KR102245471B1 - Manufacturing method of polyurethane resin for coating fabric using biomass contents - Google Patents

Abstract

The present invention relates to a method for producing a polyurethane resin for fabric coating using a biomaterial, and in detail, poly tetramethylene ether glycol (PTMG), isosorbide (ISB) and methylene diphenyl A mixture preparation step of preparing a mixture by mixing 25 to 35 parts by weight of a reactant in which a diisocyanate (methylene diphenyl diisocyanate, MDI) is mixed in a molar ratio of 1: 3 to 4: 4.5 to 5.5 and 35 to 75 parts by weight of an organic solvent, A polymerization step in which a catalyst is added to the mixture to polymerize the reactant for 11 to 13 hours at a temperature of 120 to 140°C, and a curing agent is added to the mixture through the polymerization step, at a temperature of 35 to 45°C. It characterized in that it comprises a drying step of vacuum drying for 70 to 74 hours under conditions.

Description

Manufacturing method of polyurethane resin for coating fabric using biomass contents}

The present invention relates to a method of manufacturing a polyurethane resin for fabric coating using a biomaterial, and more particularly, to a method of manufacturing a polyurethane resin for high strength fabric coating using isosorbide obtained from biomass resources.

In general, polyurethane resins have urethane bonds in their molecules and are polymer compounds synthesized mainly by reaction with diisocyanates and polyol compounds. They are excellent in abrasion resistance, oil resistance and solvent resistance, and have excellent elasticity. It is applied in various fields such as adhesives, coatings, injection products, paints, inks, paints, foams, footwear parts, clothing, and medical polymers.

In the case of polyurethane coatings, almost all of them are synthesized using polyester diol, which is inexpensive, as the main material, but it currently has sufficient thermal and mechanical properties to be used for fabric coating, but by utilizing biomass, environmental problems are solved. The development of technologies related to eco-friendly materials that can be improved is insignificant.

Korean Patent Publication No. 1994-0014478

The present invention has been devised to solve the above problems, and has sufficient thermal properties and mechanical properties to be used for fabric coating, as well as fabrics using biomaterials that can provide eco-friendly effects by utilizing biomass. An object thereof is to provide a method for producing a polyurethane resin for coating.

In the present invention, poly tetramethylene ether glycol (PTMG), isosorbide (ISB) and methylene diphenyl diisocyanate (MDI) are 1: 3 to 4: 4.5 to 5.5 A mixture preparation step of preparing a mixture by mixing 25 to 35 parts by weight of a reactant mixed at a molar ratio of and 65 to 75 parts by weight of an organic solvent, and adding a catalyst to the mixture to 11 to 13 at a temperature condition of 120 to 140°C. It characterized in that it comprises a polymerization step of performing a polymerization reaction of the reactant for a period of time and a drying step of adding a curing agent to the mixture subjected to the polymerization step, and vacuum drying for 70 to 74 hours at a temperature condition of 35 to 45°C. .

In addition, preferably, the curing agent is characterized in that 0.3 to 0.4 parts by weight is added based on 100 parts by weight of the mixture.

In addition, preferably, the organic solvent is characterized in that one or more selected from the group consisting of dimethyl formamide (DMF) and methyl ethyl ketone (MEK).

The method for producing a polyurethane resin for fabric coating using a biomaterial according to the present invention uses isosorbide derived from biomass as a polyol, thereby securing excellent thermal properties and mechanical properties, and at the same time as compared to the conventional polyurethane resin for fabric coating. There is an advantage that it can provide an environmentally friendly effect.

1 is a flow chart of a method for manufacturing a polyurethane resin for fabric coating using a bio material according to the present invention.
2 is a graph measuring the polymerization state of the polyurethane resins according to Examples and Comparative Examples 1 to 4;
3 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to the embodiment.
4 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 1.
5 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 2.
6 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 3.
7 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 4.
8 is a graph measuring the tensile strength of the polyurethane resins according to Examples and Comparative Examples 1 to 4.

Hereinafter, the technical idea of the present invention will be described in more detail using the accompanying drawings.

The accompanying drawings are only an example illustrated to describe the technical idea of the present invention in more detail, so the technical idea of the present invention is not limited to the form of the accompanying drawings.

1 is a flow chart of a method for manufacturing a polyurethane resin for fabric coating using a bio material according to the present invention. As shown in Figure 1, the method for producing a polyurethane resin for fabric coating using a biomaterial according to the present invention includes a mixture manufacturing step (S100), a polymerization step (S200), and a drying step (S300).

First, in the mixture preparation step (S100), poly tetramethylene ether glycol (PTMG), isosorbide (ISB) and methylene diphenyl diisocyanate (MDI) are 1: 3 to 4: This is a step of preparing a mixture by mixing 25 to 35 parts by weight of the reactant mixed at a molar ratio of 4.5 to 5.5 and 65 to 75 parts by weight of an organic solvent.

In the case of polytetramethylene ether glycol, it is preferable to use a weight average molecular weight of 2000, and when the weight average molecular weight of polytetramethylene ether glycol is less than 2000, the flexibility and low temperature characteristics of the final polymer polyurethane resin It is not excellent, and if the weight average molecular weight of polytetramethylene ether glycol exceeds 2000, the viscosity may be high during the synthesis of the prepolymer, resulting in a gel, and there is a concern that the tensile strength and 100% modulus may be lowered.

In addition, when the number of moles of the isosorbide is less than 3 per 1 mole of the polytetramethylene ether glycol, the environmentally friendly effect may be insufficient, whereas when the number of moles of the isosorbide exceeds 4, the diol content increases. As a result, there is a concern that mechanical properties may deteriorate.

In addition, when the number of moles of the methylene diphenyl diisocyanate is less than 4.5 with respect to 1 mole of the polytetramethylene ether glycol, there is a concern that the polyurethane may not be sufficiently synthesized, whereas the number of moles of the methylene diphenyl diisocyanate is more than 5.5. In this case, there is a concern that an excess of diisocyanate that has not participated in the reaction reacts with moisture in the air and is easily cured.

That is, as described above, the present invention has an eco-friendly effect compared to the conventional polyurethane resin for fabric coating by using biomass-derived isosorbide, and polytetramethylene ether glycol, isosorbide and methylene diphenyl diisocyanate When used in the molar ratio range of 1: 3 to 4: 4.5 to 5.5, it has sufficient thermal properties to be used as a polyurethane resin for fabric coating, and has excellent mechanical properties compared to the conventional polyurethane resin for fabric coating. It was confirmed that, and the related content will be described in detail in Experimental Example 1 below.

Meanwhile, the organic solvent is selected from the group consisting of dimethyl formamide (DMF) and methyl ethyl ketone (MEK).

Specifically, the organic solvent is preferably used in a mixture of 25 to 35 parts by weight of dimethylformamide and 65 to 75 parts by weight of methyl ethyl ketone.

Since the methyl ethyl ketone has a low boiling point (i.e., volatilization temperature), it can be mixed with dimethylformamide to lower the boiling point of dimethylformamide, which has the effect of shortening the drying time (i.e., volatilization time) of the drying step to be described later. have.

Accordingly, when the methyl ethyl ketone is mixed in less than 65 parts by weight, the above-described effect of shortening the drying time cannot be sufficiently exhibited, and when the methyl ethyl ketone is mixed in more than 75 parts by weight, the boiling point is relatively lowered, and thus poly There is a problem in that the physical properties of the urethane resin solid content cannot be maintained as it is.

That is, the above blending ratio is a result obtained by a number of experiments by the present inventors as a range capable of sufficiently shortening the drying time of the drying step, although the reactant is sufficiently dissolved and does not have an undesirable effect on the reaction.

These organic solvents are poly tetramethylene ether glycol (PTMG), isosorbide (ISB), and methylene diphenyl diisocyanate so that the solid content of the reactant in the mixture can be 25 to 35%. It is preferable that 65 to 75 parts by weight of the reactant in which diisocyanate, MDI) is mixed is mixed with 25 to 35 parts by weight.

When the organic solvent is mixed in an amount of less than 65 parts by weight and the solid content of the reactant exceeds 35%, the viscosity of the mixture is too high, so that the mixture is difficult to be uniformly mixed, and workability is deteriorated.

On the other hand, when the organic solvent is mixed in an amount of more than 75 parts by weight and the solid content of the reactant is less than 25%, there is a problem that unnecessary energy is consumed during drying and curing due to a relatively high content of the organic solvent. As a result, there is a fear that the manufacturing cost will rise.

Next, the polymerization step (S200) is a step of performing a polymerization reaction of the reactant for 11 to 13 hours at a temperature condition of 120 to 140°C by adding a catalyst to the mixture.

This is the optimum condition for sufficiently polymerizing the reactants. If the reaction is carried out for less than 11 hours under a temperature condition of less than 120°C, sufficient polymerization efficiency cannot be obtained, which is not preferable. In the case of reaction, not only the activity of the catalyst decreases, but also there is a problem that a polymer mass is easily generated, which is not preferable.

In addition, as the catalyst used in the polymerization step (S200), it is preferable that dibutyltin dilaurae (DBTDL), which is an organometallic catalyst, is used as a urethanization reaction catalyst.

In the case of the dibutyl tin dilaurate catalyst, since the catalyst is adequately active, side reactions occur less during synthesis, and there is an effect of improving the storage stability of the synthesized polyurethane resin.

In addition, it is preferable that 0.03 parts by weight of the catalyst is added based on 100 parts by weight of the solid content of the reactant in the mixture.

Specifically, when the catalyst is mixed in an amount of less than 0.03 parts by weight, sufficient catalytic activity does not appear, so that the reaction rate is slow and unreacted substances may remain. When the catalyst is mixed in an amount exceeding 0.03 parts by weight, the reaction rate is Although faster, oligomers of low molecular weight are produced, which may lead to a decrease in mechanical properties.

That is, 0.03 parts by weight of the catalyst is added based on 100 parts by weight of the solid content of the reactant in the mixture to ensure the excellent mechanical properties of the polyurethane resin, as well as to ensure that the polymerization reaction of the reactant can proceed smoothly by exhibiting the catalytic performance sufficiently. It is preferable to be, and the related information can be confirmed in Experimental Example 1 below.

Next, the drying step (S300) is a step of vacuum drying for 70 to 74 hours at a temperature condition of 35 to 45°C by adding a curing agent to the mixture that has undergone the polymerization step (S200).

This is the optimum condition for obtaining a high-purity polyurethane resin by completely removing the residual organic solvent in the mixture. When drying for less than 70 hours at a temperature condition of less than 35°C, sufficient drying is not performed and the residual solvent cannot be completely removed. It is not preferable because it is not possible, and if it is dried for more than 74 hours in a temperature condition of more than 45°C, decomposition of the polymer may occur due to excessive drying, and thus the physical properties of the finally formed polyurethane resin may be deteriorated. not.

Ethylene diamine (EDA) is used as the curing agent, and 0.3 to 0.4 parts by weight is preferably added based on 100 parts by weight of the mixture.

In the case of the ethylene diamine, it is preferable that a diamine compound having a weight average molecular weight of 60 to 200 is used.If the weight average molecular weight of ethylene diamine is less than 60, the reactivity is too fast to control the reactivity, and the final product may become hard. On the other hand, when the weight average molecular weight exceeds 200, there is a problem that the reactivity may be slowed and the elastic modulus of the final product may decrease.

In addition, when the curing agent is mixed in less than 0.3 parts by weight, the curing speed is slow or the curing is insufficient, resulting in a problem that thermal properties including heat resistance are deteriorated. When the curing agent is mixed in excess of 0.4 parts by weight, the curing time This rapidly accelerates, resulting in poor appearance, shortened pot life, which not only allows gel formation during mixing, but also causes excessive curing, resulting in a rapid deterioration of the mechanical properties of the polyurethane resin. It can be found in 1.

<Experimental Example 1>

In this Experimental Example 1, an experiment was conducted to measure the thermal decomposition temperature and tensile strength of the polyurethane resin for fabric coating according to the type of polyol, and the production ratio of the polyurethane resin for fabric coating according to Examples and Comparative Examples 1 to 4 was See Table 1 below.

In the example, a polyurethane resin for fabric coating was prepared using poly tetramethylene ether glycol (PTMG) and isosorbide (ISB) as a polyol.

In Comparative Example 1, a polyurethane resin for fabric coating was prepared using poly tetramethylene ether glycol (PTMG) and ethylene glycol (EG) as polyols.

In Comparative Example 2, a polyurethane resin for fabric coating was prepared using poly tetramethylene ether glycol (PTMG) and diethylene glycol (DEG) as polyols.

In Comparative Example 3, a polyurethane resin for fabric coating was prepared using poly tetramethylene ether glycol (PTMG) and 1,4-butanediol (1,4-butanediol, 1,4-BD) as a polyol. .

In Comparative Example 4, polytetramethylene ether glycol (PTMG) and 1,6-hexanediol (1,6-hexanediol, 1,6-HD) were used as polyols to prepare a polyurethane resin for fabric coating. I did.

division MW
(g/mol) Ratio Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Example poly tetramethylene ether glycol
(PTMG) 2000 0.04 80 80 80 80 80 ethylene glycol
(EG) 62.07 0.13 8.07 - - - - diethylene glycol
(DEG) 106.12 - 13.80 - - - 1,4-
butanediol
(1,4-BD) 90.12 - - 11.72 - - 1,6-
hexanediol
(1,6-HD) 118.17 - - - 15.36 - isosorbide (ISB) 146.14 - - - - 19.00 methylene diphenyl diisocyanate
(MDI) 262.35 0.2 52.47 52.47 52.47 52.47 52.47 Ethylene diamine
(EDA) 60.10 0.03 1.80 1.80 1.80 1.80 1.80 DMF - 3 98.38 102.39 100.93 103.48 106.03 MEK - 7 229.55 238.90 235.50 241.46 247.40 dibutyltin dilaurae
(DBTDL) - - 0.03 wt% of solid content

As disclosed in Table 1 above, the mixed mixture was subjected to the polymerization step (S200) under the same conditions for 12 hours at a temperature of 130°C, and when the polymerization step (S200) was completed, the polymerization was performed using an FT-IR spectrometer. Was measured, and the result is referred to FIG. 2.

2 is a graph measuring the polymerization state of the polyurethane resins according to Examples and Comparative Examples 1 to 4;

As shown in FIG. 2, the polyurethane resin according to Examples and Comparative Examples 1 to 4 showed no isocyanate (-NCO) peak in the wavelength range ^{of 2200 cm -1, so that the polymerization reaction of the polyurethane resin was} You can see that it went well.

Accordingly, it was confirmed that the reaction conditions of the polymerization step (S200), including the type and mixing ratio of the catalyst, and temperature conditions and reaction time described above, are optimal conditions for sufficiently polymerizing the reactants.

In addition, the mixture according to Examples and Comparative Examples 1 to 4 that went through the polymerization step (S200) was added with a curing agent, and the drying step (S300) was performed under the same conditions for 72 hours at a temperature of 40°C. 0.3 parts by weight of ethylene diamine (EDA) was added based on 100 parts by weight of the mixture.

Upon completion of the drying step (S300), the thermal decomposition temperature (ie, thermal stability) and tensile strength of the polyurethane resins according to Examples and Comparative Examples 1 to 4 were measured, and the results are as follows.

First, when measuring the thermal decomposition temperature, a thermogravimetric analyzer (TGA) was used to measure a temperature increase rate of 10°C/min and a temperature range of 0 to 800°C in a nitrogen atmosphere. Refer to Table 2 below for the result of the thermal decomposition temperature of the polyurethane resin.

division Comparative Example 1 Comparative Example 2 Comparative Example 3 Comparative Example 4 Example Pyrolysis temperature
(℃) 411.44 407.09 406.95 408.33 395.62

As disclosed in Table 2, the polyurethane resin according to the embodiment has a decomposition temperature similar to that of Comparative Examples 1 to 4 used as a polyurethane resin for conventional fabric coating, so that it is used as a polyurethane resin for fabric coating. It was confirmed that it had sufficient thermal properties (ie, thermal stability), and graphs measuring the thermal decomposition temperature of the polyurethane resins according to Examples and Comparative Examples 1 to 4 are shown in FIGS. 3 to 7.

3 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to the embodiment, Figure 4 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 1, and Figure 5 is a polyurethane resin according to Comparative Example 2 Is a graph measuring the thermal decomposition temperature of, FIG. 6 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 3, and FIG. 7 is a graph measuring the thermal decomposition temperature of the polyurethane resin according to Comparative Example 4.

In addition, the results of measuring the tensile strength of the polyurethane resins according to Examples and Comparative Examples 1 to 4 refer to FIG. 8, and FIG. 8 is a graph measuring the tensile strength of the polyurethane resins according to Examples and Comparative Examples 1 to 4 to be.

As shown in FIG. 8, the tensile strength of the polyurethane resin according to the embodiment was shown to be the most excellent, and it can be seen that it has excellent mechanical properties compared to the polyurethane resin for conventional fabric coating.

Accordingly, the polyurethane resin for fabric coating according to the present invention uses isosorbide derived from biomass to have an eco-friendly effect and at the same time secure sufficient thermal properties and mechanical properties.

It goes without saying that the present invention is not limited to the above-described embodiments, and the scope of application is various, and various modifications can be implemented without departing from the gist of the present invention claimed in the claims.

S100: Mixture preparation step
S200: polymerization step
S300: drying step

Claims (3)

Poly tetramethylene ether glycol (PTMG), isosorbide (ISB) and methylene diphenyl diisocyanate (MDI) are mixed in a molar ratio of 1: 3 to 4: 4.5 to 5.5 A mixture preparation step of preparing a mixture by mixing 25 to 35 parts by weight of the reactant and 65 to 75 parts by weight of an organic solvent;
A polymerization step of performing a polymerization reaction of the reactant for 11 to 13 hours at a temperature condition of 120 to 140°C by adding a catalyst to the mixture; And
Including; a drying step of adding a curing agent to the mixture subjected to the polymerization step and vacuum drying for 70 to 74 hours at a temperature condition of 35 to 45°C
The organic solvent is mixed with 25 to 35 parts by weight of dimethyl formamide (DMF) and 65 to 75 parts by weight of methyl ethyl ketone (MEK),
Dibutyltin dilaurae (DBTDL) is used as the catalyst, and 0.03 parts by weight is added based on 100 parts by weight of the reactant,
Ethylene diamine (EDA) is used as the curing agent, and 0.3 to 0.4 parts by weight is added based on 100 parts by weight of the mixture. delete delete

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