JP6183124B2 - Aqueous polyurethane resin dispersion - Google Patents

Description

  The present invention relates to an aqueous polyurethane resin dispersion in which a polyurethane resin is dispersed in an aqueous medium. The present invention also relates to a coating composition containing the aqueous polyurethane resin dispersion and a polyurethane resin film obtained by heating and drying the composition containing the polyurethane resin dispersion.

The water-based polyurethane resin dispersion is an environmentally friendly material that can provide a coating film having adhesiveness, abrasion resistance, rubber-like properties, etc., and can reduce volatile organic substances compared to conventional solvent-based polyurethane. It is a material that is being replaced by solvent-based polyurethane.
Polycarbonate polyol is a useful compound that can be used as a raw material for polyurethane resins. By reacting with isocyanate compounds, it produces durable polyurethane resins used for rigid foams, flexible foams, paints, adhesives, synthetic leather, ink binders, etc. can do. The characteristics of the polyurethane resin using polycarbonate polyol are expressed by the high cohesive strength of the carbonate group, and are described as being excellent in water resistance, heat resistance, oil resistance, elastic recovery, wear resistance, weather resistance, and the like ( For example, refer nonpatent literature 1). In addition, coating films obtained by applying an aqueous urethane resin dispersion using polycarbonate polyol as a raw material are also known to be excellent in light resistance, heat resistance, hydrolysis resistance, oil resistance, etc. (for example, patents) Reference 1).

  As described above, an aqueous polyurethane resin dispersion using a polycarbonate polyol exhibits good characteristics, but is not sufficient as compared with a solvent-based polyurethane. In particular, the solvent resistance and water resistance of the coating film are insufficient. In order to improve such characteristics, a crosslinked structure is introduced into a polyurethane resin, or a composition in which a crosslinking material such as an epoxy resin or a polyfunctional isocyanate is introduced is crosslinked at the time of curing. Among them, the aqueous polyurethane resin dispersion having a blocked isocyanato group is stable at room temperature, and thus has a high utility value as a one-part crosslinking reactive dispersion having high storage stability (for example, Patent Document 2 and Patent Reference 3). It is also known that an aqueous polyurethane resin dispersion using a polycarbonate polyol as a raw material has a feature of high adhesion to an electrodeposition coating film (see, for example, Patent Document 4).

  Furthermore, the present inventors have controlled the film-forming speed after coating by an aqueous polyurethane resin dispersion having a specific amount of a blocked isocyanate group having a urethane bond, a urea bond, and a carbonate bond. The film can be re-dispersed in water, and the coating obtained by applying and heat treatment is excellent in water resistance and solvent resistance, and is excellent in adhesion to the electrodeposition coating film. It has been found that since the breaking energy in tension is high, the impact resistance is also excellent (see, for example, Patent Document 5).

JP-A-10-120757 Japanese Patent Laid-Open No. 2002-128551 JP 2000-104015 A JP 2005-220255 A International Publication No. 2010/098316 Pamphlet

“Latest Polyurethane Materials and Applied Technologies”, CMC Publishing Co., Ltd. Chapter 2 Page 43

However, the conventional aqueous polyurethane resin dispersion has a problem that the paint is dripped when the vertical surface is applied because the viscosity increase ratio in the process of forming the coating film is small.
In spray coating, which is mainly used for painting on vertical surfaces, it is necessary that the viscosity be low before discharging from the spray. And when the droplet discharged from the spray passes through the air and deposits on the substrate, it is considered that the solid content concentration becomes about 1.5 times.
Therefore, the present invention maintains the performance of good water resistance, good detergency, high breaking energy, and good adhesion to the electrodeposition surface, while the solid content concentration is generally used from 30% by weight to 45%. An object of the present invention is to obtain an aqueous polyurethane resin dispersion having a high viscosity increase ratio when the weight percentage is reached.

The present invention has been made to solve the above problems, and specifically has the following configuration.
[1] (a) a polyisocyanate compound, (b) one or more polyol compounds including a polycarbonate polyol having a number average molecular weight of 800 to 3,500, (c) an acidic group-containing polyol compound, and (d) 80 to 180 ° C. A polyurethane obtained by reacting (A) a polyurethane prepolymer obtained by reacting a blocking agent for an isocyanato group dissociated in step (B) and (B) a chain extender having reactivity with the isocyanate group of the polyurethane prepolymer. The resin is an aqueous polyurethane resin dispersion dispersed in an aqueous medium,
The (b) polyol compound contains a polyol containing an alicyclic structure, and the (B) chain extender contains an alkanedioic acid dihydrazide having 4 to 10 carbon atoms,
The polyurethane resin has a urethane bond content ratio and a urea bond content ratio of 8 to 13 wt% based on solid content, a carbonate bond content ratio of 15 to 40 wt% based on solid content, The ring structure content ratio is 18 to 30% by weight based on the solid content, and the content ratio of the isocyanate group to which the blocking agent is bonded is 0.3 to 2.0% by weight based on the solid content and in terms of isocyanate group, An aqueous polyurethane resin dispersion having a weight average molecular weight of 20,000 to 100,000.
[2] The aqueous polyurethane resin dispersion according to [1], wherein the alkanedioic acid dihydrazide having 4 to 10 carbon atoms is adipic acid dihydrazide.
[3] The aqueous polyurethane resin dispersion according to any one of [1] or [2], wherein the acid value is 10 to 30 mg KOH / g.
[4] (a) The aqueous polyurethane resin dispersion according to any one of [1] to [3], wherein the polyisocyanate compound is an alicyclic diisocyanate.
[5] (d) The blocking agent according to any one of [1] to [4], wherein the blocking agent is at least one selected from oxime compounds, pyrazole compounds, and malonic ester compounds. An aqueous polyurethane resin dispersion.
[6] A coating material composition comprising the aqueous polyurethane resin dispersion according to any one of [1] to [5].
[7] A polyurethane resin film produced by heating and drying a composition containing the aqueous polyurethane resin dispersion according to any one of [1] to [5].

According to the present invention, when the solid content concentration is changed from 30% by weight to 45% by weight while maintaining the performance of good water resistance, good detergency, high breaking energy, and good adhesion to the electrodeposition surface. An aqueous polyurethane resin dispersion having a high viscosity increase ratio can be provided.
According to the present invention, when a film is formed on a substrate, the viscosity at a high solid content concentration of 45% by weight or the like is high, the coating dripping at the time of coating film formation can be suppressed, and a large breaking energy in tension and An aqueous polyurethane resin dispersion capable of achieving excellent adhesion to a substrate can be provided.
Moreover, since the coating film obtained using the water-based polyurethane resin dispersion of this invention has high adhesiveness to an electrodeposition coating film, it can be utilized as a protective film of a steel plate. The polyurethane resin film of the present invention can also be used as a decorative film.
According to the present invention, the breaking energy in tension is high, the swelling rate in aqueous cleaning liquid (for example, an aqueous solution containing alcohol, amine, amino alcohol, cellosolve, etc.) is high, and recoating is possible. An aqueous polyurethane resin dispersion having a high viscosity at the solid content concentration can be obtained. The coating film formed from the aqueous polyurethane resin dispersion of the present invention is useful as a protective coating for an electrodeposition coating film on steel sheets for building materials, electrical equipment, vehicles, industrial equipment, office machines and the like.
According to the present invention, it is possible to obtain an aqueous polyurethane resin dispersion that forms a coating film having high breaking energy in tension, low swelling rate in water, and high water resistance.
According to the present invention, an aqueous polyurethane resin dispersion capable of reducing the water swelling rate of a coating film while maintaining an elastic modulus of 50 MPa or more and forming a coating film having both scratch resistance and impact resistance is obtained. Can do.

  In this specification, the numerical range indicated using “to” indicates a range including the numerical values described before and after “to” as the minimum value and the maximum value, respectively. Further, the amount of each component in the composition means the total amount of the plurality of substances present in the composition unless there is a specific notice when there are a plurality of substances corresponding to each component in the composition.

  The aqueous polyurethane resin dispersion of the present invention includes (a) a polyisocyanate compound, (b) one or more polyol compounds including a polycarbonate polyol having a number average molecular weight of 800 to 3,500, (c) an acidic group-containing polyol compound, and (D) (A) a polyurethane prepolymer obtained by reacting an isocyanate group blocking agent that dissociates at 80 to 180 ° C., and (B) a chain extender having reactivity with the isocyanate group of the polyurethane prepolymer. The polyurethane resin obtained by the reaction is dispersed in an aqueous medium, the sum of the urethane bond content and the urea bond content is 8 to 13% by weight based on the solid content, and the carbonate bond content. Is 15 to 40% by weight based on solid content, and the alicyclic structure content ratio is 18 to 30% by weight based on solid content Yes, the content ratio of the isocyanate group to which the blocking agent is bound is 0.3 to 2.0% by weight in terms of solid content and in terms of isocyanate group, and (B) a chain extender has 4 carbon atoms as an essential component. 10 to 10 alkanedioic acid dihydrazide is contained in an amount of 2 to 10% by weight based on solid content, and the weight average molecular weight is 20,000 to 100,000.

[(A) polyisocyanate compound]
The polyisocyanate compound (a) that can be used in the present invention is not particularly limited as long as it is a compound having two or more isocyanato groups, and is an aromatic polyisocyanate compound, a linear or branched aliphatic polyisocyanate compound, and Any of an alicyclic polyisocyanate compound may be sufficient. Specific examples of the polyisocyanate compound include 1,3-phenylene diisocyanate, 1,4-phenylene diisocyanate, 2,4-tolylene diisocyanate (TDI), 2,6-tolylene diisocyanate, and 4,4′-diphenylenemethane. Diisocyanate (MDI), 2,4-diphenylmethane diisocyanate, 4,4′-diisocyanatobiphenyl, 3,3′-dimethyl-4,4′-diisocyanatobiphenyl, 3,3′-dimethyl-4,4 ′ -Aromatic polyisocyanate compounds such as diisocyanatodiphenylmethane, 1,5-naphthylene diisocyanate, m-isocyanatophenylsulfonyl isocyanate, p-isocyanatophenylsulfonyl isocyanate; ethylene diisocyanate, tetramethylene diisocyanate, Samethylene diisocyanate (HDI), dodecamethylene diisocyanate, 1,6,11-undecane triisocyanate, 2,2,4-trimethylhexamethylene diisocyanate, lysine diisocyanate, 2,6-diisocyanatomethylcaproate, bis (2- Aliphatic polyisocyanate compounds such as isocyanatoethyl) fumarate, bis (2-isocyanatoethyl) carbonate, 2-isocyanatoethyl-2,6-diisocyanatohexanoate; isophorone diisocyanate (IPDI), 4,4 ′ -Dicyclohexylmethane diisocyanate (hydrogenated MDI), cyclohexylene diisocyanate, methylcyclohexylene diisocyanate (hydrogenated TDI), bis (2-isocyanatoethyl) -4-dichlorohexene 1,2-dicarboxylate, 2,5-norbornane diisocyanate, and alicyclic polyisocyanate compounds such as 2,6-norbornane diisocyanate Natick sulfonates and the like. These polyisocyanate compounds may be used individually by 1 type, and may use multiple types together.

Among the polyisocyanate compounds (a), alicyclic polyisocyanate compounds are preferable, and alicyclic diisocyanate compounds are more preferable. By using the alicyclic polyisocyanate compound, it is possible to obtain a coating film that is less susceptible to yellowing, and the resulting coating film tends to have a higher hardness.
Among the alicyclic polyisocyanate compounds, 4,4′-dicyclohexylmethane diisocyanate (hydrogen) from the viewpoint that the reactivity can be easily controlled and the resulting coating film has a high elastic modulus and a low water swelling ratio. Additive MDI) is particularly preferred.

[(B) Polyol compound]
The (b) polyol compound in the present invention is a polyol compound that does not contain one or more acidic groups including a polycarbonate polyol having a number average molecular weight of 800 to 3,500. (B) The polyol compound may contain other polyol compounds other than polycarbonate polyol having a number average molecular weight of 800 to 3500 and containing no acidic group. That is, (c) acidic group-containing polyol described later is not included in (b) polyol compound.
The (b) polyol compound includes a polyol containing an alicyclic structure.

[[(B-1) Polycarbonate polyol having a number average molecular weight of 800 to 3500]] The polycarbonate polyol having a number average molecular weight of 800 to 3500 that can be used in the present invention is acidic with a number average molecular weight of 800 to 3500. There is no particular limitation as long as it is a polycarbonate polyol containing no group.
When the number average molecular weight of the polycarbonate polyol is less than 800, there are problems such as low breaking energy in tension of the obtained coating film. When the number average molecular weight of the polycarbonate polyol exceeds 3500, there are problems such as inferior film forming properties of the resulting aqueous polyurethane resin dispersion. As a number average molecular weight, 1500-3200 are more preferable and 2000-3000 are still more preferable from a viewpoint of the fracture | rupture energy and film forming property in the tension | pulling of a coating film. When two or more types of polycarbonate polyols having different molecular weights are used in combination, the average molecular weight when mixed is preferably within this range.

  The proportion of the polycarbonate polyol having the (b-1) number average molecular weight of 800 to 3500 in the total weight of the (b) polyol compound is from 50% by weight from the viewpoint of the breaking energy in the tension of the coating film to be formed. It is preferably 100% by weight, more preferably 70% by weight to 100% by weight, and particularly preferably 85% by weight to 100% by weight.

In the present invention, the number average molecular weight (Mn) of the polycarbonate polyol is determined from the hydroxyl value according to the following formula.
Mn = (56100 × valence) / hydroxyl value In the above formula, the valence is the number of hydroxyl groups in one molecule, and the hydroxyl value is measured according to the method B of JIS K 1557. When the polycarbonate polyol is polycarbonate diol, the valence is 2.

As the polycarbonate polyol, a polycarbonate polyol produced by a general production method such as a transesterification method between a polyol and a carbonate ester or a phosgene method can be used.
Examples of the polyol used as a raw material for the polycarbonate polyol include ethylene glycol, 1,3-propanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, 1,7-pentanediol, , 8-octanediol, 1,9-nonanediol, 1,10-decanediol, linear aliphatic diol such as 1,12-dodecanediol, 1,3-butanediol, 3-methylpentane-1, Branched aliphatic diols such as 5-diol, 2-ethylhexane-1,6-diol, 2-methyl-1,3-pentanediol, neopentyl glycol, 2-methyl-1,8-octanediol; , 3-cyclohexanediol, 1,4-cyclohexanediol, 2,2′-bis (4-hydroxycyclohexane Xylyl) propane, alicyclic diols such as 1,3-cyclohexanedimethanol, 1,4-cyclohexanedimethanol; aromatic diols such as 1,4-benzenedimethanol; polyfunctional polyols such as trimethylolpropane and pentaerythritol And so on. The said polyol can also be used as the said polycarbonate polyol using only one type, and can also be used as a polycarbonate polyol using 2 or more types together.
As the polycarbonate polyol, one or more selected from the group consisting of the linear aliphatic diol, the branched aliphatic diol, the alicyclic diol, the aromatic diol, and the polyfunctional polyol are used as raw materials. The polycarbonate polyol used as the above is preferable, the polycarbonate polyol using the linear aliphatic diol and / or the branched aliphatic diol as a raw material, and the polycarbonate using the diol containing the alicyclic diol as a raw material. It is more preferable to use a polyol together, and it is more preferable to use a polycarbonate polyol using the linear aliphatic diol as a raw material and a polycarbonate polyol using a diol containing an alicyclic diol as a raw material. .
Moreover, it is preferable that carbon number is 2-20, as for the various diol used as the raw material of polycarbonate polyol, it is more preferable that it is 3-12, and it is more preferable that it is 3-8.

[[(B-2) Other polyol compounds]]
In the present invention, (b-2) other polyol compounds can be mixed in the (b) polyol compound in addition to the (b-1) polycarbonate polyol having a number average molecular weight of 800 to 3500.
Although there is no restriction | limiting in particular as said other polyol compound, For example, polyester polyol, polyether polyol, polycarbonate polyol other than number average molecular weight 800-3500, aliphatic diol, alicyclic diol, aromatic diol, polyfunctionality A polyol etc. are mentioned. Among these, an aliphatic diol, an alicyclic diol, or a polycarbonate polyol having a number average molecular weight other than 800 to 3500 is preferable. Here, (b-2) the other polyol compound does not include the (c) acidic group-containing polyol compound described in the next section.

[(C) Acid group-containing polyol compound]
The (c) acidic group-containing polyol compound that can be used in the present invention is not particularly limited as long as it is a compound having at least one acidic group and two or more hydroxy groups. Examples of the acidic group include a carboxy group and a sulfo group. The acidic group-containing polyol compound is preferably an acidic group-containing diol compound, and more preferably an acidic group-containing diol compound having 5 to 8 carbon atoms. Specific examples of the acidic group-containing polyol compound include 2,2-dimethylolpropionic acid, 2,2-dimethylolbutanoic acid, N, N-bishydroxyethylglycine, N, N-bishydroxyethylalanine, 3,4 -Dihydroxybutanesulfonic acid, 3,6-dihydroxy-2-toluenesulfonic acid, etc. are mentioned. Although these can also use only 1 type, multiple types can also be used together. Among the acidic group-containing polyol compounds, 2,2-dimethylolpropionic acid is preferable from the viewpoint of availability.

[(D) Blocking agent]
In the present invention, as the blocking agent for the isocyanato group, one that dissociates from the isocyanato group at 80 to 180 ° C. is used. Here, the blocking agent for the isocyanato group is a compound that can react with the isocyanato group to convert the isocyanato group to another functional group, and can be reversibly converted from another functional group to the isocyanato group by heat treatment. Means.
Examples of the blocking agent that dissociates from an isocyanato group at 80 to 180 ° C. include, for example, malonic acid diester compounds such as dimethyl malonate and diethyl malonate; pyrazole compounds such as 1,2-pyrazole and 3,5-dimethylpyrazole Oxime compounds such as 1,2,4-triazole and methyl ethyl ketoxime; diisopropylamine, caprolactam and the like. These can use only 1 type and can also use multiple types together.
Among the blocking agents, from the viewpoint of dissociation temperature, one or more selected from the group consisting of oxime compounds, pyrazole compounds and malonic acid diester compounds are preferred, from the viewpoint of high storage stability and low temperature thermal crosslinkability, Pyrazole compounds are more preferable, and 3,5-dimethylpyrazole is particularly preferable.

[(A) Polyurethane prepolymer]
The polyurethane prepolymer (A) that can be used in the present invention includes (a) a polyisocyanate compound, (b) one or more polyol compounds including a polycarbonate polyol having a number average molecular weight of 800 to 3,500 (hereinafter, simply referred to as “polyol compound”). And (c) a polyurethane prepolymer obtained by reacting an acidic group-containing polyol compound and (d) an isocyanate group blocking agent that dissociates at 80 to 180 ° C. (hereinafter also simply referred to as “blocking agent”). is there.
Although there is no restriction | limiting in particular as a manufacturing method of the said polyurethane prepolymer, For example, the following methods are mentioned.
First, in the presence or absence of a urethanization catalyst, (a) a polyisocyanate compound, (b) a polyol compound, and (c) an acidic group-containing polyol compound are reacted to carry out a urethanization reaction, Thereafter, (d) a blocking agent is reacted in the presence or absence of a blocking catalyst to perform a blocking reaction to synthesize a polyurethane prepolymer (A) in which a part of the terminal isocyanate groups are blocked. .
Secondly, in the presence or absence of a blocking catalyst, (a) a polyisocyanate compound and (d) a blocking agent were reacted to perform a blocking reaction to block part of the isocyanate group. A polyisocyanate compound is synthesized, and (b) a polyol compound and (c) an acidic group-containing polyol compound are reacted in the presence or absence of a urethanization catalyst to perform a urethanation reaction, and (A) polyurethane This is a method for synthesizing a prepolymer.

The urethanization catalyst is not particularly limited, and examples thereof include salts of metals such as tin-based catalysts (trimethyltin laurate, dibutyltin dilaurate, etc.) and lead-based catalysts (lead octylate, etc.), and organic and inorganic acids, and Examples include organometallic derivatives, amine catalysts (triethylamine, N-ethylmorpholine, triethylenediamine, etc.), diazabicycloundecene catalysts, and the like. Among them, dibutyltin dilaurate is preferable from the viewpoint of reactivity.
The blocking catalyst is not particularly limited, and examples thereof include alkaline catalysts such as dibutyltin dilaurate and sodium methoxide.
The conditions for the urethanation reaction and the reaction conditions for the blocking reaction are not particularly limited, and can be appropriately selected according to the reactivity of the components used. For example, the reaction conditions for the urethanization reaction can be 3 to 15 hours at a temperature of 50 to 100 ° C. The reaction conditions for the blocking reaction can be 1 to 5 hours at a temperature of 50 to 100 ° C.
The urethanization reaction and the blocking reaction may be performed independently or continuously.

[(B) Chain extender]
The (B) chain extender that can be used in the present invention contains, as an essential component, (B-1) at least one of alkanedioic acid dihydrazide having 4 to 10 carbon atoms. (B) As the chain extender, (B-1) only an alkanedioic acid dihydrazide having 4 to 10 carbon atoms may be used, or (B-1) an alkanedioic acid dihydrazide having 4 to 10 carbon atoms and (B -2) Other chain extenders may be used in combination.

(B) The amount of the chain extender added is such that the hydrazide group (—CONHNH ₂ ) and amino group (—NH ₂ ) with respect to the free isocyanate group in the polyurethane prepolymer are 0.7 to 1.3 equivalents. The addition amount is preferable. (B-1) When alkanedioic dihydrazide having 4 to 10 carbon atoms and (B-2) other chain extender are used in combination, (B-1) 4 to 10 carbon atoms in all chain extenders The alkanedioic acid dihydrazide ratio is preferably 10 mol% or more and 90 mol% or less, more preferably 30 mol% or more and 90 mol% or less, and particularly preferably 50 mol% or more and 90 mol% or less.

  (B-1) The content of the alkanedioic acid dihydrazide having 4 to 10 carbon atoms must be 2 to 10% by weight based on the solid content in the total mass of the aqueous polyurethane resin dispersion. It is preferably contained in an amount of 2 to 8% by weight, more preferably 3 to 7% by weight, more preferably 3.5 to 6.5% by weight. More preferably. (B) Since the chain extender contains alkanedioic acid dihydrazide, the high hydrogen bonding ability of alkanedioic acid dihydrazide increases the rupture energy and hydrophilicity of the coating film, and it is possible to recoat with an aqueous cleaning solution. It becomes possible to give a coating film resistant to possible impact. Furthermore, the water resistance of the formed coating film is excellent. When the content of alkanedioic acid dihydrazide is 10% by weight or less based on the solid content of the aqueous polyurethane resin dispersion, the water swelling rate of the coating film is lowered, and the water resistance is further improved. On the other hand, when the content of alkanedioic acid dihydrazide is 2% by weight or more based on the solid content of the aqueous polyurethane resin dispersion, the breaking energy becomes sufficiently large.

  Furthermore, when the alkanedioic acid dihydrazide has 4 to 10 carbon atoms, an effect is obtained that a stable aqueous dispersion that forms a coating film having high breaking energy can be obtained. The alkanedioic acid preferably has 4 to 8 carbon atoms, more preferably 5 to 7 carbon atoms.

  Examples of the alkanedioic acid dihydrazide having 4 to 10 carbon atoms include succinic acid dihydrazide, adipic acid dihydrazide, azelaic acid dihydrazide, sebacic acid dihydrazide, and among them, adipic acid dihydrazide is preferable from the viewpoint of dispersion stability. These may be used alone or in combination of two or more.

  As (B) chain extender, in addition to C4-C10 alkanedioic acid dihydrazide, (B-2) other chain extenders may be used in combination. (B-2) Other chain extenders are not particularly limited as long as they are compounds having two or more functional groups (preferably amino groups, hydroxy groups, etc.) capable of reacting with an isocyanato group. Other chain extenders include, for example, ethylenediamine, 1,4-tetramethylenediamine, 2-methyl-1,5-pentanediamine, 1,4-butanediamine, 1,6-hexanediamine, 1,4-hexane. Diamine, 3-aminomethyl-3,5,5-trimethylcyclohexylamine, alkylenediamine such as 1,3-bis (aminomethyl) cyclohexane, xylylenediamine, piperazine, 2,5-dimethylpiperazine, diethylenetriamine, triethylenetetramine And the like, polyol compounds such as ethylene glycol, propylene glycol, 1,4-butanediol and 1,6-hexanediol, polyalkylene glycols represented by polyethylene glycol, water and the like. These may be used alone or in combination of two or more. The other chain extender is preferably a primary diamine compound, more preferably an alkylene diamine having two primary amino groups (hereinafter also referred to as “primary alkylene diamine”), and still more preferably. C1-C12 primary alkylene diamine is mentioned, Especially preferably, C5-C9 primary alkylene diamine is mentioned.

  When the chain extender contains (B-2) other chain extender, its content is preferably 0 to 3% by weight based on the solid content of the aqueous polyurethane resin dispersion, 0.5 to It is more preferably 2.5% by weight, and particularly preferably 0.5 to 2% by weight. (B-2) When the content of the other chain extender is 3% by weight or less, the breaking energy in tension of the coating film tends to increase.

  The amount of the (B) chain extender added is preferably equal to or less than the equivalent of the unblocked isocyanato group serving as the chain extension starting point in the (A) urethane prepolymer, more preferably not blocked. It is 0.7-0.99 equivalent of an isocyanato group. When a chain extender is added below the equivalent of unblocked isocyanato groups, the molecular weight of the chain-extended urethane polymer tends to be suppressed, and the obtained aqueous polyurethane resin dispersion is applied. There exists a tendency for the intensity | strength of the obtained coating film to improve more.

[Aqueous polyurethane resin dispersion]
Although it does not restrict | limit especially as a manufacturing method of the water-based polyurethane resin dispersion of this invention, For example, it can manufacture with the following method.
As described above, after the step of reacting (a) a polyisocyanate compound, (b) a polyol compound, (c) an acidic group-containing polyol compound, and (d) a blocking agent to obtain a polyurethane prepolymer, the polyurethane prepolymer The step of neutralizing acidic groups therein, the step of dispersing the polyurethane prepolymer in an aqueous medium, and the step of reacting the polyurethane prepolymer with a chain extender (B) to obtain an aqueous polyurethane resin dispersion A polyurethane resin dispersion can be produced.
In the said manufacturing method, the process of neutralizing an acidic group and the process of disperse | distributing a polyurethane prepolymer in an aqueous medium may be performed separately, and may be performed together.
In the above production method, the chain extender may be added after the polyurethane prepolymer is dispersed in the aqueous medium or during the dispersion.
Each of the above steps may be performed in an inert gas atmosphere or in the air.

In the aqueous polyurethane resin dispersion of the present invention, the total of the urethane bond content and the urea bond content in the aqueous polyurethane resin dispersion needs to be 8 to 13% by weight based on the solid content. It is preferably ˜12% by weight, more preferably 9.5 to 12% by weight, and particularly preferably 10 to 11.5% by weight. Here, the content ratio of the urethane bond means the content ratio of the urethane bond unit (-NHCOO-) in the solid content of the polyurethane resin, and the content ratio of the urea bond means the urea bond unit (in the solid content of the polyurethane resin ( -NHCONH-) means the content ratio.
When the total content of the urethane bond and the urea bond is less than 8% by weight, the coating film cannot be sufficiently formed, and there is a problem that the coating film surface becomes sticky after drying. Further, if the total content of the urethane bond and urea bond exceeds 13% by weight, the redispersibility of the paint or coating film in an aqueous solvent is poor when the aqueous polyurethane resin dispersion is applied to a substrate. In some cases, it may be difficult to remove and re-apply.

The urethane bond content in the aqueous polyurethane resin dispersion is not particularly limited as long as the sum of the urea bond content and the urea bond content is 8 to 13 wt% based on the solid content. The content of urethane bonds in the aqueous polyurethane resin dispersion is preferably 5 to 9% by weight, more preferably 5 to 8% by weight, and 6 to 8% by weight based on the solid content. Particularly preferred.
The content of urea bonds in the aqueous polyurethane resin dispersion is not particularly limited as long as the sum of the content of urethane bonds and the content of urethane bonds is 8 to 13% by weight based on the solid content. The content of urea bonds in the aqueous polyurethane resin dispersion is preferably 2 to 5% by weight, more preferably 2.5 to 4.5% by weight, based on the solid content, and 2.8 to 4%. More preferably, it is 2% by weight.
Here, the content ratio of the urethane bond and the content ratio of the urea bond in the aqueous polyurethane resin dispersion can be calculated from the charged amounts of the respective components when the aqueous polyurethane resin dispersion is prepared. It can also be calculated from the infrared absorption spectrum of the coating film.

In the aqueous polyurethane resin dispersion of the present invention, the content of carbonate bonds in the aqueous polyurethane resin dispersion needs to be 15 to 40% by weight based on the solid content, and more preferably 18 to 35% by weight. It is preferably 20 to 30% by weight, and particularly preferably. Here, the content ratio of the carbonate bond means the content ratio of the carbonate bond unit (—OCOO—) in the solid content of the polyurethane resin. The content of carbonate bonds in the aqueous polyurethane resin dispersion can be calculated from the amount of each component charged when preparing the aqueous polyurethane resin dispersion. It can also be calculated from the infrared absorption spectrum of the coating film.
When the content of the carbonate bond is less than 15% by weight, there is a problem that the obtained coating film has a low elongation at break and only a coating film that is vulnerable to impact can be obtained. Moreover, when the content rate of the carbonate bond exceeds 40% by weight, the coating film cannot be formed sufficiently, and there is a problem that the coating film surface becomes sticky even after drying.

In the aqueous polyurethane resin dispersion of the present invention, the content ratio of the isocyanate group blocked with the blocking agent needs to be 0.3 to 2.0% by weight in terms of solid content and in terms of isocyanate group. More preferably, it is 0.3 to 1.5% by weight, still more preferably 0.3 to 1.2% by weight, and particularly preferably 0.4 to 1.2% by weight. Here, the content ratio of the blocked isocyanate group means that the content ratio of the blocked isocyanate group in the solid content of the polyurethane resin is calculated as the content ratio of the isocyanate group (—NCO). . The content ratio of blocked isosinato groups in the aqueous polyurethane resin dispersion can be calculated from the charged amount of each component when the aqueous polyurethane resin dispersion is prepared.
There exists a problem that the adhesiveness to the electrodeposition coating board surface of the coating film obtained as the content rate of the said isocyanato group blocked is less than 0.3 weight% is bad. Further, when the content ratio of the blocked isocyanate group exceeds 2.0% by weight, there is a problem that the elongation at break of the obtained coating film is small and only a coating film weak against impact can be obtained.

The weight average molecular weight of the polyurethane resin needs to be 20,000 or more and 100,000 or less, preferably 30,000 or more and 85,000 or less, and 40,000 or more and 85,000 or less. Is more preferably 45,000 or more and 85,000 or less, and particularly preferably 45,000 or more and less than 70,000. When the weight average molecular weight of the polyurethane resin is 20,000 or more, the elongation at break of the obtained coating film becomes larger, and the coating film is resistant to impact. Further, when the weight average molecular weight of the polyurethane resin is 100,000 or less, the redispersibility of the paint or coating film in an aqueous solvent is further improved when the obtained polyurethane resin dispersion is applied to a substrate. Therefore, the removal becomes easy, and it becomes easier to repaint.
In particular, when the weight average molecular weight of the polyurethane resin is 45,000 or more and less than 70,000, the swelling ratio to the aqueous cleaning liquid tends to be high, and there is a tendency to be more excellent in cleaning properties, and the swelling ratio to water is low. There is a tendency to be superior.
Moreover, it is also preferable that the weight average molecular weights of a polyurethane resin are 70,000 or more and 100,000 or less, and it is more preferable that they are 70,000 or more and 85,000 or less. When the weight average molecular weight of the polyurethane resin is 70,000 or more and 100,000 or less, the swelling ratio to water tends to decrease, and the water resistance tends to be excellent. Furthermore, the elastic modulus of the coating film to be formed tends to increase, and the impact resistance of the coating film tends to be superior.
In the present invention, the weight average molecular weight is measured by gel permeation chromatography (GPC), and is a converted value obtained from a standard polystyrene calibration curve prepared in advance.

  The acid value of the polyurethane resin dispersion is not particularly limited, but is preferably 10 to 30 mgKOH / g, more preferably 13 to 26 mgKOH / g, and particularly preferably 14 to 20 mgKOH / g. . There exists a tendency for the dispersibility in an aqueous medium to improve that the acid value of the said polyurethane resin dispersion is the range of 10-30 mgKOH / g.

The polyurethane resin contained in the aqueous polyurethane resin dispersion is required to have an alicyclic structure in an amount of 18 to 30% by weight based on solid content, and (b) has an alicyclic structure derived from a polyol compound. It is essential. Furthermore, it is more preferable to have an alicyclic structure derived from polyisocyanate.
The content of the alicyclic structure in the aqueous polyurethane resin dispersion is required to be 18 to 30% by weight, more preferably 18 to 26% by weight, and 13 to 22% by weight based on the solid content. More preferably, it is particularly preferably 18 to 22% by weight. When the content of the alicyclic structure in the aqueous polyurethane resin dispersion is 18% by weight or more, the viscosity at a low solid content concentration in the coating film formation becomes high, and the dripping of the film can be prevented. Further, when the content ratio of the alicyclic structure in the aqueous polyurethane resin dispersion is 30% by weight or less, when the obtained aqueous polyurethane resin dispersion is applied to a base material, Since the redispersibility is high, the removal becomes easy, and it becomes easier to repaint.
For example, when the alicyclic structure is a cyclohexane ring, the content ratio of the alicyclic structure based on the solid content is a portion obtained by removing two hydrogen atoms from cyclohexane (the cyclohexane residue) in the solid content in the aqueous polyurethane resin dispersion. It shows how many groups are present.

〔Neutralizer〕
The aqueous polyurethane resin dispersion of the present invention preferably contains a neutralizing agent that neutralizes at least some of the acidic groups of the polyurethane resin. The neutralizing agent is used, for example, to neutralize at least some of the acidic groups of the polyurethane prepolymer and disperse the polyurethane prepolymer in the aqueous medium. The aqueous polyurethane resin dispersion is preferably obtained by reacting a polyurethane prepolymer dispersed in an aqueous medium with a chain extender.
Examples of the neutralizing agent include trimethylamine, triethylamine, tri-n-propylamine, tributylamine, triethanolamine, aminomethylpropanol, aminomethylpropanediol, aminoethylpropanediol, trihydroxymethylaminomethane, monoethanolamine. Organic amines such as triisopropanolamine, inorganic alkali salts such as potassium hydroxide and sodium hydroxide, and ammonia. These may be used alone or in combination of two or more.
Among the neutralizing agents, from the viewpoint of workability, organic amines are preferable, and triethylamine is more preferable.
The amount of neutralizing agent added is, for example, 0.4 to 1.2 equivalents, preferably 0.6 to 1.0 equivalents per equivalent of acidic group.

[Optional ingredients]
In the aqueous polyurethane resin dispersion of the present invention, amino alcohol, monoalcohol and monoamine can be used as optional components. For example, (A) a polyurethane prepolymer and amino alcohol are reacted in a state in which the polyurethane prepolymer is dispersed in water, whereby a hydroxyl group is included at the molecular terminal of the polyurethane prepolymer. As a result, the chain can be extended by a reaction with the isocyanate group that is generated by deblocking when the coating film is dried by heating. Thus, when adjusting the degree of crosslinking and controlling the elastic modulus of the coating film, it is effective to use amino alcohol. When amino alcohol is added as an optional component, the amount of amino alcohol added is preferably less than 2% by weight and more preferably less than 1% by weight based on the solid content of the aqueous polyurethane resin dispersion. Examples of amino alcohols include ethanolamine, butanolamine, hexanolamine and the like, and ethanolamine is preferred from the viewpoint of water dispersibility.

  By using monoalcohol or monoamine as an optional component, the molecular end of the polyurethane prepolymer becomes non-reactive, so that the degree of crosslinking can be adjusted and the elastic modulus of the coating film can be controlled. When monoalcohol or monoamine is added as an optional component, the addition amount of monoalcohol and monoamine is preferably less than 2% by weight, more preferably less than 1% by weight based on the solid content of the aqueous polyurethane resin. . Examples of the monoalcohol include ethanol, n-propanol, isopropanol, n-butanol, hexanol, octanol and the like, and n-butanol is more preferable from the viewpoint of ease of production. Examples of the monoamine include ethylamine, n-propylamine, isopropylamine, n-butylamine, n-hexylamine and the like.

From the viewpoint of reactivity, the monoalcohol is preferably used in the production of the (A) polyurethane prepolymer. The monoamine is preferably used after (A) the polyurethane prepolymer is dispersed in an aqueous medium, and is preferably used before (B) the chain extender is added.
When adding the said monoalcohol, it is preferable to make it react in the state heated at 60 degreeC or more from the point which improves a reaction rate. When adding the said monoamine, it is preferable to make it react in the state of 60 degrees C or less from the point which suppresses a side reaction.

[Aqueous medium]
In the present invention, the polyurethane resin is dispersed in an aqueous medium. Examples of the aqueous medium include water and a mixed medium of water and a hydrophilic organic solvent.
Examples of the water include clean water, ion-exchanged water, distilled water, and ultrapure water, preferably considering the availability of polyurethane resin particles due to the availability and the influence of salt. Ion exchange water is mentioned.

Examples of the hydrophilic organic solvent include lower monohydric alcohols such as methanol, ethanol and propanol; polyhydric alcohols such as ethylene glycol and glycerin; N-methylmorpholine, dimethyl sulfoxide, dimethylformamide, N-methylpyrrolidone, N- Examples include aprotic hydrophilic organic solvents such as ethyl pyrrolidone, dipropylene glycol dimethyl ether (DMM), and β-alkoxypropionic acid amide.
The amount of the hydrophilic organic solvent in the aqueous medium is preferably 0 to 20% by weight, and more preferably 0 to 10% by weight.

The coating film obtained by applying the aqueous polyurethane resin dispersion of the present invention is excellent in water resistance and solvent resistance, and is excellent in adhesion to the electrodeposition coating film.
There are two types of electrodeposition coatings, anionic and cationic. Generally, the cationic type uses a modified epoxy resin as a base resin and is crosslinked with isocyanate, whereas the anionic type is crosslinked by oxidative polymerization. Since the secondary hydroxyl group produced by ring opening of the epoxy group remains in the cationic type and the carboxyl group is introduced in the anionic type, the blocking agent is used in the heat drying step of the aqueous polyurethane resin dispersion of the present invention. Is considered to cause a cross-linking reaction with a free isocyanato group formed by dissociation. Such electrodeposition coatings are used in heavy machinery, industrial machinery such as agricultural machinery, vehicles such as automobiles and bicycles, building materials such as prefabricated steel frames, fire doors and sashes, electrical equipment such as switchboards, elevators, and microwave ovens. Yes.

The aqueous polyurethane resin dispersion of the present invention can be applied, for example, on a substrate on which the electrodeposition coating film is formed using a coating apparatus or the like and baked at a temperature of 80 to 250 ° C. A drying step can be provided before the baking step, or baking can be performed at a time after the aqueous polyurethane resin dispersion is applied and dried, and another coating material is applied and dried.
When the applied aqueous polyurethane resin dispersion is baked, the blocking agent of the blocked isocyanate group is dissociated to form a cross-linked structure with an acidic group or other isocyanate group. A coating film having high hardness can be formed.
A general method can be used for the baking step and the drying step.

[Coating material composition]
As the coating material composition of the present invention, the above-mentioned aqueous polyurethane resin dispersion may be used as it is, or a coating material composition may be prepared by adding various additives.
The additives include plasticizers, antifoaming agents, leveling agents, fungicides, rust inhibitors, matting agents, flame retardants, tackifiers, thixotropic agents, lubricants, antistatic agents, thickeners, thickeners. Examples thereof include a viscosity agent, a diluent, a pigment, a dye, an ultraviolet absorber, a light stabilizer, an antioxidant, and a filler.
The coating material composition of the present invention can be applied to coating (film formation) of various substrates such as metal, ceramic, synthetic resin, nonwoven fabric, woven fabric, knitted fabric, and paper.

[Polyurethane resin film]
The polyurethane resin film of the present invention (hereinafter also referred to as “polyurethane film”) is produced by heating and drying a composition containing the aqueous polyurethane resin dispersion.
As the composition containing the aqueous polyurethane resin dispersion, the above-mentioned aqueous polyurethane resin dispersion may be used as it is, or a composition prepared by adding various additives to the aqueous polyurethane resin dispersion may be used. .
The additives include plasticizers, antifoaming agents, leveling agents, fungicides, rust inhibitors, matting agents, flame retardants, tackifiers, thixotropic agents, lubricants, antistatic agents, thickeners, thickeners. Examples thereof include a viscosity agent, a diluent, a pigment, a dye, an ultraviolet absorber, a light stabilizer, an antioxidant, and a filler.

  The method for producing the polyurethane resin film is not particularly limited. For example, the above-described aqueous polyurethane resin dispersion is coated on a releasable substrate using various coating apparatuses, and then dried to release the releasability. The method of peeling a base material and the said polyurethane resin film is mentioned.

The releasable substrate is not particularly limited, and examples thereof include a glass substrate, a plastic substrate such as polyethylene terephthalate and polytetrafluoroethylene, and a metal substrate. The peelable substrate is obtained by treating the surface of each substrate with a release agent.
Although it does not restrict | limit especially as said coating device, For example, a bar coater, a roll coater, a gravure roll coater, an air spray etc. are mentioned.

  Although it does not restrict | limit especially as thickness of the polyurethane resin film of this invention, 0.01 mm-0.5 mm are preferable.

Next, the present invention will be described in more detail with reference to examples and comparative examples.
The physical properties were measured as follows.
(1) Hydroxyl value: Measured according to JIS K 1557 method B.
(2) Free isocyanate group content: 0.5 g of the reaction mixture after completion of the urethanization reaction was sampled and added to a mixed solution of 0.1 mL / L (liter) of dibutylamine-tetrahydrofuran (THF) solution and 10 mL of THF. Then, unconsumed dibutylamine was titrated with 0.1 mol / L hydrochloric acid. From the difference between the titration value and the blank experiment, the molar concentration of the isocyanate group remaining in the reaction mixture was calculated. The molar concentration was converted to the weight fraction of isocyanato groups to obtain the free isocyanate group content. The indicator used for titration is bromophenol blue.
(3) Acid value: 100 g of the aqueous polyurethane resin dispersion was diluted 10 times with pure water, and 10 g of acetic acid was mixed and stirred at room temperature. The precipitated solid was filtered with a 120 mesh stainless steel wire mesh. 600 g of water was poured into the obtained solid, stirred for 30 minutes at room temperature and allowed to stand, and then the solid was filtered through a 120-mesh stainless wire mesh. The same operation was repeated 5 times. After the remaining solid was dried at 60 ° C. for 24 hours, the acid value was measured according to the indicator titration method of JIS K 1557.
(4) The content of urethane bonds based on solid content (urethane bond content) and the content of urea bonds based on solid content (urea bond content) are determined from the proportion of each raw material in the aqueous polyurethane resin dispersion, The molar concentration (mole / g) of the urea bond was calculated and expressed as a weight fraction. The weight fraction was based on the solid content of the aqueous polyurethane resin dispersion. An aqueous polyurethane resin dispersion (0.3 g) was applied to a glass substrate with a thickness of 0.2 mm, and the weight remaining after heating and drying at 140 ° C. for 4 hours was measured. The partial concentration was used. The weight fraction was calculated using the product of the total weight of the aqueous polyurethane resin dispersion and the solid content concentration as the solid content weight.
(5) For the solid content of carbonate bonds (carbonate bond content), the molar concentration of carbonate bonds (mol / g) is calculated from the charge ratio of each raw material of the aqueous polyurethane resin dispersion, and converted to the weight fraction. I wrote what I did. The weight fraction was calculated based on the solid content of the aqueous polyurethane resin dispersion by the same method as the content of the urethane bond based on the solid content.
(6) The content of the alicyclic structure based on the solid content (alicyclic structure content) represents the weight fraction of the alicyclic structure calculated from the charge ratio of each raw material of the aqueous polyurethane resin dispersion. The weight fraction was calculated based on the solid content of the aqueous polyurethane resin dispersion by the same method as the content of the urethane bond based on the solid content.
(7) The weight average molecular weight of the polyurethane resin in the aqueous polyurethane resin dispersion was measured by gel permeation chromatography (GPC), and a conversion value obtained from a standard polystyrene calibration curve prepared in advance was described.
(8) The content of the isocyanate group to which the blocking agent based on the solid content in the aqueous polyurethane resin dispersion is bound (in terms of isocyanate group, blocked NCO content) is calculated by setting the charged molar amount of the blocking agent to the weight of the isocyanate group. The ratio divided by the solid content weight of the aqueous polyurethane resin dispersion was expressed. The solid content weight of the aqueous polyurethane resin dispersion was calculated by the same method as the content based on the solid content of the urethane bond.
(9) The content of alkanedioic acid dihydrazide based on the solid content (alkanedioic acid dihydrazide content) represents the weight fraction of alkanedioic acid dihydrazide calculated from the charge ratio of each raw material of the aqueous polyurethane resin dispersion. The weight fraction was calculated based on the solid content of the aqueous polyurethane resin dispersion by the same method as the content of the urethane bond based on the solid content.

(10) Swelling ratio of coating film to water: 0.3 mL of aqueous polyurethane resin dispersion was applied on a glass plate at a thickness of 72 μm (bar coater # 36) until the solid content concentration of the coating film reached 90%. Heat drying at 50 ° C. This coating film was immersed in ion exchange water at 28 ° C. for 6 hours, and the coating film weight before and after immersion was measured. The swelling ratio of the coating film into water was calculated by the following formula. The solid content concentration of the dried coating film was calculated by the same method as the content ratio of the urethane bond based on the solid content.
(Swelling ratio) = [(weight of coating film after water immersion) − (weight of coating film before water immersion)] / (weight of coating film before water immersion) × 100
(11) Swelling ratio of dry coating film to aqueous cleaning solution: Aqueous cleaning solutions containing 5%, 4%, 1% and 90% of butyl cellosolve, isopropanol, dimethylethanolamine and ion-exchanged water on a weight basis were prepared. . An aqueous polyurethane resin dispersion (0.3 mL) was coated on a glass plate at a thickness of 72 μm (bar coater # 36), and dried by heating at 50 ° C. until the solid content concentration of the coating film reached 90%. This coating film was immersed in an aqueous cleaning solution at 28 ° C. for 15 seconds, and the coating film weight before and after immersion was measured. The swelling ratio of the coating film into the aqueous cleaning solution was calculated by the following formula. The solid content concentration of the dried coating film was calculated by the same method as the content ratio of the urethane bond based on the solid content.
(Swelling ratio) = [(weight of coating film after immersion in aqueous cleaning liquid) − (weight of coating film before immersion in aqueous cleaning liquid)] / (weight of coating film before immersion in aqueous cleaning liquid) × 100
(12) The elastic modulus, tensile strength, and elongation at break of the polyurethane resin film were measured by a method based on JIS K 7311. The measurement conditions were a measurement temperature of 23 ° C., a humidity of 50%, and a tensile speed of 100 mm / min.
(13) The breaking energy was obtained by integrating the stress from the zero elongation of the elongation-stress curve to the elongation at break.
(14) Adhesion to the electrodeposition layer (electrodeposition coating film) surface was evaluated as follows. An aqueous polyurethane resin dispersion was applied to a thickness of 0.2 mm on an automobile steel plate cationic electrodeposition coating plate (manufactured by Nippon Test Panel Co., Ltd.) and dried by heating at 120 ° C for 3 hours and at 140 ° C for 30 minutes. A cross-cut peel test was carried out. The coating film was cut at an interval of 1 mm vertically and horizontally in an area of 5 mm × 5 mm, and after sticking an adhesive tape, the number of cells remaining on the surface of the electrodeposition layer when peeled was visually evaluated. For example, the case where 15 out of 25 remained was described as 15/25.
(15) The viscosity at each solid content concentration in film formation was evaluated as follows. The aqueous polyurethane resin dispersion was concentrated while stirring to each solid content concentration, and the viscosity of the obtained concentrated liquid at 25 ° C. was measured with a rheometer (ARES-RFS manufactured by TA Instruments). A cone plate having a diameter of 25 mm and a cone angle of 0.03998 rad was used, and the shear rate was set to 0.1 sec ⁻¹ . In order to prevent drying during measurement, the interface between the sample and air was covered with Shin-Etsu Silicone KF-96A-6CS.
(16) The viscosity increase ratio was calculated by calculating how many times the viscosity at a solid content concentration of 45% by weight and the viscosity at a solid content concentration of 47% by weight were higher than the viscosity at a solid content concentration of 30% by weight, respectively.

[Example 1]
[Production of aqueous polyurethane resin dispersion (1)]
In a reaction vessel into which a stirrer, a reflux condenser and a thermometer were inserted, ETERNCOLLUH-300 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2906; hydroxyl value 38.6 mgKOH / g; 1,6-hexanediol and carbonic acid 270 g of polycarbonate diol obtained by reacting with dimethyl), ETERNACOLL UM90 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 916; hydroxyl value 122.5 mg KOH / g; 1,4-cyclohexanedimethanol and 1,6 -30.2 g of hexanediol (3: 1 in molar ratio) and polycarbonate diol obtained by reacting dimethyl carbonate, 20.9 g of 2,2-dimethylolpropionic acid (DMPA) and N-methylpyrrolidone (NMP) 149g He was charged under a nitrogen gas stream. 125 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.35 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and a urethanization reaction was performed over 5 hours. Thereafter, 4.33 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The content of free NCO groups at the end of the urethanization reaction was 2.24% by weight. From the mixture of 15.6 g of triethylamine added to and mixed with the reaction mixture, 566 g was extracted and added to 850 g of water under vigorous stirring. Subsequently, 23.9 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (1) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (1), the swelling rate in washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (A)]
The aqueous polyurethane resin dispersion (1) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (A). The film thickness of the obtained polyurethane film (A) is 0.15 mm, and the tensile properties are shown in Table 2.

[Example 2]
[Production of aqueous polyurethane resin dispersion (2)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-300 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2906; hydroxyl value 38.6 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 247 g, ETERRNACOLL UM90 (registered trademark; Ube Industries polycarbonate diol; number average molecular weight 916; hydroxyl value 122.5 mg KOH / g; 1,4-cyclohexanedimethanol and 1,6-hexanediol (mol) Polycarbonate diol obtained by reacting 3: 1) and dimethyl carbonate in a ratio) 54.3 g, 2,2-dimethylolpropionic acid (DMPA) 18.4 g and N-methylpyrrolidone (NMP) 146 g in a nitrogen stream Prepared below. 126 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.38 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C. to carry out a urethanization reaction over 5 hours. Thereafter, 6.67 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.07% by weight. 540 g was extracted from the mixture obtained by adding and mixing 13.9 g of triethylamine to the reaction mixture, and added to 820 g of water under strong stirring. Subsequently, 21.5 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (2) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (2), the swelling rate in the washing water, the result of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (B)]
The aqueous polyurethane resin dispersion (2) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (B). The film thickness of the obtained polyurethane film (B) is 0.15 mm, and the tensile properties are shown in Table 2.

[Example 3]
[Production of aqueous polyurethane resin dispersion (3)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-300 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2906; hydroxyl value 38.6 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. 207 g of polycarbonate diol obtained in this manner, ETERNACOLL UM90 (registered trademark; polycarbonate diol manufactured by Ube Industries, Ltd.); number average molecular weight 916; hydroxyl value 122.5 mg KOH / g; 1,4-cyclohexanedimethanol and 1,6-hexanediol (mol) Polycarbonate diol obtained by reacting 3: 1) and dimethyl carbonate in a ratio) 97.2 g, 2,2-dimethylolpropionic acid (DMPA) 19.4 g and N-methylpyrrolidone (NMP) 152 g Prepared below. 144 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.38 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C. to carry out a urethanization reaction over 5 hours. Thereafter, 7.69 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued for 1.5 hours at the same temperature to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.28% by weight. From the mixture obtained by adding and mixing 14.6 g of triethylamine to the reaction mixture, 566 g was extracted and added to 870 g of water under strong stirring. Subsequently, 24.9 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (3) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (3), the swelling rate in washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (C)]
The aqueous polyurethane resin dispersion (3) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and at 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (C). The film thickness of the obtained polyurethane film (C) is 0.15 mm, and the tensile properties are shown in Table 2.

[Example 5]
[Production of aqueous polyurethane resin dispersion (4)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-300 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2906; hydroxyl value 38.6 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. 300 g of polycarbonate diol obtained in this manner, ETERNACOLL UC-100 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 969; hydroxyl value 115.8 mg KOH / g; 1,4-cyclohexanedimethanol and dimethyl carbonate are reacted. Polycarbonate diol) 25.1 g, 2,2-dimethylolpropionic acid (DMPA) 22.0 g and N-methylpyrrolidone (NMP) 160 g were charged under a nitrogen stream. 132 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.40 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C. to carry out a urethanization reaction over 5 hours. Thereafter, 9.90 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 1.84% by weight. 600 g was extracted from the mixture obtained by adding 16.5 g of triethylamine to the reaction mixture, and added to 900 g of water under strong stirring. Subsequently, 21.2 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (4) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (4), the swelling rate in the washing water, the result of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (D)]
The aqueous polyurethane resin dispersion (4) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (D). The film thickness of the obtained polyurethane film (D) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 1]
[Production of aqueous polyurethane resin dispersion (5)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2000; hydroxyl value 56.1 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 272 g, 2,2-dimethylolpropionic acid (DMPA) 18.5 g and N-methylpyrrolidone (NMP) 176 g were charged under a nitrogen stream. 125 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.3 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C. to carry out a urethanization reaction over 5 hours. Thereafter, 10.4 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued for 1.5 hours at the same temperature to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 1.78% by weight. 564 g was extracted from the mixture obtained by adding and mixing 13.9 g of triethylamine to the reaction mixture, and added to 870 g of water under strong stirring. Then, 36.5 g of 35% by weight 2-methyl-1,5-pentanediamine (MPMD) aqueous solution was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (5) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (5), the swelling rate in the washing water, the result of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (E)]
The aqueous polyurethane resin dispersion (5) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (E). The film thickness of the obtained polyurethane film (E) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 2]
[Production of aqueous polyurethane resin dispersion (6)]
In a reaction vessel in which a stirrer, a reflux condenser and a thermometer were inserted, ETERNCOLLUH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 1986; hydroxyl value 56.4 mgKOH / g; 1,6-hexanediol and carbonic acid (Polycarbonate diol obtained by reacting with dimethyl) 310 g, 2,2-dimethylolpropionic acid (DMPA) 18.3 g, and N-methylpyrrolidone (NMP) 154 g were charged under a nitrogen stream. Thereafter, the mixture was heated and stirred at 60 ° C. to confirm that DMPA was dissolved. 133 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.38 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C. to carry out a urethanization reaction over 5 hours. Thereafter, 11.2 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued for 1.5 hours at the same temperature to obtain a polyurethane prepolymer. The content ratio of free isocyanate groups at the end of the urethanization reaction was 1.79% by weight. The reaction mixture was cooled to 80 ° C., 601 g was extracted from the mixture obtained by adding and mixing 13.9 g of triethylamine, and added to 869 g of water under strong stirring. A chain extension reaction was carried out by adding 10.7 g of a 35% by weight hydrazine (HDZ) aqueous solution to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (6) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (6), the swelling rate in the washing water, the result of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (F)]
The aqueous polyurethane resin dispersion (6) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (F). The film thickness of the obtained polyurethane film (F) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 3]
[Production of water-based polyurethane resin (7)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2000; hydroxyl value 56.1 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 261 g, 2,2-dimethylolpropionic acid (DMPA) 17.5 g and N-methylpyrrolidone (NMP) 166 g were charged under a nitrogen stream. 115 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.3 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and stirring was continued for 5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.50% by weight. 512 g was extracted from the mixture obtained by adding and mixing 13.3 g of triethylamine to the reaction mixture, and added to 850 g of water under strong stirring. Subsequently, 48.0 g of 35% by weight 2-methyl-1,5-pentanediamine (MPMD) aqueous solution was added to carry out chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (7) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (7), the swelling rate in washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (G)]
The aqueous polyurethane resin dispersion (7) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (G). The film thickness of the obtained polyurethane film (G) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 4]
[Production of water-based polyurethane resin (8)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2000; hydroxyl value 56.1 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 261 g, 2,2-dimethylolpropionic acid (DMPA) 17.5 g and N-methylpyrrolidone (NMP) 166 g were charged under a nitrogen stream. 115 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.3 g of dibutyltin dilaurate (catalyst) were added, and the mixture was heated to 90 ° C. and stirred for 5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.50% by weight. 512 g was extracted from the mixture obtained by adding and mixing 13.3 g of triethylamine to the reaction mixture, and added to 850 g of water under strong stirring. Next, 33.6 g of 35% by weight 2-methyl-1,5-pentanediamine (MPMD) aqueous solution was added to carry out chain extension reaction, and 22.3 g of 35% by weight butylamine (BA) aqueous solution was added to seal the molecular ends. Reaction was performed to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (8) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (8), the swelling rate in the washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Manufacture of polyurethane film (H)]
The aqueous polyurethane resin dispersion (8) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (H). The film thickness of the obtained polyurethane film (H) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 5]
[Production of aqueous polyurethane resin dispersion (9)]
In a reaction vessel similar to that in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2036; hydroxyl value 55.1 mg KOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) obtained in this manner, 2,2-dimethylolpropionic acid (DMPA) 18.6 g and N-methylpyrrolidone (NMP) 154 g were charged under a nitrogen stream. 130 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.37 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and a urethanization reaction was carried out over 5 hours. Thereafter, 1.26 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.58% by weight. 572 g was extracted from the mixture obtained by adding and mixing 14.7 g of triethylamine to the reaction mixture, and added to 870 g of water under strong stirring. Subsequently, 28.4 g of adipic acid dihydrazide (ADH) was added to perform a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (9) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (9), the swelling rate in the washing water, the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (I)]
The aqueous polyurethane resin dispersion (9) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (I). The film thickness of the obtained polyurethane film (I) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 6]
[Production of aqueous polyurethane resin dispersion (10)]
In a reaction vessel similar to that in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2036; hydroxyl value 55.1 mg KOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 300 g, 2,2-dimethylolpropionic acid (DMPA) 17.1 g and N-methylpyrrolidone (NMP) 155 g were charged under a nitrogen stream. 125 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.37 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and a urethanization reaction was performed over 5 hours. Thereafter, 2.44 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued for 1.5 hours at the same temperature to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.31% by weight. 568 g was extracted from the mixture obtained by adding and mixing 13.5 g of triethylamine to the reaction mixture, and added to 860 g of water under strong stirring. Subsequently, 25.3 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (10) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (10), the swelling rate in washing water, the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (J)]
The aqueous polyurethane resin dispersion (10) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (J). The film thickness of the obtained polyurethane film (J) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 7]
[Production of aqueous polyurethane resin dispersion (11)]
In the same reaction vessel as in Example 1, ETERRNACOLL UH-300 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2906; hydroxyl value 38.6 mgKOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 331 g, 2,2-dimethylolpropionic acid (DMPA) 21.9 g and N-methylpyrrolidone (NMP) 159 g were charged under a nitrogen stream. 125 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.39 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and a urethanization reaction was performed over 5 hours. Thereafter, 9.66 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 1.75% by weight. 611 g was extracted from the mixture obtained by adding and mixing 16.6 g of triethylamine to the reaction mixture, and added to 890 g of water under strong stirring. Subsequently, 20.3 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (11) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (11), the swelling rate in the washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Manufacture of polyurethane film (K)]
The aqueous polyurethane resin dispersion (11) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (K). The film thickness of the obtained polyurethane film (K) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 8]
[Production of aqueous polyurethane resin dispersion (12)]
In a reaction vessel similar to that in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2036; hydroxyl value 55.1 mg KOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 302 g, 2,2-dimethylolpropionic acid (DMPA) 17.1 g and N-methylpyrrolidone (NMP) 150 g were charged under a nitrogen stream. 124 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.35 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and a urethanization reaction was performed over 5 hours. Thereafter, 4.15 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 2.20% by weight. 551 g was extracted from the mixture obtained by adding and mixing 13.4 g of triethylamine to the reaction mixture, and added to 850 g of water under strong stirring. Subsequently, 23.2 g of adipic acid dihydrazide (ADH) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (12) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (12), the swelling rate in washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (L)]
The aqueous polyurethane resin dispersion (12) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (L). The film thickness of the obtained polyurethane film (L) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 9]
[Production of aqueous polyurethane resin dispersion (13)]
An aqueous polyurethane resin dispersion was produced in the same manner as in Example 1 except that 15.9 g of 2-methyl-1,5-pentanediamine (MPMD) was used as the chain extender. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (13) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (13), the swelling rate in the washing water, the result of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (M)]
The aqueous polyurethane resin dispersion (13) was applied as a coating material composition on a glass plate, and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (M). The film thickness of the obtained polyurethane film (M) is 0.15 mm, and the tensile properties are shown in Table 2.

[Comparative Example 10]
[Production of aqueous polyurethane resin dispersion (14)]
In a reaction vessel similar to that in Example 1, ETERRNACOLL UH-200 (registered trademark; polycarbonate diol manufactured by Ube Industries; number average molecular weight 2036; hydroxyl value 55.1 mg KOH / g; 1,6-hexanediol and dimethyl carbonate were reacted. Polycarbonate diol) 69.9 g, polypropylene glycol (number average molecular weight 2000, hydroxyl value 56.1 mg KOH / g) 69.1 g, 2,2-dimethylolpropionic acid (DMPA) 9.19 g and N-methylpyrrolidone (NMP) 69.4 g was charged under a nitrogen stream. 64.2 g of 4,4′-dicyclohexylmethane diisocyanate (hydrogenated MDI) and 0.17 g of dibutyltin dilaurate (catalyst) were added and heated to 90 ° C., and a urethanization reaction was performed over 5 hours. Thereafter, 5.50 g of 3,5-dimethylpyrazole (DMPZ) was injected, and stirring was continued at the same temperature for 1.5 hours to obtain a polyurethane prepolymer. The free NCO group content at the end of the urethanization reaction was 1.97% by weight. 269 g was extracted from the mixture obtained by adding and mixing 7.08 g of triethylamine to the reaction mixture, and added to 360 g of water under strong stirring. Subsequently, 19.9 g of a 35% by weight 2-methyl-1,5-pentanediamine aqueous solution (MPMD) was added to carry out a chain extension reaction to obtain an aqueous polyurethane resin dispersion. Content ratio of urethane bond, content ratio of urea bond, content ratio of carbonate bond, weight average molecular weight, content ratio of alicyclic structure, acid value, content of alkanedioic acid dihydrazide in the obtained aqueous polyurethane resin dispersion (14) The ratio and the content ratio of blocked isocyanate groups (in terms of isocyanate groups) are shown in Table 1. Table 2 shows the water swelling rate of the coating film of the aqueous polyurethane resin dispersion (14), the swelling rate in the washing water, the results of the adhesion test to the electrodeposition surface, and the viscosity.

[Production of polyurethane film (N)]
The aqueous polyurethane resin dispersion (14) was applied as a coating material composition on a glass plate and dried at 120 ° C. for 3 hours and 140 ° C. for 30 minutes to obtain a good coating layer. The obtained coating layer was peeled off to produce a polyurethane film (N). The film thickness of the obtained polyurethane film (N) is 0.15 mm, and the tensile properties are shown in Table 2. In Table 2, the swelling ratio of the polyurethane film (N) in the cleaning solution was not measurable because no coating film remained.

  The aqueous polyurethane resin dispersion of the present invention can be widely used as a raw material for paints and coating agents.

Claims (7)

(A) a polyisocyanate compound, (b) one or more polyol compounds including a polycarbonate polyol having a number average molecular weight of 800 to 3,500, (c) an acidic group-containing polyol compound, and (d) dissociating at 80 to 180 ° C. A polyurethane resin obtained by reacting (A) a polyurethane prepolymer obtained by reacting an isocyanate group blocking agent with (B) a chain extender having reactivity with the isocyanate prepolymer of the polyurethane prepolymer, An aqueous polyurethane resin dispersion dispersed in an aqueous medium,
The (b) polyol compound contains a polyol containing an alicyclic structure, and the (B) chain extender contains an alkanedioic acid dihydrazide having 4 to 10 carbon atoms,
The polyurethane resin has a urethane bond content ratio and a urea bond content ratio of 8 to 13 wt% based on solid content, a carbonate bond content ratio of 15 to 40 wt% based on solid content, The ring structure content ratio is 18 to 30% by weight based on the solid content, and the content ratio of the isocyanate group to which the blocking agent is bonded is 0.3 to 2.0% by weight based on the solid content and in terms of isocyanate group, An aqueous polyurethane resin dispersion in which an alkanedioic acid dihydrazide having 4 to 10 carbon atoms is 2 to 10% by weight on a solid basis and a weight average molecular weight is 20,000 to 100,000.   The aqueous polyurethane resin dispersion according to claim 1, wherein the alkanedioic acid dihydrazide having 4 to 10 carbon atoms is adipic acid dihydrazide.   The aqueous polyurethane resin dispersion according to claim 1, wherein the acid value is 10 to 30 mg KOH / g.   (A) The water-based polyurethane resin dispersion as described in any one of Claims 1-3 whose polyisocyanate compound is alicyclic diisocyanate.   (D) The aqueous polyurethane resin dispersion according to any one of claims 1 to 4, wherein the blocking agent is at least one selected from an oxime compound, a pyrazole compound, and a malonic ester compound.   The coating material composition containing the water-based polyurethane resin dispersion as described in any one of Claims 1-5.   The polyurethane resin film manufactured by heat-drying the composition containing the water-based polyurethane resin dispersion as described in any one of Claims 1-5.