Formaldehyde-free crosslinking emulsion polymer systems based on vinyl ester dialkoxyhydroxyethyl acrylamide co- and terpolymers

Abstract: Formaldehyde free crosslinking emulsion polymers are prepared by the addition of N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide to a vinyl ester based polymer. The resultant emulsions can be used as binders for nonwovens or fiberfill or as woodworking adhesives.

Description: Emulsion polymers prepared from vinyl esters, particularly those prepared from vinyl acetate and ethylene, have wide application as adhesives and as binders in industry. These binders may experience unacceptable loss in strength in the presence of water and other solvents. To reduce this problem, various crosslinking comonomers and/or post-added crosslinkers can be incorporated into the binders. The most successful of these crosslinkers have been N-methylol acrylamide [NMA] and urea-formaldehyde [U/F] condensates. While the latter are low in cost, compatible with aqueous emulsions and rapidly cured under acid catalysis, their consequent emission of low levels of formaldehyde, a suspect carcinogen, make them undesirable for many applications. To overcome or minimize the potential carcinogenicity and irritant properties of formaldehyde, many functional monomers that do not contain formaldehyde have been added to the emulsion polymers. Many of the functional monomers, such as acrylamido glycolic acid and its derivatives, have provided acceptable results in acrylate containing emulsions, but do not satisfactorily copolymerize with adhesives and binders containing vinyl esters, particularly vinyl acetate. Thus, most of the functional monomers that can readily be incorporated into acrylic emulsion polymers do not yield comparable results in vinyl acetate containing systems because these monomers hydrolyze during emulsion polymerization with the hydrophilic vinyl esters, and thereby lose their effectiveness. However, when N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide is polymerized into emulsion polymers containing substantial amounts of vinyl esters, the resultant polymers exhibit excellent performance as nonwoven binders or adhesives in non-formaldehyde containing systems. Thus, the present invention is directed to emulsion polymers comprising more than 50% vinyl ester and 1 to 15% by weight of the N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide wherein the alkoxy group contains 1-4 carbon atoms. The use of N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide provides superior results in vinyl ester copolymer systems and particularly in ethylene/vinyl acetate copolymers. Moreover, the N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide functional comonomer may be used in vinyl acetate containing emulsion copolymers prepared in the presence of surfactants and/or protective colloids; as such, the emulsion polymers herein may be readily formulated into a wide range of non-formaldehyde systems including those used as binders for nonwovens and fiberfill, and also in woodworking adhesive compositions. While any N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide having 1 to 4 carbon atoms in the alkoxy group can be utilized herein, N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide [DMHEA] is now the most commercially viable. The N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide monomers and their preparation are described in US-A 4,918,139 issued April 17, 1990 to Cuirassier, et al. While vinyl acetate is the most commonly employed vinyl ester, other C₁ to C₁₃ esters of alkanoic acids are also useful herein. Typical examples of vinyl esters include: vinyl formate, vinyl propionate, vinyl butyrate, vinyl isobutyrate, vinyl valerate, vinyl 2-ethylhexanoate, vinyl isooctanoate, vinyl nonoate, vinyl decanoate, vinyl pivalate, and vinyl versatate. Additionally, depending on the end use of the resultant emulsion, the vinyl ester may be polymerized with varying amounts, up to about 49% by weight, of one or more other copolymerizable comonomers. Suitable comonomers include olefins such as ethylene, vinyl halides such as vinyl chloride, and C₁ to C₈ alkyl acrylates or methacrylates. The precise amount of the copolymerizable comonomer used will vary depending upon the nature of the comonomer as well as the end use of the emulsion. Thus, the nature of ethylene is such that it can be incorporated into vinyl ester emulsion systems only at levels up to about 35% by weight. In contrast, the vinyl halides as well as the alkyl acrylates and methacrylates can be used at higher levels, e.g., up to about 49% by weight of the polymer. Optionally, small amounts of other functional monomers, including coreactive comonomers may be employed. Thus, olefinically unsaturated carboxylic acids having from 3 to 6 carbon atoms or the alkanedioic acids having from 4 to 6 carbon atoms may be used, e.g., acrylic acid, methacrylic acid, crotonic acid, itaconic acid, maleic acid or fumaric acid or mixtures thereof, in amounts sufficient to provide up to about 10% by weight of monomer units in the final copolymer. Additionally, the use of up to about 15% by weight of an hydroxyalkyl (C₂ to C₄) acrylate or methacrylate has been found to be beneficial in furthering the performance of the N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide. Also, polyunsaturated copolymerizable monomers may be present in small amounts, i.e., up to about 1% by weight. Such comonomers would include copolymerizable polyolefinically unsaturated monomers such as vinyl crotonate, allyl acrylate, allyl methacrylate, diallyl maleate, divinyl adipate, diallyl adipate, diallyl phthalate, ethylene glycol diacrylate, ethylene glycol dimethacrylate, butanediol dimethacrylate, methylene bis-acrylamide, and triallyl cyanurate. Finally, certain copolymerizable monomers that assist in the stability of the copolymer emulsion, e.g. acrylamide and vinyl sulphonic acid, are also useful herein. These latter monomers, if employed, are added in very low amounts from 0.1 to 2% by weight of the monomer mixture. Conventional batch, semi-batch or continuous polymerization procedures may be utilized herein. Generally, the monomers are polymerized in an aqueous medium (under pressures not exceeding 100 atmospheres if ethylene is employed) in the presence of a catalyst and at least one emulsifying agent. If ethylene is used in the polymerization, the quantity of ethylene entering into the copolymer is influenced by the pressure, the agitation and the viscosity of the polymerization medium. Thus, to increase the ethylene content of the copolymer, higher pressures are employed. A pressure of at least about 10 atmospheres is most suitably employed. The mixture is thoroughly agitated to dissolve the ethylene, the agitation being continued until substantial equilibrium is achieved. This generally requires about 15 minutes; however, more or less time may be required depending upon the vessel, the efficiency of the agitation, and the specific system. Suitable polymerization catalysts are water-soluble and able to form free-radicals. Examples are those generally used in emulsion polymerization, such as hydrogen peroxide, sodium persulphate, potassium persulphate, ammonium persulphate and tert-butyl hydroperoxide, in amounts between 0.01 and 3% by weight, preferably 0.01 and 1% by weight based on the total amount of the emulsion. They can be used alone, or together with reducing agents as redox catalysts in amounts of 0.01 to 3% by weight, preferably 0.01 to 1% by weight based on the total amount of the emulsion. Suitable reducing agents include ferrous salts, sodium dithionite, sodium metabisulphite, sodium thiosulphate and ascorbic acid. The catalysts can be charged in the aqueous emulsifier solution and/or be added during the polymerization in doses. The polymerization is carried out at a pH between 2 and 7, preferably between 3 and 5. In order to maintain the pH range, it may be useful to work in the presence of customary buffer systems, for example, in the presence of alkali metal acetates, alkali metal carbonates, alkali metal phosphates. Polymerization regulators, like mercaptans, aldehydes, chloroform, ethylene chloride and trichloroethylene, can also be added in some cases. The emulsifying agents are those generally used in emulsion polymerization, or optionally can be protective colloids. It is also possible to use emulsifiers alone or in mixtures with protective colloids. In the case of emulsions which are to be formulated into binders for nonwovens or fiberfill, it is especially advantageous to use an anionic, cationic or nonionic emulsifier or surfactant. The emulsifiers can be anionic, cationic, nonionic surface-active compounds or mixtures thereof. Suitable anionic emulsifiers are, for example, alkyl sulphonates, alkylaryl sulphonates, alkyl sulphates, sulphates of hydroxyalkanols, alkyl and alkylaryl disulphonates, sulphonated fatty acids, sulphates and phosphates of polyethoxylated alkanols and alkylphenols, and esters of sulphosuccinic acid. Suitable cationic emulsifiers are, for example, alkyl quaternary ammonium salts and alkyl quaternary phosphonium salts. Examples of suitable nonionic emulsifiers are the addition products of 5 to 50 moles of ethylene oxide adducted to straight-chain and branched-chain alkanols with 6 to 22 carbon atoms, or alkylphenols, or higher fatty acids, or higher fatty acid amides, or primary and secondary higher alkylamines; as well as block copolymers of propylene oxide with ethylene oxide and mixtures thereof. When combinations of emulsifying agents are used, it is advantageous to use a relatively hydrophobic emulsifying agent in combination with a relatively hydrophilic agent. The amount of emulsifying agent is generally from 1 to 10, preferably from 2 to 8% by weight of the monomers used in the polymerization. Various protective colloids may also be used in place of or in addition to the emulsifiers described above. The use of protective colloids is especially desirable in polymer emulsions that are to be formulated into woodworking adhesives. Suitable colloids include partially acetylated polyvinyl alcohol, e.g., up to 50% acetylated, casein, hydroxyethyl starch, carboxymethyl cellulose, and gum arabic as known in the art of synthetic emulsion polymer technology. In general, these colloids are used at levels of 0.5 to 4% by weight of the total emulsion. The emulsifier or protective colloid used in the polymerization can be added in its entirety to the initial charge to the polymerization zone or a portion of the emulsifier, e.g., from 25 to 90% thereof, can be added continuously or intermittently during polymerization. The particle size of the latex can be regulated by the quantity of nonionic or anionic emulsifying agent or protective colloid employed. To obtain smaller particle sizes, greater amounts of emulsifying agents are used. As a general rule, the greater the amount of the emulsifying agent employed, the smaller the average particle size. The polymerization reaction is generally continued until the residual vinyl acetate monomer content is below about 1%. The completed reaction product is then allowed to cool to about room temperature while sealed from the atmosphere. The emulsions are produced and used at relatively high solids contents, e.g., between 35 and 70%, preferably not less than 50%, although they may be diluted with water if desired. When the emulsion is to be formulated into a binder for nonwovens or fiberfill, there may be present in the latex binders other additives conventionally employed in similar binders, including defoamer, pigments, catalysts, wetting agents, thickeners, and external plasticizers. The choice of materials, as well as the amounts employed, are well known to those skilled in the art. These materials may be added just before application, if their stability in the dispersion or solution is low, or they may be formulated into the aqueous dispersion of the binder and stored, if the stability in aqueous dispersion is high. Binders described above are suitably used to prepare nonwoven fabrics by a variety of methods known to the art which, in general, involve the impregnation of a loosely assembled web of fibers with the binder latex, followed by moderate heating to dry the web. This moderate heating also serves to cure the binder by forming a crosslinked interpolymer. Before the binder is applied it is optionally mixed with a suitable catalyst for the crosslinking reaction. Acid catalysts such as mineral acids, e.g., HCl, or organic acids, e.g., oxalic acid, or acid salts, e.g. ammonium chloride, are suitable to be used as known in the art. The amount of catalyst is generally 0.5 to 2% of the total resin. The starting fibrous web can be formed by any one of the conventional techniques for depositing or arranging fibers in a web or layer. These techniques include carding, garnetting, and air-laying. Individual webs or thin layers formed by one or more of these techniques can also be lapped or laminated to provide a thicker layer for conversion into a heavier fabric. In general, the fibers extend in a plurality of diverse directions in general alignment with the major plane, overlapping, intersecting and supporting one another to form an open porous structure. Examples of the fibers to be used in the starting web are the natural cellulose fibers such as wood pulp and chemically modified celluloses such as regenerated cellulose. (Cellulose fibers mean those fibers containing predominantly C₆H₁₀O₅ groupings.) Often the fibrous starting web contains at least 50% cellulose fibers, which can be natural, synthetic, or a combination thereof. Other fibers in the starting web may comprise natural fibers, such as wool; artificial fibers, such as cellulose acetate; synthetic fibers, such as polyamides, e.g., nylon, polyesters, e.g., "Dacron", acrylics, e.g., "Dynel", "Orion", polyolefins, e.g., polyethylene, polyvinyl chloride, or polyurethane, alone or in combination with one another. This fibrous web is then subjected to at least one of several types of latex bonding operations to anchor the individual fibers together to form a self-sustaining web. Some of the better known methods of bonding are overall impregnation, spraying or printing the web with intermittent or continuous, straight or wavy lines or areas of binder extending generally transversely or diagonally across the web and additionally, if desired, along the web. The amount of binder, calculated on a dry basis, applied to the fibrous starting web suitably ranges from 10 to 100 parts or more per 100 parts of the starting web and preferably from 20 to 45 parts per 100 parts of the starting web. The impregnated web is then dried and cured. The fabrics are suitably dried by passing them through an air oven or over a series of heated cans and then through a curing oven or sections of hot cans. Ordinarily, convection air drying is effected at 65-95°C followed by curing at 145-155°C. However, other time-temperature relationships can be employed as is well known in the art, with shorter times at higher temperatures or longer times at lower temperatures being used. For example, the curing step can be carried out at 135°C for about 15 minutes or more in a laboratory or pilot line but may require only 2 to 20 seconds on high pressure, high efficiency steam cans used in high speed production. If desired, the drying and curing can be effected in a single exposure or step. In the case of vinyl ester emulsions for fiberfill, it is generally desirable to employ polymers comprising at least about 85% by weight of the vinyl ester, preferably vinyl acetate, and to carry out the polymerization in the presence of an emulsifier or surface active agent. Fiberfill is a generic term used to describe a variety of nonwoven fabrics for a variety of end uses. The common feature of all fiberfill products is a measure of loft or thickness in the fabric. This loft is a characteristic of value because it imparts insulation to outerwear and bed quilt stuffing, cushioning in furniture padding, dust holding capacity to filter media and resiliency to scrubbing pads. The most common construction of a fiberfill product is a loosely garnetted, cross-lapped or air laid web of 6 to 30 denier polyester staple fibers, which is bonded (locked in its particular fiber arrangement) by an emulsion polymer binder. Fiberfill products can be made with other fibers, e.g., polyamide, cellulose acetate, rayon, glass, alone or in blends with each other. Some fiberfill is sold without a bonding agent but the material will lack durability, tensile strength and resiliency when compared to a bonded product. Bonding methods other than emulsion polymers, such as needle punching and meltable fibers and powders are also used, but the polymer emulsion method produces the optimum strength/loft ratios for the majority of fiberfill markets. In the case of vinyl ester containing emulsions for use as woodworking adhesives, the emulsion polymer is prepared in a protective colloid, preferably polyvinyl alcohol, with at least about 85% of the vinyl ester monomer. The resultant emulsions may be used in any conventional woodworking adhesive compositions and formulated with such additives as are commonly used in the production of these adhesives. The adhesives may also be formulated with a fusion aid such as tetrahydrofurfuryl alcohol, ethylene glycol diacetate and ethylene glycol monoethyl ether acetate as taught in US-A-4,474,915, present in the amount of 1 to 7% of polymer solids, by weight. The addition of acidic, metal salt curing agents may also be desired in order to accelerate the cure of the formulated adhesive. The preferred curing agents for use herein comprise acidic, metal salts from the group consisting of chromic nitrate, chromic perchlorate, aluminum nitrate, aluminum chloride, zinc nitrate and para-toluene sulphonic acid. The proportion of acidic, metal salt curing agent that is added will depend upon the rate of cure that is desired in the final product, but a practical range has been found to be from 0.003 to 0.12 gram equivalents of curing agent (anhydrous basis) for each 100 grams of the total weight of the blend of the adhesive composition. If fusion aids are used in the formulation, it may be desirable to add crosslinking inhibitors such as are described in US-A-4,085,074 issued April 18, 1978 to M. C. Woo and re-issued as US-B-30,576. Typical inhibitors include ammonia, alkylamines (e.g., triethylamine) and alkanolamines (e.g., triethanolamine and N-methylethanolamine). When used, they are added ordinarily in amounts such that the mole ratio of the inhibitor to the curing agent is in the range from 0.1 to 1.7. They may be added to the vessel at the end of the polymerization reaction or they may be added just before or with the curing agent. Their addition improves the storage stability of the adhesives. Emulsion polymers were prepared according to the examples listed in Table I. Detailed descriptions of each follow after this Table. Example # Major monomers % w/w Minor monomers % w/w Solids % Viscosity mPascP (20rpm) pH Grit % 1 5.2 NMA 52.0 80 4.9 0.002 2 85 Vinyl Acetate 8.4 AGA, 6.7 HPA 47.5 33 3.5 0.001 3 15 Ethylene 8.2 AGAME, 6.7 HPA 49.7 2100 2.2 0.002 4 8.9 MAGME, 6.7 HPA 55.6 40 2.4 0.023 5 5.2 DMHEA 3.9 HPA 55.2 45 3.7 0.004 6 3.0 NMA 50.0 120 3.1 0.012 7 50 Methyl 4.8 AGA, 3.9 HPA 50.2 75 1.9 0.004 8 Methacrylate 4.7 AGAME, 3.9 HPA 50.2 75 1.7 0.004 9 50 Bury Arylate 5.1 MAGME, 3.9 HPA 50.3 33 2.8 0.057 10 5.2 DMHEA, 3.9 HPA 48.8 225 3.1 0.008 11 3.0 NMA 49.4 74 3.2 0.004 12 75 Vinyl Acetate 4.7 AGAME, 3.9 HPA 46.0 50 2.3 0.010 13 25 Butyl Arylate 6.0 AGABE, 3.9 HPA 44.9 23 2.9 0.041 14 5.2 DMHEA 3.9 HPA 48.2 123 3.5 0.004 15 100 Vinyl Acetate 3.5 NMA 46.3 55 3.2 0.002 16 6.1 DMHEA 45.7 53 4.4 0.003 17 100 Vinyl Acetate 3.0 NMA 52.3 6400 4.5 0.022 18 3.0 DMHEA 49.7 8200 4.0 0.048 NMA = N-methylol acrylamide AGA = acrylamido glycolic acid AGAME = AGA methyl ester AGABE = AGA butyl ester MAGME = methyl acrylamido glycolate methyl ether DMHEA = N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide HPA = 2-hydroxypropyl acrylate EXAMPLE 1 A typical ethylene/vinyl acetate emulsion polymer containing N-methylol acrylamide was prepared as a control according to the following. A 10 liter stainless steel autoclave equipped with heating/cooling means, variable rate stirrer and means of metering monomers and initiators was employed. To the 10 liter autoclave was charged 540g (of a 20% w/w solution) sodium alkyl aryl polyethylene oxide sulphate (3 moles ethylene oxide), 60g (of a 70% w/w solution) alkyl aryl polyethylene oxide (30 moles ethylene oxide), 36g (of a 25% w/w solution in water) sodium vinyl sulphonate, 2g sodium formaldehyde sulphoxylate, 0.6g sodium acetate, 9g (of a 1% solution in water) ferrous sulphate solution and 1100g water. After purging with nitrogen all the vinyl acetate (3600g) was added and the reactor was pressurized to 38.66 kg/cm² (550 psi) with ethylene and equilibrated at 50°C for 15 minutes. The polymerization was started by metering in solutions of 14g tertiary butyl hydroperoxide in 250g water and 11.5g sodium formaldehyde sulphoxylate in 250g water. The initiators were added at a uniform rate over 3.5 hours. Concurrently added with the initiators over a period of 3 hours was a solution comprising 460g N-methylol acrylamide (48% w/w solution in water) and 0.5g sodium acetate in 1250g water. During the polymerization, the temperature of the reaction was maintained at 80-85°C and at the end of the reaction, the emulsion was transferred to an evacuated vessel (30 liters) to remove residual ethylene from the system. This product was used for comparison with other examples as listed in Table II. EXAMPLE 2 The procedure was as in Example 1, except for the following: a) The sodium formaldehyde sulphoxylate in the initial charge was replaced by 2.1g ascorbic acid. b) The monomer solution added over 3 hours comprised 356g acrylamido glycolic acid monohydrate [AGA], 284g 2-hydroxypropyl acrylate, and 1.7g sodium acetate in 1200g water, accompanied by a solution of 70g of 30% ammonia in 350g water. c) The polymerization was initiated with solutions of 14.6g of 30% hydrogen peroxide in 250g water and 10g ascorbic acid in 250g water. EXAMPLE 3 The procedure was as in Example 2, except that the monomer solution added over 3 hours comprised 348g acrylamido glycolic acid methyl ester [AGAME], 284g 2-hydroxypropyl acrylate, and 1.0g sodium acetate in 1500g water. EXAMPLE 4 The procedure was as in Example 3, except that 378g methyl acrylamido glycolate methyl ether [MAGME] were used in place of acrylamido glycolic acid methyl ester [AGAME]. EXAMPLE 5 The procedure was as in Example 3, except for the following: a) The monomer solution added over 3 hours comprised 539g N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide [DMHEA] (50% w/w solution in water, 82% active), 164g 2-hydroxypropyl acrylate, and 1.0g sodium acetate in 1000g water. b) The polymerization was initiated with solutions of 18g of 30% hydrogen peroxide in 250g water and 12.8g ascorbic acid in 250g water. EXAMPLE 6 A typical acrylic emulsion polymer containing N-methylol acrylamide was prepared as a control according to the following. A 2 liter glass reactor equipped with a heating/cooling jacket, variable rate stirrer and means of metering monomers and initiators was employed. To the 2 liter reactor was charged 1g (of a 20% w/w solution) sodium alkyl aryl sulphonate, 3g (of a 70% w/w solution) alkyl aryl polyethylene oxide (30 moles ethylene oxide), 0.8g ammonium persulphate, 0.6g sodium acetate and 350g water. After purging with nitrogen, 30g methyl methacrylate and 25g butyl acrylate were added and the reactor was equilibrated at 30°C for 5 minutes. The polymerization was started by heating to 78°C and maintained by metered addition of a solution of 1.0g ammonium persulphate in 40g water. The initiator was added at a uniform rate over 3.5 hours. Concurrently added with the initiators over the same period of 3.5 hours was a pre-emulsified blend of 220g methyl methacrylate, 225g butyl acrylate and 31.3g N-methylol acrylamide (48% w/w solution in water) in a solution of 10g (of a 20% w/w solution) sodium alkyl aryl sulphonate and 6g (of a 70% w/w solution) alkyl aryl polyethylene oxide sulphate (30 moles ethylene oxide) in 76g water. During the additions and for 45 minutes afterwards, the temperature of the reaction was maintained at 78-80°C. This product was used for comparison with other examples as listed in Table II. EXAMPLE 7 The procedure was as in Example 6, except for the following: a) The pre-emulsified blend contained 24.2g acrylamido glycolic acid monohydrate [AGA] and 19.3g 2-hydroxypropyl acrylate instead of the N-methylol acrylamide, with 120g added water. b) The initiation was maintained with a solution of 1.1g ammonium persulphate in 40g water. EXAMPLE 8 The procedure was as in Example 6, except for the following: a) The amount of ammonium persulphate in the initial charge was 1.0g. b) The pre-emulsified blend contained 23.6g acrylamido glycolic acid methyl ester [AGAME] and 19.3g 2-hydroxypropyl acrylate instead of the N-methylol acrylamide, with 108g added water. c) The initiation was maintained with solutions of 1.5g ammonium persulphate in 40g water and 1.3g sodium metabisulphite in 40g water. EXAMPLE 9 The procedure was as in Example 6, except that the pre-emulsified blend contained 25.7g methyl acrylamido glycolate methyl ether [MAGME] and 19.3g 2-hydroxypropyl acrylate instead of the N-methylol acrylamide, with 121g added water. EXAMPLE 10 The procedure was as in Example 6, except that the pre-emulsified blend contained 63.4g N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide [DMHEA] (50% w/w solution in water, 82% active) and 19.3g 2-hydroxypropyl acrylate instead of the N-methylol acrylamide. In preparing the samples for testing, lengths of 15 gram per square meter polyester were saturated using a Mathis Padder and a batch of 100 parts binder, 2 parts surfactant, 1 part catalyst and sufficient water to give a 20% solids dilution, with a dry pick up of approximately 40 parts binder per 100 parts polyester web. The saturated web was dried for 2 minutes at 145°C in a laboratory contact drier. Similar test samples were obtained using: i) 15 gram per square meter rayon with the binder diluted to 18% solids giving a dry pick up of approximately 25 parts per 100 web and ii) 34 gram per square meter pulp with the binder diluted to 12% solids giving a dry pick up of approximately 17 parts per 100 web. The tensile tests were run on a standard Instron tester set at 7.62 cm (3 inch) gauge length and 12.7 cm (5 inch) crosshead speed. The wet tensile was run after soaking specimens one minute in a 0.5% solution of Aerosol OT wetting agent, a surfactant of American Cyanamid Company. The solvent tensile was run after soaking the specimens one minute in methyl ethyl ketone. The results obtained by testing the binders of Examples 1-10 are shown in Table II. Results shown reflect the average of 8 tests. Results are presented relative to the control batches which contain N-methylol acrylamide. Thus the figures against Examples 2-5 are percentages of the corresponding result for Example 1. Similarly, the figures against Examples 7-10 are percentages of the corresponding result for Example 6. Example Numbers EVA ACRYLIC Pulp Rayon Polyester Pulp Rayon Polyester 1 & 6 (NMA) Dry (100) (100) Wet Solvent 2 & 7 (AGA) Dry 100 113 37 89 112 60 Wet 40 68 27 84 106 56 Solvent 15 4 5 57 41 30 3 & 8 (AGAME) Dry 103 122 70 112 86 75 Wet 54 75 43 77 88 78 Solvent 18 14 10 89 73 37 4 & 9 (MAGME) Dry 103 155 67 100 106 72 Wet 55 78 54 73 81 66 Solvent 37 52 17 53 60 47 5 & 10 (DMHEA) Dry 107 85 82 119 140 101 Wet 80 70 73 109 111 81 Solvent 65 63 49 114 167 117 These results presented in Table II show that all of the crosslinkers perform quite well, compared to NMA, in an acrylic polymer. However, in an EVA polymer, all except DMHEA have deficient wet strength and solvent resistance especially on cellulosic fibers. The solvent resistance, in particular is a stringent test of the effectiveness of the crosslinker in this kind of application. DMHEA is also unique in giving good performance across all substrates under all conditions. Further, this superior performance of DMHEA in the EVA copolymer is achieved with only 5.2 parts per 100 EVA compared with 8.4 used for AGA, 8.2 for AGAME and 8.9 for MAGME. In addition to the above, DMHEA also has utility in vinyl/acrylic copolymers containing a high fraction of vinyl acetate, as indicated by the following Examples. EXAMPLE 11 A typical vinyl/acrylic emulsion polymer containing N-methylol acrylamide was prepared as a control using the procedure of Example 6 except for replacing the methyl methacrylate with vinyl acetate, 50g in the initial charge and 325g in the pre-emulsified blend. The amount of butyl acrylate was also adjusted to 5g in the initial charge and 120g in the pre-emulsified blend. This product was used for comparison with other examples as listed in Table III. EXAMPLE 12 The procedure was as in Example 11, except that the pre-emulsified blend contained 23.6g acrylamido glycolic acid methyl ester [AGAME] and 19.3g 2-hydroxypropyl acrylate instead of the N-methylol acrylamide, with 130g added water. EXAMPLE 13 The procedure was as in Example 12, except that the pre-emulsified blend contained 29.9g acrylamido glycolic acid butyl ester [AGABE] instead of the methyl ester [AGAME]. EXAMPLE 14 The procedure was as in Example 12, except that the pre-emulsified blend contained 63.4g N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide [DMHEA] (50% w/w solution in water, 82% active) instead of the AGAME. Binders were prepared from Examples 11-14 and tested as described above with the results shown in Table III. As before, results shown reflect the average of 8 tests and they are presented relative to the control batches, which contain N-methylol acrylamide. Thus the figures against Examples 12-14 are percentages of the corresponding result for Example 11. Example Numbers Vinyl/Acrylic Pulp Rayon Polyester 11 (NMA) Dry (100) Wet Solvent 12 (AGAME) Dry 79 79 100 Wet 52 56 65 Solvent 33 30 21 13 (AGABE) Dry 75 89 80 Wet 32 56 53 Solvent 16 32 21 14 (DMHEA) Dry 95 97 91 Wet 75 86 81 Solvent 67 102 74 Once again, DMHEA is seen to give good wet strength and solvent resistance and is the only formaldehyde-free crosslinker to give acceptable performance across all of the substrates. The following Examples illustrate the use of DMHEA in a vinyl acetate homopolymer as a binder for fiberfill. The comparison is made with a commonly used fiberfill binder, whose performance properties and technical value are well known and which is based on the crosslinking monomer N-methylol acrylamide. EXAMPLE 15 The standard vinyl acetate emulsion homopolymer containing N-methylol acrylamide was prepared as a control according to the following. A 2 liter glass reactor equipped with a heating/cooling jacket, variable rate stirrer and means of metering monomers and initiators was employed. To the 2 liter reactor was charged 12g (of a 25% w/w solution) calcium alkyl aryl polyethylene oxide phosphate, 0.8g (of a 70% w/w solution) alkyl aryl polyethylene oxide (40 moles ethylene oxide), 0.8g sodium vinyl sulphonate, 0.4g calcium acetate and 400g water. After purging with nitrogen, 50g vinyl acetate were added and the reactor was equilibrated at 30°C for 5 minutes. The polymerization was started by heating to 60°C and then adding a solution of 0.5g sodium persulphate in 12g water. The reaction was maintained by metered addition of a solution of 0.8g sodium persulphate in 40g water. The initiator was added at a uniform rate over 4 hours. Concurrently added with the initiator over the same period of 4 hours was a pre-emulsified blend of 450g vinyl acetate, 0.8g sodium vinyl sulphonate and 36.5g N-methylol acrylamide (48% w/w solution in water) in a solution of 20g (of a 25% w/w solution) calcium alkyl aryl polyethylene oxide phosphate, 15g (of a 70% w/w solution) alkyl aryl polyethylene oxide (40 moles ethylene oxide) and 0.7g calcium acetate in 96g water. The temperature of the reaction was brought to and maintained at 74-76°C for the duration of the additions and for 45 minutes afterwards. EXAMPLE 16 The procedure was as in Example 15, except that the pre-emulsified blend contained 74g N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide [DMHEA] (50% w/w solution in water, 82% active) instead of the N-methylol acrylamide. The binders were applied by diluting with water to 20% solids and adjusting the pH to 2.5. This preparation was then sprayed onto 30 cm (12 inch) squares of 130 gram/square meter polyester batting using a commercially available spraygun. The batts were dried for 1 minute on each side followed by a 1 minute cure at 130°C in a Werner Mathis oven. The polyester batt was commercially produced and was a garnetted and crosslapped web of 6 denier Hoechst Celanese 295 fiber. The batts were sewn into bags consisting of one side polyester tricot knit and the other 90x76 count bleached 80/20 polyester/cotton print cloth. The sewn bags were washed five times in a commercially available Sears Kenmore Model 80 washing machine along with ballast of five terrycloth towels. The machine settings were: water temperature warm/warm, water level medium and cycle time of cotton heavy. A 118 g (4oz) cup of Tide detergent, a product of Proctor & Gamble, Cincinnati, Ohio, was added at the beginning of each wash. The batts were rated using the ASTM standard ratings and were not dried between washes. The results are shown in Table IV. Example Bail Weight g/m² % Binder Add-On Wash Cycle 1 2 3 4 5 15 (NMA) 11.8 22.4 5.0 5.0 5.0 5.0 4.5 16 (DMHEA) 12.4 20.2 5.0 4.5 4.0 4.0 4.0 Ratings: 5 = best, 1 = worst. The results presented in Table IV show that substitution of DMHEA into this standard fiberfill binder gave a product with very good wash performance compared to the control and is acceptable for many end-uses where durability is required. The following Examples illustrate the use of DMHEA in a vinyl acetate homopolymer based emulsion prepared with a protective colloid such as polyvinyl alcohol and employed as a wood working adhesive. In evaluating the DMHEA containing polymer, the emulsion was compared with a commonly used wood working adhesive, whose performance properties and technical values are well known, comprising a protective colloid (polyvinyl alcohol) stabilized latex of vinyl acetate homopolymer incorporating the crosslinking monomer N-methylol acrylamide. EXAMPLE 17 The standard vinyl acetate emulsion homopolymer stabilized by a protective colloid, polyvinyl alcohol, and containing N-methylol acrylamide was prepared as a control according to the following. A 2 liter glass reactor equipped with heating /cooling jackets, variable speed stirrer and means of metering monomer and initiator was employed. To the 2 liter reactor was charged 135g (of a 10% w/w solution in water) of medium viscosity, 88% hydrolyzed polyvinyl alcohol, 0.10g sodium acetate, 0.50g (of a 1% w/w solution in water) ferrous sulphate solution, 0.34g sodium formaldehyde sulphoxylate, 1.25g of Lanolubric (a coconut fatty acid defoamer), and 140g of water. The pH was adjusted to 5.2 with phosphoric acid. After purging with nitrogen, 75g of vinyl acetate was charged to the reactor. The polymerization was then initiated at 60°C by metering in a solution of 1.00g of ammonium persulphate in 35g of water and 0.59g of sodium formaldehyde sulphoxylate in 35g of water at a rate of 6 ml/hour. The reaction temperature was allowed to rise to 74°C. At this temperature, the catalyst solution addition rate was increased to 8 ml/hour. Concurrently added with the initiator at 74°C over a period of 3 hours were 425g of vinyl acetate and 31.3g of N-methylol acrylamide (48% w/w solution in water), both monomers being pre-emulsified with 1.67g (of a 75% w/w solution in water) sodium salt of a dialkyl sulphosuccinate, 7.5g (of a 70% w/w solution in water) alkyl aryl polyethylene oxide (30 moles ethylene oxide), 50g (of a 10% w/w solution in water) of medium viscosity, 88% hydrolyzed polyvinyl alcohol, 3.5g of 10% ammonium hydroxide solution and 115g of water. On completing the addition of the pre-emulsified monomer mixture, the catalyst addition was continued for another half hour to ensure completion of reaction. The characteristics of the latex obtained are shown in Table I. EXAMPLE 18 Using the general procedure described in Example 17, the test batch was prepared by replacing NMA by 36.5 g of DMHEA (50% w/w solution in water, 82% active) and the characteristics of the latex are shown in Table I. In testing the emulsion polymers, the wood working adhesives were first formulated according to the following: A - Latex base (Control / Test batch) = 94.0 B - Ethylene glycol diacetate (Eastman Chemicals) = 3.0 Water=3.0 C - Versenex 80 (Dow Chemicals Co.) = 0.2 Water=0.2 D - Aluminium chloride solution (20% w/w) = 5.0 The latex base 'A' was first mixed with the fusion aid 'B' to form a smooth dispersion followed by the iron scavenger 'C'. This mixture was allowed to age overnight. Then the cure accelerator 'D' was mixed in for 30 minutes. Three ply birch veneer laminations were glued up with the grains perpendicular and using eight wet mils thickness of the above formulations. The laminations were then hot pressed at 6,9 bars (100 psi). A hot press cure schedule of 150°C for 30 minutes was selected (Ref. US-A 3,252,931). From these constructions ten splints were cut into specimens 2.5 cm (one inch) wide by 12.7 cm (five inches) in length. A 2.5 cm (one inch) notch in the center was cut 2/3 of the way through to the middle veneer yielding a 2.5 cm² (one square inch) test area. The laminated samples were allowed to cure for 7 days at room temperature. After the seven-day cure period, five splint specimens from each lamination were subjected to four hours in boiling water followed by a 20 hour drying period at about 63°C (145°F). The specimens were again immersed in boiling water for 4 hours followed by a 30 minute room temperature water soak: The splint specimens were then pulled apart wet via an Instron Tester at 1.25 cm (0.5 inches) per minute. Results are reported as kg/cm² (pounds per square inch) required to pull the splints apart and the resulting percent wood tear observed. The results of the tests are shown in Table V. Specimen # Example 17 (NMA) Example 18 (DMHEA) kg/cm² (psi) % Tear kg/cm² (psi) % Tear 1 9.49 (135) 100 9.84 (140) 95 2 8.78 (125) 100 9.13 (130) 85 3 8.43 (120) 100 8.43 (120) 100 4 8.43 (120) 100 8.08 (115) 10 5 9.13 (130) 100 9.49 (135) 85 The results in Table V indicate that N-methylol acrylamide [NMA] can be substituted with an equal weight of dimethoxyhydroxyethyl acrylamide [DMHEA] to give emulsion woodworking adhesives with excellent tensile strength and water resistance.

Claims: An emulsion polymer comprising more than 50% vinyl ester and 1 to 15% by weight of N-(2,2-dialkoxy-1-hydroxy)ethyl acrylamide wherein the alkoxy group contains 1 to 4 carbon atoms. The emulsion polymer of Claim 1 additionally comprising up to 49% by weight of at least one copolymerizable comonomer selected from the group consisting of olefins, vinyl halides and C₁ to C₈ alkyl acrylates or methacrylates. The emulsion polymer of Claim 1 additionally comprising up to 10% by weight of a olefinically unsaturated carboxylic acid having from 3 to 6 carbon atoms. The emulsion polymer of Claim 1 additionally comprising up to 15% by weight hydroxyalkyl (C₂ to C₄) acrylate. A nonwoven binder composition comprising the emulsion polymer of Claim 1. The nonwoven binder composition of Claim 5 comprising vinyl acetate, 5 to 35% by weight ethylene, 1 to 15% by weight N-(2,2-dimethoxy -1-hydroxy)ethyl acrylamide and up to 10% by weight hydroxypropyl acrylate. A method of binding nonwoven fibrous webs comprising the steps of (a) impregnating the web with a binder composition comprising an emulsion polymer, the emulsion polymer comprising more than 50% by weight of a vinyl ester, 1 to 15% by weight of N-(2,2-dialkoxy-1-hydroxy) ethyl acrylamide and (b) curing the binder. The method of Claim 7 wherein the binder composition comprises vinyl acetate, 5 to 35% by weight ethylene, 1 to 15% by weight N-(2,2-dimethoxy-1-hydroxy)ethyl acrylamide and up to 10% by weight hydroxypropyl acrylate. A method for binding fiberfill comprising the steps of (a) impregnating the fibers with an emulsion comprising more than 50% by weight of a vinyl ester and 1 to 15% by weight of N-(2,2-dialkoxy-1-hydroxy) ethyl acrylamide and (b) curing the binder. A woodworking adhesive composition comprising a protective colloid stabilized emulsion polymer comprising more than 50% by weight of a vinyl ester and 1 to 15% by weight of N-(2,2-dialkoxy-1-hydroxy) ethyl acrylamide. The woodworking adhesive of Claim 10 further formulated with 1 to 7% by weight of the polymer solids of a fusion aid. The adhesive of Claim 11 wherein the fusion aid is selected from the group consisting of tetrahydrofurfuryl alcohol, ethylene glycol diacetate and ethylene glycol monoethyl ether acetate. The woodworking adhesive of Claim 10 wherein the protective colloid is polyvinyl alcohol.

Inventors: CHANDRAN RAMA S, HALLAM MALCOLM F, IOVINE CARMINE P, KUKKALA PRAVIN K, LEIGHTON JOHN C, MUDGE PAUL R, CHANDRAN, RAMA S., HALLAM, MALCOLM F., IOVINE, CARMINE P., KUKKALA, PRAVIN K., LEIGHTON, JOHN C., MUDGE, PAUL R.
Applicants: NAT STARCH CHEM INVEST, NATIONAL STARCH AND CHEMICAL INVESTMENT HOLDING CORPORATION
Application year: 1992
Main classification: C08F218
IPC codes: C08L31, C08F218, D04H1, C09J131