KR20160136502A - Method for manufacturing uv curable oligomer using long chain dicarboxylic acid derived from biomass resources, and uv curable coating composition - Google Patents

Abstract

The present invention relates to a process for producing an ultraviolet curable oligomer using a long chain dicarboxylic acid derived from biomass and an ultraviolet curable coating composition using the ultraviolet curable oligomer. The ultraviolet curable coating material of the present invention is a conventional material recycling type material By using a urethane acrylate oligomer prepared from vegetable oil in an ultraviolet curable coating agent, a very environmentally friendly coating agent can be provided.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an ultraviolet-curable oligomer using a long-chain dicarboxylic acid derived from biomass, and an ultraviolet curable coating composition using the same. BACKGROUND ART < RTI ID = 0.0 >

The present invention relates to the preparation of long chain dicarboxylic acid-derived ultraviolet curable oligomers derived from biomass and an ultraviolet curable coating composition using the same.

Polyester / polyurethane / polyamide / acrylic polymer produced by using long chain dicarboxylic acid can be used variously in coatings and the like, and is particularly applicable to an ultraviolet ray curable coating agent. In general, many commercial products, including optical functional products such as lenses, optical screens, optical filters, prism sheets, and the like, are made of thermosetting or thermoplastic polymers. For example, polycarbonate, polymethylmethacrylate, polyurethane, polyester, phenol resin, cellulose resin, polystyrene, styrene copolymer, epoxy resin and the like. However, many thermosetting and thermoplastic polymers as described above are excellent in dimensional stability, transparency and impact resistance, but are poor in abrasion resistance and solvent resistance, and products made from the polymers are vulnerable to scratches and abrasion. For this reason, the above-mentioned resin products are subjected to wear-resistant hard coating on their surfaces in order to protect them from physical or mechanical damage.

Of these, ultraviolet curable acrylic coating agents can be cured in a short time, can be cured at room temperature, and are used as surface protective coatings for various plastic products. In order to apply such an ultraviolet curable acrylic coating agent, it is required to have excellent hardness, excellent adhesion to a resin and a plastic film, surface hardness and appearance of a coating film.

A generally used ultraviolet curable acrylic coating agent is a composition comprising an acrylic polymer, a urethane polymer, an epoxy polymer, a silicon polymer, or a silica compound as a binder in the form of a monomer or oligomer, and adding a photoinitiator and an additive thereto And cured by light irradiation such as ultraviolet rays to have hard coatability.

The materials used for the conventional coating materials are derived from petroleum, and it is a big problem that environmental problems such as depletion of petroleum resources and carbon dioxide emission and environmental hormone-induced harmful substances are discharged, so that alternative technologies and products are urgently needed There is a need to be established. In the future, as prices of petroleum-derived products surge and petroleum resources become depleted, demand for alternative products using endless biomass resources is expected to increase. Efforts to replace existing petrochemical-based chemical industries with biomass- Trend.

The prior art related to the present invention is Korea Unexamined Patent Publication No. 2010-0072566, but the yield is low, and satisfactory adhesion and pencil hardness are not exhibited.

Accordingly, the present inventors have completed the present invention by synthesizing a polyester polyol using a long-chain dicarboxylic acid derived from biomass and using it for the preparation of an ultraviolet curable oligomer.

Accordingly, an object of the present invention is to provide a process for producing a urethane acrylate oligomer which is an ultraviolet curable coating material raw material having excellent pencil hardness and adhesion.

In order to achieve the above object, the present invention provides a process for producing a photocurable oligomer comprising the steps of:

a) adding an aliphatic diol to a biomass-derived dicarboxylic acid and performing an esterification reaction at 150 to 250 ° C to prepare a polyester polyol;

b) adding a polyisocyanate to the polyester polyol and reacting the polyester polyol at a temperature of 40 to 90 ° C for 2 to 24 hours to prepare a urethane prepolymer; And

c) adding acrylate to the urethane prepolymer to prepare a urethane acrylate oligomer.

In one embodiment of the present invention, the dicarboxylic acid may be represented by the following general formula (1).

≪ Formula 1 >

In Formula 1, n is an integer of 9 to 13.

In another embodiment of the present invention, the aliphatic diol is selected from the group consisting of ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, And at least one diol selected from the group consisting of hexanediol, neopentyl glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, dipropylene glycol, and tripropylene glycol.

In another embodiment of the present invention, the polyester polyol may have a number average molecular weight of 400 to 8,000.

In another embodiment of the present invention, the polyisocyanate is selected from the group consisting of hexamethylene diisocyanate (HDI), dimer acid diisocyanate, lysine diisocyanate, isophorone diisocyanate (IPDI), hydrogenated diphenylmethane diisocyanate (H12MDI) And may be at least one polyisocyanate selected from the group consisting of rhenylene diisocyanate, cyclohexane diisocyanate, 1,3-bis (isocyanatomethyl) cyclohexane, and norbornene diisocyanate.

Also, the present invention can provide an ultraviolet curable coating composition comprising 40 to 80 parts by weight of the urethane acrylate oligomer, 1 to 15 parts by weight of the photoinitiator, and 0.1 to 10 parts by weight of the additive for surface control.

The present invention relates to a process for producing a polyester polyol by using a dicarboxylic acid derived from biomass, adding a polyisocyanate to the polyester polyol to prepare a urethane prepolymer, adding urethane acrylate oligomer to the urethane prepolymer By incorporating the urethane acrylate oligomer into the coating agent, it is possible to provide a coating composition having both excellent adhesion and pencil hardness.

The present invention relates to a process for the preparation of a UV-curable coating composition using a petroleum-derived product, and a process for producing the same. The process comprises the steps of: preparing a polyester polyol from a biomass-derived long chain dicarboxylic acid And ultraviolet curable oligomers having various acrylic functional groups are synthesized by using the synthesized oligomers. It is an object of the present invention to provide an environmentally friendly ultraviolet curable coating composition having excellent appearance and surface hardness by using ultraviolet curable oligomers synthesized using raw materials derived from biomass.

That is, the present invention provides a process for producing an ultraviolet-curable oligomer comprising the steps of:

a) preparing an polyester polyol by adding an aliphatic diol to a dicarboxylic acid and performing an esterification reaction at 150 to 250 ° C;

b) adding a polyisocyanate to the polyester polyol and reacting the polyester polyol at a temperature of 40 to 90 ° C for 2 to 24 hours to prepare a urethane prepolymer; And

c) adding acrylate to the urethane prepolymer to prepare a urethane acrylate oligomer.

The present invention can provide an ultraviolet curable coating composition comprising the urethane acrylate oligomer, the photoinitiator, the additive for controlling the surface, and the organic solvent prepared by the above method.

The polyester polyol used in the preparation of the urethane acrylate oligomer is also characterized in that it contains a long chain dicarboxylic acid derived from a biomass represented by the following formula (1).

≪ Formula 1 >

In Formula 1, n is an integer of 9 to 13.

The ultraviolet curing type urethane acrylate oligomer of the present invention is produced by first synthesizing a urethane prepolymer (B) having an isocyanate group at a molecular end obtained by reacting a polyester polyol (A) with a polyisocyanate, and then adding a (meth) To obtain a urethane acrylate oligomer (C) having a (meth) acrylic group at the molecular end. The ultraviolet curing type coating agent (D) was prepared using the obtained urethane acrylate and then coated on a PET film to measure the physical properties of the cured coating film.

(A) Polyester Polyol

The polyester polyol can be prepared by an esterification reaction between a dicarboxylic acid and a diol. The dicarboxylic acid used in the production of the polyester polyol is a dicarboxylic acid having no aromatic skeleton, and examples thereof include succinic acid, adipic acid, azelaic acid, sebacic acid, dodecanedicarboxylic acid, maleic anhydride, fumaric acid and And 10 to 60% by weight of at least one member selected from the group consisting of the long-chain dicarboxylic acids derived from the biomass, and it should include at least one of the long-chain dicarboxylic acids derived from the biomass . It is preferable that the biodegradable polymer is produced from the biomass-derived long chain dicarboxylic acid oleic acid or ricinoleic acid by a bioprocess.

The diol used in the production of the polyester polyol is a diol having no aromatic skeleton and includes, for example, ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,3-butanediol, 1,4 Aliphatic diols such as butanediol, 1,5-pentanediol, 1,6-hexanediol, neopentyl glycol, diethylene glycol, triethylene glycol, tetraethylene glycol, dipropylene glycol and tripropylene glycol It is preferable that at least one kind contains 20 to 80% by weight.

The polyester polyol of the present invention can be obtained, for example, by first performing a partial esterification reaction, and then subjecting the resulting reaction product to esterification reaction at a higher temperature and a reduced pressure. At this time, an esterification catalyst may be coexistent. The esterification reaction is preferably carried out at 150 to 250 ° C, more preferably 180 to 220 ° C. Also, the molecular weight of the synthesized polyester polyol can be controlled by controlling the equivalent ratio of the dicarboxylic acid to the diol used. The number average molecular weight of the polyester polyol of the present invention is preferably from 400 to 8,000, more preferably from 700 to 4,000. When the number average molecular weight of the polyester polyol is within this range, the urethane prepolymer having an isocyanate group at the terminal in the two-step reaction does not rise in the anomalous viscosity, and a urethane prepolymer having an appropriate melt viscosity can be obtained.

(B) urethane having an isocyanate group at the molecular terminal Prepolymer

Next, the urethane prepolymer (B) having an isocyanate group at the molecular end used in the present invention will be described. The isocyanate-terminated urethane prepolymer can be obtained by essentially using a polyester polyol (A) having no aromatic skeleton and a polyisocyanate having no aromatic skeleton.

Polyisocyanate having no aromatic skeleton means a compound having two or more isocyanate groups in the molecule. In the present invention, any of aliphatic polyisocyanate and alicyclic polyisocyanate can be used. These may be used alone or in combination of two or more. Examples of the aliphatic polyisocyanate include hexamethylene diisocyanate (HDI), dimeric acid diisocyanate, and lysine diisocyanate. Examples of the alicyclic polyisocyanate include isophorone diisocyanate (IPDI), hydrogenated diphenylmethane diisocyanate (H12MDI), hydrogenated xylylene diisocyanate, cyclohexane diisocyanate, 1,3-bis (isocyanatomethyl) Hexane, norbornenedisocyanate, and the like.

The isocyanate group-terminated urethane prepolymer (B) is prepared by adding an isocyanate group (NCO group) of a polyisocyanate to an hydroxyl group (OH group) of the polyester polyol (A) in an excessively equivalent ratio, .

In the synthesis of the isocyanate-terminated urethane prepolymer (B), the ratio of the isocyanate equivalent (NCO equivalent) of the polyisocyanate to the hydroxyl equivalent (OH equivalent) of the polyester polyol (A) (i.e., [NCO / OH equivalent ratio] It may be set in consideration of target physical properties, product quality, reaction behavior and the like, and is preferably in the range of 1.5 / 1.0 to 10.0 / 1.0 equivalent ratio, more preferably 2.0 / 1.0 to 5.0 / 1.0 equivalent ratio.

[Method 1] A polyester polyol (A) obtained by removing water from a polyisocyanate introduced into a reaction vessel is dropped into a reaction vessel and divided into a batch Or a method in which the reaction is carried out until the hydroxyl group of the polyester polyol (A) substantially disappears, or [2] a method in which polyisocyanate is added dropwise to the polyester polyol (A) , A method of dividing or batching the polyester polyol (A) by a suitable means and allowing the polyester polyol (A) to react until substantially no hydroxyl groups are present. In order to safely and normally proceed the reaction while controlling the exothermic reaction during the reaction, a dropwise addition or division method is preferable.

The isocyanate-terminated urethane prepolymer (B) is usually prepared in the absence of a solvent, but may be carried out in a solvent such as methyl ethyl ketone, ethyl acetate, dimethylformamide or toluene for the purpose of reaction stability. These solvents may be used alone or in combination of two or more.

The reaction conditions (temperature, time, etc.) of the isocyanate-terminated urethane prepolymer (B) may be set within a range that can be normally controlled in consideration of reaction behavior and product quality, and are not particularly limited. It is usually carried out at a reaction temperature of 40 to 90 DEG C and a reaction time of 2 to 24 hours. The reaction system can be selected from, for example, a batch system, semi-continuous system, continuous system and the like, and is not particularly limited.

Further, in producing the isocyanate-terminated urethane prepolymer (B), a urethane-forming catalyst may be used if necessary. The catalyst may be appropriately added at any stage of the raw material introduction step and the reaction step. The method of adding the catalyst is not particularly limited such as batch, division, and continuous. Examples of the urethanization catalyst include titanium tetrabutoxide, dibutyltin oxide, dibutyltin dilaurate, tin 2-ethylcaproate, zinc naphthenate, cobalt naphthenate, zinc 2-ethylcaproate, molybdic glycolate, And organic metal compounds such as potassium acetate, zinc stearate, stannous octylate and dibutyltin dilaurate.

(C) at the molecular end ( Meta ) Acrylic  Have Urethane acrylate Oligomer

Next, the urethane acrylate oligomer (C) (hereinafter referred to as "urethane acrylate oligomer (C)") having a (meth) acrylic group at the molecular end used in the present invention will be described.

The urethane acrylate oligomer (C) preferably has a hydroxyl group-containing (meth) acrylic compound in an amount of from 5 to 300 parts by mass, more preferably from 10 to 100 parts by mass, per 100 parts by mass of the isocyanate-terminated urethane prepolymer (B) And the reaction was carried out in the range of the above-mentioned range. When the isocyanate group of the isocyanate group-terminated urethane prepolymer (B) is reacted with a (meth) acrylic compound having a hydroxyl group within this range, excellent curability and mechanical strength after coating, durability and substrate adhesion can be exhibited on the substrate .

Examples of the (meth) acrylic compound having a hydroxyl group include 2-hydroxyethyl (meth) acrylate, 2-hydroxypropyl (meth) acrylate, 3-hydroxypropyl (meth) Butyl (meth) acrylate, pentaerythritol triacrylate, and the like. Of these, 2-hydroxyethyl acrylate, 2-hydroxyethyl acrylate, Pentaerythritol triacrylate is preferred. It is more preferable to use an acrylate modified by using the caprolactone derivative of the above formula (2) in order to have the self-healing property to be achieved in the present invention. Specifically, M-100 of Miwon Company is exemplified. These may be used alone or in combination of two or more.

The (meth) acrylic equivalent of the urethane acrylate oligomer (C) is in the range of 450 to 1100 g / equivalent, preferably in the range of 500 to 900 g / equivalent, more preferably in the range of 500 to 750 g / Range. When the (meth) acrylic equivalent is within this range, excellent surface hardness and good ultraviolet curing properties can be exhibited. However, when the (meth) acrylic equivalent of the urethane acrylate oligomer (C) is less than 450 g / equivalent, the hardness of the obtained thin film molded article becomes excessively high, and there may be a problem in adhesion with the coated surface. When the (meth) acryl equivalent is more than 1100 g / equivalent, the curing reaction by ultraviolet irradiation tends to become insufficient, and tackiness may occur on the surface of the coating film.

The urethane-forming reaction of the isocyanate-terminated urethane prepolymer (B) with the (meth) acrylic compound having a hydroxyl group may be non-catalytic or urethane-forming, and is not particularly limited. When an urethane catalyst is used, it can be appropriately added at an early stage or at any stage in the middle of the urethane reaction. Examples of the urethanization catalyst include nitrogen-containing compounds such as triethylamine, triethylenediamine and N-methylmorpholine, organic metal salts such as potassium acetate, zinc stearate and stannous octylate, And organic metal compounds such as dibutyltin dilaurate. The amount of the urethanization catalyst to be used is not particularly limited so long as it does not adversely affect the safety during reaction, the stability of the intermediate or the product, the quality, and the like.

(D) Urethane acrylate Oligomer  UV-curable coating composition used

The ultraviolet curable coating composition of the present invention provides an ultraviolet curable coating composition comprising 40 to 80 parts by weight of the urethane acrylate oligomer (C), 1 to 15 parts by weight of a photoinitiator, and 0.1 to 10 parts by weight of a surface control additive.

The photoinitiator used in the present invention acts to cure the coating film by being activated by ultraviolet rays. Examples of the photoinitiator include benzophenone compounds, benzyldimethacetal compounds, acetophenone compounds, anthraquinone compounds, benzyl ketal compounds, and mixtures thereof. Specific examples of the photoinitiator include 2,2-dimethoxy-2-phenylacetophenone, 1-hydroxycyclohexylphenylketone, 1 -hydroxydimethylphenylketone, 2-hydroxy 1,2- , 2-methyl1-4 (methylthio) phenyl-2-morpholinopropanone, 2-benzyl 2-dimethylamino 1- (4-morpholinophenyl) -Butanone, bis (2,4,6-trimethylbenzoyl) -phenylphosphine oxide, and the like. Commercially available products include Irgacure 184, Irgacure 907, Irgacure 819 Irgacure 369 from BASF, Darocure 1173 and Darocure 4043 from Merck. The amount of the photoinitiator is used in an amount of 1 to 10 parts by weight based on 100 parts by weight of the total composition. If the amount is less than 1 part by weight, sufficient hardening of the coating film is difficult and physical properties are deteriorated.

The surface modifying additive used in the present invention is used for improving defoam, slip and leveling, and preferably a silicone compound, a silicone modified polyacrylate compound and the like can be used. Specifically, Tego Rad 2500, 2250 (product name), and BYK-Chemie BYK-306, 310, 331 (product name) of Tego-Chemie can be mentioned. The amount of the surface modifying additive used is preferably in the range of 0.1-10 parts by weight with respect to the total composition in consideration of the range not adversely affecting the coating film performance.

In the present invention, an appropriate amount of an organic solvent may be added to adjust the viscosity. The organic solvent serves to facilitate the coating operation and uniform the application. Examples of usable organic solvents include ketone-based compounds, acetate-based compounds, aromatic compounds, and alcohol-based compounds, and these may be used alone or in combination of two or more. The amount of the organic solvent to be used may be 20 to 80 parts by weight based on the total composition.

Hereinafter, preferred embodiments of the present invention will be described in order to facilitate understanding of the present invention. However, the following examples are provided only for the purpose of easier understanding of the present invention, and the present invention is not limited by the following examples.

Example

Example  One. Biomass  Derived dicarboxylic acid production

For the production of dicarboxylic acid from the biomass feedstock, a 1 L oil-in-water culture was carried out using a strain having an expression system (E. coli BL21 (DE3) pAPTm-E6BVMO-ADH) at all times. pH control was performed using pH stat mode. Low concentration cultures (<10 OD) were performed at 37 ° C and high concentration cultures (> 10 OD) at 20 ° C. After incubation, protein expression was confirmed by SDS-PAGE. The conversion process was performed at 35 oC for a smooth bioconversion.

In the case of the substrate concentration of 60 mM, recinoleic acid was all converted. Therefore, in order to select the maximum substrate concentration, after the initial 100 mM addition, the reaction was continued for 4 hours and 50 mM was further added. .

It can be seen that the intermediate keto compound is added to the latter half of the reaction depending on a large amount of the substrate. In order to improve the accuracy of the analysis, the concentration of fermentation broth was determined to be about 26g / L when the total amount of the fermentation broth was extracted with ethyl acetate and the productivity was 4.3g / L / h. The concentration of the substrate is considered to be about 100 mM.

Bioconversion experiments at 100 mM were conducted to improve conversion and productivity. After culturing the strain to OD 116, 100mM of substrate Ricinoleic acid was added at 35 o C for bioconversion. The conversion yield was about 83%, and the productivity per hour and volume was 2.6 g / L / h.

Example  2. Polyester Of polyol  synthesis

Synthetic example  2.1

35.6 g of 1,11-undecanedioic acid (derived from biomass), 24.1 g of adipic acid, 58.4 g of diethylene glycol, and 0.2 g of dibutyltinoxide are placed in a 250 ml 3-neck round flask, and the temperature is raised to 150 ° C. to conduct a dehydration reaction. The dehydration reaction was continued while increasing the reaction temperature to 210 ° C. at a rate of 10 ° C. per hour, and when the theoretical dehydration yield was reached, the reaction was terminated to synthesize a polyester polyol (A1).

Synthetic example  2.2

Synthesis was carried out under the same conditions as in Synthesis Example 2.1 except that 1,11-undecanedioic acid used in the synthesis was changed to a petroleum-derived raw material instead of the biomass-derived material, to synthesize an ester polyol (A2).

Example  3. Urethane acrylate Oligomer  synthesis

Synthetic example  3.1

15.6 g of the polyester polyol (A1), 0.06 g of DBTDL (Dibutyltin dilaurate) and 16 g of MEK are placed in a 100 mL 3-neck round flask and the temperature is raised to 60 ° C. 18 g of IPDI (isophorone diisocyanate) is slowly dropped at 60 캜 using a dropping funnel. If the exothermic reaction is severe, heat is controlled by cooling water. After completion of the IPDI dropwise addition, the NCO% was measured while maintaining the reaction at 78 캜, and the point in time when the NCO% remained unchanged was confirmed to synthesize the urethane prepolymer (B) having an isocyanate group at the molecular end. After cooling to 60 캜, 0.02 g of a polymerization inhibitor and 12.2 g of 2-HEA (2-hydroxyethyl acrylate) are added. If the exothermic reaction is severe, heat is controlled by cooling water. The NCO% was measured while maintaining the reaction at 78 ° C to confirm that all the isocyanates did not react, and the reaction was terminated. Finally, a bifunctional urethane acrylate oligomer (C1) having one acryl group at each terminal was synthesized.

Synthetic example  3.2

A bifunctional urethane acrylate oligomer (C2) was synthesized under the same conditions as in Synthesis Example 3.1 except that the polyester polyol used in the synthesis was changed to the polyester polyol (A2) obtained in Synthesis Example 2.2.

Synthetic example  3.3

A 6-functional urethane acrylate oligomer (C3) was synthesized in the same manner as in Synthesis Example 3.1, except that 2-HEA used in Synthesis Example 3.1 was changed to PETA (Pentaerythritol triacrylate).

Synthetic example  3.4

A 6-functional urethane acrylate oligomer (C4) was synthesized in the same manner as in Synthesis Example 3.2 except that 2-HEA used in Synthesis Example 3.2 was changed to PETA (Pentaerythritol triacrylate).

Example  4. Preparation of ultraviolet curable coating composition

UV-curable coating agents were prepared using urethane acrylate oligomers (C1 to C4) synthesized in Synthesis Examples 3.1 to 3.4, photoinitiators, additives for surface control, and organic solvents in the amounts shown in Table 1 below.

Ingredient (parts by weight) Synthesis Example 3.1 Synthesis Example 3.2 Synthesis Example 3.3 Synthesis Example 3.4 Urethane acrylate oligomer C1 64.5 C2 64.5 C3 64.5 C4 64.5 Photoinitiator (Irgacure-184) 2.6 2.6 2.6 2.6 Additives for surface conditioning (Tego RAD2500) 0.6 0.6 0.6 0.6 Organic solvents (MEK) 32.3 32.3 32.3 32.3 Sum 100 100 100 100

&Lt; Evaluation of physical properties of UV curable coating composition >

The UV-curable coating solution prepared above was coated on a PET film with a Mater bar (# 22) and allowed to stand in a 70 ° C oven for 3 minutes. The solvent was blown off and cured by a UV curing machine to measure the physical properties of the coating film. The physical properties of the coating film were measured for adhesion and pencil hardness. The results are shown in Table 2. The physical properties evaluation method is as follows.

(1) Pencil Hardness

The pencil hardness was evaluated by a pencil hardness meter according to the test method of ASTM D3502.

(2) Adhesion

Cross-cuts were made at intervals of 1 mm with a knife according to the test method of KSD 6711-92.

Test Items Synthesis Example 3.1 Synthesis Example 3.2 Synthesis Example 3.3 Synthesis Example 3.4 Attachment 100/100 100/100 100/100 100/100 Pencil hardness HB 3H B H

As a result of the evaluation of the test items, the pencil hardnesses of Synthesis Examples 3.1 and 3.3, which are urethane acrylate oligomers synthesized using long-chain dicarboxylic acids derived from biomass, were compared with urethane oligomers synthesized using long chain dicarboxylic acids derived from petroleum And the pencil hardness increases as the number of functional groups of the synthesized urethane acrylate oligomer increases. It is possible to apply an environmentally friendly coating agent without lowering the physical properties by replacing the existing petroleum-derived raw material with the raw material derived from the biomass.

It will be understood by those skilled in the art that the foregoing description of the present invention is for illustrative purposes only and that those of ordinary skill in the art can readily understand that various changes and modifications may be made without departing from the spirit or essential characteristics of the present invention. will be. It is therefore to be understood that the above-described embodiments are illustrative in all aspects and not restrictive.

Claims (6)

A process for preparing an ultraviolet-curable oligomer comprising the steps of:
a) adding an aliphatic diol to a biomass-derived dicarboxylic acid and performing an esterification reaction at 150 to 250 ° C to prepare a polyester polyol;
b) adding a polyisocyanate to the polyester polyol and reacting the polyester polyol at a temperature of 40 to 90 ° C for 2 to 24 hours to prepare a urethane prepolymer; And
c) adding acrylate to the urethane prepolymer to prepare a urethane acrylate oligomer.
The method according to claim 1,
Wherein the dicarboxylic acid is represented by the following formula (1).
&Lt; Formula 1 >

In Formula 1, n is an integer of 9 to 13.
The method according to claim 1,
The aliphatic diol may be at least one selected from the group consisting of ethylene glycol, 1,2-propanediol, 1,3-propanediol, 1,3-butanediol, 1,4-butanediol, 1,5-pentanediol, 1,6-hexanediol, neopentyl glycol , At least one diol selected from the group consisting of diethylene glycol, triethylene glycol, tetraethylene glycol, dipropylene glycol, and tripropylene glycol.
The method according to claim 1,
Wherein the polyester polyol has a number average molecular weight of 400 to 8,000.
The method according to claim 1,
The polyisocyanate may be selected from the group consisting of hexamethylene diisocyanate (HDI), dimer acid diisocyanate, lysine diisocyanate, isophorone diisocyanate (IPDI), hydrogenated diphenylmethane diisocyanate (H12MDI), hydrogenated xylylene diisocyanate, cyclohexane diisocyanate, , 3-bis (isocyanatomethyl) cyclohexane, and norbornene diisocyanate. 3. The process for producing an ultraviolet-curable oligomer according to claim 1, wherein the polyisocyanate is a polyisocyanate.
40 to 80 parts by weight of the urethane acrylate oligomer of claim 1, 1 to 15 parts by weight of a photoinitiator, and 0.1 to 10 parts by weight of an additive for surface control.