KR102382133B1 - Preparation method of olefin polymer - Google Patents

Abstract

The present invention relates to an olefin-based polymer formed by copolymerization of an olefin-based monomer and an olefin-based comonomer, wherein the olefin-based polymer has a softening point of 80° C. to 120° C., and a first melting temperature and a second melting temperature of different values. have

Description

Method for producing an olefin-based polymer {PREPARATION METHOD OF OLEFIN POLYMER}

The present invention relates to a method for producing an olefin-based polymer, and to a method for producing an olefin-based polymer including a first melting temperature and a second melting temperature in different ranges.

A metallocene catalyst, one of the catalysts used to polymerize olefins, is a compound in which ligands such as a cyclopentadienyl group, an indenyl group, and a cycloheptadienyl group are coordinated to a transition metal or transition metal halide compound. have

It is known that the olefin-based polymer polymerized using such a metallocene catalyst has a narrow molecular weight distribution (MWD) as well as a constant comonomer distribution compared to the olefin-based polymer polymerized by a conventional Ziegler-Natta catalyst.

On the other hand, in general, an olefin-based polymer polymerized using a single metallocene catalyst has a single melting temperature (Tm), and thus has low thermal stability because crystals are melted and crystallized only at a specific temperature.

The problem to be solved by the present invention is to provide an olefin-based polymer having a melting temperature (Tm) in different ranges and having excellent thermal stability. Another object of the present invention is to provide an olefin-based polymer having a relatively low density and molecular weight, but a high softening point.

The problems of the present invention are not limited to the technical problems mentioned above, and other technical problems not mentioned will be clearly understood by those skilled in the art from the following description.

The method for producing an olefin-based polymer according to an embodiment of the present invention for solving the above problems is an olefinic monomer and an olefin in the presence of a single olefin polymerization catalyst including a transition metal compound represented by the following Chemical Formula A-2 or A-3 A method for producing an olefin-based polymer copolymerizing a based comonomer, wherein the copolymerized olefin-based polymer has a softening point of 91.8°C to 104.1°C, and has a first melting temperature and a second melting temperature, the first melting temperature and the second melting temperature The two melting temperatures may have different values, the first melting temperature being 52.0°C to 70.5°C, and the second melting temperature being 89.8°C to 107.1°C.

<Formula A-2>

<Formula A-3>

The total crystallinity may be 5% to 15%.

A ratio of a first crystallinity that is a degree of crystallinity with respect to the first melting temperature and a second degree of crystallinity that is a degree of crystallinity with respect to the second melting temperature may be 99:1 to 75:25.

The weight average molecular weight may be from 5,000 g/mol to 60,000 g/mol.

The content of the comonomer may be 10 wt% to 50 wt%.

The density may be 0.860 g/cm 3 to 0.900 g/cm 3 .

The olefin-based monomer and the olefin-based comonomer may be ethylene and 1-octene, respectively.

Details of other embodiments are included in the detailed description and drawings.

According to the embodiments of the present invention, there are at least the following effects.

The olefin-based polymer of the present invention includes different ranges of melting temperatures (Tm) and has excellent thermal stability.

In addition, the olefin-based polymer of the present invention has excellent physical properties by simultaneously satisfying the characteristics of low density, low molecular weight and high softening point.

Effects according to the embodiments of the present invention are not limited by the contents exemplified above, and more various effects are included in the present specification.

1 is a DSC curve of the ethylene/1-octene copolymer synthesized in Preparation Example 1.
2 is a DSC Curve of the ethylene/1-octene copolymer synthesized in Preparation Example 2.
3 is a DSC curve of the ethylene/1-octene copolymer synthesized in Preparation Example 3.

Advantages and features of the present invention and methods of achieving them will become apparent with reference to the embodiments described below in detail in conjunction with the accompanying drawings. However, the present invention is not limited to the embodiments disclosed below, but will be implemented in a variety of different forms, and only these embodiments allow the disclosure of the present invention to be complete, and common knowledge in the technical field to which the present invention belongs It is provided to fully inform the possessor of the scope of the invention, and the present invention is only defined by the scope of the claims.

The olefin-based polymer according to an embodiment of the present invention may be a polymer of an olefin-based monomer or a copolymer of an olefin-based monomer and a comonomer.

Olefin-based monomers are C _2-20 alpha-olefin, C _1-20 diolefin, C _3-20 cyclo-olefin and C _3-20 cyclodiolefin. It may be one or more selected from the group consisting of.

In an exemplary embodiment, the olefinic monomer is ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-undecene , 1-dodecene, 1-tetradecene, 1-hexadecene, and the like, but is not limited thereto. The olefin-based polymer may be a homopolymer including only one type of the olefin-based monomers exemplified above, or a copolymer including two or more types. For example, the olefin-based polymer may be a copolymer in which ethylene and 1-octene are copolymerized.

The olefin-based polymer according to an embodiment of the present invention may include a plurality of melting temperatures. When the olefin-based polymer includes a plurality of melting temperatures, since the crystals are melted and crystallized at the plurality of temperatures, thermal stability is high and excellent properties can be exhibited in a high-temperature melt adhesive.

In one embodiment, the olefinic polymer may comprise a first melting temperature and a second melting temperature. The second melting temperature may be higher than the first melting temperature. A difference between the second melting temperature and the first melting temperature may be 10°C to 80°C.

In a specific embodiment, the first melting temperature (Tm1) of the olefin-based polymer may be -20 to 80°C, and the second melting temperature (Tm2) may have a value within the range of 80 to 120. Preferably, the first melting temperature (Tm1) may be 0°C to 80°C, and the second melting temperature (Tm2) may be 80°C to 140°C. More preferably, the first melting temperature (Tm1) may be 30°C to 80°C, and the second melting temperature (Tm2) may be 90°C to 120°C, but is not limited thereto.

The olefin-based polymer may have a crystallinity of 2% to 20%. Preferably, it may have a crystallinity of 5% to 15%.

The degree of crystallinity can be calculated by measuring the heat of fusion (ΔH ) on a DSC curve obtained from a differential scanning calorimeter (DSC) and substituting it in Equation 1 below.

[Equation 1]

Crystallinity (%) = ΔH _measurement /ΔH _100% *100

The heat of fusion (ΔH _measurement ) can be obtained by measuring the area formed by the temperature ()-flow (W/g) curve and the linear reference line for this curve on the DSC Curve. ΔH _100% is the measured theoretical enthalpy of melting for a 100% crystalline olefinic polymer and is 290 J/g.

The crystallinity of the olefin-based polymer has a close correlation with the solubility and adhesion performance of the olefin-based polymer. When the degree of crystallinity of the olefin-based polymer is 4% or more, the copolymer can be easily prepared, and a crystalline region of a certain level or higher can be secured, thereby maintaining adhesive performance. In addition, when the crystallinity is 8% or more, it shows excellent properties in the pot life, which is the time the adhesive cures. That is, the olefin-based polymer having a crystallinity of 8% or more may exhibit excellent properties in a hot melt adhesive due to a short pot life and high adhesion. When the degree of crystallinity of the olefin-based polymer is 13% or less, solubility in a solvent is high, which is advantageous in securing manufacturing convenience.

The total crystallinity of the olefin-based polymer may be calculated as the sum of the degree of crystallization at each melting temperature. For example, the olefin-based polymer has a first degree of crystallinity within a range of a first melting temperature (Tm1) and a second degree of crystallinity within a range of a second melting temperature (Tm2). It can be calculated as the sum of the second degree of crystallinity.

When the second melting temperature is higher than the first melting temperature, the first degree of crystallinity at the first melting temperature of the relatively low temperature may be greater than the second degree of crystallinity. In one embodiment, when the first melting temperature (Tm1) is -20 ℃ to 80, the first crystallinity may be 3% to 15%. When the second melting temperature is 80° C. to 120° C., the second crystallinity may be 0.05% to 0.7%.

A ratio of the first degree of crystallinity to the second degree of crystallinity may be, for example, 1:0.1 to 1:0.25. In other words, the ratio of the first degree of crystallinity to the second degree of crystallinity of the olefin-based polymer may be 99:1 to 80:20.

The weight average molecular weight (Mw) of the olefin-based polymer may be 5,000 g/mol to 60,000 g/mol, and the molecular weight distribution (MWD) of the olefin-based polymer may be 1.3 to 3.0. The molecular weight distribution can be calculated by Equation 2 below.

[Equation 2]

MWD = Mw/Mn

In Equation 2, Mn is a number-average molecular weight, and Mw is a weight-average molecular weight.

When the weight average molecular weight of the olefin-based polymer is 60,000 g/mol or less, compatibility with other solvents is excellent. Specifically, for example, when the olefin-based polymer is used in a hot melt adhesive, it may be uniformly mixed with other constituents such as a tackifying resin and wax.

The content of the comonomer of the olefin-based polymer may be 10 wt% to 50 wt%. In addition, the olefin-based polymer may have a density of 0.860 g/cm 3 to 0.900 g/cm 3 .

In general, as the content of the comonomer increases, the density of the olefin-based polymer decreases, and the side branch ratio increases, thereby increasing the adhesion. However, if the content of the comonomer is too high, the crystallinity of the polymer decreases and the ratio of the amorphous substance increases, so it may be difficult to solidify the polymer. When the comonomer content is 10 wt% to 50 wt%, excellent adhesion may be secured while maintaining the fluidity of the olefin-based polymer.

The softening point of the olefin-based polymer may be 80 °C to 120 °C. When the softening point of the olefin-based polymer is 80° C. or higher, it is not softened in an environment in which it can be generally placed, so that the application range is broadened. On the other hand, when the softening point is too high, a high temperature must be provided in order to process the olefin-based polymer, and thus processability may decrease and pot life may increase. From this point of view, the softening point of the olefin-based polymer may be 120° C. or less.

The present invention provides an adhesive prepared by using the above-described olefin-based polymer according to another embodiment. In an exemplary embodiment, the olefinic polymer described above may be prepared as a hot melt adhesive.

As described above, the olefin-based polymer of the present invention has a plurality of melting points and satisfies an appropriate total crystallinity and density range. can

Hereinafter, a method for producing an olefin-based polymer according to an embodiment of the present invention will be described.

The olefin-based polymer according to an embodiment of the present invention includes polymerizing olefin monomers under a catalyst for olefin polymerization. Olefin monomers are, for example, ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, 1-octene, 1-decene, 1-undecene as described above. , 1-dodencene, 1-tetradecene and 1-hexadecene, and the like, and the olefin polymer may be a homopolymer or a copolymer.

The olefin-based polymer may be prepared, for example, by a gas phase polymerization method, a solution polymerization method, or a slurry polymerization method. When the olefin polymer is prepared by the solution polymerization method or the slurry polymerization method, examples of the solvent used include a C _5-12 aliphatic hydrocarbon solvent such as pentane, hexane, heptane, nonane, decane, and isomers thereof; aromatic hydrocarbon solvents such as toluene and benzene; hydrocarbon solvents substituted with chlorine atoms such as dichloromethane and chlorobenzene; mixtures thereof, and the like, but are not limited thereto.

In general, an olefin-based polymer having a plurality of melting temperatures can be synthesized using a hybrid catalyst including a plurality of catalysts. However, in the synthesis method using the hybrid catalyst, it is difficult to predict and control the activity and copolymerization of each hybrid catalyst, so it is difficult to prepare an olefin-based polymer having properties suitable for the use, and the two or more catalyst components are not uniformly mixed. , quality control is not easy.

Accordingly, in the method for preparing an olefin-based polymer according to an embodiment, the olefin polymer is synthesized using a single catalyst. When a polymer is synthesized using a single catalyst, it is common for the polymer to have a single melting temperature, but the transition metal compound represented by the following formula A-1 shows a melting temperature of two or more in the olefin polymer even if it participates in the polymerization process as a single catalyst. Confirmed.

<Formula A-1>

In the formula A-1,

M is a Group 4 transition metal, and may be titanium (Ti), zirconium (Zr), or hafnium (Hf). In one embodiment, M may be zirconium.

each X is independently halogen, C _1-20 alkyl, C _2-20 alkenyl, C _2-20 alkynyl, C _6-20 aryl, C _1-20 alkyl C _6-20 aryl, C _6-20 aryl C _1-20 alkyl, C _1-20 alkylamido, C _6-20 arylamido or C _1-20 alkylidene. In one embodiment, X can be C _1-6 alkyl.

Each Q may independently be carbon (C), silicon (Si), germanium (Ge), or tin (Sn). For example, Q can be carbon.

R ¹ to R ¹⁴ are each hydrogen, independently substituted or unsubstituted C _1-20 alkyl, substituted or unsubstituted C _2-20 alkenyl, substituted or unsubstituted C _6-20 aryl, substituted or unsubstituted C _1-20 alkyl C _6-20 aryl, substituted or unsubstituted C _6-20 aryl C _1-20 alkyl, substituted or unsubstituted C _1-20 heteroalkyl, substituted or unsubstituted C _3-20 heteroaryl , substituted or unsubstituted C _1-20 alkylamido, substituted or unsubstituted C _6-20 arylamido, substituted or unsubstituted C _1-20 alkylidene, or substituted or unsubstituted C _1-20 silyl can be In addition, R ¹ to R ¹² may be each independently connected to adjacent groups to form a substituted or unsubstituted saturated or unsaturated C _4-20 ring.

In an exemplary embodiment, the transition metal compound represented by Formula A-1 may be a compound represented by the following A-2 or a compound represented by the following A-3, but Examples of the olefin polymerization catalyst of the present invention are as follows It is not limited to compounds.

<A-2>

<A-3>

The olefin polymerization catalyst composition of the present invention may further include a co-catalyst compound.

The promoter compound may include at least one of a compound represented by the following Chemical Formula 1, a compound represented by Chemical Formula 2, and a compound represented by Chemical Formula 3.

<Formula 1>

In Formula 1, n is an integer of 2 or more, and R _a may be a halogen atom, a C _1-20 hydrocarbon group, or a halogen-substituted C _1-20 hydrocarbon group. Specifically, R _a may be methyl, ethyl, n-butyl, or isobutyl, but is not limited thereto.

<Formula 2>

In Formula 2, D is aluminum (Al) or boron (B), R _b , R _c and R _d are each independently a halogen atom, a C _1-20 hydrocarbon group, a halogen-substituted C _1-20 hydrocarbon group, or It may be a C _1-20 alkoxy group. Specifically, when D is aluminum, R _b , R _c and R _d may each independently be methyl or isobutyl, and when D is boron, R _b , R _c and R _d are each independently pentafluoro It may be phenyl, but is not limited thereto.

<Formula 3>

[LH] ⁺ [Z(A) ₄ ] ^- or [L] ⁺ [Z(A) ₄ ] ^-

In Formula 3, L is a neutral or cationic Lewis base, [LH] ⁺ or [L] ⁺ is a Bronsted acid, Z is a group 13 element, A is each independently a substituted or unsubstituted C _6- It may be a ₂₀ aryl group or a substituted or unsubstituted C _1-20 alkyl group. Specifically, the [LH] ⁺ may be a dimethylanilinium cation, the [Z(A) ₄ ] ^- may be [B(C ₆ F ₅ ) ₄ ] ^- , and the [L] ⁺ may be [( C ₆ H ₅ ) ₃ C] ⁺ , but is not limited thereto.

The olefin polymerization catalyst of the present invention may further include a carrier supporting a transition metal compound and a cocatalyst compound.

The carrier may include a material containing a hydroxyl group on the surface, and preferably a material having a highly reactive hydroxyl group and a siloxane group that is dried to remove moisture from the surface. For example, silica dried at high temperature, silica-alumina, and silica-magnesia may be used, and these are typically oxides, carbonates, such as Na ₂ O, K ₂ CO ₃ , BaSO ₄ , and Mg(NO ₃ ) ₂ ; It may contain sulfate, and nitrate components. Alternatively, carbon, zeolite, magnesium chloride, or the like may be included. However, the present invention is not limited thereto, and it is not particularly limited as long as it can support the transition metal compound and the co-catalyst compound.

As a method of supporting the transition metal compound and the cocatalyst compound for an olefin polymerization catalyst on a carrier, a physical adsorption method or a chemical adsorption method may be used.

In an exemplary embodiment, the physical adsorption method is a method in which a solution in which a transition metal compound for an olefin polymerization catalyst is dissolved is brought into contact with a carrier and then dried, a solution in which a transition metal compound for an olefin polymerization catalyst and a cocatalyst compound are dissolved is brought into contact with a carrier A method in which the transition metal compound for an olefin polymerization catalyst is dissolved, or a solution in which the transition metal compound for an olefin polymerization catalyst is dissolved is contacted with a carrier and dried to prepare a carrier on which the transition metal compound for an olefin polymerization catalyst is supported, and separately from this, a solution in which the promoter compound is dissolved It may be a method of contacting the carrier and drying the carrier to prepare a carrier on which the cocatalyst compound is supported, and then mixing them.

In an exemplary embodiment, the chemical adsorption method is a method in which a promoter compound is first supported on the surface of a carrier, and then a transition metal compound for an olefin polymerization catalyst is supported on the promoter compound, or a functional group (e.g., In the case of silica, it may be a method of covalently bonding a hydroxy group (-OH)) on the silica surface and a catalyst compound.

Hereinafter, specific examples of the olefin-based polymer of the present invention and specific experimental examples for measuring physical properties of the prepared olefin-based polymer will be described.

Transition metal compounds represented by A-2 and A-3 were reported by Ewen and Razavi on the method for preparing a syndiotactic polypropylene polymer and the synthesis of a metallocene compound in which Cp and Fluorenyl are linked. Chem. Soc., 110, 6255 (1988) and J. Organomet. Chem., 435, 299 (1992). The transition metal compound represented by A-2 was prepared by a method known in the above paper, and the transition metal compound represented by A-3 was prepared by the method of Example 1 below.

[Example 1] Me ₂ C(Cp)(2,7- tert -Bu-Flu)HfMe ₂ Preparation of (transition metal compound represented by A-3)

Step A: Ligand 2,2-[(cyclopentadienyl)-(2,7-di- tert -butylfluorenyl)] synthesis of propane

MeLi (1.73 g, 3.77 mmol, 1.6 M in diethyl ether) was added to a solution of 2,7-di- tert -butylfluorene (1 g, 3.59 mmol) in diethyl ether (15 mL) at -30 ^o C. After raising the temperature to room temperature, the mixture was stirred for 3 hours. 6,6-dimethylfulvene (400 mg, 3.77 mmol) was diluted in diethyl ether (5 mL) and added at -30 ^o C, followed by raising the temperature to room temperature and stirring for 12 hours.

After completion of the reaction, the organic layer was separated by extraction with diethyl ether and aqueous NH ₄ Cl, and the ligand 2,2-[(cyclopentadienyl)-(2,7) through column chromatography (hexane: dichloromethane = 100: 1, v/v). -di- tert -butylfluorenyl)] propane was obtained to obtain 1.04 g (75%).

Step B: [(cyclopentadienyl)-(2,7-di- tert -butylfluorenyl)] dilithium synthesis of compounds

2,2-[(cyclopentadienyl)-(2,7-di-tert-butylfluorenyl)] propane (304 mg, 0.79 mmol) in diethyl ether (10 mL)n-BuLi (689 mg, 1.62 mmol, 1.6 M in hexane) -30^oAfter addition at C, the temperature was raised to room temperature and stirred for 12 hours. The resulting solid was filtered and dried under vacuum to [(cyclopentadienyl)-(2,7-di-tert-butylfluorenyl)] dilithium Compound 316 mg (100%) is obtained.

Step C: Isopropylidene [(cyclopentadienyl)-(2,7-di- tert -butylfluorenyl)] synthesis of hafnium dichloride

In a solution of HfCl ₄ (94 mg, 0.29 mmol) dispersed in toluene (5 mL), isopropylidene [(cyclopentadienyl)-(2,7-di- tert -butylfluorenyl)] dilithium (116 mg, 0.29 mmol) in toluene (5 mL) was added at -30 ^o C, and then the temperature was raised to room temperature and stirred for 48 hours. After completion of the reaction, the mixture was extracted with toluene, filtered, and then toluene was removed under vacuum and washed with hexane . 105 mg (57%) of the compound is obtained.

Step D: Me ₂ C(Cp)(2,7- tert -Bu-Flu)HfMe ₂ synthesis of

Isopropylidene [(cyclopentadienyl)-(2,7-di- tert -butylfluorenyl)] hafnium dichloride (95 mg, 0.15 mmol) in toluene (8 mL) was added with a solution of MeMgBr (130 mg, 0.38 mmol, 3.0 M in diethyl ether) diluted in toluene (2 mL) at -30 ^o C. Then, it is stirred for 2 hours while refluxing at 70 ^o C. After completion of the reaction, extraction with toluene was filtered, and toluene was removed under vacuum to remove Me ₂ C(CP)(2,7- tert -Bu-Flu)HfMe _{2 (} transition metal compound represented by A-3) 87 mg (97 %) is obtained.

[ ¹ H-NMR (C ₆ D ₆ , 300 MHz): 7.93 (d, 2H), 7.69 (s, 2H), 7.44-7.38 (m, 2H), 6.05 (t, 2H), 5.45 (t, 2H) ), 2.03 (s, 6H), 1.29 (s, 18H), -1.31 (s, 6H)].

[Example 2] Preparation of ethylene/1-octene copolymer

An ethylene/1-octene copolymer was prepared using an autoclave continuous process reactor. Specifically, after filling the autoclave continuous process reactor with 1-octene, a triisobutylaluminum compound (0.682 mmol/min), a transition metal compound represented by A-2 or A-3 prepared above (0.08 μmol/min) ) and dimethylanilinium tetrakis (pentafluorophenyl) borate cocatalyst (0.45 μmol/min) were simultaneously introduced into the reactor. Then, ethylene (0.5 kg/h) was introduced into the autoclave reactor, and the copolymer (Preparation Examples 1 to 5) was obtained by maintaining the temperature at 150° C. for at least 10 minutes in a continuous process at a pressure of 90 bar, and then performing a copolymerization reaction. got it Preparation Examples 1 to 5 were obtained by changing the input amount of 1-octene and the amount of hydrogen input in the production method, respectively.

Table 1 summarizes the polymerization conditions of Preparation Examples 1 to 5.

production example catalyst 1-octene dosage
(ml/min) hydrogen input
(g/hr) catalytic activity
(KgPE/gCat hr) One A-2 9.3 0.2 221 2 A-2 7.5 0.2 195 3 A-2 9.3 0.3 215 4 A-3 11.2 0.0 158 5 A-3 7.2 0.3 168

[Experimental Example] Measurement of physical properties of ethylene/1-octene copolymer

The physical properties of the polymers prepared in Preparation Examples 1 to 5 were measured and shown in Table 2 below. For comparison, conventional copolymers (Comparative Examples 1 and 2) were obtained and physical properties were measured together. In Comparative Example 1 and Comparative Example 2, DOW's Affinity 1900 and Affinity 1950 were used, respectively.

DSC Curves for Preparation Examples 1 to 5 and Comparative Examples were obtained using a Differential Scanning Calorimeter (DSC, device name: DSC 2920), and the melting temperature (Tm) and the degree of crystallinity (Crystallinity) were measured using this. did. The first degree of crystallinity means the degree of crystallinity at the first melting temperature (Tm1), and the second degree of crystallinity means the degree of crystallinity at the second melting temperature (Tm2).

1 to 3 are DSC curves for the copolymers of Preparation Examples 1 to 3, respectively. A first degree of crystallinity and a second degree of crystallinity were obtained using FIGS. 1 to 3 and Equation 3 below.

[Equation 3]

First crystallinity (%) = ΔH _{measurement 1} /ΔH _100% *100, ΔH _100% =290 (J/g)

Second crystallinity (%) = ΔH _measurement2 /ΔH _100% *100, ΔH _100% =290 (J/g)

Here, ΔH _{measurement 1} is the heat of fusion corresponding to the area of the region including the first melting temperature, and ΔH _{measurement 2} means the heat of fusion corresponding to the area of the region including the second melting temperature.

In addition, the total degree of crystallinity means the sum of the first degree of crystallinity and the second degree of crystallinity, and the degree of crystallinity ratio represents the ratio of the first degree of crystallinity and the second degree of crystallinity.

The weight average molecular weight (Mw) and molecular weight distribution (MWD) were measured using Gel Permeation Chromatography (GPC). The softening point was measured using the Ring and ball softening method (ASTM D-36). Specifically, in order to measure the softening point, about 5-6 g of the sample is put in a ring for sample production, heated and melted, the melted sample is cooled, and a ball is placed on the cooled resin and put into the softening point measuring device, The softening point was measured as the ball of the resin that reached the softening point fell while increasing the temperature.

EX Comonomer (wt%) Density (g/cm3) Mw (g/mol) MWD Softening Point (℃) Tm1(℃) Tm2(℃) First crystallinity (%) Second degree of crystallinity (%) Total crystallinity (%) Crystallinity ratio (first degree of crystallinity: second degree of crystallinity) Preparation Example 1 30.4 0.865 27,302 1.86 101.3 56.3 103.6 8.11 0.37 8.48 96:4 Preparation Example 2 26.9 0.876 31,211 1.70 104.1 70.5 107.1 11.66 0.42 12.08 97:3 Preparation 3 31.4 0.865 19,942 2.40 92.9 52.0 103.7 9.15 0.42 9.57 96:4 Preparation 4 33.8 0.865 45,791 2.14 97.2 52.8 98.5 4.54 0.12 5.66 80:20 Production Example 5 30.1 0.875 5,715 2.40 91.8 69.1 89.8 13.27 2.49 15.86 84:16 Comparative Example 1 33.7 0.870 23,535 1.65 83.6 69.5 10.26 Comparative Example 2 31.3 0.874 26,490 1.64 86.7 73.0 11.08

As shown in Table 2, the olefin-based polymer of the present invention has a first melting temperature (Tm1) and a second melting temperature (Tm2) even though it is prepared under a single catalyst.

In addition, while the olefin-based polymer of the present invention has two melting points, the total crystallinity and density have similar values to those of Comparative Examples, and have a higher softening point than Comparative Examples within the crystallinity and density range. Accordingly, the olefin-based polymer of the present invention exhibits excellent performance in a high-temperature melt adhesive due to excellent heat resistance and adhesion.

Above, embodiments belonging to the spirit of the invention have been described in detail with reference to the exemplified chemical structural formulas and preparation examples. However, the spirit of the invention is not limited to the illustrated chemical structural formulas and preparation examples, and the spirit of the invention may be variously modified based on the illustrated chemical structural formulas and preparation examples. The exemplified chemical structural formulas and manufacturing examples are provided to completely inform those of ordinary skill in the art to which the invention belongs the scope of the spirit of the invention, and the scope of the invention is within the scope of the claims. It is only defined by Therefore, it should be understood that the embodiments described above are illustrative in all respects and not restrictive.

Claims (7)

A method for producing an olefin-based polymer by copolymerizing an olefin-based monomer and an olefin-based comonomer in the presence of a single olefin polymerization catalyst comprising a transition metal compound represented by the following formula A-2 or A-3,
The copolymerized olefin-based polymer is
a softening point of 91.8° C. to 104.1° C.,
having a first melting temperature and a second melting temperature,
The first melting temperature and the second melting temperature have different values,
The first melting temperature is 52.0 ℃ to 70.5 ℃,
The second melting temperature is a method for producing an olefin-based polymer of 89.8 °C to 107.1 °C.
<Formula A-2>

<Formula A-3>

According to claim 1,
A method for producing an olefin-based polymer having a total crystallinity of 5% to 15%. 3. The method of claim 2,
The ratio of the first degree of crystallinity, which is the degree of crystallinity to the first melting temperature, and the second degree of crystallinity, which is the degree of crystallinity, which is the degree of crystallinity, to the second melting temperature is 99:1 to 75:25. According to claim 1,
A method for producing an olefin-based polymer having a weight average molecular weight of 5,000 g/mol to 60,000 g/mol. According to claim 1,
A method for producing an olefin-based polymer wherein the content of the comonomer is 10 wt% to 50 wt%. According to claim 1,
A method for producing an olefin-based polymer having a density of 0.860 g/cm 3 to 0.900 g/cm 3 . According to claim 1,
The method for producing an olefin-based polymer, wherein the olefin-based monomer and the olefin-based comonomer are ethylene and 1-octene, respectively.

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