JP5162734B2 - Reactive surfactant, resin composition and coating composition - Google Patents

Description

  The present invention relates to a reactive surfactant, a resin composition containing the same, and a coating composition.

  Antifouling paint additives that impart hydrophilicity to the coating film and can wash away dirt on the exterior of buildings due to rainfall include compounds obtained by polymerizing ethylene oxide or propylene oxide with glycerin or pentaerythritol (Patent Documents) 1) and a crosslinked polymer obtained by a reaction between an epoxy group-containing compound and a hydroxyl group-containing compound are known (Patent Document 2).

JP-A-11-279454 JP 2003-253197 A

The antifouling paint additive described in Patent Document 1 has a problem that the water resistance of the coating film is poor and the hydrophilicity (antifouling property) imparted to the coating film disappears in a short time. In addition, in the paint additive described in Patent Document 2, when it is attempted to impart sufficient hydrophilicity (antifouling property) to the coating film, the water resistance is significantly reduced. There is a problem that the property (antifouling property) is remarkably lowered, that is, it is difficult to balance hydrophilicity and water resistance.
An object of the present invention is to provide a coating film with sufficient hydrophilicity (antifouling property) without impairing the water resistance of the coating film, and excellent in hydrophilic retention ability (long-term antifouling property) over a long period of time. To provide a reactive surfactant.

The inventor of the present invention has reached the present invention as a result of intensive studies to solve the above problems.
That is, the reactive surfactant of the present invention is a reactive surfactant used as a monomer that constitutes a part of the vinyl resin used as a binder for coatings, and without affecting the water resistance of the coating film. A reactive surfactant that can form a coating film that imparts hydrophilicity to and has a hydrophilicity-holding ability, and comprises the polyoxyalkylene compound (Y) represented by the general formula (1) as an essential component Is the gist.

{R (-OA) n-} m Q (1)

  However, in the general formula (1), Q is a reaction residue obtained by removing a hydrogen atom from m primary hydroxyl groups of non-reducing di- or trisaccharides, OA is an oxyalkylene group having 2 to 4 carbon atoms, and R is A (meth) acryloyl group, a 3- (meth) acryloyloxy-2-hydroxypropyl group or a hydrogen atom is represented, and at least one R is a (meth) acryloyl group and / or 3- (meth) acryloyloxy-2-hydroxy. A propyl group, n is an integer of 1 to 30, m is an integer of 2 to 4, the total number of OA is an integer of 10 to 80, and R, OA, (OA) n, Q, n, and m are respectively It may be the same or different.

Further, the reactive surfactant of the present invention is a reactive surfactant used as a monomer constituting a part of a vinyl resin used as a binder for paint, and the coating film without impairing the water resistance of the coating film. A reactive surfactant capable of imparting hydrophilicity to the film and forming a coating film having hydrophilicity-retaining ability, a non-reducing di- or trisaccharide (a1), an alkylene oxide having 2 to 4 carbon atoms (a2) ) And (meth) acrylic acid (a3) and / or a polyoxyalkylene compound having structure (1) and / or a non-reducing di- or trisaccharide (a1), alkylene having 2 to 4 carbon atoms A polyoxyalkylene compound having a structure (2) produced by a chemical reaction of oxide (a2) and glycidyl (meth) acrylate (a4) is an essential component,
The gist is that the amount of the alkylene oxide (a2) used is 10 to 80 parts by mole relative to 1 part by mole of the non-reducing di- or trisaccharide (a1).

  The reactive surfactant of the present invention imparts sufficient hydrophilicity (antifouling property) to a coating film without impairing the water resistance of the coating film, and has a long-term hydrophilic retention ability (long-term antifouling property). An excellent coating film can be formed. That is, when the reactive surfactant of the present invention is used, a coating film remarkably excellent in water resistance, hydrophilicity and hydrophilicity retention ability can be easily obtained.

  In the general formula (1), the di- or trisaccharide that can constitute the reaction residue (Q) obtained by removing a hydrogen atom from m primary hydroxyl groups of a non-reducing di- or trisaccharide is sucrose (saccharose). ), Trehalose, isotrehalose, isosaccharose, gentianose, raffinose, meretitol, planteose and the like. Among these, sucrose, trehalose, gentianose, raffinose and planteose are preferable from the viewpoint of water resistance, hydrophilicity (antifouling property) and hydrophilicity retention ability (long-term antifouling property), more preferably sucrose and raffinose. And sucrose is particularly preferable from the viewpoint of supply ability and cost.

  Examples of the oxyalkylene group (OA) having 2 to 4 carbon atoms include oxyethylene, oxypropylene, oxybutylene, and a mixture thereof. Among these, oxyethylene is preferable from the viewpoint of hydrophilicity (antifouling property) and hydrophilicity retention ability (long-term antifouling property), and oxypropylene and oxybutylene are preferable and more preferable from the viewpoint of water resistance. Is a mixture of oxypropylene and oxypropylene and oxyethylene from the viewpoints of both hydrophilicity (antifouling property), hydrophilic retention ability (long-term antifouling property) and water resistance. Moreover, n OA may be the same or different. A plurality of (OA) n may be the same or different.

  When (OA) n contains a plurality of types of oxyalkylene groups, the bonding order (block, random and combinations thereof) and content of these oxyalkylene groups are not limited, but block or block It is preferable to include a combination with a random state. In this case, it is preferable to contain oxyethylene in order to further improve hydrophilicity (antifouling property). When oxyethylene is included, the content ratio (mol%) is preferably 2 to 20, more preferably 3 to 18, particularly preferably 4 to 17, and most preferably 5 based on the total number of moles of oxyalkylene groups. ~ 15.

  Further, when (OA) n contains an oxyethylene group and an oxypropylene group or / and oxybutylene group, the oxypropylene and / or oxybutylene may be located at the end away from the reaction residue (Q). preferable. That is, when (OA) n contains an oxyethylene group, it is preferable that the oxyethylene group can be directly bonded to the reaction residue (Q). In addition, when (OA) n includes a plurality of types of oxyalkylene groups, it preferably includes a block shape.

In the present invention, "(meth) acryl ..." means "acryl ..." and "methacryl ...".
Of the (meth) acryloyl group, 3- (meth) acryloyloxy-2-hydroxypropyl group and hydrogen atom, a 3- (meth) acryloyloxy-2-hydroxypropyl group and a hydrogen atom are preferred. In addition, from the viewpoint of hydrophilic retention ability (long-term antifouling property), the content of the (meth) acryloyl group and the 3- (meth) acryloyloxy-2-hydroxypropyl group is preferably 1 to 3, more preferably One or two, particularly preferably one. Within this range, the hydrophilic retention ability (long-term antifouling property) is further improved.

n is preferably an integer of 1 to 30, more preferably an integer of 2 to 27, particularly preferably an integer of 4 to 26, and most preferably an integer of 5 to 25. Within this range, the hydrophilicity, hydrophilicity retention ability and water resistance of the coating film are further improved.
m is an integer of 2 to 4, for example, 3 for sucrose, 2 for trehalose, and 4 for meletitose. Within this range, the hydrophilicity and hydrophilicity retention ability of the coating film are further improved.
n or m may all be the same, or some or all may be different.
The total number of OA is preferably an integer of 10 to 80, more preferably an integer of 13 to 70, particularly preferably an integer of 17 to 60, and most preferably an integer of 20 to 50. Within this range, the water resistance, hydrophilicity retention ability and hydrophilicity of the coating film are further improved.

Examples of the polyoxyalkylene compound represented by the general formula (1) include compounds represented by the following chemical formulas. P represents an oxypropylene group, E represents an oxyethylene group, B represents an oxybutylene group, Q ¹ represents a reaction residue obtained by removing three primary hydroxyl group hydrogen atoms from sucrose, and Q ² represents a primary hydroxyl group from trehalose. The reaction residue obtained by removing 2 hydrogen atoms, Q ³ represents the reaction residue obtained by removing 3 primary hydroxyl atoms from raffinose, H represents a hydrogen atom, C represents a carbon atom, and O represents an oxygen atom. .

  Of these, polyoxyalkylene compounds represented by the formula (3), (5), (6), (10) or (11) are preferable, and more preferably the formula (6), (10) or (11). It is a polyoxyalkylene compound represented by this.

  Examples of the polyoxyalkylene compound (Y) represented by the general formula (1) include non-reducing di- or trisaccharides (a1), C2-C4 alkylene oxides (a2), and (meth) acrylic acid (a3). ) And a non-reducing di- or trisaccharide (a1), a C2-C4 alkylene oxide (a2) and glycidyl (meta ) A polyoxyalkylene compound (2) having the structure (2) that can be produced by a chemical reaction of acrylate (a4) is included. A polyoxyalkylene compound having a structure that can be produced by these chemical reactions may have a distribution in the number of n and m. In this case, strictly speaking, it becomes a mixture of a plurality of types of polyoxyalkylene compounds. In this, the polyoxyalkylene compound represented by the general formula (1) is included. Even in this case, the manufacturing method is not limited.

About the following usage-amount, it is common also in any case of the polyoxyalkylene compound which has a structure (1) or (2).
As usage-amount (mol part) of alkylene oxide (a2), 10-80 are preferable with respect to 1 mol part of non-reducing di- or trisaccharide (a1), More preferably, it is 13-70, Most preferably, it is 17 ~ 60, most preferably 20-50. Within this range, the hydrophilicity, hydrophilicity retention ability and water resistance are further improved.

  As usage-amount (mol part) of (meth) acrylic acid (a3), 1-2 are preferable with respect to 1 mol part of non-reducing disaccharide or trisaccharide (a1), More preferably, it is 1-1.8. Particularly preferred is 1 to 1.5, and most preferred is 1 to 1.2. Within this range, the hydrophilicity retention ability is further improved.

  As a usage-amount (mol part) of a glycidyl (meth) acrylate (a4), 1-2 are preferable with respect to 1 mol part of non-reducing di- or trisaccharide (a1), More preferably, it is 1-1.8. Particularly preferred is 1 to 1.5, and most preferred is 1 to 1.2. Within this range, the hydrophilicity retention ability is further improved.

  As the non-reducing di- or trisaccharide (a1), the same disaccharide or trisaccharide that can constitute the reaction residue (Q) in the general formula (1) can be used, and the preferred range is also the same.

  As the alkylene oxide (a2), an alkylene oxide having 2 to 4 carbon atoms can be used, and examples thereof include ethylene oxide (EO), propylene oxide (PO), butylene oxide (BO), and mixtures thereof. Of these, ethylene oxide is preferable from the viewpoint of hydrophilicity (antifouling property) and hydrophilicity retention ability (long-term antifouling property), and propylene oxide and butylene oxide are preferable from the viewpoint of water resistance of the coating film, More preferred are propylene oxide and a mixture of propylene oxide and ethylene oxide from the viewpoints of both hydrophilicity (antifouling property), hydrophilic retention ability (long-term antifouling property) and water resistance.

Moreover, when using multiple types of alkylene oxides, the order of reaction (block, random and combinations thereof) and the usage rate are not limited, but it is preferable to include a block or a combination of block and random. . In this case, it is preferable to contain ethylene oxide in order to further improve hydrophilicity (antifouling property). When EO is contained, the use ratio (mol%) of EO is preferably 2 to 20, more preferably 3 to 18, particularly preferably 4 to 17, and most preferably 5 based on the total number of moles of alkylene oxide. ~ 15.
When EO and PO or / and BO are included, it is preferable to react PO and / or BO after reacting EO to the non-reducing disaccharide or trisaccharide (a1).

  The production method of the polyoxyalkylene compound (Y) represented by the general formula (1) is not limited. For example, <1> a non-reducing disaccharide or trisaccharide (a1) and an alkylene oxide having 2 to 4 carbon atoms ( a step of chemically reacting a2) to obtain a reaction product (a12), and a reaction of the reaction product (a12) and (meth) acrylic acid (a3) to form a polyoxyalkylene compound (1) having the structure (1) And <2> a step of chemically reacting the non-reducing di- or trisaccharide (a1) and the alkylene oxide (a2) having 2 to 4 carbon atoms to obtain a reaction product (a12), and A method including a step of obtaining a polyoxyalkylene compound (2) having the structure (2) by reacting the reaction product (a12) and glycidyl (meth) acrylate (a4) is included.

  For the chemical reaction (addition reaction) of the non-reducing disaccharide or trisaccharide (a1) and the alkylene oxide (a2), a known method (Japanese Patent Application Laid-Open No. 2004-224945) can be applied, and anionic polymerization, cationic polymerization, etc. Or you may implement by any forms, such as coordination anionic polymerization. These polymerization forms may be used alone or in combination according to the degree of polymerization.

For the addition reaction of alkylene oxide (a2), a known reaction catalyst (Japanese Patent Application Laid-Open No. 2004-224945) can be used. In addition, when using the amide demonstrated below as a reaction solvent, it is not necessary to use a reaction catalyst.
When a reaction catalyst is used, the amount used (% by weight) is preferably 0.01 to 1, more preferably based on the total weight of the non-reducing di- or trisaccharide (a1) and the alkylene oxide (a2). Is 0.03 to 0.8, particularly preferably 0.05 to 0.6. When it is within this range, the economy (required production time, catalyst cost, etc.), the purity of the product (monodispersity, etc.), etc. are further improved.

When a reaction catalyst is used, it is preferable to remove the reaction catalyst from the reaction product. As the removal method, an alkali adsorbent such as synthetic aluminosilicate {for example, trade name: Kyoward 700, manufactured by Kyowa Chemical Industry Co., Ltd. } (JP-A-53-123499, etc.), a method of dissolving in a solvent such as xylene or toluene and washing with water (JP-B-49-14359, etc.), a method using an ion exchange resin (JP-A-51 No. 23211, etc.) and a method of filtering a carbonate formed by neutralizing an alkaline catalyst with carbon dioxide (Japanese Patent Publication No. 52-33000).
As the end point of the removal of the reaction catalyst, the CPR (Controlled Polymerization Rate) value described in JIS K1557-1970 is preferably 20 or less, more preferably 10 or less, particularly preferably 5 or less, and most preferably 2 or less. is there.

A known reaction vessel (JP 2004-224945 A) or the like can be used for the reaction. As the reaction atmosphere, it is preferable that the inside of the reaction apparatus is evacuated or dried in an inert gas atmosphere (such as argon, nitrogen and carbon dioxide) before introducing the alkylene oxide (a2) into the reaction system. Moreover, as reaction temperature (degreeC), 80-150 are preferable, More preferably, it is 90-130. The reaction pressure (gauge pressure: MPa, hereinafter the same) is preferably 0.8 or less, more preferably 0.5 or less.
The end point of the reaction can be confirmed by the following method. That is, when the reaction temperature is kept constant for 15 minutes, the reaction end point is determined when the decrease in the reaction pressure becomes 0.001 MPa or less. The required reaction time is usually 4 to 12 hours.

  A reaction solvent can be used in the step of addition reaction of the non-reducing di- or trisaccharide (a1) and the alkylene oxide (a2). As the reaction solvent, those having no active hydrogen are preferred, and more preferred are those capable of dissolving the non-reducing di- or trisaccharide (a1), alkylene oxide (a2) and reaction product (a12).

As such a reaction solvent, alkyl amides having 3 to 8 carbon atoms and heterocyclic amides having 5 to 7 carbon atoms can be used.
Examples of the alkylamide include N, N-dimethylformamide (DMF), N, N-dimethylacetamide, N, N-diethylacetamide, N-methyl-N-propylacetamide, 2-dimethylaminoacetaldehyde dimethylacetal and the like.
Examples of the heterocyclic amide include N-methylpyrrolidone, N-methyl-ε-caprolactam, and N, N-dimethylpyrrolecarboxylic acid amide.

Of these, alkylamide and N-methylpyrrolidone are preferred, DMF, N, N-dimethylacetamide and N-methylpyrrolidone are more preferred, DMF and N-methylpyrrolidone are most preferred, and DMF is most preferred.
When a reaction solvent is used, the amount used (% by weight) is preferably 20 to 200, more preferably 40 to 180, based on the weight of the non-reducing di- or trisaccharide (a1) and the alkylene oxide (a2). Especially preferably, it is 60-150.

When a reaction solvent is used, it is preferable to remove the reaction solvent after the reaction. The residual amount (% by weight) of the reaction solvent is preferably 0.1 or less, more preferably 0.05 or less, particularly preferably 0.01 or less, based on the weight of the polyoxyalkylene compound (Y). is there. The residual amount of the reaction solvent can be determined by gas chromatography using an internal standard substance.
Examples of the method for removing the reaction solvent include the method described in JP-A-2005-132916.

  For the reaction of the reaction product (a12) and (meth) acrylic acid (a3), an ordinary esterification reaction can be applied. For example, the reaction can be performed in the presence of hydroquinone using a reaction catalyst. The reaction catalyst includes an acidic substance or a basic substance. Examples of acidic substances include mineral acids {such as sulfuric acid, hydrochloric acid, and phosphoric acid} and metal salts {such as cobalt naphthenate}. Basic materials include alkali metal or alkaline earth metal hydroxides {lithium hydroxide, sodium hydroxide, potassium hydroxide, rubidium hydroxide, cesium hydroxide, magnesium hydroxide, calcium hydroxide, barium hydroxide, etc. } Etc. are mentioned. Of these, metal salts and alkali metal hydroxides are preferable, and cobalt naphthenate and sodium hydroxide are more preferable.

  For the reaction of the reaction product (a12) and (meth) acrylic acid (a3), a container with heating, cooling, stirring and a reflux tube can be used. The reaction temperature (° C.) is preferably 60 to 200, more preferably 80 to 180. The reaction atmosphere is preferably a dry inert gas atmosphere. The end point of the reaction can be confirmed by the fact that water distilled into the reflux tube cannot be observed, or by measuring the acid value.

  The acid value (mgKOH / g) of the reaction product of the reaction product (a12) and (meth) acrylic acid (a3) is preferably 0.1 or less, more preferably 0.05 or less, particularly preferably 0.8. 01 or less. The acid value is measured according to JIS K0070-1992.

  When using a reaction catalyst, it is preferable to remove from the polyoxyalkylene compound (Y), and the removal method similar to the above can be applied as the removal method.

  For the reaction of the reaction product (a12) and glycidyl methacrylate (a4), an ordinary epoxy reaction can be applied. For example, the reaction can be performed in the presence of hydroquinone using a reaction catalyst. As the reaction catalyst, a known alkylene oxide addition reaction catalyst or the like can be used. The reaction temperature (° C.) is preferably 60 to 200, more preferably 80 to 180. The reaction atmosphere is preferably a dry inert gas atmosphere. Confirmation of the reaction end point can be performed by measuring an epoxy index or the like.

  The epoxy index (eq./kg) of the reaction product of the reaction product (a12) and glycidyl methacrylate (a4) is preferably 0.01 or less, more preferably 0.002 or less, particularly preferably 0.001 or less. It is. The epoxy index is a value obtained by dividing 1000 by an epoxy equivalent (g / eq.), And is measured according to JIS K7236: 2001.

  When using a reaction catalyst, it is preferable to remove from the polyoxyalkylene compound (Y), and the removal method similar to the above can be applied as the removal method.

  The polyoxyalkylene compound (Y) may be used after purification {purification treatment by column chromatography, decompression distillation treatment and decolorization treatment of unreacted raw materials, etc.}.

  The reactive surfactant of the present invention may contain a trace amount of a reaction solvent and a polymerization inhibitor (hydroquinone, etc.) present when preparing the polyoxyalkylene compound (Y). Moreover, in order to prevent the polymerization of the polyoxyalkylene compound (Y), a polymerization inhibitor (hydroquinone or the like) may be added. The addition amount of the polymerization inhibitor may be a normal addition amount, for example, about 100 ppm.

  The reactive surfactant of the present invention can be applied as various surfactants having reactivity, and includes a monomer constituting a part of the vinyl resin {emulsifier for emulsion polymerization of vinyl monomer. } And paint additives and the like.

  Other vinyl monomers constituting vinyl resin {including vinyl monomers used for emulsion polymerization. } Is not limited as long as it can be copolymerized with the polyoxyalkylene compound (Y), and known vinyl monomers and the like can be used.

  The vinyl resin can be used as a binder for paints, is suitable as a resin for water-based paints or a resin for non-aqueous paints, is further suitable as a resin for water-based paints, and is optimal as a resin for aqueous emulsion paints. The paint is preferably an aqueous paint or a non-aqueous paint, more preferably an aqueous paint, and particularly preferably an aqueous emulsion paint. Examples of the aqueous emulsion paint include acrylic, vinyl acetate, styrene, halogenated olefin, acrylic-urethane, and acrylic-silicone paints.

  When used as a monomer constituting a part of the vinyl resin, the amount of the reactive surfactant of the present invention used is the amount (% by weight) of the polyoxyalkylene compound (Y) contained in the reactive surfactant of the present invention. Is based on the weight of all monomers {including the polyoxyalkylene compound (Y)}, preferably 1 to 20, more preferably 2 to 19, particularly preferably 3 to 18, more particularly preferably 4 to 17, Preferably it is 5-15. Within this range, when applied as a paint binder or the like, hydrophilicity (antifouling property), hydrophilicity retention ability (long-term antifouling property) and water resistance are further improved.

  When the reactive surfactant of the present invention is used as an additive for coatings, there is no limitation on the method for preparing a coating composition comprising the coating and the reactive surfactant of the present invention. For example, (1) a pigment is used. A method of adding and mixing the reactive surfactant of the present invention at the time of dispersion, and (2) adding and mixing the reactive surfactant of the present invention when the binder resin and various additives are blended into the dispersed pigment. Any of the method and (3) a method of adding and mixing the reactive surfactant of the present invention immediately before coating may be used.

  The addition amount (% by weight) to the paint is preferably 0.1 to 5, more preferably 0.2 to 4.5, particularly preferably 0.3 to 4, and more particularly preferably based on the weight of the paint. Is 0.4 to 3.5, most preferably 0.5 to 3. Within this range, hydrophilicity (antifouling property), hydrophilicity retention ability (long-term antifouling property) and water resistance are further improved.

  The paint using the reactive surfactant of the present invention can be applied to an object to be coated by an ordinary method, such as brush coating, roller coating, air spray coating, airless coating, roll coater coating, and flow coater coating. A painting method can be applied.

  EXAMPLES Hereinafter, although an Example demonstrates this invention further in detail, this invention is not limited to this. Unless otherwise specified, “part” means “part by weight” and “%” means “% by weight”.

<Example 1>
In a pressure-resistant reaction vessel (1) capable of stirring, heating, cooling, dropping, pressurizing with nitrogen, and depressurization with a vacuum pump, 342 parts (1 mole part) of purified granulated sugar {manufactured by Taiwan Sugar Co., Ltd. {Mitsubishi Gas Chemical Co., Ltd., the same applies hereinafter} After 500 parts were charged, the operation of pressurizing with nitrogen gas to 0.4 MPa and discharging to 0.02 MPa was repeated three times. (Hereinafter abbreviated as “nitrogen substitution”). Thereafter, the temperature was raised to 100 ° C. with stirring, and at this temperature, 232 parts (4 mole parts) of propylene oxide (PO) was added dropwise over 3 hours, and stirring was further continued for 3 hours at the same temperature to leave the remaining PO. Reacted. Next, 432 parts (6 mole parts) of butylene oxide (BO) was added dropwise over 3 hours, and stirring was continued for 2 hours at the same temperature to react with the remaining BO. Thereafter, DMF was removed at 120 ° C. under reduced pressure (−0.05 to −0.098 MPa: hereinafter simply referred to as “reduced pressure”) to obtain a sucrose / PO4 mol / BO6 mol adduct (S1). The DMF content (gas chromatography method using an internal standard; the same applies hereinafter) was 0.05%.

  In a reaction vessel (2) with a reflux tube that can be heated, cooled and stirred, 1006 parts (1 mole part) of sucrose / PO4 mole / BO6 mole adduct (S1), methacrylic acid {reagent special grade, Wako Pure Chemical Industries, Ltd. )} 90.3 parts (1.05 mol parts), hydroquinone {reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.} 0.1 part and cobalt naphthenate {reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.} When 0.05 part was added and stirred at 80 ° C. for 2 hours and then at 100 ° C. for 3 hours while flowing nitrogen at a rate of 10 mL / min in the reaction solution, no water was observed in the reflux tube. . The reflux tube and the nitrogen introduction tube were removed, and dehydration was performed at 80 ° C. under reduced pressure for 1 hour to obtain the reactive surfactant (Y1) {(S1) 1 mol / methacrylic acid 1 mol) of the present invention. The ester value of (Y1) (the number of mg of KOH required to completely saponify the ester contained in 1 g of the sample) was 52 mgKOH / g.

<Example 2>
Into a pressure-resistant reaction vessel (1) similar to that in Example 1, 342 parts (1 mol part) of trehalose {manufactured by Wako Pure Chemical Industries, Ltd.} and 500 parts of DMF were added, followed by nitrogen substitution. Thereafter, the temperature was raised to 100 ° C. while stirring, and then 754 parts (13 mole parts) of PO was added dropwise at this temperature over 6 hours, and stirring was continued for 3 hours at the same temperature to react with the remaining PO. . Thereafter, DMF was removed under reduced pressure at 120 ° C. to obtain a trehalose / PO13 molar adduct (S2). The DMF content was 0.06%.

  A pressure-resistant reaction vessel (1) similar to that in Example 1 was charged with 1096 parts (1 mole part) of trehalose / PO13 mole adduct (S2) and 0.3 part (0.005 mole part) of potassium hydroxide under reduced pressure. And dehydrated at 120 ° C. for 1 hour. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, and 142 parts (1 mol part) of Bremer GH {manufactured by Nippon Oil & Fats Co., Ltd., glycidyl methacrylate, hereinafter the same} was added dropwise over 4 hours, and stirring was further continued for 1 hour to complete the reaction system. It was confirmed that the pressure reached an equilibrium, and the reactive surfactant (Y2) {(S2) 1 mol / glycidyl methacrylate 1 mol} of the present invention was obtained. The ester value of (Y2) was 45.5 mgKOH / g.

<Example 3>
Raffinose {manufactured by Wako Pure Chemical Industries, Ltd.} 504 parts (1 mole part) and 800 parts of DMF were charged into a pressure-resistant reaction vessel (1) similar to that in Example 1, and then purged with nitrogen. Thereafter, the temperature was raised to 100 ° C. while stirring, and then 986 parts (17 mole parts) of PO was added dropwise at this temperature over 8 hours, and stirring was further continued for 3 hours at the same temperature to react with the remaining PO. Thereafter, DMF was removed under reduced pressure at 120 ° C. to obtain a raffinose / PO 17 mol adduct (S3). The DMF content was 0.04%.

  In the same reaction vessel (2) as in Example 1, 1490 parts (1 mole part) of raffinose / PO 17 mole adduct (S3), acrylic acid {reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.} 75.6 parts ( 1.05 mol part), 0.1 part of hydroquinone and 0.05 part of cobalt naphthenate were added, and nitrogen was passed through the reaction solution at a rate of 10 mL / min for 2 hours at 80 ° C. and then at 100 ° C. for 3 hours. After stirring for a period of time, no distillation of water was observed in the reflux tube. The reflux tube and the nitrogen introduction tube were removed, and dehydration was performed at 80 ° C. under reduced pressure for 1 hour to obtain the reactive surfactant (Y3) {(S3) 1 mol / acrylic acid 1 mol) of the present invention. The ester value of (Y3) was 35.8 mgKOH / g.

<Example 4>
Into a pressure resistant reaction vessel (1) similar to that in Example 1, 342 parts (1 mol part) of purified granulated sugar and 800 parts of DMF were added and then purged with nitrogen. Thereafter, the temperature was raised to 100 ° C. while stirring, and 1160 parts (20 mole parts) of PO was dropped at this temperature over 8 hours, and stirring was further continued for 3 hours at the same temperature to react with the remaining PO. Thereafter, DMF was removed under reduced pressure at 120 ° C. to obtain a sucrose / PO 20 molar adduct (S4). The DMF content was 0.06%.

  In a pressure-resistant reaction vessel (1) similar to that in Example 1, 1502 parts (1 mol part) of sucrose / PO 17 mol adduct (S4) and 0.3 part (0.005 mol part) of potassium hydroxide were charged under reduced pressure. And dehydrated at 120 ° C. for 1 hour. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, and 142 parts (1 mole part) of Bremmer GH was added dropwise over 4 hours, and stirring was further continued for 1 hour to confirm that the pressure of the reaction system had completely reached equilibrium. Reactive surfactant (Y4) {(S4) 1 mol / glycidyl methacrylate 1 mol} was obtained. The ester value of (Y4) was 34.2 mgKOH / g.

<Example 5>
In a pressure-resistant reaction vessel (1) similar to Example 1, 1502 parts (1 mol part) of sucrose / PO 17 mol adduct (S4) obtained in Example 4 and 5 parts (0.09 mol part) of potassium hydroxide Then, nitrogen substitution was performed. Thereafter, the temperature was raised to 130 ° C. with stirring, and dehydration was performed under reduced pressure for 1 hour. Subsequently, PO580 part (10 mol part) was dripped at 110 degreeC over 3 hours, and also stirring was continued at the same temperature for 1 hour, and the remaining PO was made to react. Next, after adding 20 parts of ion-exchanged water at 90 ° C., 60 parts of Kyoward 700 {manufactured by Kyowa Chemical Industry Co., Ltd.} was added and stirred at the same temperature for 1 hour. Furthermore, at the same temperature, no. Filter using 2 filter papers {manufactured by Toyo Filter Paper Co., Ltd.} to remove Kyoward 700 and dehydrate at 120 ° C. for 1 hour under reduced pressure (hereinafter “Kyoword treatment”). To obtain a sucrose / PO 30 molar adduct (S5).

  In a pressure-resistant reaction vessel (1) similar to that in Example 1, 2082 parts (1 mole part) of sucrose / PO 30 mole adduct (S5) and 0.4 part (0.007 mole part) of potassium hydroxide were charged under reduced pressure. And dehydrated at 120 ° C. for 1 hour. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, and 142 parts (1 mole part) of Bremer GH was added dropwise over 4 hours, and stirring was further continued for 1 hour to confirm that the pressure of the reaction system had completely reached equilibrium. Surfactant (Y5) {(S5) 1 mol / glycidyl methacrylate 1 mol} was obtained. The ester value of (Y5) was 25.2 mgKOH / g.

<Example 6>
In the same pressure resistant reactor (1) as in Example 1, 1096 parts (1 mole part) of trehalose / PO13 mole adduct (S2) obtained in Example 2 and potassium hydroxide {reagent special grade, Wako Pure Chemical Industries, Ltd. ) Made and used amounts are displayed in pure equivalents excluding moisture. Thereafter, the same} 5 parts (0.09 mole part) was added, and then nitrogen substitution was performed. Thereafter, the temperature was raised to 130 ° C. with stirring, and dehydration was performed under reduced pressure for 1 hour. Next, 1566 parts (27 mole parts) of PO at 110 ° C. was added dropwise over 8 hours, and stirring was continued for 3 hours at the same temperature to react with the remaining PO, followed by Kyoward treatment to add 40 moles of trehalose / PO. A product (S6) was obtained.

  Into a pressure-resistant reaction vessel (1) similar to that in Example 1, 2662 parts (1 mol part) of trehalose / PO 40 mol adduct (S6) and 0.4 part (0.007 mol part) of potassium hydroxide were charged under reduced pressure. And dehydrated at 120 ° C. for 1 hour. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, and 142 parts (1 mole part) of Bremer GH was added dropwise over 4 hours, and stirring was further continued for 1 hour to confirm that the pressure of the reaction system had completely reached equilibrium. Surfactant (Y6) {(S6) 1 mol / glycidyl methacrylate 1 mol) was obtained. The ester value of (Y6) was 19.6 mgKOH / g.

<Example 7>
1490 parts (1 mol part) of raffinose / PO 17 mol adduct (S3) obtained in Example 3 and 7 parts (0.12 mol part) of potassium hydroxide were added to the pressure-resistant reaction vessel (1) similar to Example 1. After the addition, nitrogen substitution was performed. Thereafter, the temperature was raised to 130 ° C. with stirring, and dehydration was performed under reduced pressure for 1 hour. Next, 1914 parts (33 mole parts) of PO was added dropwise at 110 ° C. over 8 hours. Stirring was continued for 3 hours at the same temperature, and the remaining PO was reacted, then treated with Kyoward to add raffinose / PO 50 moles. A product (S7) was obtained.

  In the same reaction vessel (2) as in Example 1, 3404 parts (1 mole part) of raffinose / PO 50 mole adduct (S7), 90.3 parts (1.05 mole part) of methacrylic acid, 0.1 part of hydroquinone and When 0.05 parts of cobalt naphthenate was charged and stirred at 80 ° C. for 2 hours and then at 100 ° C. for 3 hours while flowing nitrogen at a rate of 10 mL / min, water was found to distill into the reflux tube. I can't. The reflux tube and the nitrogen introduction tube were removed, and dehydration was performed at 80 ° C. under reduced pressure for 1 hour to obtain the reactive surfactant (Y7) {(S7) 1 mol / methacrylic acid 1 mol) of the present invention. The ester value of (Y7) was 16.3 mgKOH / g.

<Example 8>
In a pressure-resistant reaction vessel (1) similar to that in Example 1, 2082 parts (1 mol part) of sucrose / PO 30 mol adduct (S5) obtained in Example 5 and 6.2 parts (0.11 mol part) of potassium hydroxide were used. ), And nitrogen substitution was performed. Thereafter, the temperature was raised to 130 ° C. with stirring, and dehydration was performed under reduced pressure for 1 hour. Next, 1740 parts of PO (30 mole parts) was added dropwise at 110 ° C. over 5 hours, and stirring was continued for 2 hours at the same temperature to react with the remaining PO, followed by Kyoward treatment to add 60 moles of sucrose / PO. A product (S8) was obtained.

  A pressure-resistant reaction vessel (1) similar to that in Example 1 was charged with 3822 parts (1 mol part) of sucrose / PO 60 mol adduct (S8) and 0.4 parts (0.007 mol part) of potassium hydroxide under reduced pressure. And dehydrated at 120 ° C. for 1 hour. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, and 142 parts (1 mole part) of Bremer GH was added dropwise over 4 hours, and stirring was further continued for 1 hour to confirm that the pressure of the reaction system had completely reached equilibrium. Surfactant (Y8) {(S8) 1 mol / glycidyl methacrylate 1 mol} was obtained. The ester value of (Y8) was 14.3 mgKOH / g.

<Example 9>
Into a pressure resistant reaction vessel (1) similar to that in Example 1, 342 parts (1 mole part) of purified granulated sugar and 2000 parts of DMF were added, and then purged with nitrogen. Thereafter, the temperature was raised to 100 ° C. while stirring, and then at this temperature, 176 parts (4 mole parts) of ethylene oxide (EO) was added dropwise over 2 hours, and stirring was further continued for 1 hour at the same temperature to leave the remaining EO. Reacted. Subsequently, 3828 parts (66 mol parts) of PO were added dropwise over 10 hours, and the stirring was continued for 4 hours at the same temperature to react with the remaining PO. Thereafter, DMF was removed under reduced pressure at 120 ° C. to obtain an adduct (S9) of sucrose / EO 4 mol / PO 66 mol. The DMF content was 0.05%.

  In a pressure-resistant reaction vessel (1) similar to that in Example 1, 4346 parts (1 mol part) of sucrose / EO 4 mol / PO 66 mol adduct (S9) and 0.4 part (0.007 mol part) of potassium hydroxide were charged. The mixture was dehydrated at 120 ° C. for 1 hour under reduced pressure. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, 170.4 parts (1.2 mole parts) of Bremer GH was added dropwise over 4 hours, and stirring was further continued for 1 hour to confirm that the pressure of the reaction system had reached equilibrium, The reactive surfactant (Y9) {(S9) 1 mol / glycidyl methacrylate 1.2 mol} of the present invention was obtained. The ester value of (Y9) was 14.8 mgKOH / g.

<Example 10>
Into a pressure resistant reaction vessel (1) similar to that in Example 1, 342 parts (1 mole part) of purified granulated sugar and 2000 parts of DMF were added, and then purged with nitrogen. Thereafter, the temperature was raised to 100 ° C. while stirring, and 396 parts (9 parts by mole) of EO was added dropwise at this temperature over 2 hours, and stirring was further continued for 1 hour at the same temperature to react with the remaining EO. Subsequently, 4118 parts (71 mole parts) of PO was added dropwise over 12 hours, and stirring was continued for 4 hours at the same temperature to react with the remaining PO. Thereafter, DMF was removed under reduced pressure at 120 ° C. to obtain an adduct (S10) of sucrose / EO 9 mol / PO 71 mol. The DMF content was 0.06%.

  In a pressure-resistant reaction vessel (1) similar to that in Example 1, 4856 parts (1 mole part) of sucrose / EO 9 mol / PO 71 mole adduct (S10) and 0.4 part (0.007 mole part) of potassium hydroxide were charged. The mixture was dehydrated at 120 ° C. for 1 hour under reduced pressure. Next, after cooling to 80 ° C., 0.1 part of hydroquinone was added and stirred for 10 minutes. The pressure was reduced again at the same temperature, and 213 parts (1.5 parts by mole) of Bremer GH was added dropwise over 4 hours, and stirring was further continued for 1 hour to confirm that the pressure of the reaction system had completely reached equilibrium. Reactive surfactant (Y10) {(S10) 1 mol / glycidyl methacrylate 1.5 mol} was obtained. The ester value of (Y10) was 16.8 mgKOH / g.

<Comparative Example 1>
To the pressure-resistant reaction vessel (1) similar to that in Example 1, 136 parts (1 mole part) of pentaerythritol {special reagent grade, manufactured by Wako Pure Chemical Industries, Ltd.} and 2000 parts of DMF were added to perform nitrogen substitution. Thereafter, the temperature was raised to 100 ° C. while stirring, and 1740 parts (30 mole parts) of PO was added dropwise at the same temperature over 7 hours, and then stirring was continued for 3 hours at the same temperature to react with the remaining PO. Subsequently, 880 parts (20 mole parts) of EO was dropped over 2 hours, and then stirring was continued for 30 minutes at the same temperature to react with the remaining EO. Next, after the temperature was raised to 110 ° C., DMF was removed under reduced pressure at this temperature and then at 120 ° C., and a comparative surfactant (F1) {pentaerythritol / PO 30 mol / EO 20 mol polyoxyalkylene compound }. The DMF content of (F1) was 0.02%.

<Comparative example 2>
In the same reaction vessel (2) as in Example 1, 275.6 parts (0.1 mol part) of pentaerythritol / PO 30 mol / EO 20 mol adduct (F1) obtained in Comparative Example 1 and 10.3 parts of methacrylic acid (0.12 mol part), 0.1 part of hydroquinone and 0.05 part of cobalt naphthenate were charged, and nitrogen was passed through the reaction solution at a rate of 10 mL / min for 2 hours at 80 ° C., then at 100 ° C. When the mixture was stirred for 3 hours, no distillation of water was observed in the reflux tube. The reflux tube and the nitrogen introduction tube were removed, and dehydrated at 80 ° C. for 1 hour under reduced pressure. Comparative reactive surfactant (F2) {pentaerythritol / PO 30 mol / EO 20 mol adduct / methacrylic acid 1 mol} for comparison Got. The ester value of (F2) was 20 mgKOH / g.

<Comparative Example 3>
In a pressure resistant reaction vessel (1) similar to that in Example 1, stearyl glycidyl ether {manufactured by NOF Corporation, product name: Epiol SK} 652 parts (2 mole parts), polyoxyethylene glycol {Sanyo Chemical Industries, Ltd. Product, molecular weight 600, product name: PEG-600} 600 parts (1 mole part) and triethylenediamine {reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.} 3 parts were charged, and nitrogen substitution was performed. Then, after stirring at 100 ° C. for 5 hours, a comparative surfactant (F3) {2 mol of stearyl glycidyl ether / polyoxyalkylene compound of 1 mol of polyoxyethylene glycol} was obtained.

<Preparation of evaluation resin>
(1) Vinyl resin solution (JSt)
In a reaction vessel equipped with a reflux tube and a nitrogen introduction tube capable of heating, cooling and stirring, 500 parts of propylene glycol monomethyl ether {manufactured by Nippon Emulsifier Co., Ltd., product name: MFG} is charged and stirred while introducing nitrogen. The temperature was raised to ° C. Next, while maintaining the same temperature, styrene {reagent special grade, manufactured by Wako Pure Chemical Industries, Ltd.} 208 parts (2 mole parts), 2-ethylhexyl methacrylate {manufactured by NOF Corporation, product name: Blemmer EHMA-25} 138 .6 parts (0.7 mol parts), n-butyl methacrylate {Nippon Yushi Co., Ltd., product name: Blemmer BMA} 142 parts (1 mol parts), AE-350 {Nippon Yushi Co., Ltd., polyethylene glycol A mixed liquid of monoacrylate, number average molecular weight: 423} 126.9 parts (0.3 mole parts), 86 parts of methacrylic acid (1 mole part) and 2 parts of azobisisobutyronitrile was added dropwise over 4 hours. Thereafter, the mixture was stirred at 120 ° C. for 2 hours to obtain a 58.5% yellow transparent vinyl resin solution having a nonvolatile content (sample amount: about 5 g: 105 ° C. × 1.5 hours).
Next, under reduced pressure, propylene glycol monomethyl ether is removed at 60 to 90 ° C. to make the nonvolatile content about 80%, and further with a deionized water / 10% ammonia water, a nonvolatile resin content of 40%, pH 8 vinyl resin solution (JSt )

(2) Vinyl resin solutions (J1) to (J10) and comparative vinyl resin solutions (JC1) to (JC3)
"AE-350 {Nippon Yushi Co., Ltd., Polyethylene glycol monoacrylate, number average molecular weight: 423} 126.9 parts (0.3 mol parts)" obtained in Examples 1 to 10 In the same manner as above except that the surfactants (F1) to (F3) obtained in (Y1) to (Y10) and Comparative Examples 1 to 3 were changed to the amounts shown in Table 1, the non-volatile content was 40%, Vinyl resin solutions (J1) to (J10) having a pH of 8 and vinyl resin solutions (JC1) to (JC3) for comparison were obtained.

Table 1 shows the weight average molecular weights of the vinyl resin solution (JSt), the vinyl resin solutions (J1) to (J10), and the comparative vinyl resin solutions (JC1) to (JC3).
In addition, the weight average molecular weight is measured under the following conditions using gel permeation chromatography (GPC) with polystyrene having a known molecular weight as a standard substance, and is calculated by removing the peak of propylene glycol monomethyl ether used as a solvent. did.

Apparatus: manufactured by Tosoh Corporation (model HLC-8120GPC)
Column: Toso-type SuperH-4000 × 2 and the same type SuperH-3000 × 1 column connected in series Detector: Differential refraction detector Data processor: Data processor manufactured by Tosoh Corporation SC-8020)
Column temperature: 40 ° C
Eluent: THF (reagent grade 1, manufactured by Katayama Chemical)
Flow rate: 0.5 ml / min.
Sample concentration: 1% by weight
Sample solution injection volume: 10 μl

<Adjustment of paint and test piece>
(1) Standard paint Using an Excel auto homogenizer (model ED, manufactured by Nippon Seiki Co., Ltd.) equipped with impeller-type blades in the grinding process and the let-down process at room temperature (20-30 ° C) with the raw material composition shown in Table 2 Was mixed at 3000 rpm for 5 hours to obtain an aqueous emulsion paint. The obtained paint was confirmed to have no particles of 5 microns or more by the crush gauge method (JIS K5400-1990).
This aqueous emulsion paint was diluted with water to 77 KU (25 ° C.) with a stoma viscometer (JIS K5400-1990) to obtain a standard paint.

Remarks) Source and name, etc. 1: Dispersant manufactured by San Nopco Co., Ltd. 2: Thickener manufactured by San Nopco Co., Ltd. 3: Defoamer manufactured by San Nopco Co., Ltd. 4: Dioxide produced by Ishihara Sangyo Co., Ltd. Titanium 5: Preservative made by San Nopco Co., Ltd. 6: Film forming regulator made by Eastman Chemical Co., Ltd. 7: Thickener made by San Nopco Co., Ltd.

(2) Evaluation paints (1) to (10) and comparative evaluation paints (H1) to (H3)
Evaluation paint in the same manner as above except that “vinyl resin solution (JSt)” is changed to “vinyl resin solutions (J1) to (J10)” or “vinyl resin solutions for comparison (JC1) to (JC3)” (1) to (10) and comparative evaluation paints (H1) to (H3) were obtained.

(3) Test piece Polyester film degreased with acetone {Product name: Lumirror 75-S10, manufactured by Panac Co., Ltd., used with a thickness of 0.1 mm cut to 10 × 8 cm} using an applicator Standard paints, evaluation paints (1) to (10) and comparative evaluation paints (H1) to (H3) were applied so that the wet film thickness was 200 μm. Next, a test piece (test piece) was prepared by allowing it to stand for 7 days in a control room (hereinafter abbreviated as a temperature control room) adjusted to 25 ° C. and 50% relative humidity, leaving the coating surface horizontal and drying. Standard), (1) to (10) and (H1) to (H3) were obtained.

<Evaluation>
Contamination resistance {difference in whiteness} of the coating film was evaluated by hydrophilicity {contact angle with water}, water resistance {visual judgment}, and outdoor exposure test. The results are shown in Table 3.

  In addition, regarding the relationship between the contact angle of the coating film with water and the contamination reduction property, the smaller the contact angle, the better the contamination reduction property (contamination resistance, ease of carrying away dirt adhered to the surface due to raindrops). (Public-private joint research "development of structural fouling technology", Ministry of Construction Public Works Research Institute, Chemistry Laboratory). In addition, the test paint pieces are immersed in deionized water for 24 hours and then dried, and the coating film that maintains the contact angle with water of 50 degrees or less even after the accelerated durability test is measured. There is a report that it is difficult {Nobuhiro Kenmochi, “Surface Properties and Contamination of Paints for Exterior Walls”, Paint Engineering, 28, [4] 147 (1993); Toshikazu Nakaya, “Development of Antifouling Paints for Architecture "JETI, 42, [5] 8 (1994)}.

1. Contact angle with water (antifouling)
Take a test piece of 1x5 cm from the test piece, drop 0.02 ± 0.005 mL of deionized water onto the surface of the coating, and measure the contact angle of the water drop after 1 minute. Contact angle. The contact angle was measured using a contact angle meter CAA manufactured by Kyowa Chemical in a temperature control room (25 ° C., 60% relative humidity).

2. Contact angle after immersion treatment (long-term antifouling property)
After taking a test piece of 1 × 5 cm from the test piece and immersing it in deionized water at 25 ° C. for 24 hours, the coating is placed in a temperature-controlled room (about 25 ° C., about 60% relative humidity). It was left to dry in the same room for 24 hours so that the surface was horizontal. Subsequently, the contact angle with water was measured in the same manner as described above, and this was defined as the contact angle after the immersion treatment.

3. Water resistance Take a 5 x 5 cm test piece from the test piece and immerse it in deionized water at 25 ° C for 24 hours, then lift it from the water and the number and size of blisters generated on the coating surface. Etc. were visually observed and evaluated according to the following criteria.

A: No blister.
○: There are some blisters having a diameter of about 0.1 mm.
Δ: Some blisters with a diameter of 0.5 mm or more.
X: There are many blisters with a diameter of 0.5 mm or more.

4). Difference in whiteness (-△ L value, outdoor exposure test)
A test piece (10 × 8 cm) was attached to a slate plate using a double-sided tape to obtain a test plate. A test plate is installed on the roof of the 6-story building in Tokai City, Aichi Prefecture (approx. 25 m above ground) so that the painted surface is 45 degrees to the horizontal plane and the painted surface faces true north. For about 6 months. Thereafter, the dust or dirt adhering to the surface of the test coating piece is scraped three times with a cotton cloth soaked with the same amount of water as its own weight, and after removing moisture with a dry cotton cloth, the whiteness (L2 ) Was measured. The absolute value (−ΔL) of the value obtained by subtracting the whiteness (L1) of the test coating piece before exposure from the whiteness (L2) was calculated, and this was calculated as “difference in whiteness (−ΔL). " In addition, it shows that long-term antifouling property is so favorable that the difference (-(DELTA) L) of whiteness is small. The whiteness was measured using SPECTRO COLOR METERMODEL PF-10 manufactured by Nippon Denshoku Industries Co., Ltd.

  From Table 3, paints prepared using the reactive surfactants of the present invention {evaluation paints (1) to (10); Examples 1 to 10} are paints using standard paints and comparative surfactants. Compared with {Evaluation paints (H1) to (H3)}, the difference in contact angle with water (initial and after immersion treatment) and whiteness is extremely small, hydrophilicity (antifouling property), hydrophilicity retention ability ( Long-term antifouling property) was extremely high. Moreover, it was recognized that the coating material prepared using the reactive surfactant of the present invention does not impair the water resistance of the coating film.

  The reactive surfactant of the present invention can be applied to both water-based paints and non-aqueous paints, and among these, it is particularly suitable for imparting a contamination reducing function to water-based paints. Is suitable. Examples of the aqueous emulsion paint include acrylic, vinyl acetate, styrene, halogenated olefin, acryl-urethane, and acryl-silicon paints. And the reactive surfactant of this invention is very useful for the coating material (especially aqueous emulsion coating material) painted outdoors, such as an outer wall.

Claims (5)

It is a reactive surfactant used as a monomer that constitutes part of a vinyl resin used as a binder for paints,
A reactive surfactant capable of imparting hydrophilicity to a coating film without impairing the water resistance of the coating film and capable of forming a coating film having a hydrophilic holding ability,
A reactive surfactant comprising a polyoxyalkylene compound (Y) represented by the general formula (1) as an essential component.

{R (-OA) n-} m Q (1)

However, in the general formula (1), Q is a reaction residue obtained by removing a hydrogen atom from m primary hydroxyl groups of non-reducing di- or trisaccharides, OA is an oxyalkylene group having 2 to 4 carbon atoms, and R is A (meth) acryloyl group, a 3- (meth) acryloyloxy-2-hydroxypropyl group or a hydrogen atom is represented, and at least one R is a (meth) acryloyl group and / or 3- (meth) acryloyloxy-2-hydroxy. A propyl group, n is an integer of 1 to 30, m is an integer of 2 to 4, the total number of OA is an integer of 10 to 80, and R, OA, (OA) n, Q, n, and m are respectively It may be the same or different. The reactive surfactant according to claim 1, wherein Q is a reaction residue obtained by removing a hydrogen atom from three primary hydroxyl groups of sucrose. It is a reactive surfactant used as a monomer that constitutes part of a vinyl resin used as a binder for paints,
A reactive surfactant capable of imparting hydrophilicity to a coating film without impairing the water resistance of the coating film and capable of forming a coating film having a hydrophilic holding ability,
A polyoxyalkylene compound having a structure (1) produced by a chemical reaction of a non-reducing di- or trisaccharide (a1), a C2-C4 alkylene oxide (a2) and (meth) acrylic acid (a3), And / or a polyoxy having a structure (2) produced by a chemical reaction of a non-reducing di- or trisaccharide (a1), a C2-C4 alkylene oxide (a2) and a glycidyl (meth) acrylate (a4) An alkylene compound as an essential component,
A reactive surfactant, wherein the amount of the alkylene oxide (a2) used is 10 to 80 parts by mole relative to 1 part by mole of the non-reducing di- or trisaccharide (a1). The polyoxyalkylene compound (Y) and vinyl monomer contained in the reactive surfactant according to any one of claims 1 to 3 are essential constituent monomers, and the content of the polyoxyalkylene compound (Y) unit is a vinyl monomer. And a vinyl resin of 1 to 20% by weight based on the weight of the polyoxyalkylene compound (Y). The coating material containing the vinyl resin of Claim 4.