar coater and dried at 12000 for 30 seconds. The paper to which the sample was applied was subjected to blocking resistance test, gloss measurement, adhesion test and scratch test. The results are shown in Table 2, which indicate that blocking resistance and gloss were excellent and that as a whole, the product was excellent. Examnle 2 Components were charged into the vessel so that the NO/P would be 35:65 and the monomer ratio would be (MMA/2-EHA)/MAA=(60/40)/1.5 (Tg= -2.2 C). More particularly, the polymerization was carried out by using 203.9 g of nitrocellulose (RS 1/8) of a water content of 46.4%, 120 g of DSS, 80 g of 2-EEL, 3 g of GILA, 215.7 g of distilled water, 10.2 g of anionic composite phosphate ester emulsifier and 36.3 g of sulfate emulsifier of nonionic surfactant. 25 parts of BCeA were added to 100 parts of the resulting aqueous polymer dispersion. The mixture was applied to a paper, dried and subjected to the tests. The results are shown in Table 2 which indicate that blocking resistance and gloss were excellent and that as a whole, the product was excellent. Ex,mmole 2 Components were charged into the vessel so that NC/P would be 25/75 and the monomer ratio would be (MMA/2-EHA)/MAA=(50/50)/1.5 (Tg = -20.2 C). More particularly, the polymerization was carried out by using 100.7 g of nitrocellulose (SS 1/4) of a water content of 32.7,%', 100 g of MMA, lOOg of 2-EfiA, 3 g of MAA, 8.8 g of anionic composite phosphate ester emulsifier and 14.7 g of anionic alkylaryl sulfate emulsifier in the same manner as in Example 1. 10 parts of BCeA and 5 parts of dibutyl phthalate (hereinafter referred to as DBP) were added to 100 parts of the resulting aqueous polymer dispersion. The whole was stirred thoroughly and allowed to stand for one day, applied to a hiding rate test paper with a No.10 bar coater and dried at 1200C for 30 seconds. . The resultant coated paper was subjected to tests to obtain results shown in Table 2 which indicate that blocking resistance, gloss and adhesion were excellent and that as a whole, the product was excellent. native Example 1 Components were charged into the vessel so that the NC/P ratio would be 20/80 and the monomer ratio would be (?iv2-)A'vLA=(30/70)/l.5 (Tg = 49.900). Namely, the polymerization was carried out by using 94.7 g of nitrocellulose (RS 1/8) of a water content of 46.4,% 60 g of MMA, 140 g of 2- , 3 g of AA, 8.3 g anionic composite phosphate ester emulsifier, 13.8 g of anionic alkylaryl sulfate emulsifier and 216.7 g of distilled water in the same manner as in Example 1. BCeL was added thereto in the same manner as in the preceding examples and the mixture was applied to a paper, dried and subjected to the tests. The results are shown in Table 2. Example 4 Components were charged into the vessel so that the i ratio would be 20/80 and the monomer ratio would be (MMA/BA)/MAA=(30/70)/1.5 (Tg= -20.7 C). Namely, the polymerization was carried out by using 126.2 g of nitrocellulose (BS 1/16) of a water content of 59.80:0?, 60 g of t2th, 140 g of BA and 3 g of NAA in the same manner as in Example 1. After the addition of BCeA, application to a paper and drying the sample was tested to obtain the results shown in Table 2. Example 5 Components were charged into the vessel so that the NC/P ratio would be 25/75 and the monomer ratio would be (UL/)/AA=(40/60)/l.5 (Tg = 17.800). Namely, the polymerization was carried out by using 126.2 g of nitrocellulose (RS 1/8) of a water content of 46.4%', 80 g of NANA, 120 g of EA, 3 g of AA, 10.7 g of anionic composite phosphate ester emulsifier and 17.8 g of anionic all:;ylaryl sulfate emulsifier in the same manner as in Example 1. Then, BCeA and DBP were added thereto and the mixture was applied to a paper, dried and subjected to the tests in the same manner as in Example 2. The results are shown in Table 2. Exawmple 6 Components were charged into the vessel so that NC/P ratio would be 35/65 and the monomer ratio would be (St/BA)/AA=(3o/70)/l.5 (g = -21.4 C). Namely, the polymerization was carried out by using 200.6 ;r of nitrocellulose (RS 1/4) of a water content of 45.5%, 60 g of St, 140 g of BA, 3 g of MAA, 13.1 g of anionic composite phosphate ester emulsifier and 21.9 g of anionic alkylaryl sulfate emulsifier in the same manner as in Example 1. Then, BCeA was added thereto and the mixture was applied to a paper, dried and subjected to the tests in the same manner as above. The results are shown in, Table 2. It is apparent that the product had excellent blocking resistance and gloss. Comparative Example 2 Components were charged so that NC/P would be 20/80 and the monomer ratio would be (MMA/2-EHA)/MAA = (89.5/10.5)/1.5 (Tg = 70.0 C). Namely, the polymerization was carried out by using 93.1 g of nitrocellulose (RS 1/4) of a water content of 45.5%', 179 g of iStA, 21 g of 2-ErA, 3 g of r, 8.2 g of anionic composite phosphate ester emulsifier and 13.7 g of anionic alkylaryl sulfate emulsifier in the same manner as in Example 1 and the mixture then treated also in the same manner as in Example 1. The results of the tests are shown in Table 2. Example 7 Components were charged into the vessel os that NC/P ratio would be 30/70 and the monomer ratio would be (MMA/2-EHA/GMA)/MAA=(65/30/5)/1.5 (Tg = 16.600). Namely, the polymerization was carried out by using 162.3 g of nitrocellulose (RS 1/8) of a water content of 46.4%', 130 g of MMA, 60 g of 2-EllA, 10 g of Gi, 3 g of i'lAA, 11.9 g of anionic composite phosphate ester emulsifier and 19.8 g of anionic alkylaryl sulfate in the same manner as in Example 1, the mixture then treated also in the same manner as in Example 1 and subjected to the tests. The results are shown in Table 2. Comparative Example 3 10 parts of BCeA and 5 parts of DBP were added to 100 parts of the aqueous polymer dispersion obtained in Comparative Example 2 and the whole was stirred thoroughly. After allowing to stand for one day, the mixture was applied to a paper, dried and subjected to the tests to obtain the results shown in Table 2. Comparative Example 4 A product of solvent type (a vinyl polymer of P. Company) was directly applied to a hiding rate test paper with a No.10 bar-coater, then dried and subjected to the tests to obtain the results shown in Table 2. Comparative Example 5 A product of acrylic emulsion type (a product of Q. Company) was poly'rized and treated in' the same manner as in Comparative Example 4 to obtain the results shown in Table 2. The following Table 1 gives the compositions and properties of the dispersions described in the above Examples. Table 1 Compositions and properties of emulsions EMI14.1 <SEP> Proporties <SEP> of <SEP> emulsion <tb> --------------------------------------------------------------------------- <SEP> Tg <SEP> NC/NC+P <SEP> NC <SEP> -------------------------------- <SEP> Monomer <SEP> ratio <SEP> N.V. <SEP> Vis. <SEP> pU <SEP> MFT <tb> <SEP> ---------------------------------------------------------- <SEP> MMA <SEP> St <SEP> 2-EHA <SEP> BA <SEP> EA <SEP> GMA <SEP> MAA <SEP> AA <tb> --------------------------------------------------------------------------------------------------------------------------------------------------- Example <tb> <SEP> 1 <SEP> 70 <SEP> 30 <SEP> 1.5 <SEP> 18.6 <SEP> 0.30 <SEP> RS <SEP> 1/8 <SEP> 44.9 <SEP> 14 <SEP> 6.7 <SEP> > 80 <tb> --------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 2 <SEP> 60 <SEP> 40 <SEP> 1.5 <SEP> -2.2 <SEP> 0.35 <SEP> RS <SEP> 1/8 <SEP> 45.2 <SEP> 12 <SEP> 6.7 <SEP> > 80 <tb> --------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 3 <SEP> 50 <SEP> 50 <SEP> 1.5 <SEP> -20.2 <SEP> 0.25 <SEP> SS <SEP> 1/4 <SEP> 44.2 <SEP> 12 <SEP> 6.6 <SEP> 41 <tb> ----------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 4 <SEP> 30 <SEP> 70 <SEP> 1.5 <SEP> -20.7 <SEP> 0.20 <SEP> RS <SEP> 1/16 <SEP> 45.8 <SEP> 10 <SEP> 6.7 <SEP> 34 <tb> ------------------------------------------------------------------------------------------------------------------------------------------------------ <SEP> 5 <SEP> 40 <SEP> 60 <SEP> 1.5 <SEP> 17.8 <SEP> 0.25 <SEP> RS <SEP> 1/8 <SEP> 45.0 <SEP> 12 <SEP> 6.5 <SEP> 72 <tb> -------------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 6 <SEP> 30 <SEP> 1.5 <SEP> -21.4 <SEP> 0.35 <SEP> RS <SEP> 1/4 <SEP> 45.4 <SEP> 16 <SEP> 6.2 <SEP> 37 <tb> --------------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 7 <SEP> 65 <SEP> 30 <SEP> 5 <SEP> 1.5 <SEP> 16.6 <SEP> 0.35 <SEP> RS <SEP> 1/8 <SEP> 45.2 <SEP> 11 <SEP> 6.3 <SEP> > 80 <tb> ------------------------------------------------------------------------------------------------------------------------------------------------------------- Comparative <SEP> 30 <SEP> 70 <SEP> 1.5 <SEP> -49.9 <SEP> 0.20 <SEP> RS <SEP> 1/8 <SEP> 44.6 <SEP> 30 <SEP> 6.7 <SEP> > 0 <tb> Example <tb> <SEP> 1 <tb> ---------------------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 2 <SEP> 89.5 <SEP> 10.5 <SEP> 1.5 <SEP> 70 <SEP> 0.20 <SEP> RS <SEP> 1/4 <SEP> 45.8 <SEP> 14 <SEP> 6.5 <SEP> > 80 <tb> ---------------------------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 4 <SEP> vinyl <SEP> polymer <SEP> of <SEP> the <SEP> solvent <SEP> type <SEP> - <SEP> - <SEP> - <SEP> (35.1) <SEP> (300) <SEP> - <SEP> ----------------------------------------------------------------------------------------------------------------------------------------------------------------------------- <SEP> 5 <SEP> 26.5 <SEP> 15.5 <SEP> 5.0 <SEP> - <SEP> - <SEP> - <SEP> 41.5 <SEP> 110 <SEP> 7.0 <SEP> 63 <tb> ------------------------------------------------------------------------------------------------------------------------------------------------------------------------- Measurement of properties of emulsion Solid content (N.V.) : One gram of emulsion (Em) was weighed into a 3cm x 3cm aluminium vessel, dried in a geer oven at 6000 till'constant weight was attained. Then, weight of the sample was measured and solid content was calculated from the weight. Viscosity (Vis) : Measured with BI-viscometer (rotor No. 1) at 60 rpm, 3000. Minimum film-forming temp. (hE) : Measured with a minimum film-forming temperature measuring device (a product of Terakawa Seisaku-sho Co.) (temp. range: 0-80 C) Table 2 Pronerties of coating films EMI16.1 <tb> I <SEP> i <SEP> Pronertics <SEP> of <SEP> coating <SEP> films <tb> <SEP> al) <SEP> I <SEP> 3lock- <SEP> films <SEP> r,cratch <SEP> Remarks <tb> <SEP> \ <SEP> Recipe <SEP> Gloss <tb> <SEP> ing <SEP> re- <SEP> sion <SEP> resis <tb> <SEP> sistance <SEP> tance <tb> ""Ixam <tb> ple <SEP> 1 <SEP> A <SEP> 79 <SEP> o <SEP> o <SEP> o <tb> <SEP> 2 <SEP> A <SEP> 79 <SEP> o <SEP> o <SEP> o <SEP> 0 <tb> <SEP> 3' <SEP> B <SEP> 74 <SEP> o <SEP> o <SEP> o <tb> <SEP> 4 <SEP> A <SEP> 74 <SEP> o <SEP> o <SEP> o <tb> <SEP> 5 <SEP> B <SEP> 75 <SEP> o <SEP> o <SEP> o <SEP> 0 <tb> <SEP> 6 <SEP> 1 <SEP> 82 <SEP> o <SEP> o <SEP> o <tb> <SEP> 7 <SEP> B <SEP> 76 <SEP> o <SEP> o <SEP> o <tb> Compa <tb> rative <tb> A <SEP> 60 <SEP> Y <SEP> 0 <tb> ple <SEP> 1 <tb> <SEP> 2 <SEP> A <SEP> 45 <SEP> x <SEP> x <SEP> x <tb> <SEP> 3 <SEP> 3 <SEP> 38 <SEP> x <SEP> x <tb> <SEP> Solvent-type <tb> <SEP> re <SEP> 79 <SEP> x <SEP> o <SEP> ss <SEP> (a <SEP> vinyl <SEP> poly <tb> <SEP> mer <SEP> of <SEP> P <SEP> Co. <tb> <SEP> 5 <SEP> - <SEP> 63 <SEP> x <SEP> o <SEP> o <SEP> Acrylic <SEP> Em <tb> <SEP> (a <SEP> product <tb> <SEP> of <SEP> Q <SEP> Co.) <tb> *1) Recipe A : Emulsion (Em) 100 Parts, BOcA 15 Parts n B 1 Zm 100 Parts, BCeA 10 Parts DBP 5 Parts *2) Judgement of properties of coating films: o : good # : : slightly bad x z bad

Claims: 7. A composition as claimed in any one of claims 1 to 6 in which the polymerization-of the monomer is effected using a radical initiator. 8. A composition as claimed in any one of claims 1 to 7 in which the polymerization temperature ranges from Oo to 2000C. 9. A composition as claimed in any one of claims 1 to 8 in which the film forming assistant is a glycol ether acetate. 10. A composition as claimed in claim 9 in which up to 15 parts by weight, based on 100 parts by weight of the composition, of a co-solvent or plasticizer are contained therein. 11. A composition as claimed in any one of claims 1 to 10 in which the film forming assistant is used in an amount of 5 to 25 parts by weight per 100 parts by weight of the aqueous polymer dispersion, when the concentration of polymer in the dispersion is about 45 weight percent. 12. Glazed papers obtained by coating papers with an aqueous polymer dispersion composition as claimed in any one of claims 1 to 11 and drying the coated papers.

Inventors: ASAMI, MASAHIRO, MIKUMO, MASATOSHI, TAKENAKA, FUMIO, TOBA, HIROTAKA
Applicants: DAICEL LTD.
Application year: 1979
Main classification: D21H1
IPC codes: B41M7, C08F251, D21H19