JP2009173752A - Polymer emulsifier and polyolefin-based resin emulsion using the same - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To obtain an emulsion maintaining low-temperature film-formability of the emulsion, and low-temperature adhesiveness and transparency of a dried film in addition to emulsion stability, and hardly causing coagulation and viscosity increase even if a hydrophilic organic solvent or an additive having ionicity is added thereto and mechanical shear is added. <P>SOLUTION: The polymer emulsifier contains a copolymer containing 5-40 mol% structural unit derived from an anionic monomer having a (meth)acryloyl group and a hydrophilic group as a copolymer component, 5-30 mol% structural unit derived from a cationic monomer comprising an alkylaminoalkyl (meth)acrylate as a main component as a copolymer component, and 1-20 mol% structural unit derived from a nonionic monomer having a specific structure as a copolymer component, and having a 1/2 method temperature of ≥40°C and ≤140°C by a flow tester of the copolymer. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

  The present invention relates to a polymer emulsifier whose dry film has excellent low-temperature film-forming properties and transparency, and a polyolefin resin emulsion using the same.

  In recent years, polyolefin resins such as polypropylene and polyethylene have been used for daily necessities, automotive parts, building materials and the like from the viewpoints of versatility, strength, physical properties, ease of molding, solvent resistance, and appearance.

  These polyolefin resins were difficult to bond due to the low polarity of the polyolefin resins themselves. Therefore, it was necessary to use an adhesion-imparting component such as chlorinated polypropylene dissolved in an organic solvent for bonding these polyolefin resins.

  However, in recent years, there has been a strong demand for solvent-free paints for environmental protection and safety and health, and conventional solvent-based paints are being made water-based (see Patent Documents 1 and 2). In addition, it has been pointed out that chlorinated polyolefin resins may generate highly toxic dioxins when discarded by incineration.

  For example, in the case of an ethylene / vinyl acetate copolymer, the ethylene / vinyl acetate copolymer is first heated and melted, and then an anionic or nonionic emulsifier is added and stirred. Then, the method obtained by adding hot water and emulsifying using mechanical shear force, such as a homomixer, is mentioned (refer patent document 3).

  However, when the above-mentioned anionic emulsifier and nonionic emulsifier are used, there is a risk of bleeding out when the obtained product is used. On the other hand, a method for producing an aqueous polymer dispersion using a neutralized product of a specific acrylic copolymer with improved emulsion stability as an anionic water-soluble polymer dispersant is known (Patent Document 4). reference).

  However, this anionic water-soluble polymer dispersant can improve the dispersion stability. However, when water, volatile base, etc. evaporate from the obtained polymer dispersion, Carboxyl groups cause intramolecular or intermolecular association, resulting in an increase in melt viscosity, hindering the fusion of emulsion resin particles, resulting in poor film formation at low temperatures, and low temperature of the resulting dried film. Adhesiveness and transparency may be inferior, and its application may be limited.

  On the other hand, a method for producing an aqueous polymer dispersion using a neutralized product of a specific acrylic copolymer having excellent low-temperature film-forming properties as a cationic water-soluble polymer dispersant is known (see Patent Document 5). .

  However, the dry film obtained using this cationic water-soluble polymer dispersant is improved in low-temperature film-forming property, low-temperature adhesiveness, and transparency, but with an anionic aqueous dispersion used for general purposes. There is a restriction that it is difficult to use the mixture.

  As an improvement method, Japanese Patent Application No. 2006-195891 discloses an anionic monomer having (meth) acrylic acid as a main component and a cationic monomer having N, N-dimethylaminoethyl methacrylate as a main component. A method of using an amphoteric polymer emulsifier obtained by polymerizing a monomer mixture containing benzene has been studied.

Japanese Patent Laid-Open No. 06-336568 JP-A-11-106600 JP 57-61035 A JP 58-127752 A JP 58-118843 A

  However, when the amphoteric polymer emulsifier is used, the carboxyl group of the amphoteric polymer emulsifier causes a barrier between particles due to the formation of hydrogen bonds during film formation, which adversely affects the film formation. May be insufficient.

  In addition, hydrophilic organic solvents and pigments are added to make emulsions using the above amphoteric polymer emulsifiers into paints and adhesives. By adding the additive which has, the emulsification stability of the said polymer emulsifier may fall, and an aggregate may be generated. When aggregates are generated in the paint or adhesive, streaks and blisters are generated on the coated surface, resulting in a problem of reducing the commercial value. Further, when a coating machine or the like that is mechanically sheared is used, there may be a problem that the aggregation of emulsion particles is promoted or the viscosity is increased.

  Therefore, the present invention solves such problems, maintains emulsion stability at low temperature, maintains low temperature adhesion property and transparency of dry film as well as emulsification stability, and has hydrophilic organic solvents and ionic properties. It is an object to obtain an emulsion that does not cause aggregation or increase in viscosity even when mechanically sheared by adding an additive having a viscosity.

This invention contains 5-30 mol% of a structural unit derived from an anionic monomer having a (meth) acryloyl group and a hydrophilic group (component (A)) as a copolymer component, and is an alkyl (meth) acrylate. A nonionic monomer comprising a structural unit derived from a cationic monomer (component (B)) having aminoalkyl as a main component, as a copolymerization component, and represented by the following chemical formula (1) The structural unit derived from the body (component (C)) is contained in an amount of 1 to 20 mol% as a copolymer component, and the 1/2 method temperature of the copolymer by a flow tester is 40 ° C. or higher and 140 ° C. or lower The above problem has been solved by obtaining a molecular emulsifier.
_{R 1 - (C n H 2n} O) m -R 2 ... (1)
(In the formula, R ₁ represents a group selected from a (meth) acryloyloxy group and a (meth) acryloyloxyethoxy group; R ₂ represents H or an alkyl group having 1 to 4 carbon atoms; 3 represents an integer, and m represents an integer of 4 to 25.)

  According to this invention, since it has a structural unit derived from a predetermined nonionic monomer, even if a hydrophilic organic solvent or an ionic additive is added, the emulsion stabilization effect by mechanical shearing can be maintained. it can.

  In addition, since it has a structural unit derived from a predetermined cationic monomer, it prevents the formation of a barrier between particles due to hydrogen bond formation during film formation, improves film formation, and improves the surface smoothness of the thin film. Can be improved. And transparency can also be improved.

  Moreover, since it has the structural unit which has anionic group, and the structural unit which has cationic property, the characteristic that an emulsion stabilization effect increases further by affinity of both can be exhibited.

Hereinafter, the present invention will be described in detail.
The polymer emulsifier according to the present invention is a copolymer having a structural unit derived from a specific anionic monomer, a structural unit derived from a cationic monomer, and a structural unit derived from a nonionic monomer as a copolymerizable component. An emulsifier containing a polymer.

[(A) component]
The specific anionic monomer (hereinafter referred to as “component (A)”) refers to an anionic monomer having a (meth) acryloyl group and a hydrophilic group. In the present specification, “(meth) acryloyl” and “(meth) acryl” mean “acryloyl or methacryloyl” and “acryl or methacryl”.

  Examples of the hydrophilic group include a carboxyl group, a sulfonic acid group, a phosphoric acid group, and an acidic phosphate group, and at least one of them is used.

  Examples of the component (A) include (meth) acrylic acid, itaconic acid, citraconic acid, maleic acid, crotonic acid, fumaric acid, maleic acid monoalkyl ester, and fumaric acid monoalkyl ester. These may use only 1 type and may mix and use 2 or more types.

[B component]
The specific cationic monomer (hereinafter referred to as “component (B)”) refers to a cationic monomer mainly composed of alkylaminoalkyl (meth) acrylate. This (B) component is used in order to express film forming property and adhesion of a substrate.

  The alkyl group substituted with the alkylamino group of the alkylaminoalkyl (meth) acrylate constituting the component (B) is preferably an alkyl group having 1 to 6 carbon atoms.

  Examples of such alkylaminoalkyl (meth) acrylates include N, N-dimethylaminoethyl (meth) acrylate, N, N-diethylaminoethyl (meth) acrylate, and N, N- (meth) acrylate. And dimethylamino-2-aminoethyl. These may use only 1 type and may mix and use 2 or more types.

  Examples of the cationic monomer other than the above-mentioned alkylaminoalkyl (meth) acrylate include N-aminoalkyl (meth) acrylamides such as N, N-dimethylaminoethyl (meth) acrylamide.

[C component]
The specific nonionic monomer (hereinafter referred to as “component (C)”) refers to a compound represented by the formula (1) as shown below.
_{R 1 - (C n H 2n} O) m -R 2 ... (1)
In the formula, R1 represents a group selected from the following two groups (a) and (b), R2 represents H or an alkyl group having 1 to 4 carbon atoms, and n is 1 to 3. An integer is shown, and m is an integer of 4 to 25.
(A) (meth) acryloyloxy groups _(CH 2 = _CH-COO- or _{CH 2 = C (CH 3)} -COO-)
(B) (meth) acryloyloxy ethoxy _{(CH 2 = CH-COO-} CH 2 -CH 2 -O-
Or _{CH 2 = C (CH 3)} -COO-CH 2 -CH 2 -O-)

  Specific examples of the component (C) include methoxytetraethylene glycol (meth) acrylate, ethoxytetraethylene glycol (meth) acrylate, propoxytetraethylene glycol (meth) acrylate, n-butoxytetraethylene glycol (meth) acrylate, n -Pentoxytetraethylene glycol (meth) acrylate, tetrapropylene glycol (meth) acrylate, methoxytetrapropylene glycol (meth) acrylate, ethoxytetrapropylene glycol (meth) acrylate, propoxytetrapropylene glycol (meth) acrylate, n-butoxytetra Propylene glycol (meth) acrylate, n-pentoxytetrapropylene glycol (meth) acrylate, methoxypoly Ji glycol (meth) acrylate, ethoxy polyethylene glycol (meth) acrylate and the like. Among these, those having a polyethylene glycol group having 2 to 25 polyethylene glycol groups are preferred, and those having a polyethylene glycol group having 4 to 22 repeating units are more preferred. When the repeating unit is smaller than 2, it may be difficult to sufficiently exhibit the effect of improving the miscibility of the organic solvent. On the other hand, when the repeating unit is larger than 25, since the hydrophilic chain is solidified at a normal temperature, it may be difficult to exert a sufficient emulsion stabilizing effect.

[(D) component]
The copolymer constituting the polymer emulsifier according to the present invention has structural units derived from the components (A) to (C). The copolymer component used as a raw material for the copolymer is the component (A). In addition to the component to the component (C), a (meth) acrylic acid ester of an aliphatic alcohol having 1 to 22 carbon atoms (hereinafter referred to as “component (D)”) may be used.

  The component (D) is used as a component having a hydrophobic group to develop the emulsifying ability of the polymer emulsifier. Examples of the component (D) include methyl (meth) acrylate, ethyl (meth) acrylate, n-propyl (meth) acrylate, iso-propyl (meth) acrylate, and n-butyl (meth) acrylate. , Iso-butyl (meth) acrylate, t-butyl (meth) acrylate, 2-ethylhexyl (meth) acrylate, lauryl (meth) acrylate, tridecyl (meth) acrylate, stearyl (meth) acrylate, etc. It is done. Moreover, in order to improve heat fluidity and emulsifying power, two or more of these components may be mixed and used.

[Content ratio of each component]
In the copolymer constituting the polymer emulsifier according to the present invention, the content of the structural unit derived from the component (A) is required to be 5 mol% or more as the copolymerizable component, and preferably 10 mol% or more. When it is less than 5 mol%, the emulsifying ability of the polymer emulsifier tends to decrease. On the other hand, the upper limit of the content is preferably 40 mol%, and preferably 36 mol%. When it exceeds 40 mol%, the emulsifying ability of the polymer emulsifier tends to decrease, and the film forming temperature of the resulting aqueous dispersion increases, which may deteriorate the low-temperature adhesiveness and transparency of the resulting film.

  In the copolymer constituting the polymer emulsifier according to the present invention, the content of the structural unit derived from the component (B) is required to be 5 mol% or more as the copolymerizable component, and preferably 10 mol% or more. When it is less than 5 mol%, the film forming property and the adhesion of the substrate tend to be lowered. On the other hand, the upper limit of the content is preferably 30 mol%, and preferably 15 mol%. When it is more than 30 mol%, a stable emulsifier tends to be difficult to obtain.

  In the copolymer constituting the polymer emulsifier according to the present invention, the content of the structural unit derived from the component (C) is required to be 1 mol% or more as the copolymerizable component, and preferably 2 mol% or more. . If it is less than 1 mol%, the mechanical stability of the emulsion tends to be lowered. On the other hand, the upper limit of the content is preferably 20 mol%, and preferably 15 mol%. When it is more than 20 mol%, the emulsion stabilization effect tends to decrease.

  Moreover, the ratio ((A) / (B)) of the above component (A) and component (B) is preferably a molar ratio of 1.0 or more, and preferably 1.1 or more. If it is less than 1.0, the cationic property becomes strong, and it tends to be difficult to use together with an emulsion using an anionic emulsifier which is generally used. On the other hand, the upper limit of the molar ratio is preferably 2.0 and is preferably 1.9. If it is larger than 2.0, the film-forming temperature of the aqueous dispersion obtained becomes high, the low-temperature adhesiveness and transparency of the obtained film may be deteriorated, and the use tends to be limited.

  Next, when the copolymer (A) component to the component (D) are used, the constituent ratio of each component is (A) / (B) in terms of a molar ratio when the total amount is 100 mol%. / (C) / (D) = 5 to 30/5 to 30/1 to 20/20 to 70 is preferable, and 5 to 25/5 to 25/1 to 20/30 to 70 / is preferable.

  When each component is out of the above preferred range, the intended effect of the present invention may not be sufficiently obtained.

[Method for producing copolymer]
The copolymer constituting the polymer emulsifier according to the present invention can be produced by the following method.
First, the above components (A) to (D) are each weighed at a predetermined mixing ratio. Next, each component is added separately to the polymerization vessel for polymerization, or each monomer is mixed in advance and then added to the polymerization vessel for polymerization. Thereby, a copolymer can be manufactured.

  The copolymerization is carried out in the presence of a polymerization initiator at 0 to 180 ° C., preferably 40 to 120 ° C. for 0.5 to 20 hours, preferably 2 to 10 hours. This copolymerization is preferably carried out in the presence of a hydrophilic solvent such as ethanol, isopropanol or cellosolve or water.

  As the polymerization initiator, an initiator comprising a persulfate such as ammonium persulfate, potassium persulfate, sodium persulfate, etc., a redox initiator using the persulfate in combination with a sulfite, a thiosulfate reducing agent, Redox initiators using organic peroxides such as lauroyl peroxide, t-butyl hydroperoxide, cumene hydroperoxide or the like, and iron (II) salt, sulfite, thiosulfate reducing agents, etc. -Azobis (isobutyronitrile), 2,2'-azobis [2-methyl-N- (2-hydroxyethyl) propionamide], 2,2'-azobis [2- (2-imidazolin-2-yl) Propane] dihydrochloride, 2,2'-azobis (2-methylpropionamidine) dihydrochloride and other azo compounds, t-butyl Over oxy isobutyrate, 1,1-bis (t-butylperoxy) cyclohexene, t- butyl peroxybenzoate, and the like. The amount of the polymerization initiator used is preferably 0.01 to 10% by weight based on the total amount of monomers used.

  In order to improve the heat flow characteristics, it is also possible to reduce the molecular weight using a chain transfer agent or the like. In that case, in order to adjust the degree of polymerization, a known chain transfer agent such as mercaptans or lower alcohols such as methyl alcohol can be used.

  By the way, said (A) component contains an acidic hydrophilic group. Therefore, it is preferable that at least a part of the acidic hydrophilic group is neutralized with a basic substance. By neutralizing at least a part, the solubility in water is improved, the resulting polymer particle size is reduced, and the characteristics that the dispersion state in water is stabilized can be exhibited.

  The degree of neutralization, that is, the degree of neutralization is preferably 50 mol% or more, and preferably 100 mol% or more. If it is less than 50 mol%, the solubility of the resulting copolymer in water tends to be insufficient. On the other hand, the upper limit of the degree of neutralization is preferably 200 mol%, and preferably 150 mol%. When it is larger than 200 mol%, the water resistance tends to be insufficient.

  Examples of the basic substance include basic compounds such as alkali metal and alkaline earth metal hydroxides, ammonia, alkylamines, alkanolamines, morpholine, and the like. Examples of the alkali metal or alkaline earth metal hydroxide include sodium hydroxide, potassium hydroxide, magnesium hydroxide and the like, and specific examples of alkylamines include methylamine, dimethylamine, trimethylamine, ethylamine, Examples include diethylamine, and specific examples of alkanolamines include 2-amino-2-methylpropanol. Among these, it is preferable to use ammonia having volatility during low-temperature drying in order to improve the water resistance of the resulting film. Moreover, in order to raise emulsification power, sodium hydroxide and potassium hydroxide are preferable.

  Neutralization reaction is performed by making the said copolymer and a basic compound react at 20-100 degreeC for 0.1 to 3 hours.

  Further, the component (A) may be previously neutralized with a basic compound and used for copolymerization.

  Further, in order to improve the mechanical stability of an emulsion obtained by emulsifying polyolefin or the like with the above polymer emulsifier, emulsion polymerization is preferably performed in the presence of a nonionic polymer emulsifier. Examples of the location of the nonionic polymer emulsifier include a polymerization solvent and a monomer before the start of polymerization. Further, this nonionic polymer emulsifier may be present during the polymerization. Furthermore, after the polymerization, a nonionic polymer emulsifier may be present during the neutralization reaction.

  The nonionic polymer emulsifier is preferably a polyoxyalkylene ether polymer emulsifier, for example, polyoxyethylene, polyethylene oxide and polypropylene oxide block copolymer system, polypropylene oxide and polybutylene oxide block copolymer system, Polyoxyethylene alkyl ether polymer emulsifier, polyoxyethylene silicon polymer emulsifier, polyoxyethylene fatty acid mono- or polyglycerin ester polymer emulsifier, polyoxyethylene sorbitol fatty acid ester polymer emulsifier, polyethylene glycol fatty acid high Examples include molecular emulsifiers, fatty acid mono- or polyglycerin ester polymer emulsifiers, and fluorine nonionic polymer emulsifiers. In particular, block copolymers of polyethylene oxide and polypropylene oxide and polyoxyethylene alkyl ether polymer emulsifiers are preferred.

  The block copolymer of polyethylene oxide and polypropylene oxide may have a straight chain structure or a branched structure in the molecule, but preferably, the polyethylene oxide part is bonded to both ends of the propylene oxide part. In addition, a compound having a linear structure in which both ends of the molecule are hydroxyl groups (generally referred to as “pluronic nonionic polymer emulsifier”) is used.

  Furthermore, 1000-6000 are preferable and, as for the weight average molecular weight of this block copolymer, 1200-4000 are more preferable. If the weight average molecular weight is too small, the mechanical shear stability of the emulsion may not be obtained. On the other hand, if the weight average molecular weight is more than 6000, it is difficult to dissolve in water, which may reduce the stability of the emulsion.

  The addition amount (solid content) of the nonionic polymer emulsifier is preferably 1% by weight or more and more preferably 2% by weight or more based on the total monomer weight of the components (A) to (D). If it is less than 1% by weight, the mechanical stability of the emulsion tends to be insufficiently improved. On the other hand, the upper limit of the addition amount is 20% by weight, preferably 15% by weight. When it is more than 20% by weight, the water resistance may be deteriorated.

[Melting temperature]
The melt temperature of the copolymer thus obtained is a ½ method temperature of 40 ° C. or higher, preferably 50 ° C. or higher, and more preferably 60 ° C. or higher in the measurement of melt viscosity by a flow tester. When it is lower than 40 ° C, the dry film of the polymer emulsifier tends to be easily blocked. On the other hand, the upper limit of the 1/2 method temperature is preferably 140 ° C., and preferably 130 ° C. If it is higher than 140 ° C., the low-temperature film-forming property tends to decrease.

  The copolymer obtained by the above method is a polymer emulsifier by adding additives such as a fungicide, an antioxidant and a UV absorber as it is or within a range not inhibiting the effects of the present invention. It becomes.

  This polymer emulsifier can be used as an emulsifier for emulsifying a polymer substance. When an emulsified polymer substance is formed into a film, a dry film having good low-temperature film-forming property, transparency, and surface smoothness is obtained. It becomes easy to obtain. Further, it can be used as a compatibilizing agent in kneading two or more kinds of polymer substances.

  A general thermoplastic resin can be used as such a high molecular substance. As described in the item for measuring the melting temperature, the thermoplastic resin preferably has a 1/2 method temperature of 140 ° C. or lower in the measurement of the melt viscosity using a flow tester. If it is higher than 140 ° C., the low-temperature film-forming effect of the polymer emulsifier of the present invention may not be exhibited.

  Examples of the thermoplastic material having a 1/2 method temperature of 140 ° C. or lower include ethylene such as low density polyethylene, polyolefin resin such as propylene, ethylene / vinyl acetate copolymer, ethylene / acrylic acid copolymer and ester or So-called ethylene such as its salt, ethylene / methacrylic acid copolymer or its salt, ethylene / methacrylic acid ester copolymer or its salt, ethylene / ethyl acrylate / maleic anhydride copolymer, ethylene / propylene random copolymer, etc. Ethylene-based copolymers, propylene-hexene copolymers, propylene-based copolymers such as propylene-butene copolymers, polyethylene wax, ester wax, carnauba wax, Fischer-Trops wax , Micro Crystallinwa Box, paraffin wax and their oxides, low molecular weight polyamides, amide compounds such as fatty acid amides, chlorinated polyethylene, halogenated polyolefins such as chlorinated polypropylene, unsaturated carboxylic acid-modified polyolefin, rubber materials and the like.

  When the thermoplastic resin is used as a coating or adhesive for a polyolefin resin, a polyolefin resin such as a polyethylene resin or a polypropylene resin is emulsified using the polymer emulsifier, and a polyolefin resin emulsion. It is preferable to obtain

  These are conventionally substances that are difficult to make into emulsions and have been used by being dissolved in an organic solvent, and have been highly effective as paints or adhesives for polyolefin resins. By using a molecular emulsifier, it is possible to remove the solvent, and it is possible to produce a coating material or adhesive for polyolefin resin with a small environmental load.

  As a method for producing an emulsion of a thermoplastic resin such as a polyolefin resin using the polymer emulsifier of the present invention, the molten thermoplastic resin such as a polyolefin resin contains the polymer emulsifier or a neutralized product thereof. And then uniformly stirring with a homomixer. The most preferred embodiment uses a multi-screw extruder having two or more screws in a casing, and continuously supplies a polyolefin resin from the hopper of the multi-screw extruder or a midway supply port, which is heated, melted and kneaded. In addition, an aqueous solution containing the above polymer emulsifier or a neutralized product thereof is supplied under pressure from at least one supply port provided in the compression zone, metering zone, and degassing zone of the multi-screw extruder, And a thermoplastic resin such as the above-described molten polyolefin resin can be kneaded with a screw to continuously produce an emulsion from a die.

  The amount of water used is preferably used so that the solid content concentration of the obtained emulsion is 20 to 65% by weight.

  The emulsion produced in this manner is dispersed in water with polyolefin resin particles having an average particle size of 5 μm or less and a particle size of 1 μm or less of 10 wt% or more, preferably 20 wt% or more. The viscosity at 25 ° C. is 10 to 10,000 mPa · s, preferably 50 to 5,000 mPa · s. A more preferable viscosity is 50 to 2,000 mPa · s.

  This emulsion can be used as a paint, a pressure-sensitive adhesive, an ink binder, an adhesive, or an emulsion modifier, depending on the type of thermoplastic resin such as polyolefin resin to be used.

  Hereinafter, the present invention will be described more specifically with reference to examples. First, the evaluation method and the raw materials used will be described.

<Evaluation method>
[Non-volatile content]
About 1 g of the polymer emulsifier sample obtained in each production example or various emulsion samples obtained in the examples and comparative examples are precisely weighed and dried in a hot air circulating dryer at 105 ° C. for 3 hours, and then released in a desiccator. Cooled and weighed. The nonvolatile content was calculated according to the following formula.
Nonvolatile content [%] = (weight of sample after drying / weight of sample before drying) × 100

[Measurement of weight average molecular weight (Mw) by GPC]
The sample was dried at room temperature for 24 hours, dried at room temperature under reduced pressure (using a vacuum dryer LHV-122 (manufactured by Tabai Espec Co., Ltd.)) for 5 hours or more, added chloroform and methanol, and then an esterifying agent (trimethylsilyldiazomethane). The hexane solution was stirred at room temperature until allowed to dissolve (48-72 hours). Then, it was made to dry at room temperature.
The dried sample was adjusted to 0.2% with tetrahydrofuran (THF) and used as a sample.
The sample was measured under the following conditions using Shimadzu Corporation GPC-6A.
・ Flow rate: 1 ml / min
Column: PL gel 10 μm mix B (manufactured by Polymer Laboratories)
Standard sample: monodispersed PS (manufactured by Polymer Laboratories)
Reference: Sumilizer BHT (manufactured by Sumitomo Chemical Co., Ltd.)
・ Detector: RI, UV

[viscosity]
Various emulsion samples obtained in Examples and Comparative Examples were taken in a 500 ml beaker, and using VISCOMETER TV-10M (manufactured by Toki Sangyo Co., Ltd., rotor No. 1), rotating at 30 rpm and liquid temperature of 25 ° C. Measured under conditions.

[PH]
Samples of polymer emulsifier samples obtained in each production example, or various emulsion samples obtained in Examples and Comparative Examples, using a glass electrode type hydrogen ion concentration meter HM-14P (manufactured by Toa Denpa Kogyo Co., Ltd.) Was measured after adjusting the liquid temperature to 25 ° C.

[Particle size]
Various emulsion samples obtained in Examples and Comparative Examples were measured with a laser diffraction particle size distribution analyzer SALD-2100 (manufactured by Shimadzu Corporation) under the following conditions.
-Refractive index 1.50-0.20i
・ Volume distribution (median diameter)

[Melting temperature (1/2 method temperature)]
The polymer emulsifier sample obtained in each production example was allowed to stand at room temperature for 24 hours, and then vacuum-dried at room temperature for 5 hours. About 1 g was weighed and used as a sample, and an elevated flow tester (Shimadzu Corporation ( Using a CFT-500), 1/2 method temperature was measured.
Specifically, an elevated flow tester shown in FIG. 1 was used. This consists of a vertically standing cylinder 2, a plunger (piston) that can move up and down in the cylinder 2, a die 4 disposed at the lower end of the cylinder 2, and a die presser 5 that fixes the die 4. The area A of the tip surface of the plunger 1 in the cylinder 2 is 1 cm ² , and the nozzle (discharge hole) provided in the die 4 has a diameter of 1 mm and a length of 1 mm.
First, the above-mentioned weighed sample 3 is placed in the cylinder 2 and the plunger 1 is inserted into the cylinder 2. Next, a load of 10 kgf is applied to the upper portion of the plunger 1 as a load P, and the apparatus is heated so that the temperature increase rate is 6.0 ° C./min.
Then, the temperature and the descending amount of the plunger 1 were measured, and the relationship between the two was graphed. The result is as shown in the plunger drop-temperature curve (flow tester outflow curve) in FIG. In FIG. 2, the temperature at the time when the sample 3 flows out from the nozzle of the die 4 is defined as an outflow start point (flow start temperature), and the height between the outflow start point and the highest point of the obtained S-shaped curve. When h is h, the temperature at h / 2 is the ½ method temperature.

[Film-forming properties]
Various emulsion samples obtained in Examples and Comparative Examples were applied to a corona-treated surface of an OPP film (Gunze Co., Ltd .: film thickness 50 μm) with a bar coater so as to have a film thickness of 10 μm. And dried.
The film transparency when dried at 80 ° C. for 5 minutes or 120 ° C. for 5 minutes was judged visually by the following criteria.
◎: Transparency, △ Some transparency, ×: No transparency

[Adhesion evaluation]
Various emulsion samples obtained in the examples and comparative examples were placed on a polypropylene plate (thickness 5 mm) so that the thickness of the dried film was 10 μm. 16 was applied. This was heat-dried in an 80 ° C. oven for 5 minutes to obtain a film.
Based on JIS-K5400 (cross-cut peeling tape method test), the obtained film was cut with a grid-like cut with a clearance of 5 mm, and then the cellophane tape (trade name, manufactured by Nichiban Co., Ltd.) ) Was pasted. Next, one to two minutes after applying the cellophane tape, one end of the tape was held and peeled off at a right angle, and the adhesion was evaluated according to the following criteria.
○: There was no peeling at a glance at the intersection of the cuts and the square.
Δ: The area of peeling was less than 65% of the square area.
X: The area of peeling was 65% or more of the square area.

[Mechanical emulsion stability test]
100 g of various emulsion samples obtained in Examples and Comparative Examples were placed in a 250 ml plastic bottle, 30 g of isopropanol was added, and the mixture was stirred for 10 minutes with a magnetic stirrer having a stirrer size of 2.5 cm.
After that, the sample is left in a thermostatic bath at 25 ° C. for 3 hours, the sample temperature is set to 25 ° C., and the generator of the homogenizer (manufactured by Nissin Medical Science Instrument Co., Ltd.) is immersed in the sample solution, at a rotation speed of 2000 rpm. Processing was carried out for 10 minutes. The appearance of the sample after the treatment was observed, and the sample was placed on a glass plate on the order of 1 g and stretched with a glass rod to confirm the presence or absence of aggregates. The results were evaluated according to the following criteria.
◎… No change was observed ○… Viscosity increased slightly △… A small amount of agglomerates or viscosity increased ×… Agglomerates generated or became creamy

<Raw materials>
[(A) component]
Acrylic acid: manufactured by Mitsubishi Chemical Corporation, hereinafter abbreviated as “AA”.
Methacrylic acid: Mitsubishi Rayon Co., Ltd., hereinafter abbreviated as “MAA”.

[Component (B)]
N, N-dimethylaminoethyl methacrylate: Sanyo Chemical Industries, Ltd .: Methacrylate DMA, hereinafter abbreviated as “DMA”.

[Component (C)]
Methoxypolyethylene glycol methacrylate (9 ethylene oxide chains): manufactured by Kyoeisha Chemical Co., Ltd .: Light ester 130MA, hereinafter abbreviated as “130MA”.
Methoxypolyethylene glycol methacrylate (4 ethylene oxide chains): manufactured by Nippon Oil & Fats Co., Ltd .: Blemmer PME-200, hereinafter abbreviated as “PME200”.
Methoxypolyethylene glycol methacrylate (8 ethylene oxide chains): manufactured by Nippon Oil & Fats Co., Ltd .: Blemmer PME-350, hereinafter abbreviated as “PME350”.
Methoxypolyethylene glycol methacrylate (13 ethylene oxide chains): manufactured by Nippon Oil & Fats Co., Ltd .: Blemmer PME-550, hereinafter abbreviated as “PME550”.

[(D) component]
・ Methyl methacrylate: manufactured by Mitsubishi Rayon Co., Ltd., hereinafter abbreviated as “MMA”.
Lauryl methacrylate: manufactured by Mitsubishi Rayon Co., Ltd., hereinafter abbreviated as “SLMA”.

[Nonionic polymer emulsifier]
Polyoxyethylene glycol polyoxypropylene block copolymer: Daiichi Kogyo Seiyaku Co., Ltd., U108, hereinafter abbreviated as “U108”.

[Thermoplastic resin]
・ Ethylene / vinyl acetate copolymer ... Mitsui / DuPont Polychemical Co., Ltd., vinyl acetate content: 28 wt%, melting point: 74 ° C., MI at 190 ° C. (melt index, load: 2.16 kg): 150 g / 10 minutes, hereinafter abbreviated as “EVA”.
• Maleated polyethylene: ethylene / ethyl acrylate / maleic anhydride copolymer, manufactured by Sumitomo Chemical Co., Ltd .: Bondine HX8210, maleic anhydride content: 4 wt%, MI: 200 g / 10 min, hereinafter “MAH-PE” Abbreviated.
Polypropylene resin: manufactured by Mitsui Chemicals, Tuffmer XM-7070, hereinafter abbreviated as “XM7070”.

[Others]
Isopropanol: manufactured by Tokuyama Corporation, hereinafter abbreviated as “IPA”.

<Manufacture of polymer emulsifier>
(Production Example 1)
[Monomer adjustment]
IPA was added to a 50 L stainless steel bucket (addition amount was 5% by weight based on the total amount of monomers), and cooling was started in an ice bath while stirring. Subsequently, MMA and SLMA in amounts shown in Table 1 were added. Further, a mixture of AA, MAA, and 130MA in the amounts shown in Table 1 was added. Further, the amount of DMA listed in Table 1 was gradually added dropwise so that the temperature did not exceed 25 ° C. to prepare a monomer mixture.

<Polymerization reaction>
A 100 L reactor equipped with a cooling pipe, a nitrogen introduction pipe, a stirrer, a dropping funnel and a heating jacket was charged with 30 kg of IPA and 20 kg of ion-exchanged water, and the internal temperature was adjusted to 80 ° C. while stirring. After the reaction vessel was purged with nitrogen, 4 kg of the monomer mixed solution was charged all at once. Furthermore, 0.4 kg of 2,2′-azobisisobutyronitrile (manufactured by Otsuka Chemical Co., Ltd., hereinafter abbreviated as “AIBN”) was added to initiate polymerization. Furthermore, the remaining monomer mixed solution 16Kg was dropped over 4 hours to carry out polymerization. While continuing the dropwise addition of the monomer mixture for 4 hours, 0.12 kg of the polymerization initiator was added 4 times every 1 hour. After completion of dropping under the monomer mixture, aging was performed for 2 hours.
The internal temperature rose from 80 to 83 ° C., and replaced by adding water while distilling off the IPA, corresponding to the neutralization degree described in Table 1 of 25% ammonia water (total amount of AA, MAA, 130MA) After neutralization, a viscous acrylic copolymer neutralized aqueous solution was finally obtained. (Yield 97%).
Hereinafter, the obtained polymer emulsifier is referred to as “polymer emulsifier 1”.

(Production Examples 2-9)
Polymer emulsifiers 2 to 9 were obtained in the same manner as in Production Example 1 except that the monomers listed in Table 1 were used. When using U108, the amount of U108 shown in Table 1 was added after the monomer mixed solution was added.

(Example 1)
[Production of emulsion by kneader]
110 g of EVA is melted at 100 ° C. in a bi-axial kneader with different rotation and non-meshing type (Irie Shokai Co., Ltd .: PBV-03 type). The mixture was mixed for 10 minutes and evaluated using the resulting milky white emulsion. The results are shown in Table 2.

(Examples 2-8, Comparative Example 1)
Instead of the polymer emulsifier 1, the same operation as in Example 1 was carried out except that the polymer emulsifiers 2 to 9 were used to obtain respective milky white emulsions. Evaluation was performed using the obtained emulsion. The results are shown in Table 2.

Example 9
[Emulsion production by screw extruder (TEX-30)]
EVA 83 g / min was continuously supplied from a hopper of a co-rotating meshing twin screw extruder (manufactured by Nippon Steel Works: TEX-30, double thread deep groove type, L / D = 32).
Moreover, from the supply port provided in the vent part of the extruder, while continuously supplying with a polymer emulsifier 3 of 18 g / min, while continuously supplying 101 g / min of warm water with a plunger pump to the same place, Extrusion was continuously carried out at a heating temperature (cylinder temperature, the same applies hereinafter) of 110 to 130 ° C. (screw rotation speed: 300 rpm) to obtain a milky white emulsion. Evaluation was performed using the obtained emulsion. The results are shown in Table 3.

(Examples 10 to 17)
As the polymer emulsifier, polymer emulsifiers 3, 6, and 7 were used, and the same operation as in Example 9 was carried out except that the resin was changed to MAH-PE and XM7070 to obtain respective milky white emulsions. Evaluation was performed using the obtained emulsion. The results are shown in Table 3.

Schematic showing an example of a flow tester used to measure 1/2 method temperature Plunger drop-temperature curve

Explanation of symbols

1 Plunger 2 Cylinder 3 Sample 4 Die 5 Die presser

Claims (10)

Containing 5 to 40 mol% of a structural unit derived from an anionic monomer having a (meth) acryloyl group and a hydrophilic group (component (A)) as a copolymer component, and mainly comprising alkylaminoalkyl (meth) acrylate 5 to 30 mol% of a structural unit derived from a cationic monomer (component (B)) as a component and a nonionic monomer ((C (1) A polymer emulsifier containing 1 to 20 mol% of a structural unit derived from component) as a copolymerization component, and having a 1/2 method temperature of 40 to 140 ° C. by a flow tester of the copolymer.
_{R 1 - (C n H 2n} O) m -R 2 ... (1)
(In the formula, R ₁ represents a group selected from a (meth) acryloyloxy group and a (meth) acryloyloxyethoxy group; R ₂ represents H or an alkyl group having 1 to 4 carbon atoms; 3 represents an integer, and m represents an integer of 4 to 25.)   The polymeric emulsifier according to claim 1 or 2, wherein the hydrophilic group of the component (A) is at least one selected from a carboxyl group, a sulfonic acid group, a phosphoric acid group, and an acidic phosphoric acid ester group.   The component (D) comprising a (meth) acrylic acid ester of an aliphatic alcohol having 1 to 22 carbon atoms is used as a copolymer component other than the component (A), the component (B) and the component (C). 2. The polymer emulsifier according to 2.   The composition ratio of each component of the above (A), (B), (C), (D) is a molar ratio, and (A) / (B) / (C) / (D) = 5-30 / 5 The polymer emulsifier according to claim 3, which is -30/1 to 20/20 to 70 (provided that the total amount is 100).   5. The polymer emulsifier according to claim 1, wherein the ratio of the component (A) to the component (B) is (A) / (B) = 1.0 to 2.0 in terms of molar ratio. .   The polymeric emulsifier according to any one of claims 1 to 5, wherein at least a part of the acidic hydrophilic group contained in the component (A) is neutralized with a basic substance.   The polymer emulsifier according to any one of claims 1 to 6, which is obtained by polymerization in the presence of a nonionic polymer emulsifier.   The polymer emulsifier according to claim 7, wherein the nonionic polymer emulsifier is a polyoxyalkylene ether polymer emulsifier.   A polyolefin resin emulsion obtained by emulsifying a polyolefin resin using the polymer emulsifier according to claim 1.   The polyolefin resin emulsion of Claim 9 used for the binder or adhesive agent for coating materials.

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