JP5281277B2 - Surfactant composition for emulsion polymerization - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a surfactant composition for emulsion polymerization, which gives a polymer emulsion having good polymerization stability and mechanical stability and small particle diameters, and to provide a coating material having favorable gloss of a coating film. <P>SOLUTION: The surfactant composition for emulsion polymerization contains a specified polyoxyalkylene polycyclic phenylether monosulfate ester salt compound having a CMC (critical micelle concentration) of 1&times;10<SP>-5</SP>to 0.007 molL<SP>-1</SP>and a compound having a CMC of 0.007 to 0.2 molL<SP>-1</SP>(for example, a specified polyoxyethyleneoctylether sulfate ester salt or the like, a specified decylphenylether disulfonate sodium salt or the like, and a specified polyoxyethylene 1,10-decanediol disulfate sodium salt or the like) in specified proportions. A method for preparing the polymer emulsion using the surfactant composition, and a coating material containing the polymer emulsion obtained by the above method are also provided. <P>COPYRIGHT: (C)2009,JPO&amp;INPIT

Description

  The present invention relates to a surfactant composition for emulsion polymerization, a method for producing a polymer emulsion, and a polymer emulsion obtained by this production method, which give a polymer emulsion having good polymerization stability and mechanical stability and a small particle size. It is related with the coating material to contain.

  Polymer emulsions obtained by emulsion polymerization of vinyl monomers such as vinyl acetate and acrylic acid esters can be used as they are in the fields of paint, adhesives, adhesives, paper processing, fiber processing, etc. Widely used industrially. In the emulsion polymerization, as an emulsifier, an anionic surfactant such as a linear alkyl sulfate, a linear alkyl benzene sulfonate, a polyoxyethylene alkyl ether sulfate, a polyoxyethylene alkyl phenyl ether sulfate, and a polyoxy Nonionic surfactants such as ethylene linear alkyl ether and polyoxyethylene alkylphenyl ether are used alone or in a mixed system of anionic and nonionic surfactants.

  Emulsifiers in emulsion polymerization not only affect the initiation and growth reactions of polymerization, but also the stability of the polymer emulsion during polymerization (polymerization stability), and the mechanical and chemical stability of the resulting polymer emulsion. It has a great influence on freezing stability and storage stability. Conventionally, as anionic surfactants, those having a low critical micelle concentration (hereinafter referred to as CMC) effective in a small amount have been used. For example, Patent Document 1 describes a method of emulsion polymerization of a vinyl monomer in the presence of polyoxyalkylene styrenated and / or benzylated phenyl ether sulfate ester salts. However, the polymerization stability and mechanical stability have not been fully satisfactory.

On the other hand, an activator having a high CMC was not suitable as a surfactant for emulsion polymerization. The performance required for these surfactants for emulsion polymerization is good polymerization stability, mechanical stability and chemical stability of the resulting polymer emulsion, small emulsion particle size, low viscosity, and even the environment. In order to satisfy these performances, Patent Document 2 discloses a surfactant composition for emulsion polymerization comprising two types of polyoxyalkylene alkyl ether sulfates having different CMCs. Has been. However, the polymerization stability, the mechanical stability of the resulting polymer emulsion, and the coating film gloss of the resulting coating are still not fully satisfactory.
JP 56-161403 A Japanese Patent No. 3025763

  An object of the present invention is a surfactant composition for emulsion polymerization that is sufficiently satisfactory in polymerization stability and mechanical stability of a polymer emulsion, and further has a small particle size of the polymer emulsion and good coating film gloss of the resulting coating. And a method for producing a polymer emulsion, and a paint.

This invention contains the following (a) component and (b) component, and the molar ratio of (a) component and (b) component is (a) / (b) = 95 / 5-50 / 50 There are provided a surfactant composition for polymerization, a method for producing a polymer emulsion in which a monomer is emulsion-polymerized in the presence of the surfactant composition, and a paint containing the polymer emulsion obtained by this production method.
(A): wherein is represented by (I), CMC is 1 × 10 ^-5 molL ^-1 or more 0.007MolL ^-1 or less of a polyoxyalkylene polycyclic phenyl ether mono sulfate

A ¹ O is an oxyalkylene group having 2 to 4 carbon atoms, n is a number from 1 to 100 indicating the average number of added moles of the oxyalkylene group, and the n A ¹ Os may be the same or different. m represents an integer of 1 to 5, and M ¹ represents a monovalent cation. )
(B): is represented by any of formulas (II) ~ (IV), CMC is 0.007MolL ^-1 or more 0.2MolL ^-1 The following compounds

(In the above formulas (II) to (IV), R ² is a monovalent aliphatic hydrocarbon group, R ³ is a monovalent aliphatic hydrocarbon group, R ⁴ is a divalent aliphatic hydrocarbon group and one group. At least one group selected from divalent aliphatic hydrocarbon groups into which oxygen atoms are inserted, A ² O, A ³ O and A ⁴ O are each independently an oxyalkylene group having 2 to 4 carbon atoms, p, q and r are each independently a number of 1 to 100 indicating the average number of moles added of the oxyalkylene group, and p A ² O, q A ³ O and r A ⁴ O are the same or different. M ² , M ³ and M ⁴ each independently represents a monovalent cation.)

  According to the present invention, it is possible to obtain a polymer emulsion having a good polymerization stability and mechanical stability, a small particle size, and a coating film having a good coating gloss.

(A) component of the present invention, the is represented by formula (I), the view of obtaining a polymer emulsion having a small particle size, CMC is 1 × 10 ^-5 molL ^-1 or more 0.007MolL ^-1 or less, preferably 0 .0001~0.006mmolL ^-1, more preferably a compound in the range of 0.001~0.005mmolL ^-1, may be used alone or in combination thereof.
In the present invention, CMC is a value measured by an electric conductivity measurement method at 25 ° C. Specifically, it can be determined by the method described in the examples.

In the formula (I), A ¹ O represents an oxyalkylene group having 2 to 4 carbon atoms, preferably an oxyethylene group or an oxypropylene group. n is the average number of moles added of the oxyalkylene group and represents a number of 1 to 100 from the viewpoint of chemical stability of the polymer emulsion, preferably a number of 3 to 50, more preferably a number of 5 to 40, A number of ˜30 is more preferred. The n A ¹ Os may be the same or different, but if they are different, any of random addition, block addition, or a combination thereof may be used. Of the n A ¹ Os, n / 2 or more are preferably oxyethylene groups, and more preferably all are oxyethylene groups. Although m shows the integer of 1-5, the integer of 1-3 is preferable and 1 or 2 is preferable. M ¹ represents a monovalent cation, preferably a cation selected from an alkali metal such as sodium or potassium; ammonium; an amine such as alkanolamine, more preferably an alkali metal or ammonium, and even more preferably ammonium.

  The compound represented by the formula (I) can be produced by a known method. For example, styrene or benzyl chloride is added to phenol by a Friedel-Crafts reaction using aluminum chloride, zinc chloride or activated clay as a catalyst. Further, an alkylene oxide having 2 to 4 carbon atoms is added to the hydroxyl group of the addition product in the presence of a non-catalyst, a base catalyst, or an acid catalyst at normal pressure or under pressure in one step or in multiple steps to obtain amidosulfuric acid, etc. It can be produced by sulfate formation with a sulfating agent, and neutralization with a basic substance if necessary. As the sulfating agent, amidosulfuric acid is preferable from the viewpoint of preventing the benzene ring from being sulfonated.

  Examples of the polyoxyalkylene polycyclic phenyl ether monosulfate represented by the formula (I) include polyoxyalkylene (alkylene having 2 to 4 carbon atoms) styrenated phenyl ether monosulfate, polyoxyalkylene (carbon of alkylene). Number 2-4) Distyrenated phenyl ether monosulfate, polyoxyalkylene (alkylene having 2 to 4 carbon atoms) Tristyrenated phenyl ether monosulfate, polyoxyalkylene (alkylene having 2 to 4 carbon atoms) benzylation Phenyl ether monosulfate, polyoxyalkylene (alkylene having 2 to 4 carbon atoms) dibenzylated phenyl ether monosulfate, polyoxyalkylene (alkylene having 2 to 4 carbon atoms) tribenzylated phenyl ether monosulfate, etc. All It is. Of these, polyoxyalkylene (alkylene having 2 to 4 carbon atoms) distyrenated phenyl ether monosulfate and polyoxyalkylene (alkylene having 2 to 4 carbon atoms) tribenzylated phenyl ether monosulfate are preferable.

(B) component of the present invention are represented by any one of formulas (II) ~ (IV), from the viewpoint of polymerization stability of the polymer emulsion, CMC is 0.007MolL ^-1 or more 0.2MolL ^-1 or less, preferably the 0.008~0.1molL ^-1, more preferably a compound in the range of 0.01~0.06molL ^-1, may be used alone or in admixture.

In formulas (II) to (IV), R ² represents a monovalent aliphatic hydrocarbon group, preferably a linear or branched alkyl group having 6 to 11 carbon atoms, and more preferably 6 to 8 carbon atoms. R ³ represents a monovalent aliphatic hydrocarbon group, preferably a linear or branched alkyl group having 8 to 20 carbon atoms and more preferably 10 to 18 carbon atoms. R ⁴ represents at least one group selected from a divalent aliphatic hydrocarbon group and a divalent aliphatic hydrocarbon group into which one oxygen atom is inserted, and is an aliphatic group having 10 to 18 carbon atoms. A residue obtained by removing two hydroxyl groups from a dihydric alcohol and a residue obtained by removing two hydroxyl groups from a glyceryl monoalkyl ether having 11 to 21 carbon atoms are preferred. A ² O, A ³ O, and A ⁴ O each independently represents an oxyalkylene group having 2 to 4 carbon atoms, and is preferably an oxyethylene group or an oxypropylene group. p shows the number of 1-100 which shows the average addition mole number of an oxyalkylene group, However, the number of 3-50 is preferable from a chemical stability viewpoint of a polymer emulsion, and the number of 5-40 is more preferable, 8 A number of ˜30 is more preferred. q and r each independently represent a number of 1 to 100 indicating the average number of moles of oxyalkylene group added, and from the viewpoint of the chemical stability of the polymer emulsion, a number of 3 to 50 is preferred. p A ² O, q A ³ O, and r A ⁴ O may be the same or different, but in the case of different, any of random addition, block addition, or a combination thereof may be used. p / 2 or more of p A ² O, q / 2 or more of q A ³ O, and r / 2 or more of r A ⁴ O each represents an oxyethylene group. More preferably, all are oxyethylene groups. M ² , M ³ and M ⁴ each independently represent a monovalent cation, but a cation selected from alkali metals such as sodium and potassium; ammonium; amines such as alkanolamines is preferred.

The compound represented by the formula (II) is, for example, sulfated with a sulfonating agent such as sulfuric acid, chlorosulfonic acid or SO ₃ gas after adding alkylene oxide such as ethylene oxide or propylene oxide to an aliphatic monohydric alcohol. It can be produced by neutralization with NaOH or the like.

  As the compound represented by the formula (II), polyoxyethylene octyl ether sulfate, polyoxyethylene nonyl ether sulfate, polyoxypropylene polyoxyethylene undecyl ether sulfate, and the like are preferable.

  The compound represented by the formula (III) is produced, for example, by disulfonating an alkylated diphenyl ether having 8 to 20 carbon atoms of an alkyl group with sulfuric acid, chlorosulfonic acid or sulfuric anhydride, and then neutralizing with NaOH or the like. be able to.

  As the compound represented by the formula (III), decyl diphenyl ether disulfonic acid sodium salt, dodecyl diphenyl ether disulfonic acid sodium salt, tetradecyl diphenyl ether disulfonic acid sodium salt, and the like are preferable, and dodecyl diphenyl ether disulfonic acid sodium salt is more preferable.

The compound represented by the formula (IV) is, for example, an aliphatic dihydric alcohol or monoalkyl glyceryl ether added with an alkylene oxide such as ethylene oxide or propylene oxide, and then a sulfone such as sulfuric acid, chlorosulfonic acid or SO ₃ gas. It can be produced by sulfating with an agent and neutralizing with NaOH or the like.

  Examples of the compound represented by the formula (IV) include polyoxyethylene 1,10-decanediol disulfate sodium salt, polyoxyethylene 1,12-dodecanediol disulfate sodium salt, polyoxyethylene 1,2-dodecanediol disulfate Sodium sulfate, polyoxyethylene dodecyl glyceryl ether disulfate sodium salt, polyoxyethylene octadecyl glyceryl ether disulfate sodium salt, etc. are preferred, polyoxyethylene 1,10-decanediol disulfate sodium salt, polyoxyethylene dodecyl glyceryl ether disulfate Sodium sulfate is more preferable.

  Among the compounds represented by the formulas (II) to (IV) which are the component (b) of the present invention, the compound represented by the formula (III) is preferable.

  The blending ratio (a) / (b) (molar ratio) of the component (a) and the component (b) in the surfactant composition of the present invention is a polymer emulsion having a low viscosity and sufficient mechanical stability. From the viewpoint of obtaining, it is 95/5 or less, and preferably 90/10 or less. Further, from the viewpoint of obtaining a polymer emulsion having a small particle size and sufficient polymerization stability and mechanical stability, it is 50/50 or more, and preferably 70/30 or more. Therefore, from the above viewpoint, (a) / (b) (molar ratio) is 95/5 to 50/50, preferably 90/10 to 50/50, and more preferably 90/10 to 70/30.

  The content of the component (a) in the surfactant composition of the present invention is preferably 45 to 97% by weight, more preferably 60 to 90% by weight from the viewpoint of polymerization stability of the polymer emulsion and a small particle size. . In addition, the content of the component (b) is preferably 3 to 55% by weight, more preferably 10 to 40% by weight, from the viewpoint of polymerization stability of the polymer emulsion and a small particle size.

  The surfactant composition of the present invention can contain an anionic surfactant other than the components (a) and (b) of the present invention, a nonionic surfactant, and the like.

The present invention is characterized by using a surfactant composition for emulsion polymerization containing the component (a) and the component (b) at a specific ratio. By using this composition, the polymerization stability and mechanical properties are improved. It is possible to obtain a polymer emulsion having a good mechanical stability and a small particle size, and a paint having a good coating gloss.
The reason why the effect of obtaining a paint with particularly good coating film gloss is not clear, but as a result of improving the dispersibility of the pigment by the composition of the present invention, a paint with good film gloss is obtained. it is conceivable that.
The method for producing the polymer emulsion of the present invention is a method in which a monomer is emulsion-polymerized in the presence of the surfactant composition of the present invention, and the monomer used in the present invention is preferably a vinyl monomer.

  Specific examples of the monomer used in the present invention include aromatic vinyl monomers such as styrene, α-methylstyrene, and chlorostyrene; acrylic acid esters such as methyl acrylate, ethyl acrylate, and butyl acrylate; Methacrylic acid esters such as ethyl methacrylate; Vinyl monomers having a carboxyl group such as acrylic acid and methacrylic acid; Vinyl halides and vinylidene halides such as vinyl chloride, vinyl bromide and vinylidene chloride; Vinyl acetate and vinyl propionate Vinyl esters such as nitriles; nitriles such as acrylonitrile and methacrylonitrile; and conjugated dienes such as butadiene and isoprene. These monomers may be polymerized alone or in combination of two or more. Among these, the monomer is preferably at least one selected from the group consisting of aromatic vinyl monomers, acrylic acid esters, methacrylic acid esters, and vinyl monomers having a carboxyl group.

  In the production method of the present invention, the surfactant composition of the present invention is preferably used in an amount of 0.1 to 20 parts by weight, more preferably 0.5 to 5 parts by weight, with respect to 100 parts by weight of the monomer.

  As the polymerization initiator used in the method for producing the polymer emulsion of the present invention, any polymerization initiator can be used as long as it is used in ordinary emulsion polymerization. Persulfates such as potassium persulfate and ammonium persulfate, and t-butyl hydrogen peroxide Organic peroxides such as hydroperoxide, benzoyl peroxide, cumene hydroperoxide, and azo initiators such as azobisdiisobutyronitrile and 2,2-azobis (2-amidinopropane) dihydrochloride are exemplified. Persulfates are preferred. Furthermore, redox initiators in which a reducing agent such as sodium sulfite, Rongalite, ascorbic acid or the like is combined with peroxide can also be used.

  In the method for producing a polymer emulsion of the present invention, the emulsion polymerization conditions are not particularly limited, and the amount of monomer is preferably 20 to 70% by weight, more preferably 40 to 60% by weight, based on the total system. As the monomer addition method, any of a monomer dropping method, a monomer batch charging method, a pre-emulsion method, and the like can be used, but the pre-emulsion method is preferred from the viewpoint of polymerization stability.

  In the pre-emulsion method, the pre-emulsion dropping time is preferably 1 to 8 hours, and the aging time is preferably 1 to 5 hours. The polymerization temperature is adjusted by the decomposition temperature of the initiator, but is preferably 50 to 90 ° C, and particularly preferably 70 to 85 ° C in the case of persulfate.

  The paint of the present invention contains the polymer emulsion obtained by the production method of the present invention as described above. The average particle size of the polymer emulsion is preferably from 30 to 500 nm, more preferably from 80 to 300 nm, from the viewpoint of use as a paint. Here, the average particle diameter of the polymer emulsion is a value measured by the method shown in the Examples below.

  The solid content of the polymer emulsion according to the present invention is preferably 20 to 70% by weight, more preferably 30 to 60% by weight.

  The paint of the present invention can further contain a pigment, and if necessary, water, a viscosity control agent, an antifoaming agent, an antioxidant, an ultraviolet absorber and the like. Examples of pigments include extender pigments such as talc, kaolin, calcium carbonate, and barium sulfate, colored pigments such as bengara, carbon black, ultramarine, and yellow iron oxide, white pigments such as titanium dioxide and zinc oxide, titanium mica, and bismuth oxychloride. Inorganic pigments such as pearl pigments, dyes as organic synthetic dyes, organic pigments, and the like. These pigments may be used alone or in combination of two or more.

  The content of the polymer emulsion in the paint of the present invention is preferably 5 to 90% by weight, more preferably 10 to 85% by weight, and still more preferably 15 to 80% by weight in terms of solid content with respect to the solid content in the paint. It is. The content of the pigment in the paint of the present invention is preferably 5 to 95% by weight with respect to the solid content in the paint.

  The pigment is preferably blended with the polymer emulsion in the form of an aqueous dispersion, and the aqueous pigment dispersion can be prepared by a known method. For example, it can be obtained by dispersing a pigment alone or a mixture, water and, if necessary, a dispersion aid using a dispersing device. A homomixer, a sand mill, a ball mill, a roll mill, a paint shaker or the like can be used as a dispersing device. Moreover, you may add an antifoamer, a preservative, etc. as needed.

  In the examples, “%” is by weight unless otherwise specified. In the following examples, CMC was measured by the following method.

<Measurement method of CMC>
100 mL of distilled water was placed in a beaker and the electric conductivity was measured while stirring (the electric conductivity meter was CM-20S, Toa Denpa Kogyo Co., Ltd., cell CG-511B). 0.2 mL of a surfactant solution adjusted to a predetermined concentration in advance was dropped into a beaker, and the electric conductivity was read each time the solution was dropped. When the surfactant concentration of the titrant is x molL ⁻¹ and the amount of titrated titrant is y mL, the surfactant concentration C in the solution in the beaker is C = x · y / (100 + y). The inflection point when the electric conductivity is plotted against C is CMC (temperature 25 ° C.).

Examples 1-10, Comparative Examples 1-5
The following components (a), (b) and comparative components were used and blended in the proportions shown in Table 1 to prepare the surfactant compositions of the present invention and comparison. Using the obtained surfactant composition, emulsion polymerization was performed by the following method to obtain a polymer emulsion. The performance of the obtained polymer emulsion was evaluated by the following method. Moreover, the coating material was created with the following method using the obtained polymer emulsion, and gloss was measured by the following method. These results are shown in Table 1.

<(A) component>
(A-1): Polyoxyethylene (20) distyrenated phenyl ether monosulfate ammonium salt (CMC = 0.0034 mol L ⁻¹ )
(A-2): Polyoxyethylene (13) distyrenated phenyl ether monosulfate ammonium salt (CMC = 0.527 mol L ⁻¹ )
(A-3): polyoxypropylene (3) polyoxyethylene (10) distyrenated phenyl ether monosulfate ammonium salt (CMC = 0.024 mol L ⁻¹ )
(A-4): Polyoxyethylene (10) tribenzylated phenyl ether monosulfate ammonium salt (CMC = 0.002 mol L ⁻¹ )
<(B) component>
(B-1): polyoxyethylene (18) octyl ether sulfate sodium salt (CMC = 0.029 mol L ⁻¹ )
(B-2): Polyoxyethylene (12) isononyl ether sulfate sodium salt (CMC = 0.023 mol L ⁻¹ )
(B-3): Polyoxypropylene (5) Polyoxyethylene (12) Isoundecyl ether sulfate sodium salt (CMC = 0.012 mol L ⁻¹ )
(B-4): dodecyl diphenyl ether disulfonic acid sodium salt (CMC = 0.014 mol L ⁻¹ )
(B-5): Polyoxypropylene (3) Polyoxyethylene (12) 1,10-decandiol disulfate sodium salt (CMC = 0.035 mol L ⁻¹ )
(B-6): Polyoxyethylene (18) dodecyl glyceryl ether disulfate sodium salt (CMC = 0.031 mol L ⁻¹ )
<Comparison ingredients>
(C-1): Polyoxyethylene (4) nonylphenyl ether sulfate sodium salt (CMC = 0.0031 mol L ⁻¹ )
(C-2): Polyoxyethylene (18) dodecyl ether sulfate sodium salt (CMC = 0.0006 mol L ⁻¹ )
<Emulsion polymerization method>
In a 1 L flask equipped with a stirrer and a raw material inlet, 112.5 g of ion-exchanged water, 0.36 g of potassium persulfate as a polymerization initiator, and 3.6 g of the surfactant composition of the present invention or a comparative surfactant composition were added. While stirring at 500 r / min, a monomer mixture of 109.7 g of butyl acrylate, 109.7 g of styrene and 5.6 g of acrylic acid was added dropwise over about 5 minutes, and stirred for 30 minutes to give an emulsion dropping solution. Obtained.

  Next, in a 1 L separable flask equipped with a stirrer, a reflux condenser, and a raw material inlet, 162.5 g of ion-exchanged water, 0.09 g of potassium persulfate as a polymerization initiator, the surfactant composition of the present invention or the comparative composition A surfactant composition (0.90 g) and a 5% amount (17.1 g) of the above emulsion drop solution were charged, the temperature was raised to 80 ° C., and the first stage polymerization was performed for 30 minutes. Thereafter, the remaining emulsion dropping solution was added dropwise over 3 hours, and after completion of the addition, it was further aged for 1 hour. The obtained polymer emulsion was cooled to 30 ° C. or lower and filtered through a 200 mesh stainless steel wire mesh to collect aggregates in the emulsion. Aggregates adhered to the flask and the stirring blade were also collected.

<Performance evaluation method>
(1) Polymerization stability during emulsion polymerization The recovered aggregate was washed with water, dried and weighed at 26.6 kPa and 105 ° C. for 2 hours to determine the amount of aggregate. Polymerization stability was expressed in terms of the weight percent of aggregates relative to the total amount of monomers used.
In addition, it shows that it is excellent in polymerization stability, so that this value is small.
(2) Average particle diameter of polymer emulsion particles The obtained polymer emulsion was neutralized with 25% aqueous ammonia to a pH of 8-9. The average particle size of the neutralized polymer emulsion particles was measured using a dynamic light scattering particle size measuring device N4 Plus manufactured by Beckman Coulter.
In addition, it shows that it is so excellent that the average particle diameter of a polymer emulsion particle is small.
(3) Mechanical stability of polymer emulsion 50 g of the neutralized polymer emulsion was rotated with a Maron mechanical stability tester for 5 minutes under the conditions of 98 N and 1000 r / min, and the resulting aggregate was 200 mesh. After filtration with a stainless steel wire mesh, the filtration residue was washed with water, dried and weighed at 26.6 kPa and 105 ° C. for 2 hours, and the amount of agglomerates relative to the polymer was expressed in wt%.
In addition, it shows that it is excellent in mechanical stability, so that this value is small.

<How to make paint>
A 250 mL plastic container is charged with 50 g of 1 mm diameter and 2 mm diameter glass beads, 150 g of titanium dioxide, 3.75 g of Poise 530 (40% product, manufactured by Kao Corporation), and 62 g of ion-exchanged water, and stirred for 3 hours with a paint shaker. A pigment aqueous dispersion having a pigment solid content of 70% was prepared.
Next, 7.1 g of the pigment aqueous dispersion, 11.1 g of each polymer emulsion, and 1.8 g of ion-exchanged water were weighed and uniformly mixed in the flask to obtain a paint having a finished paint solid content of 50% (PWC 50%). . PWC is a value calculated by the following equation.

PWC = pigment solid content / (pigment solid content + polymer emulsion solid content) × 100
<Measuring method of gloss>
The above coating was applied to bar coater no. 8 was coated on a polypropylene film, and after coating, it was dried overnight at room temperature to obtain a coating film for evaluation. The surface gloss of this coating film was measured with a gloss meter (GM-60, manufactured by Minolta) under the condition of an incident angle of 60 °.

Examples 11-20, Comparative Examples 6-10
Except for using the surfactant composition of the present invention shown in Table 2 and the comparative surfactant composition, and using 110.8 g of butyl acrylate, 110.8 g of methyl methacrylate, and 3.4 g of acrylic acid as monomers, Emulsion polymerization was performed under the same conditions as in Examples 1 to 10 and Comparative Examples 1 to 5 to obtain a polymer emulsion, and the performance was similarly evaluated. The results are shown in Table 2.

  Also, pigment aqueous dispersions were prepared in the same manner as in Examples 1 to 10 and Comparative Examples 1 to 5, and 4.76 g of pigment aqueous dispersion, 11.1 g of each polymer emulsion, and 0.8 g of ion-exchanged water were weighed in a flask. And uniformly mixed to obtain a paint having a finished paint solid content of 50% (PWC 40%). This paint was applied onto a polypropylene film in the same manner as in Examples 1 to 10 and Comparative Examples 1 to 5, and the surface gloss of the coating film was measured. The results are shown in Table 2.

Claims (7)

The surfactant for emulsion polymerization containing the following components (a) and (b), wherein the molar ratio of the components (a) and (b) is (a) / (b) = 95 / 5-50 / 50 Agent composition.
(A): is represented by the formula (I), the critical micelle concentration (CMC) is 1 × 10 ^-5 molL ^-1 or more 0.007MolL ^-1 or less of a polyoxyalkylene polycyclic phenyl ether mono sulfate

A ¹ O is an oxyalkylene group having 2 to 4 carbon atoms, n is a number from 1 to 100 indicating the average number of added moles of the oxyalkylene group, and the n A ¹ Os may be the same or different. m represents an integer of 1 to 5, and M ¹ represents a monovalent cation. )
(B): is represented by any of formulas (II) ~ (IV), CMC is 0.007MolL ^-1 or more 0.2MolL ^-1 The following compounds

(In the above formulas (II) to (IV), R ² is a monovalent aliphatic hydrocarbon group, R ³ is a monovalent aliphatic hydrocarbon group, R ⁴ is a divalent aliphatic hydrocarbon group and one group. At least one group selected from divalent aliphatic hydrocarbon groups into which oxygen atoms are inserted, A ² O, A ³ O and A ⁴ O are each independently an oxyalkylene group having 2 to 4 carbon atoms, p, q and r are each independently a number of 1 to 100 indicating the average number of moles added of the oxyalkylene group, and p A ² O, q A ³ O and r A ⁴ O are the same or different. M ² , M ³ and M ⁴ each independently represents a monovalent cation.) The surfactant composition for emulsion polymerization according to claim 1, wherein the molar ratio of the component (a) to the component (b) is (a) / (b) = 90 / 10-60 / 40. The surfactant composition for emulsion polymerization according to claim 1 or 2, wherein the molar ratio of the component (a) to the component (b) is (a) / (b) = 90/10 to 70/30. The surfactant composition for emulsion polymerization according to any one of claims 1 to 3, wherein the polyoxyalkylene polycyclic phenyl ether monosulfate ester represented by the formula (I) is sulfated using amidosulfuric acid. . The manufacturing method of a polymer emulsion which emulsion-polymerizes a monomer in presence of the surfactant composition in any one of Claims 1-4 . The method for producing a polymer emulsion according to claim 5 , wherein the monomer is at least one selected from the group consisting of an aromatic vinyl monomer, acrylic acid esters, methacrylic acid esters, and a vinyl monomer having a carboxyl group. The coating material containing the polymer emulsion obtained by the manufacturing method of Claim 5 or 6 .