Olefin-based polymer

文档序号：395304 发布日期：2021-12-14 浏览：8次中文

阅读说明：本技术 烯烃基聚合物 (Olefin-based polymer ) 是由朴想恩李银精朴仁成金太洙李忠勳孔镇衫全晸浩郭来根于 2020-09-28 设计创作，主要内容包括：本发明涉及满足以下条件的烯烃基聚合物：(1)熔体指数(MI,190℃,2.16kg荷重条件)为0.1g/10min至10.0g/10min,(2)密度(d)为0.860g/cc至0.880g/cc,(3)当差示扫描量热精密测量法(SSA)测量时满足T(90)-T(50)≤50且T(95)-T(90)≥10。本发明的烯烃基聚合物是引入高结晶区并显示高机械刚性的低密度烯烃基聚合物。(The present invention relates to an olefin-based polymer satisfying the following conditions: (1) a melt index (MI, 190 ℃,2.16kg weight loading conditions) of from 0.1g/10min to 10.0g/10min, (2) a density (d) of from 0.860g/cc to 0.880g/cc, (3) satisfying T (90) -T (50) ≦ 50 and T (95) -T (90) ≧ 10 when measured by differential scanning calorimetry (SSA). The olefin-based polymer of the present invention is a low-density olefin-based polymer which is introduced into a high crystalline region and exhibits high mechanical rigidity.)

1. An olefin-based polymer satisfying the following conditions (1) to (3):

(1) a Melt Index (MI) of 0.1g/10min to 10.0g/10min at 190 ℃ under a 2.16kg load,

(2) a density (d) of 0.860g/cc to 0.880g/cc, and

(3) when measured by differential scanning calorimetry (SSA), the requirements of T (90) -T (50) is less than or equal to 50 and T (95) -T (90) is more than or equal to 10 are met,

wherein T (50), T (90) and T (95) are temperatures of 50%, 90% and 95% of melting when a temperature-heat capacity curve is classified from the measurement results by differential scanning calorimetry precision measurement (SSA), respectively.

2. The olefin-based polymer of claim 1, wherein the olefin-based polymer additionally satisfies the following condition: (4) the weight average molecular weight (Mw) is from 10,000g/mol to 500,000 g/mol.

3. The olefin-based polymer of claim 1, wherein the olefin-based polymer additionally satisfies the following condition: (5) a Molecular Weight Distribution (MWD) of 0.1 to 6.0.

4. The olefin-based polymer of claim 1, wherein the olefin-based polymer additionally satisfies the following condition: (6) the melting temperature is 20 ℃ to 70 ℃ when measured by Differential Scanning Calorimetry (DSC).

5. The olefin-based polymer according to claim 1, wherein the Melt Index (MI) of the olefin-based polymer is from 0.3g/10min to 5.5g/10 min.

6. The olefin-based polymer according to claim 1, wherein the olefin-based polymer satisfies 30. ltoreq. T (90) -T (50). ltoreq.40 and 10. ltoreq. T (95) -T (90). ltoreq.20 when measured by differential scanning calorimetry precision measurement (SSA).

7. The olefin-based polymer of claim 1, wherein the olefin-based polymer is a copolymer of ethylene and an alpha-olefin comonomer of 3 to 12 carbon atoms.

8. The olefin-based polymer of claim 7, wherein the alpha-olefin comonomer comprises a comonomer selected from the group consisting of 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, 1-eicosene, norbornene, norbornadiene, ethylidene norbornene, phenylnorbornene, vinyl norbornene, dicyclopentadiene, 1, 4-butadiene, 1, 5-pentadiene, 1, 6-hexadiene, styrene, alpha-methylstyrene, divinylbenzene and 3-chloromethylstyrene, or a mixture of two or more thereof.

9. The olefin-based polymer according to claim 1, wherein the olefin-based polymer is a copolymer of ethylene and 1-butene.

10. An olefin-based polymer satisfying the following conditions:

a Melt Index (MI) of from 0.4g/10min to 7.0g/10 min;

a density (d) of 0.860g/cc to 0.880 g/cc;

when measured by differential scanning calorimetry (SSA), the conditions of T (90) -T (50) being more than or equal to 20 and less than or equal to 45 and T (95) -T (90) being more than or equal to 10 and less than or equal to 30 are satisfied;

a weight average molecular weight (Mw) of 10,000 to 500,000 g/mol;

a Molecular Weight Distribution (MWD) of 0.1 to 6.0; and

a melting temperature of 20 ℃ to 60 ℃ when measured by Differential Scanning Calorimetry (DSC).

11. The olefin-based polymer according to claim 1, wherein the olefin-based polymer is an olefin-based polymer obtained by a production process comprising: polymerizing olefin-based monomers by injecting hydrogen in the presence of a catalyst composition for olefin polymerization, the catalyst composition comprising a transition metal compound of the following formula 1:

[ formula 1]

In the formula 1, the first and second groups,

R₁the groups are the same or different and are each independently hydrogen, alkyl of 1 to 20 carbon atoms, alkenyl of 2 to 20 carbon atoms, aryl, silyl, alkaryl, aralkyl or a metalloid radical of a group 4 metal substituted with a hydrocarbyl group, and two R' s₁The groups may be linked to each other by an alkylene group containing an alkyl group of 1 to 20 carbon atoms or an aryl group of 6 to 20 carbon atoms to form a ring;

R₂the radicals are identical or different and are each independently hydrogen; halogen; alkyl of 1 to 20 carbon atoms; an aryl group; an alkoxy group; an aryloxy group; or an amido group, and R₂Two or more of the groups may be linked to each other to form an aliphatic ring or an aromatic ring;

R₃the radicals are identical or different and are each independently hydrogen; halogen; alkyl of 1 to 20 carbon atoms; or a nitrogen-containing aliphatic ring or aromatic ring which is substituted or unsubstituted with an aryl group, and in the case where a plurality of substituents are present, two or more substituents among the substituents may be linked to each other to form an aliphatic ring or an aromatic ring;

m is a group 4 transition metal; and is

Q₁And Q₂Each independently is halogen; alkyl of 1 to 20 carbon atoms; an alkenyl group; an aryl group; an alkaryl group; aralkyl group; alkylamido of 1 to 20 carbon atoms; an arylamido group; or an alkylene group of 1 to 20 carbon atoms.

12. The olefin-based polymer according to claim 11, wherein the olefin-based polymer is produced by continuous solution polymerization using a continuous stirred tank reactor by injecting hydrogen gas in the presence of the catalyst composition for olefin polymerization.

13. An olefin-based polymer satisfying the following conditions:

a Melt Index (MI) of from 0.4g/10min to 7.0g/10 min;

a density (d) of 0.860g/cc to 0.880 g/cc; and

when measured by a differential scanning calorimetry (SSA) method, the conditions of T (90) -T (50) being more than or equal to 30 and less than or equal to 40 and T (95) -T (90) being more than or equal to 10 and less than or equal to 20 are satisfied,

wherein the olefin-based polymer is an olefin-based polymer obtained by a production process comprising the steps of: polymerizing olefin-based monomers by injecting hydrogen in the presence of a catalyst composition for olefin polymerization, the catalyst composition comprising a transition metal compound of the following formula 1:

[ formula 1]

In the formula 1, the first and second groups,

R₂the radicals are identical or different and are each independentlyIs hydrogen; halogen; alkyl of 1 to 20 carbon atoms; an aryl group; an alkoxy group; an aryloxy group; or an amido group, and R₂Two or more of the groups may be linked to each other to form an aliphatic ring or an aromatic ring;

m is a group 4 transition metal; and is

14. The olefin-based polymer according to claim 13, wherein the olefin-based polymer is obtained by a production method in which the hydrogen gas is injected in an amount of 0.35 to 3 parts by weight based on 1 part by weight of the olefin-based monomer.

Technical Field

Cross Reference to Related Applications

This application claims the benefit of korean patent application No. 10-2019-0121152, filed on 30.9.2019 from the korean intellectual property office, the contents of which are incorporated herein by reference.

Technical Field

The present invention relates to an olefin-based polymer, and more particularly, to a low-density olefin-based polymer that incorporates a high crystalline region and exhibits high mechanical rigidity.

Background

Polyolefins have excellent moldability, heat resistance, mechanical properties, hygienic qualities, water vapor permeability, and appearance characteristics of molded articles, and are widely used as extrusion molded articles, blow molded articles, and injection molded articles. However, there are problems in that polyolefins, particularly polyethylene, have no polar groups in the molecule, have low compatibility with polar resins (e.g., nylon), and have poor adhesion to polar resins and metals. As a result, it is difficult to use polyolefins in admixture with polar resins and metals or in lamination with such materials. In addition, polyolefin molded articles have disadvantages of low surface hydrophilicity and antistatic property.

In order to solve these problems and improve affinity for polar materials, a method of grafting a polar group-containing monomer onto a polyolefin by radical polymerization has been widely used. However, according to this method, crosslinking and molecular branching in polyolefin molecules may be cut during the grafting reaction, and the viscosity balance of the graft polymer and the polar resin is not good, and the miscibility of both is low. Further, there is a problem that the molded article has poor appearance characteristics due to gel components generated by intramolecular crosslinking or foreign substances generated by molecular chain cleavage.

In addition, as a method for producing olefin polymers (e.g., ethylene homopolymers, ethylene/α -olefin copolymers, propylene homopolymers, and propylene/α -olefin copolymers), a method of copolymerizing polar monomers in the presence of a metal catalyst (e.g., a titanium catalyst and a vanadium catalyst) has been used. However, when polar monomers are copolymerized using such a metal catalyst, there is a problem that the molecular weight distribution or composition distribution is broad and the polymerization activity is low.

In addition, as another method, a polymerization method in the presence of a metallocene catalyst formed using a transition metal compound (for example, zirconium dichloride) and an organoaluminum oxy-compound (aluminoxane) is known. In the case of using a metallocene catalyst, an olefin polymer having a high molecular weight is obtained with high activity, and the olefin polymer thus produced has a narrow molecular weight distribution and a narrow composition distribution.

In addition, as a method for preparing a polyolefin containing a polar group using a metallocene compound having a ligand of a non-crosslinked cyclopentadienyl group, a crosslinked or non-crosslinked bis-indenyl group, or an ethylene-crosslinked unsubstituted indenyl/fluorenyl group as a catalyst, a method using a metallocene catalyst is known. However, this method has a disadvantage of extremely low polymerization activity. Therefore, a method of protecting a polar group by a protecting group is performed, but in the case of introducing a protecting group, the protecting group needs to be removed after the reaction, resulting in a complicated process.

Ansa-metallocene compounds are organometallic compounds comprising two ligands linked by a bridging group, which prevents the ligands from rotating and determines the activity and structure of the metal center.

The ansa-metallocene is used as a catalyst for preparing olefin-based homopolymers or copolymers. In particular, it is known that ansa-metallocene compounds comprising cyclopentadienyl-fluorenyl ligands can produce polyethylene having a high molecular weight and thus the microstructure of polypropylene can be controlled.

In addition, ansa-metallocene compounds comprising indenyl ligands are known to have excellent activity and can produce polyolefins having improved stereoregularity.

As described above, various studies have been made on ansa-metallocene compounds capable of controlling the microstructure of olefin-based polymers, but not to a sufficient extent.

Disclosure of Invention

Technical problem

The problem to be solved by the present invention is to provide a low-density olefin-based polymer which is obtained by polymerizing an olefin-based monomer by injecting hydrogen gas using a transition metal catalyst, thereby introducing a high crystalline region and exhibiting high mechanical rigidity.

Technical scheme

In order to solve the above problems, the present invention provides an olefin-based polymer satisfying the following conditions (1) to (3):

(1) a melt index (MI, 190 ℃,2.16kg weight loading conditions) of from 0.1g/10min to 10.0g/10min, (2) a density (d) of from 0.860g/cc to 0.880g/cc, (3) satisfies T (90) -T (50) ≦ 50 and T (95) -T (90) ≥ 10 when measured by differential scanning calorimetry (SSA),

Advantageous effects

The olefin-based polymer of the invention is a low-density olefin-based polymer in which a high crystalline region is introduced and which exhibits high mechanical rigidity.

Drawings

Fig. 1 is a graph showing the measurement results of the melting temperature of the polymer of example 1 using Differential Scanning Calorimetry (DSC).

Fig. 2 is a graph showing the measurement results of the melting temperature of the polymer of comparative example 1 using Differential Scanning Calorimetry (DSC).

Fig. 3 is a graph showing the measurement results of the polymer of example 1 by differential scanning calorimetry precision measurement (SSA).

Fig. 4 is a graph showing the measurement results of the polymer of comparative example 1 by differential scanning calorimetry precision measurement (SSA).

FIG. 5 is a graph showing T (50), T (90) and T (95) after classification of the measurement results of the polymer of example 1 by differential scanning calorimetry precision measurement (SSA).

FIG. 6 is a graph showing T (50), T (90) and T (95) after classification of the measurement results of the polymer of comparative example 1 by differential scanning calorimetry precision measurement (SSA).

Detailed Description

Hereinafter, the present invention will be described in more detail to help understanding the present invention.

It is to be understood that the words or terms used in the specification and claims are not to be interpreted as meaning as defined in commonly used dictionaries. It will be further understood that the words or terms should be interpreted as having a meaning that is consistent with their meaning in the context of the relevant art and the technical idea of the present invention, based on the principle that the inventor can appropriately define the meaning of the words or terms to best explain the present invention.

The term "polymer" as used in the present invention refers to a polymer compound prepared by polymerizing monomers of the same or different types. The general term "polymer" includes the term "interpolymer" as well as "homopolymers", "copolymers", and "terpolymers". In addition, the term "interpolymer" refers to a polymer prepared by polymerizing two or more different types of monomers. The general term "interpolymer" includes the term "copolymer" (generally used to refer to polymers prepared from two different monomers) and the term "terpolymer" (generally used to refer to polymers prepared from three different monomers). The term "interpolymer" includes polymers prepared by polymerizing four or more monomers.

The olefin-based polymer of the present invention satisfies the following (1) to (3).

(1) A melt index (MI, 190 ℃,2.16kg weight loading conditions) of from 0.1g/10min to 10.0g/10min, (2) a density (d) of from 0.860g/cc to 0.880g/cc, (3) satisfying T (90) -T (50) ≦ 50 and T (95) -T (90) ≧ 10 when measured by differential scanning calorimetry (SSA).

Here, T (50), T (90) and T (95) are temperatures of 50%, 90% and 95% of melting when a temperature-heat capacity curve is classified from the measurement results by differential scanning calorimetry precision measurement (SSA), respectively.

The olefin-based polymer of the present invention has a very low density and introduces a high crystalline region, and can exhibit even higher tensile strength and tear strength with the same level of density and melt index (MI, 190 ℃,2.16kg load condition) as compared with the conventional olefin-based polymer. The olefin-based polymer of the invention is produced by a production process comprising the steps of: olefin-based monomers are polymerized by injecting hydrogen in the presence of the catalyst composition for olefin polymerization, and by injecting hydrogen during polymerization, a high crystalline region is introduced, and excellent mechanical rigidity is exhibited.

The Melt Index (MI) can be controlled by controlling the amount of comonomer used in the catalyst used in the polymerization of the olefin-based polymer and affects the mechanical properties and impact strength of the olefin-based polymer and its moldability. In the present invention, the melt index is measured under low density conditions of 0.860g/cc to 0.880g/cc according to ASTM D1238 at 190 ℃ under a 2.16kg load, and can exhibit a value of 0.1g/10min to 10g/10min, specifically 0.3g/10min to 9g/10min, more specifically 0.4g/10min to 7g/10 min.

Also, the density can be from 0.850g/cc to 0.890g/cc, specifically from 0.850g/cc to 0.880g/cc, more specifically from 0.860g/cc to 0.875 g/cc.

In general, the density of an olefin-based polymer is affected by the type and amount of monomers used for polymerization, the degree of polymerization, and the like, and for a copolymer, the influence by the amount of comonomers is significant. The olefin-based polymer of the present invention is polymerized using a catalyst composition comprising a transition metal compound having a characteristic structure, and a large amount of a comonomer can be introduced. Therefore, the olefin-based polymer of the present invention can have a low density within the above range.

In addition, the olefin-based polymer may satisfy T (90) -T (50) ≦ 50 and T (95) -T (90) ≥ 10, specifically 20 ≦ T (90) -T (50) ≦ 45 and 10 ≦ T (95) -T (90) ≦ 30, more specifically 30 ≦ T (90) -T (50) ≦ 40 and 10 ≦ T (95) -T (90) ≦ 20, when measured by differential scanning calorimetry (SSA).

T (50), T (90) and T (95) are temperatures of 50%, 90% and 95% of melting when the temperature-heat capacity curve is graded from the measurement results by differential scanning calorimetry precision measurement (SSA), respectively.

Generally, the melting temperature (Tm) is measured using differential scanning calorimetry by a first cycle comprising heating at a constant rate to a temperature about 30 ℃ above the melting temperature (Tm) and cooling at a constant rate to a temperature about 30 ℃ below the glass transition temperature (Tg) and a second cycle to obtain a peak at the standard melting temperature (Tm). The differential scanning calorimetry precision measurement (SSA) is a method as follows: more accurate crystal information was obtained by performing a process of heating to a temperature immediately before the peak of the melting temperature (Tm) after the first cycle using Differential Scanning Calorimetry (DSC) and cooling, and repeatedly performing a process of heating to a temperature about 5 ℃ lower and cooling (eur.polym.j.2015,65,132).

In the case where a small amount of high-crystallinity region is introduced into the olefin-based polymer, when the melting temperature is measured using general Differential Scanning Calorimetry (DSC), a high-temperature melting peak may not be shown, but may be measured by differential scanning calorimetry precision measurement (SSA).

In addition, the olefin-based polymer of one embodiment of the invention may additionally satisfy (4) the condition that the weight average molecular weight (Mw) is from 10,000g/mol to 500,000g/mol, specifically, the weight average molecular weight (Mw) may be from 30,000g/mol to 300,000g/mol, more specifically, from 50,000g/mol to 200,000 g/mol. In the present invention, the weight average molecular weight (Mw) is a polystyrene-equivalent molecular weight analyzed by Gel Permeation Chromatography (GPC).

In addition, the olefin-based polymer according to one embodiment of the present invention may additionally satisfy (5) a condition that a Molecular Weight Distribution (MWD) as a ratio (Mw/Mn) of a weight average molecular weight (Mw) to a number average molecular weight (Mn) is 0.1 to 6.0, and the Molecular Weight Distribution (MWD) may be specifically 1.0 to 4.0, more specifically 2.0 to 3.0.

In addition, the olefin-based polymer according to an embodiment of the present invention may satisfy (6) a condition that a melting temperature (Tm) is 20 ℃ to 70 ℃ when measured by Differential Scanning Calorimetry (DSC), wherein the melting temperature (Tm) may be specifically 25 ℃ to 60 ℃, more specifically 25 ℃ to 50 ℃.

The olefin-based polymer may be any homopolymer selected from olefin-based monomers, specifically α -olefin-based monomers, cycloolefin-based monomers, diene-olefin-based monomers, triene-olefin-based monomers, and styrene-based monomers, or a copolymer of two or more kinds. More specifically, the olefin-based polymer may be a copolymer of ethylene with an α -olefin of 3 to 12 carbon atoms, or a copolymer with an α -olefin of 3 to 10 carbon atoms.

The α -olefin comonomer may include any one selected from the group consisting of 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, 1-eicosene, norbornene, norbornadiene, ethylidene norbornene, phenyl norbornene, vinyl norbornene, dicyclopentadiene, 1, 4-butadiene, 1, 5-pentadiene, 1, 6-hexadiene, styrene, α -methylstyrene, divinylbenzene and 3-chloromethylstyrene, or a mixture of two or more thereof.

More specifically, the olefin-based copolymer according to an embodiment of the present invention may be a copolymer of ethylene and propylene, ethylene and 1-butene, ethylene and 1-hexene, ethylene and 4-methyl-1-pentene, or ethylene and 1-octene, and more specifically, the olefin copolymer according to an embodiment of the present invention may be a copolymer of ethylene and 1-butene.

If the olefin-based polymer is a copolymer of ethylene and an alpha-olefin, the amount of alpha-olefin can be 90 wt% or less, more specifically 70 wt% or less, even more specifically 5 wt% to 60 wt%, even more specifically 20 wt% to 50 wt%, based on the total weight of the copolymer. If the α -olefin is contained within this range, it is possible to easily achieve the above-mentioned physical properties.

The olefin-based polymer of one embodiment of the present invention having the above-described physical properties and constitutional features can be prepared by a continuous solution polymerization reaction in which olefin-based monomers are polymerized by injecting hydrogen gas in the presence of a metallocene catalyst composition comprising one or more transition metal compounds in a single reactor. Therefore, in the olefin-based polymer according to one embodiment of the present invention, a block in which two or more repeating units derived from any one of the monomers constituting the polymer are linearly linked is not formed in the polymer. That is, the olefin-based polymer of the present invention may not include a block copolymer, but may be selected from the group consisting of random copolymers, alternating copolymers, and graft copolymers, more specifically random copolymers.

In one embodiment of the present invention, the hydrogen gas may be injected in an amount of 0.35 to 3 parts by weight, specifically 0.4 to 2 parts by weight, more specifically 0.45 to 1.5 parts by weight, based on 1 part by weight of the olefin-based monomer injected into the reaction system. In addition, in one embodiment of the present invention, if the olefin-based polymer is polymerized by continuous solution polymerization, the amount of hydrogen injected may be 0.35 to 3kg/h, specifically 0.4 to 2kg/h, more specifically 0.45 to 1.5kg/h, based on 1kg/h of the olefin-based monomer injected into the reaction system.

In addition, in another embodiment of the present invention, in the case where the olefin-based polymer is a copolymer of ethylene and α -olefin, the injection amount of hydrogen may be 0.8 to 3 parts by weight, specifically 0.9 to 2.8 parts by weight, more specifically 1 to 2.7 parts by weight, based on 1 part by weight of ethylene. In addition, in one embodiment of the present invention, in the case where the olefin-based polymer is a copolymer of ethylene and α -olefin and polymerization is carried out by continuous solution polymerization, hydrogen may be injected into the reaction system in an amount of 0.8 to 3kg/h, specifically 0.9 to 2.8kg/h, more specifically 1 to 2.7kg/h, based on 1kg/h of ethylene.

The olefin-based polymer of the present invention can satisfy the above-mentioned physical properties if the polymerization is carried out under the injection of hydrogen in the above-mentioned amount range.

Specifically, the olefin-based copolymer of the present invention can be obtained by a production method comprising the steps of: olefin-based monomers are polymerized by injecting hydrogen gas in the presence of a catalyst composition for olefin polymerization comprising a transition metal compound of the following formula 1.

However, in the preparation of the olefin-based polymer according to one embodiment of the present invention, it should be understood that the structural range of the transition metal compound of formula 1 is not limited to the specifically disclosed type, but includes all changes, equivalents, or substitutes included in the spirit and technical scope of the present invention.

[ formula 1]

In the formula 1, the first and second groups,

m is a group 4 transition metal; and is

In another embodiment of the present invention, in formula 2, R is₁And R₂May be the same or different and are each independently hydrogen; alkyl of 1 to 20 carbon atoms; an aryl group; or a silyl group,

R₃the groups may be the same or different and may be alkyl of 1 to 20 carbon atoms; alkenyl of 2 to 20 carbon atoms; an aryl group; an alkaryl group; aralkyl group; alkoxy of 1 to 20 carbon atoms; an aryloxy group; or an amido group, and R₆Two or more of R₆The groups may be linked to each other to form an aliphatic or aromatic ring;

Q₁and Q₂May be the same or different and are each independently halogen; alkyl of 1 to 20 carbon atoms; alkylamido of 1 to 20 carbon atoms; or arylamido group, and

m may be a group 4 transition metal.

The transition metal compound represented by formula 2 has the following characteristics: the metal sites are connected by cyclopentadienyl ligands which introduce tetrahydroquinoline, maintaining the narrow angle of Cp-M-N and close monomer Q₁-M-Q₂(Q₃-M-Q₄) The angle is wide. In addition, Cp, tetrahydroquinoline, nitrogen and metal sites are connected in sequence according to a cyclic bond, forming a more stable and robust five-membered ring structure. Thus, by reaction with a compound such as methylaluminoxane and B (C)₆F₅)₃And the like, and then applied to olefin polymerization, polymerization of olefin-based polymers characterized by high activity, high molecular weight and high copolymerization properties can be achieved even at high polymerization temperatures.

Each substituent defined in the present invention will be explained in detail as follows.

The term "hydrocarbon group" used in the present invention means a monovalent hydrocarbon group of 1 to 20 carbon atoms, which is composed of only carbon and hydrogen regardless of its structure, such as alkyl, aryl, alkenyl, alkynyl, cycloalkyl, alkaryl, and aralkyl groups, unless otherwise specified.

The term "halogen" as used herein refers to fluorine, chlorine, bromine or iodine unless otherwise indicated.

The term "alkyl" as used herein refers to straight or branched chain hydrocarbon residues, unless otherwise specified.

The term "cycloalkyl" as used herein means a cycloalkyl group including cyclopropyl and the like, unless otherwise specified.

The term "alkenyl" as used herein refers to straight or branched chain alkenyl groups unless otherwise specified.

The branch may be an alkyl group of 1 to 20 carbon atoms; alkenyl of 2 to 20 carbon atoms; aryl of 6 to 20 carbon atoms; alkylaryl of 7 to 20 carbon atoms; or aralkyl of 7 to 20 carbon atoms.

The term "aryl" as used in the present invention, unless otherwise specified, denotes aryl of 6 to 20 carbon atoms, in particular phenyl, naphthyl, anthryl, phenanthryl,Pyrenyl, anthracenyl, pyridyl, dimethylamino, methoxybenzoyl and the like, but are not limited thereto.

Alkylaryl refers to an aryl group substituted with an alkyl group.

Aralkyl means an alkyl group substituted with an aryl group.

The cyclic group (or heterocyclic group) means a monovalent aliphatic or aromatic hydrocarbon group having 5 to 20 ring-forming carbon atoms and including one or more hetero atoms, and may be a single ring or a condensed ring of two or more rings. In addition, the heterocyclic group may be substituted with an alkyl group or unsubstituted. Examples thereof may include indoline, tetrahydroquinoline, and the like, but the present invention is not limited thereto.

Alkylamino refers to amino substituted with alkyl, and includes dimethylamino, diethylamino, and the like, but is not limited thereto.

According to an embodiment of the present invention, the aryl group may preferably have 6 to 20 carbon atoms, and may be specifically phenyl, naphthyl, anthracenyl, pyridyl, dimethylphenylamino, methoxybenzoyl, or the like, but is not limited thereto.

In the present invention, the silyl group may be a silyl group substituted or unsubstituted with an alkyl group of 1 to 20 carbon atoms, for example, a silyl group, a trimethylsilyl group, a triethylsilyl group, a tripropylsilyl group, a tributylsilyl group, a trihexylsilyl group, a triisopropylsilyl group, a triisobutylsilyl group, a triethoxysilyl group, a triphenylsilyl group, a tris (trimethylsilyl) silyl group, etc., but is not limited thereto.

The compound of formula 1 may be the following formula 1-1, but is not limited thereto.

[ formula 1-1]

Further, the compound may have various structures within the range defined in formula 1.

Due to the structural characteristics of the catalyst, the transition metal compound of formula 2 can incorporate a large amount of α -olefin as well as low density polyethylene, and can produce low density polyolefin copolymer at a level of 0.850g/cc to 0.890 g/cc.

The transition metal compound of formula 1 can be prepared, for example, by the following method.

[ reaction 1]

In reaction 1, R₁To R₃、M、Q₁And Q₂The same as defined in formula 1.

Formula 1 can be prepared by the method disclosed in patent laid-open publication No. 2007 and 0003071, and the entire contents of this patent document are included in the present invention.

The transition metal compound of formula 1 may be used as a catalyst for polymerization reaction as a type of composition additionally comprising one or more of the cocatalyst compounds represented by the following formulae 2,3 and 4.

[ formula 2]

-[Al(R₄)-O]_a-

[ formula 3]

A(R₄)₃

[ formula 4]

[L-H]⁺[W(D)₄]^-Or [ L]⁺[W(D)₄]^-

In the formulae 2 to 3, the first and second groups,

R₄the groups may be the same or different from each other and each independently selected from the group consisting of halogen, a hydrocarbon group of 1 to 20 carbon atoms and a halogenated hydrocarbon group of 1 to 20 carbon atoms,

a is aluminum or boron, and A is aluminum or boron,

the D groups are each independently an aryl group of 6 to 20 carbon atoms or an alkyl group of 1 to 20 carbon atoms in which one or more hydrogen atoms may be substituted with a substituent, wherein the substituent is at least any one selected from the group consisting of a halogen, a hydrocarbon group of 1 to 20 carbon atoms, an alkoxy group of 1 to 20 carbon atoms and an aryloxy group of 6 to 20 carbon atoms,

h is a hydrogen atom, and (C) is a hydrogen atom,

l is a neutral or cationic Lewis acid,

w is a group 13 element, and

a is an integer of 2 or more.

Examples of the compound represented by formula 2 may include alkylaluminoxanes such as Methylaluminoxane (MAO), ethylaluminoxane, isobutylaluminoxane and butylaluminoxane, and modified alkylaluminoxanes obtained by mixing two or more alkylaluminoxanes, specifically methylaluminoxane, Modified Methylaluminoxane (MMAO).

Examples of the compound represented by formula 3 may include trimethylaluminum, triethylaluminum, triisobutylaluminum, tripropylaluminum, tributylaluminum, dimethylaluminum chloride, triisopropylaluminum, tri-sec-butylaluminum, tricyclopentylaluminum, tripentylaluminum, triisopentylaluminum, trihexylaluminum, trioctylaluminum, ethyldimethylaluminum, methyldiethylaluminum, triphenylaluminum, tri-p-tolylaluminum, dimethylaluminum methoxide, dimethylaluminum ethoxide, trimethylboron, triethylboron, triisobutylboron, tripropylboron, tributylboron, etc., and specifically, may be selected from trimethylaluminum, triethylaluminum and triisobutylaluminum.

Examples of the compound represented by formula 4 may include triethylammonium tetraphenylboron, tributylammonium tetraphenylboron, trimethylammonium tetraphenylboron, tripropylammonium tetraphenylboron, trimethylammonium tetrakis (p-tolyl) boron, trimethylammonium tetrakis (o, p-dimethylphenyl) boron, tributylammonium tetrakis (p-trifluoromethylphenyl) boron, trimethylammonium tetrakis (p-trifluoromethylphenyl) boron, tributylammonium tetrakis (pentafluorophenyl) boron, N-diethylaniliniumtetraphenylboron, N-diethylaniliniumtetrakis (pentafluorophenyl) boron, diethylammonium tetrakis (pentafluorophenyl) boron, triphenylphosphonium tetraphenylboron, trimethylphosphonium tetraphenylboron, dimethylaniliniumtetrakis (pentafluorophenyl) borate, triethylammonium tetraphenylaluminum, tributylammonium tetraphenylaluminum, trimethylammonium tetraphenylaluminum, tripropylammonium tetraphenylaluminum, trimethylammonium tetrakis (p-tolyl) aluminum, Tripropylammonium tetrakis (p-tolyl) aluminum, triethylammonium tetrakis (o, p-dimethylphenyl) aluminum, tributylammonium tetrakis (p-trifluoromethylphenyl) aluminum, trimethylammonium tetrakis (p-trifluoromethylphenyl) aluminum, tributylammonium tetrakis (pentafluorophenyl) aluminum, N-diethylanilinium tetraphenylaluminum, N-diethylanilinium tetrakis (pentafluorophenyl) aluminum, diethylammonium tetrakis (pentafluorophenyl) aluminum, triphenylphosphonium tetraphenylaluminum, trimethylphosphonium tetraphenylaluminum, tripropylammonium tetrakis (p-tolyl) boron, triethylammonium tetrakis (o, p-dimethylphenyl) boron, triphenylcarbonium tetrakis (p-trifluoromethylphenyl) boron or triphenylcarbonium tetrakis (pentafluorophenyl) boron.

As a first method, the catalyst composition may be prepared by a preparation method comprising a step of obtaining a mixture by contacting a transition metal compound represented by formula 1 with a compound represented by formula 2 or formula 3; and a step of adding the compound represented by formula 4 to the mixture.

In addition, as a second method, the catalyst composition may be prepared by a method of contacting the transition metal compound represented by formula 1 with the compound represented by formula 4.

In the first of the preparation methods of the catalyst composition, the molar ratio of the transition metal compound represented by formula 1 to the transition metal compound represented by formula 2/the compound represented by formula 2 or formula 3 may be 1/5,000 to 1/2, specifically 1/1,000 to 1/10, more specifically 1/500 to 1/20. If the molar ratio of the transition metal compound represented by formula 1/the compound represented by formula 2 or formula 3 is greater than 1/2, the amount of the alkylating agent is too small and alkylation of the metal compound may not be completely performed, and if the molar ratio is less than 1/5,000, alkylation of the metal compound may be achieved but activation of the alkylated metal compound may not be completely performed due to a side reaction between the remaining excess alkylating agent and the activator as the compound of formula 4. In addition, the molar ratio of the transition metal compound represented by formula 1/the compound represented by formula 4 may be 1/25 to 1, specifically 1/10 to 1, more specifically 1/5 to 1. If the molar ratio of the transition metal compound represented by formula 1/the compound represented by formula 4 is greater than 1, the amount of the activator is relatively small and the activation of the metal compound may not be completely performed, and thus, the activity of the catalyst composition may be deteriorated. If the molar ratio is less than 1/25, the activation of the metal compound may be completely carried out, but it is uneconomical in view of the unit cost of the catalyst composition due to the remaining excess alkylating agent, or the purity of the resulting polymer may be lowered.

In the second one of the preparation methods of the catalyst composition, the molar ratio of the transition metal compound represented by formula 1/the compound represented by formula 4 may be 1/10,000 to 1/10, specifically 1/5,000 to 1/100, more specifically 1/3,000 to 1/500. If the molar ratio is more than 1/10, the amount of the activator is relatively small, and the activation of the metal compound may not be completely performed, and thus the activity of the resulting catalyst composition may be decreased. If the molar ratio is less than 1/10,000, the activation of the metal compound may be completely carried out, but it is uneconomical in view of the unit cost of the catalyst composition due to the remaining excess alkylating agent, or the purity of the resulting polymer may be lowered.

During the preparation of the catalyst composition, as a reaction solvent, hydrocarbon solvents such as pentane, hexane and heptane, or aromatic solvents such as benzene and toluene can be used.

Additionally, the catalyst composition may include a supported transition metal compound and a promoter compound on a support.

As the support, any support used in metallocene-based catalysts can be used without particular limitation. Specifically, the support may be silica, silica-alumina, or silica-magnesia, and any one thereof or a mixture of two or more thereof may be used.

In the case where the support is silica, since the silica support and the functional group of the metallocene compound of formula 1 may form a chemical bond, no catalyst is separated from the surface during olefin polymerization. As a result, the generation of fouling in which polymer particles aggregate on the reactor wall side or aggregate with each other during the production of the olefin-based copolymer can be prevented. In addition, the polymer of the olefin-based copolymer produced in the presence of the catalyst comprising a silica carrier is excellent in both particle shape and apparent density.

More specifically, the support may be silica or silica-alumina which includes highly reactive siloxane groups and is dried at high temperature by a method of high temperature drying or the like.

The carrier may further comprise an oxide, carbonate, sulphate or nitrate component, for example Na₂O、K₂CO₃、BaSO₄And Mg (NO)₃)₂。

The polymerization reaction for polymerizing the olefin-based monomer can be achieved by a conventional process (for example, continuous solution polymerization, bulk polymerization, suspension polymerization, slurry polymerization and emulsion polymerization) applied to polymerization of olefin monomers.

The polymerization reaction of the olefin monomer may be carried out in an inert solvent, and as the inert solvent, benzene, toluene, xylene, isopropyl alcohol, heptane, cyclohexane, methylcyclohexane, methylcyclopentane, n-hexane, 1-hexene and 1-octene may be used, but is not limited thereto.

The polymerization of the olefin-based polymer may be carried out at a temperature of about 25 ℃ to about 500 ℃, specifically, 80 ℃ to 250 ℃, more specificallyPreferably at a temperature of from 100 ℃ to 200 ℃. The reaction pressure during the polymerization may be 1kgf/cm²To 150kgf/cm²Preferably 1kgf/cm²To 120kgf/cm²More preferably 5kgf/cm²To 100kgf/cm²。

The olefin-based polymer of the present invention has improved physical properties, and therefore, can be used for blow molding, extrusion molding or injection molding in various fields and applications for packaging, construction, living goods, and the like, including materials for automobiles, electric wires, toys, fibers, and medical uses, and in particular, for automobiles requiring excellent impact strength.

In addition, the olefin-based polymer of the present invention can be effectively used for producing a molded article.

The molded article may be a blow molded article, a cast molded article, an extrusion laminate molded article, an extrusion molded article, a foam molded article, an injection molded article, a sheet, a film, a fiber, a monofilament, a nonwoven fabric or the like.

Detailed description of the preferred embodiments

Examples

Hereinafter, embodiments of the present invention will be explained in detail so that those skilled in the art to which the present invention pertains can easily perform. However, the present invention may be implemented in various different types and is not limited to the embodiments explained herein.

Preparation example 1: preparation of transition Metal Compound A

(1) Preparation of 8- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) -1,2,3, 4-tetrahydroquinoline

(i) Preparation of lithium carbamate

1,2,3, 4-tetrahydroquinoline (13.08g,98.24mmol) and diethyl ether (150ml) were placed in a Schlenk flask. The schlank flask was immersed in a low temperature bath of-78 ℃ obtained by dry ice and acetone and stirred for 30 minutes. Then, n-BuLi (39.9mL,2.5M,98.24mmol) was injected under a nitrogen atmosphere by syringe and formed a pale yellow colorAnd (3) slurry. Then, the flask was stirred for 2 hours, and the temperature of the flask was raised to room temperature while removing generated butane gas. The flask was again immersed in a low temperature bath at-78 ℃ to lower the temperature, and CO was injected₂A gas. By injecting carbon dioxide gas, the slurry disappeared into a transparent solution. The flask was connected to a bubbler (bubbler) and the temperature was raised to room temperature while removing carbon dioxide gas. Thereafter, the remaining CO was removed under vacuum₂A gas and a solvent. After the flask was transferred to a dry box, pentane was added thereto, followed by vigorous stirring and filtration to obtain lithium carbamate as a white solid compound. In this white solid compound, diethyl ether forms a coordinate bond. In this case, the yield was 100%.

¹H NMR(C₆D₆,C₅D₅N) 'delta' 1.90(t, J ═ 7.2Hz,6H, ether), 1.50(br s,2H, quinoline-CH)₂) 2.34(br s,2H, quinoline-CH)₂) 3.25(q, J ═ 7.2Hz,4H, ether), 3.87(br, s,2H, quinoline-CH)₂) 6.76 ppm (br d, J ═ 5.6Hz,1H, quinoline-CH)

¹³C NMR(C₆D₆):δ24.24、28.54、45.37、65.95、121.17、125.34、125.57、142.04、163.09(C＝O)ppm

(ii) Preparation of 8- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) -1,2,3, 4-tetrahydroquinoline

The lithium carbamate compound (8.47g,42.60mmol) prepared in step (i) above was placed in a Schlenk flask. Then, tetrahydrofuran (4.6g,63.9mmol) and 45ml of diethyl ether were added thereto in this order. The Schlenk flask was immersed in a low-temperature bath of-20 ℃ obtained by acetone and a small amount of dry ice and stirred for 30 minutes, and n-BuLi (25.1mL,1.7M,42.60mmol) was injected. In this case, the color of the reaction mixture turned red. Stirring was carried out for 6 hours while continuously maintaining-20 ℃. Dissolving CeCl in tetrahydrofuran₃2LiCl solution (129mL,0.33M,42.60mmol) and tetramethylCyclopentanone (5.89g,42.60mmol) was mixed in a syringe and then injected into the flask under a nitrogen atmosphere. During the slow raising of the flask temperature to room temperature, the thermostat was removed after 1 hour and the temperature was kept at room temperature. Then, water (15mL) was added to the flask, and ethyl acetate was added, followed by filtration to obtain a filtrate. The filtrate was transferred to a separatory funnel, and hydrochloric acid (2N,80mL) was added thereto, followed by shaking for 12 minutes. Then, saturated sodium bicarbonate solution (160mL) was added for neutralization, and the organic layer was extracted. The organic layer was dehydrated by adding anhydrous magnesium sulfate, and filtered. The filtrate was taken and the solvent was removed. The filtrate thus obtained was separated by column chromatography using a solvent of hexane and ethyl acetate (v/v,10:1) to obtain a yellow oil. The yield was 40%.

¹H NMR(C₆D₆):δ1.00(br d,3H,Cp-CH₃) 1.63-1.73(m,2H, quinoline-CH)₂)、1.80(s,3H,Cp-CH₃)、1.81(s,3H,Cp-CH₃)、1.85(s,3H,Cp-CH₃) 2.64(t, J ═ 6.0Hz,2H, quinoline-CH₂) 2.84-2.90(br,2H, quinoline-CH)₂) 3.06(br s,1H, Cp-H), 3.76(br s,1H, N-H), 6.77(t, J ═ 7.2Hz,1H, quinoline-CH), 6.92(d, J ═ 2.4Hz,1H, quinoline-CH), 6.94(d, J ═ 2.4Hz,1H, quinoline-CH) ppm

(2) [ (1,2,3, 4-tetrahydroquinolin-8-yl) tetramethylcyclopentadienyl-. eta.⁵,κ-N]Preparation of dimethyl titanium

(i) [ (1,2,3, 4-tetrahydroquinolin-8-yl) tetramethylcyclopentadienyl-. eta.⁵,κ-N]Preparation of dilithium compounds

In a dry box, 8- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) -1,2,3, 4-tetrahydroquinoline (8.07g,32.0mmol) prepared by the above step (1) and 140ml diethyl ether were put in a round-bottom flask, the temperature was lowered to-30 ℃ and n-BuLi (17.7g,2.5M,64.0mmol) was slowly added with stirring. The reaction was carried out for 6 hours while the temperature was raised to room temperature. After that, it was washed several times with diethyl ether, and filtered to obtain a solid. The remaining solvent was removed by applying vacuum to obtain dilithium compound (9.83g) as a yellow solid. The yield was 95%.

¹H NMR(C₆D₆,C₅D₅N). delta.2.38 (br s,2H, quinoline-CH)₂)、2.53(br s,12H,Cp-CH₃) 3.48(br s,2H, quinoline-CH)₂) 4.19(br s,2H, quinoline-CH)₂) 6.77(t, J ═ 6.8Hz,2H, quinoline-CH), 7.28(br s,1H, quinoline-CH), 7.75(br s,1H, quinoline-CH) ppm

(ii) (1,2,3, 4-tetrahydroquinolin-8-yl) tetramethylcyclopentadienyl-. eta.⁵,κ-N]Preparation of dimethyl titanium

In a drying oven, TiCl is added₄DME (4.41g,15.76mmol) and diethyl ether (150mL) were placed in a round bottom flask and MeLi (21.7mL,31.52mmol,1.4M) was added slowly while stirring at-30 ℃. After stirring for 15 minutes, the [ (1,2,3, 4-tetrahydroquinolin-8-yl) tetramethylcyclopentadienyl-. eta.eta.eta.⁵,κ-N]Dilithium compound (5.30g,15.78mmol) was placed in the flask. Stirring was carried out for 3 hours while the temperature was raised to room temperature. After completion of the reaction, vacuum was applied to remove the solvent, and the resulting residue was dissolved in pentane and filtered, and the filtrate was taken. The pentane was removed by applying vacuum to obtain a dark brown compound (3.70 g). The yield was 71.3%.

¹H NMR(C₆D₆):δ0.59(s,6H,Ti-CH₃)、1.66(s,6H,Cp-CH₃) 1.69(br t, J ═ 6.4Hz,2H, quinoline-CH₂)、2.05(s,6H,Cp-CH₃) 2.47(t, J ═ 6.0Hz,2H, quinoline-CH₂) 4.53(m,2H, quinoline-CH)₂) 6.84(t, J ═ 7.2Hz,1H, quinoline-CH), 6.93(d, J ═ 7.6Hz, quinoline-CH), 7.01(d, J ═ 6.8Hz, quinoline-CH) ppm

¹³C NMR(C₆D₆):δ12.12、23.08、27.30、48.84、51.01、119.70、119.96、120.95、126.99、128.73、131.67、136.21ppm

Preparation example 2: preparation of transition Metal Compound B

(1) Preparation of 2-methyl-7- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) indoline

2-methyl-7- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) indoline was prepared by the same method as in (1) of preparation example 1 except that in (1) of preparation example 1, 2-methylindoline was used instead of 1,2,3, 4-tetrahydroquinoline. The yield was 19%.

¹H NMR(C₆D₆) δ 6.97(d, J ═ 7.2Hz,1H, CH), δ 6.78(d, J ═ 8Hz,1H, CH), δ 6.67(t, J ═ 7.4Hz,1H, CH), δ 3.94(m,1H, quinoline-CH), δ 3.51(br s,1H, NH), δ 3.24-3.08(m,2H, quinoline-CH)₂Cp-CH), delta 2.65(m,1H, quinoline-CH)²)、δ1.89(s,3H,Cp-CH₃)、δ1.84(s,3H,Cp-CH₃)、δ1.82(s,3H,Cp-CH₃) δ 1.13(d, J ═ 6Hz,3H, quinoline-CH₃)、δ0.93(3H,Cp-CH₃)ppm。

(2) [ (2-methylindolin-7-yl) tetramethylcyclopentadienyl-. eta. ]⁵,κ-N]Preparation of dimethyl titanium

(i) A dilithium salt compound (compound 4g) (1.37g, 50%) complexed with 0.58 equivalent of diethyl ether was obtained by the same method as in (2) (i) of preparation example 1, except that 2-methyl-7- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) -indoline (2.25g,8.88mmol) was used instead of 8- (2,3,4, 5-tetramethyl-1, 3-cyclopentadienyl) -1,2,3, 4-tetrahydroquinoline.

¹H NMR (pyridine-d 8) at δ 7.22(br s,1H, CH), δ 7.18(d, J ═ 6Hz,1H, CH), δ 6.32(t,1H, CH), δ 4.61(brs,1H, CH), δ 3.54(m,1H, CH), δ 3.00(m,1H, CH), δ 2.35-2.12(m,13H, CH, Cp-CH3), δ 1.39(d, indoline-CH 3) ppm.

(ii) A titanium compound was prepared by the same method as in (2) (ii) of preparation example 1 using the dilithium salt compound prepared in (i) above (compound 4g) (1.37g,4.44 mmol).

¹H NMR(C₆D₆):δ7.01-6.96(m,2H,CH)、δ6.82(t,J＝7.4Hz,1H,CH)、δ4.96(m,1H,CH)、δ2.88(m,1H,CH)、δ2.40(m,1H,CH)、δ2.02(s,3H,Cp-CH₃)、δ2.01(s,3H,Cp-CH₃)、δ1.70(s,3H,Cp-CH₃)、δ1.69(s,3H,Cp-CH₃) δ 1.65(d, J ═ 6.4Hz,3H, indoline-CH₃)、δ0.71(d,J＝10Hz,6H,TiMe₂-CH₃)ppm。

Example 1

To a 1.5L continuous process reactor, hexane solvent (5kg/h) and 1-butene (0.95kg/h) were charged, and the temperature at the top of the reactor was preheated to 140.7 ℃. Triisobutylaluminum compound (0.06mmol/min), the transition metal compound B (0.40. mu. mol/min) obtained in preparation example 2 and dimethylanilinium tetrakis (pentafluorophenyl) borate cocatalyst (1.20. mu. mol/min) were simultaneously injected into the reactor. Then, hydrogen (15cc/min) and ethylene (0.87kg/h) were injected into the reactor, and copolymerization was carried out by maintaining at 141 ℃ for 30 minutes or more in a continuous process at a pressure of 89bar, thereby obtaining a copolymer. Dried in a vacuum oven for more than 12 hours and then measured for physical properties.

Examples 2 to 5

A copolymer was obtained by performing the same copolymerization reaction as in example 1, except that the amount of the transition metal compound used, the amounts of the catalyst and cocatalyst used, the reaction temperature, the amount of hydrogen injected, and the amount of the comonomer were changed as shown in table 1 below.

Comparative example 1

DF610 from Mitsui Chemicals inc.

Comparative examples 2 to 4

A copolymer was obtained by performing the same copolymerization reaction as in example 1, except that the type of the transition metal compound, the amount of the transition metal compound used, the amounts of the catalyst and the cocatalyst used, the reaction temperature, the amount of hydrogen injected, and the amount of the comonomer were changed as shown in table 1 below.

Comparative example 5

DF710 from Mitsui Chemicals inc.

Comparative example 6

DF640 from Mitsui Chemicals inc.

Comparative example 7

EG7447 from Dow co.

[ Table 1]

Experimental example 1

With respect to the copolymers of examples 1 to 5 and comparative examples 1 to 4, physical properties were evaluated according to the following methods and are shown in tables 2 and 3 below.

1) Density of polymer

Measured according to ASTM D-792.

2) Melt Index (MI) of the Polymer

The measurement was carried out in accordance with ASTM D-1238 (condition E, 190 ℃,2.16kg load).

3) Weight average molecular weight (Mw, g/mol) and Molecular Weight Distribution (MWD)

The number average molecular weight (Mn) and the weight average Molecular Weight (MW) were measured using Gel Permeation Chromatography (GPC), respectively, and the molecular weight distribution was calculated by dividing the weight average molecular weight by the number average molecular weight.

-a column: PL Olexis

-a solvent: trichlorobenzene (TCB)

-flow rate: 1.0ml/min

-sample concentration: 1.0mg/ml

-injection amount: 200 μ l

Column temperature: 160 deg.C

-a detector: agilent high temperature RI detector

-standard: polystyrene (calibrated by cubic function)

4) Melting temperature (Tm) of Polymer

The melting temperature was obtained using a differential scanning calorimeter (DSC: differential scanning calorimeter 250) manufactured by TA instruments Co. That is, the temperature was raised to 150 ℃ for 1 minute, and lowered to-100 ℃, and then the temperature was raised again. The melting point is defined as the apex of the DSC curve. In this case, the rate of increase and decrease in temperature was controlled at 10 ℃/min, and the melting temperature was obtained during the second temperature rise.

The DSC diagram of the polymer of example 1 is shown in fig. 1, and the DSC diagram of the polymer of comparative example 1 is shown in fig. 2.

5) High temperature melting Peak of Polymer and T (95), T (90) and T (50)

The measurement was performed using a differential scanning calorimeter (DSC: differential scanning calorimeter 250) manufactured by TA instrument co. and a continuous self nucleation/annealing (SSA) measurement method.

Specifically, in the first cycle, the temperature was raised to 150 ℃, held for 1 minute, and lowered to-100 ℃. In the second cycle, the temperature was raised to 120 ℃, held for 30 minutes, and lowered to-100 ℃. In the third cycle, the temperature was raised to 110 ℃, held for 30 minutes, and lowered to-100 ℃. As described above, the process of raising and lowering the temperature to-100 ℃ at intervals of 10 ℃ was repeated to-60 ℃ to crystallize in each temperature interval.

In the last cycle, the temperature was raised to 150 ℃, and the heat capacity was measured.

The temperature-heat capacity curve thus obtained is integrated for each interval, and the heat capacity of each interval with respect to the total heat capacity is graded. Here, the temperature at which 50% of the total amount melts is defined as T (50), the temperature at which 90% of the total amount melts is defined as T (90), and the temperature at which 95% of the total amount melts is defined as T (95).

FIG. 3 shows the SSA profile of the polymer of example 1, and FIG. 4 shows the SSA profile of the polymer of comparative example 1.

FIG. 5 shows a classification chart of SSA results of the polymer of example 1, and FIG. 6 shows a classification chart of SSA results of the polymer of comparative example 1.

6) Hardness (Shore A)

Hardness was measured according to the standard of ASTM D2240 using a GC610 durometer of tecclock co and a shore a durometer of Mitutoyo co.

7) Tensile and tear Strength of polymers

The olefin-based copolymers of example 1 and comparative examples 1 to 3 were extruded to produce pellet shapes, and the tensile strength and tear strength at the time of crushing were measured according to ASTM D638(50 mm/min).

[ Table 2]

[ Table 3]

When example 1 and comparative example 1 having equivalent levels of density and MI were compared, fig. 1 and 2 measured by DSC showed similar trends and similar pattern types, and no significant difference was confirmed. However, in fig. 3 and 4 measured by SSA, it can be confirmed that there is a significant difference in the high temperature region above 75 ℃. Specifically, example 1 showed a peak at 75 ℃ or higher, while comparative example did not. Comparative example 2 and comparative example 3 showed peaks in the respective regions, but were smaller in size compared to the examples. It was found that examples 1 to 5 satisfied T (90) -T (50) ≦ 50 and also satisfied T (95) -T (90) ≧ 10 due to the difference in melting in the high-temperature region, and had broad values in T (95) -T (90) as compared with comparative examples 1 to 7.

From table 3, the mechanical strength of example 1 and comparative examples 1,2 and 3 having equivalent levels of density and MI can be compared. It can be found that example 1 introduces a polymer melted at a high temperature and shows increased mechanical rigidity, and thus tensile strength and tear strength are increased as compared to comparative examples 1 to 3.

Examples 1 to 5 correspond to polymers obtained by polymerizing olefin-based monomers by injecting hydrogen and introducing a high-crystalline region. Therefore, T (90) -T (50) ≦ 50 and T (95) -T (90) ≧ 10 are satisfied, and high mechanical rigidity is exhibited. By comparison with comparative examples 2 and 4, it was confirmed that the satisfaction of T (90) -T (50) ≦ 50 and T (95) -T (90) ≧ 10 and the mechanical rigidity can be changed depending on the presence or absence of hydrogen injection and the amount thereof during the polymerization.

In addition, if the olefin-based polymer of the present invention is included in a polypropylene-based composite, it is possible to provide a polypropylene-based composite exhibiting significantly improved impact strength properties as well as excellent mechanical strength. Hereinafter, experiments in which the olefin-based polymer of the present invention was applied to a polypropylene-based composite material are shown.

Composite material preparation example 1: preparation of polypropylene-based composite material

To 20 parts by weight of the olefin copolymer prepared in example 1 were added 60 parts by weight of a high crystalline impact co-polypropylene having a melt index (230 ℃,2.16kg) of 30g/10min (CB5230, Korea Petrochemical Industrial Co. Ltd.), 20 parts by weight of talc (KCNAP-400)^TMCoatings Co.) (average particle diameter (D)₅₀) 11.0 μm), then 0.1 part by weight of AO1010(Ciba Specialty Chemicals) as antioxidant, 0.1 part by weight of tris (2, 4-di-tert-butylphenyl) phosphite (a0168) and 0.3 part by weight of calcium stearate (Ca-St) are added. Then, the resulting mixture was melted and ground using a twin-screw extruder to prepare a polypropylene-based composite compound in a pellet shape. In this case, the twin-screw extruder had a diameter of 25. phi. and a length-to-diameter ratio of 40, provided that the barrel temperature was 200 ℃ to 230 ℃, the screw rotation speed was 250rpm, and the extrusion rate was 25 kr/hr.

Composite material preparation examples 2 to 5: preparation of polypropylene-based composite material

A polypropylene-based composite was prepared by the same method as in example 1, except that olefin copolymers shown in the following table 4 were used instead of the olefin copolymer prepared in example 1. In this case, the type of polypropylene and the ratio of the olefin copolymer and the polypropylene were changed in example 5. In Table 4 below, the polypropylene represented by CB5290 is a high crystalline impact co-polypropylene (CB5290, Korea Petrochemical Industrial Co. Ltd.) having a melt index (230 ℃,2.16kg) of 90g/10 min.

Comparative composite materials preparation examples 1 to 7: preparation of polypropylene-based composite material

In Table 4 below, the polypropylene represented by CB5290 is a high crystalline impact co-polypropylene (CB5290, Korea Petrochemical Industrial Co. Ltd.) having a melt index (230 ℃,2.16kg) of 90g/10 min.

[ Table 4]

Experimental example 2: evaluation of physical Properties of Polypropylene-based composite Material

In order to confirm physical properties of the polypropylene-based composites prepared in composite preparation examples 1 to 5 and composite comparative preparation examples 1 to 7, samples were manufactured by injection molding the polypropylene-based composites at a temperature of 230 ℃ using an injection molding machine and left in a constant temperature and humidity chamber for 1 day, and then, specific gravity of the polymer, melt index, tensile strength, flexural strength and flexural modulus, low temperature and room temperature impact strength, and shrinkage rate of the polymer were measured. The physical properties of the samples thus manufactured are shown in table 5 below.

1) Specific gravity of

Measurements were made according to ASTM D792.

2) Melt index (Ml) of the Polymer

The Melt Index (MI) of the polymer was measured according to ASTM D-1238 (condition E, 230 ℃,2.16kg load).

3) Tensile strength and bending strength

Measurements were made according to ASTM D790 using INSTRON 3365 equipment.

4) Low temperature and room temperature impact strength

The room-temperature impact strength was measured under the condition of room temperature (23 ℃ C.) and the low-temperature impact strength was measured after leaving in a low-temperature room (-30 ℃ C.) for 12 hours or more, measured in accordance with ASTM D256.

[ Table 5]

Referring to table 5, when polypropylene-based composites comprising olefin-based copolymers having equivalent levels of density and MI values are compared, it can be confirmed that the polypropylene-based composites prepared using the olefin-based polymers of examples maintain similar levels of low-temperature impact strength and room-temperature impact strength and improve mechanical strength such as tensile strength and flexural strength, as compared to the polypropylene-based composites prepared using the olefin-based polymers of comparative examples. From this, it was confirmed that the mechanical rigidity of the polypropylene-based composite material can be improved by including the olefin-based copolymer of example, which has introduced a high crystalline region and exhibits high mechanical rigidity, in the polypropylene-based composite material.

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