TW202222958A - Thermoplastic resin composition - Google Patents

Abstract

The present invention relates to a thermoplastic resin composition including a polyolefin-polystyrene-based multi-block copolymer having a structure in which a polystyrene chain is attached to both ends of a polypropylene and polyolefin chain, and the thermoplastic resin composition according to the present invention has excellent elongation and tensile strength as well as high fluidity properties, and thus, may exhibit excellent molding processability.

Description

Thermoplastic resin composition

The present invention relates to a thermoplastic resin composition comprising a polyolefin-polystyrene-based multi-block copolymer having a structure in which polystyrene chains are bonded to both ends of polypropylene and polyolefin chains. Cross-referencing of related applications

This application claims Korean Patent Application No. 10-2020-0096157 filed on July 31, 2020, Korean Patent Application No. 10-2020-0095282 filed on July 30, 2020, and For the benefit of No. 10-2021-0100047, filed on July 29, 2021, the full text of these cases is hereby incorporated by reference.

In order to impart a luxurious feel to an automobile interior material, a method of injecting a resin composition composed of polycarbonate and acrylonitrile-butadiene-styrene (ABS) and then bonding to a surface material has been used. However, the problem is that the procedure is complicated and the unit price of the product increases.

Accordingly, a polypropylene-based resin composition comprising polypropylene (PP) as a main component and an impact resistance reinforcing material and an inorganic filler has been utilized. Polypropylene has excellent rigidity and moldability, and thus, is widely used as a material for automobile interior and exterior parts, but has a disadvantage of weak impact strength.

The polypropylene-based resin composition using the ethylene-α-olefin copolymer has balanced physical properties such as impact strength, elastic modulus, and flexural rigidity, has good moldability, and is inexpensive, which are advantages. However, depending on various usage environments, the polypropylene-based resin composition using the ethylene-α-olefin copolymer has limitations in securing impact resistance.

In addition, styrene-ethylene-butylene-styrene (SEBS), which is a styrene-based thermoplastic elastomer, has also been used in polypropylene-based resin compositions, but SEBS is expensive and has the ability to significantly reduce the fluidity of polypropylene. And thus cause the problem of flow marks or incomplete injection.

Therefore, there is still a need to develop a thermoplastic resin composition that maintains the high fluidity of polypropylene without deteriorating its mechanical and physical properties.

[Prior Art Literature]

[Patent Literature]

(Patent Document 1) Korean Patent Application Publication No. 10-1657925.

technical problem

An aspect of the present invention proposes a thermoplastic resin composition having excellent elongation and tensile strength while having high fluidity. technical solution

According to an aspect of the present invention, a thermoplastic resin composition is proposed, which includes (1) polypropylene, and (2) a polyolefin-polystyrene-based multiblock copolymer satisfying the following conditions (a) and (b).

(a) Complex viscosity (η*) at a temperature of 160°C and a frequency (ω) of 0.5 rad/s: 40,000 to 350,000 Pa·s,

(b) Compound viscosity at a temperature of 160°C and a frequency of 125 rad/s: 900 to 3,500 Pa·s. Beneficial effect

The thermoplastic resin composition according to the present invention has excellent elongation and tensile strength and high fluidity, and thus, can exhibit excellent moldability.

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

It will be understood that the words and terms used in the description of the present invention and the scope of the claims should not be limited to the meanings defined in commonly used dictionaries. It will be further understood that based on the principles that the inventors can properly define the meanings of such words and terms to best explain the present invention, such words and terms should be interpreted in a meaning consistent with the meaning within the scope of the art and technology relevant to the present invention .

As used herein, the term "composition" includes not only reaction products and decomposition products formed from the materials of the related composition, but also mixtures of the materials of the related composition.

As used herein, the term "polymer" refers to a polymer made by polymerizing monomers, whether of the same or different types. Thus, the generic term "polymer" encompasses the term "homopolymer" (which generally refers to a polymer made from only one monomer) and the term "interpolymer" as defined below.

As used herein, the term "interpolymer" refers to a polymer prepared by polymerizing at least two different monomers. Thus, the generic term "interpolymer" encompasses the term "copolymer" (which generally refers to a polymer made from two different monomers) and the term "polymer" (which is made from two or more different monomers) be made of).

Hereinafter, the present invention will be described in detail.

The thermoplastic resin composition according to the present invention includes (1) polypropylene, and (2) a polyolefin-polystyrene-based multiblock copolymer satisfying the following conditions (a) and (b).

(a) Complex viscosity (η*) at a temperature of 160°C and a frequency (ω) of 0.5 rad/s: 40,000 to 350,000 Pa·s,

(b) Composite viscosity at a temperature of 160°C and a frequency of 125 rad/s: 900 to 3,500 Pa·s.

Hereinafter, the respective constituent components will be described in detail.

(1) Polypropylene

In the thermoplastic resin composition according to the embodiment of the present invention, the polypropylene can be specifically a polypropylene homopolymer, or a copolymer of propylene and α-olefin monomer, wherein the copolymer can be alternating or random or block copolymer.

The α-olefin-based monomer may specifically be an aliphatic olefin having 2 to 12 carbon atoms, or 2 to 8 carbon atoms. More specifically, examples thereof may be ethylene, propylene, 1-butene, 1-pentene, 3-methyl-1-butene, 1-hexene, 4-methyl-1-pentene, 3- Methyl-1-pentene, 1-heptene, 1-octene, 1-decene, 1-undecene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-diene Decene, 4,4-dimethyl-1-pentene, 4,4-diethyl-1-hexene, 3,4-dimethyl-1-hexene and the like, and any of these may be used one or a mixture of two or more of them.

More specifically, the polypropylene may be any one or two or two selected from the group consisting of polypropylene copolymers, propylene-α-olefin copolymers, and propylene-ethylene-α-olefin copolymers. Mixtures of more, wherein the copolymer can be a random or block copolymer.

In addition, the polypropylene has a melt flow index (MI) of 0.5 g/10 min to 100 g/10 min measured at 230°C and a load of 2.16 kg. Specifically, the melt flow index (MI) may be 1 g/10 min to 90 g/10 min. When the melt flow index of polypropylene is not within the above range, problems may occur during injection molding of the thermoplastic resin composition.

Specifically, in the thermoplastic resin composition according to the embodiment of the present invention, the polypropylene may have a melt flow index (MI) of 0.5 g/10 min to 100 g/10 min measured at 230° C. and a load of 2.16 kg , specifically an impact copolymer of 1 g/10 min to 90 g/10 min, or more specifically, a polypropylene-ethylene impact copolymer. Based on the total weight of the polypropylene-based composite material, the content of the impact-resistant copolymer may be 10% to 90% by weight, specifically 20% to 80% by weight, and more specifically 40% to 60% by weight. When the impact copolymer having the above physical properties in the above content range is included as polypropylene, the strength properties, especially the room temperature strength properties, can be improved.

The impact copolymer meeting the above physical property requirements may be prepared using typical polymer preparation reactions, or may be commercially available and used. Specific examples thereof may include SEETEC™ M1600 (a product of LG Chem) and the like.

In addition, in the thermoplastic resin composition according to the embodiment of the present invention, the polypropylene may specifically have a DSC melting point in the range of 120 to 160° C. and under the conditions of 230° C. and a load of 2.16 kg measured according to ASTM-D 1238 One or more random polypropylene copolymers having a melt flow rate (MFR) in the range of 5 g/10 min to 120 g/10 min. Based on the total weight of the polypropylene-based composite material, the content of the random propylene copolymer may be 10% to 90% by weight, specifically 20% to 80% by weight, and more specifically 40% to 60% by weight. When the polypropylene having the above physical properties is included in the above content range, the mechanical strength, such as hardness, of the thermoplastic resin composition can be improved. The random propylene copolymers meeting the above physical property requirements can be prepared using typical polymer preparation reactions, or can be purchased and used. Specific examples thereof may include Braskem™ PP R7021-50RNA of Braskem America Inc., Formolene™ 7320A of Formosa Plastics Corporation of USA, and the like.

(2) Polyolefin-polystyrene-based multi-block copolymer

In the thermoplastic resin composition according to the embodiment of the present invention, the polyolefin-polystyrene-based multi-block copolymer is characterized by satisfying the following conditions (a) and (b).

(a) Complex viscosity (η*) at a temperature of 160°C and a frequency (ω) of 0.5 rad/s: 40,000 to 350,000 Pa·s,

(b) Composite viscosity at a temperature of 160°C and a frequency of 125 rad/s: 900 to 3,500 Pa·s.

The inventors of the present invention have conducted studies to produce polyolefin-polystyrene-based multi-block copolymers excellent in processability, and have confirmed that by using a novel transition metal compound as a catalyst, it is possible to obtain a specific complex viscosity range and utilize This is a polyolefin-polystyrene-based multi-block copolymer that realizes desired processability.

That is, the polyolefin-polystyrene-based multiblock copolymer contained in the thermoplastic resin composition of the present invention is produced using a specific transition metal compound having a novel structure as a catalyst described below, and The copolymer has a low compound viscosity in a processing range (eg, a high frequency range), and thus, exhibits excellent processability.

A composite viscosity map can be measured as a function of frequency using, for example, the Advanced Rheological Expansion System (ARES). The frequency refers to the angular velocity applied to the composite solution and its units are rad/s. As the frequency increases, the velocity of the composite solution decreases, which is known as shear thinning. That is, the graph shows that the composite viscosity (poise) of the y-axis according to the frequency of the x-axis (rad/s) is related to the fluidity, and the lower the slope of the composite viscosity with respect to frequency, the lower the fluidity, and the higher the slope, the higher the liquidity.

Compared with typical polyolefin-polystyrene-based multi-block copolymers, the polyolefin-polystyrene-based multi-block copolymer contained in the thermoplastic resin composition of the present invention has a high frequency range (especially It has a low compound viscosity at 120 to 500 rad/s), and therefore, the magnitude of shear thinning is large, thereby exhibiting excellent flow processability.

Specifically, the composite viscosity of the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition of the present invention is measured at a temperature of 160° C., specifically, at a frequency of 0.5 rad/s. The compound viscosity is 40,000 to 350,000 Pa·s, and the compound viscosity at a frequency of 125 rad/s is 900 to 3,500 Pa·s. Specifically, the compound viscosity at a frequency of 0.5 rad/s is 45,000 to 300,000 Pa·s, the compound viscosity at a frequency of 125 rad/s is 1,000 to 3,300 Pa·s, and more specifically, at 0.5 rad/s The compound viscosity at a frequency of s is 46,000 to 290,000 Pa·s, and the compound viscosity at a frequency of 125 rad/s is 1,000 to 3,200 Pa·s.

The complex viscosity (poise), which is related to frequency (frequency, rad/s), has a great correlation with the fluidity of the copolymer. The higher the slope of the complex viscosity with respect to each frequency, the higher the flowability, which means that the processability of the copolymer is good. The correlation between the frequency-dependent complex viscosity and the fluidity of the copolymer can be described via parameters such as MI 5 (@230°C), and the like.

The polyolefin-polystyrene-based multi-block copolymer may have a weight average molecular weight of 50,000 to 400,000 g/mol, specifically 60,000 to 350,000 g/mol, or 70,000 to 300,000 g/mol, or 70,000 to 280,000 g/mol .

In addition, the molecular weight distribution of the polyolefin-polystyrene-based multi-block copolymer may be 1.5 to 3.0, specifically 1.6 to 2.5, 1.6 to 2.0, 1.5 to 2.5, 1.5 to 2.0, or 1.6 to 1.9.

The weight-average molecular weight and number-average molecular weight are the polystyrene-converted molecular weights analyzed by gel permeation chromatography (GPC), and the molecular weight distribution is calculated from the ratio (weight-average molecular weight)/(number-average molecular weight).

The polyolefin-polystyrene-based multiblock copolymer may be one or more selected from the group consisting of: polystyrene-poly(ethylene-co-propylene)-polystyrene block copolymer , polystyrene-poly(ethylene-co-1-butene)-polystyrene block copolymer, polystyrene-poly(ethylene-co-1-pentene)-polystyrene block copolymer, polystyrene Styrene-poly(ethylene-co-1-hexene)-polystyrene block copolymer, polystyrene-poly(ethylene-co-1-heptene)-polystyrene block copolymer, and polyphenylene Ethylene-poly(ethylene-co-1-octene)-polystyrene block copolymer.

In addition, the polyolefin block of the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition of the present invention may include one or more of repeating units represented by the following formula.

[Formula a]

In the above formula a,

R ₁ can be hydrogen, an alkyl group having 1 to 20 carbon atoms, an alkyl group having 1 to 20 carbon atoms substituted with a silyl group, an aralkyl group having 7 to 20 carbon atoms, or a silyl group substituted an aralkyl group having 7 to 20 carbon atoms, and

n may be an integer from 1 to 10,000.

Alternatively, according to embodiments of the present invention, R ₁ may be hydrogen, or an alkyl group having 3 to 20 carbon atoms.

Alternatively, according to embodiments of the present invention, R ₁ may be hydrogen, or an alkyl group having 3 to 12 carbon atoms. Specifically, R ₁ can be hydrogen, or an alkyl group having 4 to 12 carbon atoms.

Alternatively, n may be an integer from 10 to 10,000. Specifically, n may be an integer of 500 to 7,000.

Meanwhile, in the formula shown in the specification of the present invention, "*" is the end point of the repeating unit and represents a connection point.

When the polyolefin block includes two or more repeating units represented by the above formula a, the polyolefin block may include repeating units represented by the following formula b.

[Formula b]

In the above formula b,

Each of R1 _' and R1" is independently hydrogen, alkyl having ₁ to 20 carbon atoms, alkyl substituted with silyl having 1 to 20 carbon atoms, aryl having 7 to 20 carbon atoms an alkyl group, or a silyl-substituted aralkyl group having 7 to 20 carbon atoms, wherein R ₁ ' and R ₁ ″ are different from each other,

0 < p < 1, and

n' may be an integer from 1 to 10,000.

Alternatively, according to an embodiment of the present invention, R ₁ ′ and R ₁ ″ may each independently be hydrogen, or an alkyl group having 3 to 20 carbon atoms, and specifically, may each independently be hydrogen, or an alkyl group having 3 The alkyl group having to 12 carbon atoms, and more specifically, may each independently be hydrogen, or an alkyl group having 4 to 12 carbon atoms.

Alternatively, n' may specifically be an integer of 10 to 10,000, and more specifically, n' may be an integer of 500 to 7,000.

According to an embodiment of the present invention, in the above formula b, either one of R ₁ ′ or R ₁ ″ can be hydrogen, and the other can be a substituent other than hydrogen in the above substituents.

That is, when the polyolefin block includes two or more repeating units represented by the above formula a, the structure in which R ₁ is hydrogen and R ₁ is an alkyl group having 1 to 20 carbon atoms other than hydrogen, a silicon The structure of a radical-substituted alkyl group having 1 to 20 carbon atoms, an aralkyl group having 7 to 20 carbon atoms, or a silicon group-substituted aralkyl group having 7 to 20 carbon atoms may be randomly linked. Specifically, a structure in which R ₁ is hydrogen and a structure in which R ₁ is an alkyl group having 3 to 20 carbon atoms other than hydrogen may be linked randomly.

Or, more specifically, the polyolefin block has a structure in which R ₁ is a hydrogen structure and R ₁ is a structure in which an alkyl group having 3 to 12 carbon atoms is connected to each other. More specifically, the polyolefin block has a structure in which R ₁ is hydrogen and R ₁ is an alkyl group having 4 to 12 carbon atoms.

When the polyolefin block includes two or more repeating units represented by the above formula a, the polyolefin block may include a structure in which R ₁ in the above formula a is hydrogen and R ₁ has a substituent other than hydrogen structure, the weight ratio is 30:90 to 70:10, the specific weight ratio is 40:60 to 60:40, and the more specific weight ratio is 45:75 to 55:25.

When the polyolefin block includes a structure in which R ₁ in the above formula a is hydrogen and a structure in which R ₁ has a substituent other than hydrogen in the above range, the structure of the obtained block copolymer includes appropriate The degree of branching, and therefore, has a high modulus value of 300% and a high elongation at the rupture value, thereby exhibiting excellent elasticity, and also exhibiting high molecular weight and broad molecular weight distribution, and therefore, can have excellent Processability.

In addition, the first polystyrene block of the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition of the present invention may include one or more repeating units represented by the following formula c.

[Formula c]

In the above formula c,

R ₂ is an alkyl group having 6 to 20 carbon atoms, or a halogen-substituted aryl group having 6 to 20 carbon atoms, an alkyl group having 1 to 12 carbon atoms, a ring having 3 to 12 carbon atoms an alkyl group, an alkoxy group having 1 to 8 carbon atoms, or an aryl group having 6 to 12 carbon atoms, and

l is an integer from 10 to 1,000.

R ₂ can be phenyl, or unsubstituted or halogen-substituted phenyl, alkyl with 1 to 8 carbon atoms, cycloalkyl with 3 to 12 carbon atoms, cycloalkyl with 1 to 8 carbon atoms Alkoxy, or aryl having 6 to 12 carbon atoms. Alternatively, _R2 can be phenyl.

l is an integer of 10 to 1,000, and may specifically be an integer of 50 to 700. l When it is within the above range, the viscosity of the polyolefin-polystyrene block copolymer prepared by the method of the present invention can be at an appropriate level.

In particular, in the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition of the present invention, the polyolefin block includes the repeating unit represented by the above formula a and includes the above formula c The first polystyrene blocks of the represented repeating units can be joined to each other to form a complex block represented by the following formula d.

[Formula d]

In the above formula d,

R ₁ can be hydrogen, an alkyl group having 1 to 20 carbon atoms, an alkyl group having 1 to 20 carbon atoms substituted with a silyl group, an aralkyl group having 7 to 20 carbon atoms, or a silyl group substituted an aralkyl group having 7 to 20 carbon atoms, and

R ₂ is an alkyl group having 6 to 20 carbon atoms, or a halogen-substituted aryl group having 6 to 20 carbon atoms, an alkyl group having 1 to 12 carbon atoms, a ring having 3 to 12 carbon atoms alkyl, alkoxy having 1 to 8 carbon atoms or aryl having 6 to 12 carbon atoms,

l is an integer from 10 to 1,000, and

n is an integer from 1 to 10,000.

Alternatively, in the above formula d, R ₁ , R ₂ , l and n are the same as defined in formula a and formula c, respectively.

Alternatively, where the polyolefin block includes repeating units represented by formula a above, a complex block formed by coupling a first polystyrene block including repeating units represented by formula c above may be represented by formula e below .

[Formula e]

In the above formula e, R ₁ ′, R ₁ ″, R ₂ , p, l and n′ are the same as those defined in formula a or c, respectively.

In addition, in one example of the present invention, when the polyolefin-polystyrene-based multi-block copolymer is prepared, the styrene-based monomer can form a polyolefin block, and the styrene-based monomer can be coupled to the organozinc at the same time compounds and polymerize to form separate styrenic polymer blocks. In this disclosure, the isolated styrenic polymer block is referred to as the second polystyrene block. The second polystyrene block may include repeating units represented by the following formula f.

[Formula f]

In the above formula f,

R ₃ is an aryl group having 6 to 20 carbon atoms, or a halogen-substituted aryl group having 6 to 20 carbon atoms, an alkyl group having 1 to 12 carbon atoms, a ring having 3 to 12 carbon atoms an alkyl group, an alkoxy group having 1 to 8 carbon atoms, or an aryl group having 6 to 12 carbon atoms, and

m is an integer from 10 to 1,000.

Alternatively, according to an embodiment of the present invention, R ₃ can be phenyl, or unsubstituted or halogen-substituted phenyl, alkyl having 1 to 8 carbon atoms, cycloalkyl having 3 to 12 carbon atoms , an alkoxy group having 1 to 8 carbon atoms, or an aryl group having 6 to 12 carbon atoms. Alternatively, _R3 can be phenyl.

m is an integer of 10 to 1,000, and may specifically be an integer of 50 to 700.

That is, the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition of the present invention may include the first polystyrene block including the repeating unit represented by the above formula c and the above The second polystyrene block represented by formula f.

Accordingly, the block copolymer composition may comprise a triblock copolymer comprising a polyolefin block comprising one or more repeating units represented by the following formula a, including by the following formula The first polystyrene block of the repeating unit represented by c, and the second polystyrene block including the repeating unit represented by the following formula f.

[Formula a]

[Formula c]

[Formula f]

In the above formula,

R ₁ is hydrogen, alkyl having 1 to 20 carbon atoms, alkyl substituted with silyl having 1 to 20 carbon atoms, aralkyl having 7 to 20 carbon atoms, or silyl substituted aralkyl having 7 to 20 carbon atoms,

R ₂ and R ₃ are aryl groups having 6 to 20 carbon atoms, or halogen-substituted aryl groups having 6 to 20 carbon atoms, alkyl groups having 1 to 12 carbon atoms, 3 to 12 carbon atoms atomic cycloalkyl, alkoxy having 1 to 8 carbon atoms or aryl having 6 to 12 carbon atoms,

n is an integer from 10 to 10,000, and

Each of l and m is independently an integer from 10 to 1,000.

Alternatively, in the above formula, R ₁ , R ₂ , R ₃ , n, l and m are the same as defined in formula a, c and f, respectively.

Preparation method of polyolefin-polystyrene multi-block copolymer

The method for preparing the polyolefin-polystyrene-based multi-block copolymer is characterized by comprising (S1) by using an organozinc compound as a chain transfer agent, in a catalyst composition including a transition metal compound represented by the following formula 1 In the presence of, polymerizing an olefin-based monomer to form a polyolefin block, and (S2) in the presence of an alkyllithium compound including a silicon atom and a triamine compound, by anionic polymerization of the polyolefin block and the styrene-based monomer The reaction forms polystyrene blocks.

By using the transition metal compound represented by Formula 1, which is effectively used in the polymerization reaction of olefin-based monomers, as a catalyst, and then continuously performing an anionic polymerization reaction of styrene, a polyolefin-polyphenylene to be described later is formed. Ethylene block, the polyolefin-polystyrene-based multi-block copolymer formed by the method for preparing the polyolefin-polystyrene-based multi-block copolymer can exhibit specific height of tanδ peak and half of tanδ peak height width.

Step (S1)

Step (S1) is a step of polymerizing an olefin-based monomer to form a polyolefin block by using an organozinc compound as a chain transfer agent in the presence of a catalyst composition including a transition metal compound represented by the following formula 1.

[Formula 1]

In Equation 1 above,

Each of R ₁ to R ₁₁ is independently hydrogen, alkyl having 1 to 20 carbon atoms, alkenyl having 2 to 20 carbon atoms, alkynyl having 2 to 20 carbon atoms, alkynyl having 3 to 20 carbon atoms Cycloalkyl of carbon atoms, aryl group of 6 to 20 carbon atoms, arylalkoxy of 7 to 20 carbon atoms, alkoxy of 1 to 20 carbon atoms, 7 to 20 carbon atoms atomic alkaryl, alkylsilyl having 1 to 20 carbon atoms, or aralkyl having 7 to 20 carbon atoms.

Two or more of R ₁ to R ₁₁ adjacent to each other may be connected to each other to form an aliphatic ring having 3 to 20 carbon atoms or an aromatic ring having 6 to 20 carbon atoms, and

Each of X ₁ and X ₂ is independently hydrogen, halogen, hydroxy, amine, thio, silyl, cyano, nitro, alkyl having 1 to 20 carbon atoms, 2 to 20 carbon atoms Alkenyl, alkynyl having 2 to 20 carbon atoms, cycloalkyl having 3 to 20 carbon atoms, aryl having 6 to 20 carbon atoms, alkaryl having 7 to 20 carbon atoms, Aralkyl groups of 7 to 20 carbon atoms, heteroaryl groups of 5 to 20 carbon atoms, alkoxy groups of 1 to 20 carbon atoms, aryloxy groups of 6 to 20 carbon atoms, 1 to 20 carbon atoms Alkylamino groups of 20 carbon atoms, arylamine groups of 6 to 20 carbon atoms, alkylthio groups of 1 to 20 carbon atoms, arylthio groups of 6 to 20 carbon atoms, arylthio groups of 1 to 20 carbon atoms Alkylsilyl with carbon atoms, or arylsilyl with 6 to 20 carbon atoms.

When the polymerization is carried out in the presence of excess chain transfer agent (eg, (Et) ₂ Zn) relative to the catalyst, the olefin polymer chain initiates a rapid transalkylation reaction between zinc (Zn) and hafnium (Hf) and It grows uniformly from dialkylzinc, thereby achieving living polymerization, which is called coordination chain transfer polymerization (CCTP). Typically used metallocene catalysts cannot perform living polymerization via β-elimination procedures, and the few catalysts known to be useful in CCTP can only perform single polymerization of ethylene and α-olefins, so it is difficult to The polymerization of ethylene and alpha-olefins is carried out via CCTP. Therefore, it is extremely difficult to use general transition metal compounds as catalysts to conduct living polymerization via CCTP and obtain block copolymers.

On the other hand, the hafnium compound represented by the above formula 1 is a [N ^{amine group} , N, C ^-aryl ]HfMe ₂ -type complexes exhibiting excellent α-olefin incorporation capacity in the polymerization of ethylene and α-olefins. In particular, the molecular weight or alpha-olefin content of the olefin polymer varies depending on the content of the chain transfer agent, indicating that this compound was successfully used in CCTP and that the beta-removal reaction that occurred was negligible enough to be ignored. That is, using the hafnium compound represented by the above formula 1, the polymerization reaction of ethylene and an α-olefin-based monomer can be carried out by a living polymerization reaction via CCTP, and block copolymers having various block compositions can be successfully produced .

In addition, the hafnium compound can be used to convert and perform CCTP to anionic styrene polymerization to synthesize polyolefin-polystyrene block copolymers. As mentioned above, the hafnium compound can be successfully used as a catalyst for the production of olefin polymers, which is a unique feature achievable through the novel structure of the hafnium compound represented by Formula 1 above.

Specifically, in Formula 1 above, R ₁ to R ₁₁ may each independently be hydrogen, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, or a cycloalkyl group having 6 to 20 carbon atoms. Aryl of 20 carbon atoms. Preferably, R ₁ to R ₁₀ may be hydrogen, and at the same time, R ₁₁ may be hydrogen, or an alkyl group having 1 to 20 carbon atoms, or an aryl group having 6 to 20 carbon atoms. More preferably, R ₁ to R ₁₀ may be hydrogen, and at the same time, R ₁₁ may be hydrogen, or an alkyl group having 1 to 20 carbon atoms.

Alternatively, in Formula 1 above, R ₁ to R ₁₁ may each independently be hydrogen, an alkyl group having 1 to 20 carbon atoms, or an aryl group having 6 to 20 carbon atoms. At this time, R ₃ and R ₄ may be connected to each other to form an aromatic ring having 5 to 20 carbon atoms, eg, a benzene ring. Preferably, R ₃ and R ₄ may be connected to each other to form a benzene ring, and at this time, R ₁₁ may be an alkyl group having 1 to 20 carbon atoms, or an aryl group having 6 to 20 carbon atoms.

Alternatively, in Formula 1 above, R ₁ , R ₂ , and R ₅ to R ₁₀ may be hydrogen, and R ₃ , R ₄ , and R ₁₁ may each independently be hydrogen, or have 1 to 20 carbon atoms. Alkyl, wherein _R3 and R4 may be attached to each other to form an aromatic ring having ₅ to 20 carbon atoms, eg, a benzene ring.

Meanwhile, X ₁ and X ₂ may each independently be hydrogen, an alkyl group having 1 to 20 carbon atoms, a cycloalkyl group having 3 to 20 carbon atoms, or an aryl group having 6 to 20 carbon atoms, And preferably, each may be independently an alkyl group having 1 to 20 carbon atoms, wherein X ₁ and X ₂ may be the same as each other.

In the present invention, the term "alkyl" refers to a straight or branched chain hydrocarbon radical.

In the present invention, the term "alkenyl" refers to a straight-chain or branched-chain alkenyl group.

In the present invention, the term "aryl" preferably has 6 to 20 carbon atoms, and may specifically be phenyl, naphthyl, anthracenyl, pyridyl, dimethylanilinyl, anisole, etc., but not this limit.

In the present invention, the term "alkaryl" refers to an aryl group substituted with the above alkyl group.

In the present invention, the term "aralkyl" refers to an alkyl group substituted with the above aryl group.

In the present invention, the term "alksilyl" may be a silyl group substituted with an alkyl group having 1 to 20 carbon atoms, eg, trimethylsilyl or triethylsilyl.

In the present invention, the term "alkylamino group" refers to an amino group substituted with the above alkyl group, for example, dimethylamino group, diethylamino group, etc., but not limited thereto.

In the present invention, unless otherwise stated, "hydrocarbyl" refers to a monovalent hydrocarbon group having 1 to 20 carbon atoms and consisting only of carbon and hydrogen, such as alkyl, aryl, alkenyl, alkynyl, cycloalkyl , alkaryl, or aralkyl, regardless of structure.

More specifically, the hafnium compound represented by the above formula 1 may be a hafnium compound represented by the following formula 1a or 1b.

[Formula 1a]

[Formula 1b]

In the above formulas 1a and 1b,

R ₁₁ is hydrogen, alkyl having 1 to 20 carbon atoms, alkenyl having 2 to 20 carbon atoms, alkynyl having 2 to 20 carbon atoms, cycloalkyl having 3 to 20 carbon atoms, Aryl having 6 to 20 carbon atoms, arylalkoxy having 7 to 20 carbon atoms, alkoxy having 1 to 20 carbon atoms, alkaryl having 7 to 20 carbon atoms, an alkylsilyl group of 1 to 20 carbon atoms, or an aralkyl group of 7 to 20 carbon atoms, and

Each of X ₁ and X ₂ is independently hydrogen, halogen, hydroxy, amine, thio, silyl, cyano, nitro, alkyl having 1 to 20 carbon atoms, 2 to 20 carbon atoms Alkenyl, alkynyl having 2 to 20 carbon atoms, cycloalkyl having 3 to 20 carbon atoms, aryl having 6 to 20 carbon atoms, alkaryl having 7 to 20 carbon atoms, Aralkyl groups of 7 to 20 carbon atoms, heteroaryl groups of 5 to 20 carbon atoms, alkoxy groups of 1 to 20 carbon atoms, aryloxy groups of 6 to 20 carbon atoms, 1 to 20 carbon atoms Alkylamino groups of 20 carbon atoms, arylamine groups of 6 to 20 carbon atoms, alkylthio groups of 1 to 20 carbon atoms, arylthio groups of 6 to 20 carbon atoms, arylthio groups of 1 to 20 carbon atoms Alkylsilyl with carbon atoms, or arylsilyl with 6 to 20 carbon atoms.

The hafnium compound may be represented by any one of Formula 1-1 to Formula 1-5, but is not limited thereto. Any hafnium compound corresponding to Formula 1 is included in the present invention.

[Formula 1-1]

[Formula 1-2]

[Formula 1-3]

[Formula 1-4]

[Formula 1-5]

The hafnium compound of the present invention can be prepared by a step including the reaction of a compound represented by the following formula 2 and a compound represented by the following formula 3.

[Formula 2]

[Formula 3] Hf(X ₁ X ₂ ) ₂

In the above formula,

The definitions of R ₁ to R ₁₁ , and X ₁ and X ₂ are the same as those described above.

Meanwhile, when preparing the hafnium compound represented by the above formula 1, depending on the structure of the finally prepared hafnium compound, the step of preparing the ligand compound may be performed in various ways as follows.

For example, when R ₃ and R ₄ in the ligand compound do not form a ring with each other and R ₁₁ is a hydrogen atom, as shown below, the ligand compound can be prepared by a hydrogenation reaction under a ruthenium catalyst and then combined with the formula The compound shown in 3, which is a hafnium precursor, is reacted to obtain a hafnium compound.

[Reaction 1]

Alternatively, when R ₃ and R ₄ in the ligand compound structure do not form a ring with each other and R ₁₁ is a substituent rather than a hydrogen atom, as shown in the following reaction formula 2, first use an organolithium compound to introduce R ₁₁ and then Hydrogenation under ruthenium catalyst to obtain coordination compounds.

[Reaction 2]

Alternatively, in the ligand compound structure, when _R3 and R4 are connected to each other and form an aromatic ring with ₅ to ₂₀ carbon atoms and R11 is a substituent rather than a hydrogen atom, as shown below, use first The organolithium compound is introduced into R ₁₁ and then, in order to prevent the hydrogenation reaction of an aromatic ring (eg, naphthyl), hydrogenation is carried out under a Pd/C catalyst to prepare a ligand compound.

[Reaction 3]

That is, the hafnium compound can be prepared by alkylation and hydrogenation of the compound, which is a precursor of the ligand compound, under appropriate reagents and reaction conditions, and the hafnium is introduced into the produced therein. The specific type of alkylation reagent, reaction temperature and pressure, etc. can be appropriately changed by those skilled in the art in consideration of the structure of the final compound and experimental conditions.

In the present invention, the organozinc compound is a material as a chain transfer agent, which induces chain transfer during the preparation of the polymerization reaction to obtain a copolymer, and may be specifically a compound represented by the following formula 4.

[Formula 4]

In the above formula 4,

A is an alkylene group having 1 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, or a halogen-substituted aryl group having 6 to 20 carbon atoms, having 1 to 12 carbon atoms an alkyl group of 3 to 12 carbon atoms, a cycloalkyl group of 3 to 12 carbon atoms, an alkoxy group of 1 to 8 carbon atoms, or an aryl group of 6 to 12 carbon atoms, and

B is an arylidene group of 6 to 12 carbon atoms substituted with an alkenyl group of 2 to 12 carbon atoms.

Alternatively, A may be an alkylene group having 1 to 20 carbon atoms, an aryl group having 6 to 12 carbon atoms, or a halogen-substituted aryl group having 6 to 20 carbon atoms, an aryl group having 1 to 12 carbon atoms an alkyl group of 1 to 12 carbon atoms, a cycloalkyl group of 3 to 12 carbon atoms, an alkoxy group of 1 to 8 carbon atoms, or an aryl group of 6 to 12 carbon atoms, and

B may be an arylidene group having 6 to 12 carbon atoms substituted with an alkenyl group having 2 to 8 carbon atoms.

Formula 4 may have a structure in which both ends of the formula are double bonds. For example, when B is an alkenyl-substituted aryl group, the aryl group is attached to A and the double bond of the alkenyl group substituting the aryl group can be located in the outermost portion of Formula 4.

In the presence of the catalyst composition, when the organozinc compound reacts with one or more olefin-based monomers, the olefin-based monomer can be inserted between the zinc (Zn) of the organozinc compound and the organic group (A) to The polymerization reaction is completed.

The organic zinc compound may be mixed in an amount of 1 to 200 equivalents based on 1 equivalent of the above transition metal compound of Formula 1, specifically, the amount may be 10 to 100 equivalents based on 1 equivalent of the above transition metal compound of Formula 1 .

The organozinc compound does not contain impurities such as THF and a large amount of magnesium salts, and therefore, can be supplied in high purity, and accordingly, can be used as a chain transfer agent, and is advantageous for olefin polymerization.

The catalyst composition may additionally include a co-catalyst compound. At this time, the co-catalyst compound is used to activate the transition metal compound represented by formula 1, and those skilled in the art can be used as the co-catalyst. For example, one or more selected from the following formulae 5 to 7 may be used as the auxiliary catalyst.

[Formula 5] -[Al(R _a )-O] _m -

[Formula 6] D(R _a ) ₃

[Formula 7] [LH] ⁺ [Z(A) ₄ ] ^- or [L] ⁺ [Z(A) ₄ ] ^-

In the above formula,

Each of R is independently _halogen , hydrocarbyl having 1 to 20 carbon atoms, or halogen-substituted hydrocarbyl having 1 to 20 carbon atoms,

m is an integer greater than or equal to 2,

D is aluminum or boron,

L is a natural or cationic Lewis acid,

Z is a group 13 element,

Each of A is independently an aryl group having 6 to 20 carbon atoms, or an alkyl group having 1 to 20 carbon atoms in which one or more hydrogen atoms may be substituted with a substituent, and

The substituent of A is halogen, hydrocarbon group having 1 to 20 carbon atoms, alkoxy group having 1 to 20 carbon atoms, or aryloxy group having 6 to 20 carbon atoms.

The compound represented by the above formula 5 is not particularly limited as long as it is an alkylaluminoxane. Preferred examples thereof include methylaluminoxane, ethylaluminoxane, isobutylaluminoxane, butylaluminoxane, and the like, and a particularly preferred compound is methylaluminoxane.

The compound represented by the above formula 6 is not particularly limited, but preferable examples thereof include trimethylaluminum, triethylaluminum, triisobutylaluminum, tripropylaluminum, tributylaluminum, dimethylaluminum chloride, triisobutylaluminum Aluminum propyl, aluminum tri-secondary butyl, aluminum tricyclopentyl, aluminum tripentyl, aluminum triisoamyl, aluminum trihexy aluminum, aluminum trioctyla, ethyl dimethyl aluminum, methyl diethyl aluminum Aluminum, triphenyl aluminum, tri-p-tolyl aluminum, dimethyl aluminum methoxide, dimethyl aluminum ethoxide, trimethyl boron, triethyl boron, triisobutyl boron, tripropyl boron, Tributylboron, etc. Particularly preferred compounds are selected from the group consisting of trimethylaluminum, triethylaluminum, and triisobutylaluminum.

Examples of the compound represented by the above formula 7 include, when Z is boron, for example, di(octadecyl)methylammonium tetrakis(pentafluorophenyl)borate [(C ₁₈ H ₃₇ ) ₂ N(H)Me] ⁺ [ B(C ₆ F ₅ ) ₄ ] ^- , bis(octadecyl) methylammonium tetra(phenyl)borate, tetra[3,5-bis(trifluoromethyl)phenyl]boronic acid bis(phenyl)boronic acid bis (Octadecyl)methylammonium, triethylammonium tetraphenylborate, tributylammonium tetraphenylborate, trimethylammonium tetraphenylborate, tripropylammonium tetraphenylborate, trimethylammonium tetrakis(p-tolyl)borate , Trimethylammonium tetrakis (o-, p-dimethylphenyl) borate, tributylammonium tetrakis (p-trifluoromethylphenyl) borate, trimethylammonium tetrakis (p-trifluoromethylphenyl) borate, tetrakis (p-trifluoromethylphenyl) borate Tributylammonium pentafluorophenyl)borate, tetrapentylboronic acid, N,N-diethylanilinium, N,N-diethylanilinium tetraphenylborate, N,N tetrakis(pentafluorophenyl)boronic acid -Diethylanilinium, diethylammonium tetrakis(pentafluorophenyl)borate, triphenylphosphonium tetraphenylborate, trimethylphosphonium tetraphenylborate, trimethylammonium tetraphenylborate, tripropyltetraphenylborate Ammonium, trimethylammonium tetrakis(p-tolyl)borate, tripropylammonium tetrakis(p-tolyl)borate, triethylammonium tetrakis(o, p-dimethylphenyl)borate, tetrakis(o, p-dimethyl ammonium borate) trimethylammonium borate, tributylammonium tetrakis(p-trifluoromethylphenyl)borate, trimethylammonium tetrakis(p-trifluoromethylphenyl)borate, tributylammonium tetrafluorophenylborate, tetraphenyl N,N-diethylanilinium tetrafluorophenylborate, N,N-diethylanilinium tetrafluorophenylborate, diethylammonium tetrafluorophenylborate, triphenylphosphonium tetraphenylborate, tetrakis(p-triphenylphosphonium) fluoromethylphenyl)borate triphenylcarbocation, tetrakis(pentafluorophenyl)borate triphenylcarbocation, or a combination thereof, and when Z is aluminum, for example, triethylammonium tetraphenylaluminate, tetraphenylaluminate Tributylammonium phenylaluminate, trimethylammonium tetraphenylaluminate, tripropylammonium tetraphenylaluminate, trimethylammonium tetrakis(p-tolyl)aluminate, tripropylammonium tetrakis(p-tolyl)aluminate, Triethylammonium tetrakis(o, p-dimethylphenyl)aluminate, tributylammonium tetrakis(p-trifluoromethylphenyl)aluminate, trimethylammonium tetrakis(p-trifluoromethylphenyl)aluminate , tributylammonium tetrakis(pentafluorophenyl)aluminate, N,N-diethylanilinium tetraphenylaluminate, N,N-diethylanilinium tetraphenylaluminate, tetrakis(pentafluorophenyl) ) N,N-diethylanilinium aluminate, diethylammonium tetrapentatentraphenylalumium, triphenylphosphonium tetraphenylaluminate, trimethylphosphonium tetraphenylaluminate, Triethylammonium tetraphenylaluminate, tributylammonium tetraphenylaluminate, or a combination thereof, but not limited thereto.

In particular, the cocatalyst used in the present invention may be a compound represented by the above formula 7, and may specifically be di(octadecyl)methylammonium tetrakis(pentafluorophenyl)borate.

In addition, the cocatalysts used in the present invention can be prepared in anhydrous hydrocarbon solvents. For example, the hydrocarbon solvent may be one or more selected from the group consisting of butane, pentane, neopentane, hexane, cyclohexane, methylcyclohexane, heptane, octane , benzene, toluene, xylene, and ethylbenzene, but not limited thereto. Any solvent available in the art can be used in anhydrous form.

In the present invention, when the cocatalyst is prepared in an anhydrous hydrocarbon solvent, at least one peak appears in each of the range of 1.75 ppm to 1.90 ppm or the range of 1.90 ppm to 2.00 ppm in ¹ H NMR. This indicates that the proton attached to the α-carbon adjacent to nitrogen, sulfur, or phosphorus contained in L exhibits different peaks. For example, when the compound represented by formula 1 is [(C ₁₈ H ₃₇ ) ₂ N(H)Me] ⁺ [B(C ₆ F ₅ ) ₄ ] ^- , in its ¹ H NMR spectrum, it exists in N CH ₂ Each of the two protons has a different signal.

In addition, the hafnium compound and the cocatalyst represented by Formula 1 can also be used in the form of being carried on a carrier. The support can be silicon oxide or aluminum oxide, but is not limited thereto.

The olefin monomer introduced as a reactant in step (S1) may be ethylene, propylene, 1-butene, 1-pentene, 4-methyl-1-pentene, 1-hexene, 1-heptene, Monomers formed from 1-octene, 1-decene, 1-undecene, 1-dodecene, 1-tetradecene, 1-hexadecene, 1-eicosene, or mixtures thereof, etc. . The olefin monomers may be used alone, or two or more of them may be used in combination.

Step (S1) can be performed, for example, in a homogeneous solution state. At this time, as the solvent, a hydrocarbon solvent or an olefin monomer itself may be used as a medium. The hydrocarbon solvent may be an aliphatic hydrocarbon solvent having 4 to 20 carbon atoms, specifically isobutane, hexane, cyclohexane, methylcyclohexane, and the like. The solvent may be used alone, or two or more of them may be used in combination.

The polymerization temperature of step (S1) may vary depending on reactants, reaction conditions, etc., but may be specifically 70 to 170°C, specifically 80 to 150°C, or 90 to 120°C. Within the above range, the solubility of the polymer can be increased and the catalyst can be thermally stabilized.

The polymerization reaction of step (S1) can be carried out in a batch, semi-continuous, or continuous manner, and can also be carried out in two or more steps with different reaction conditions.

The compound prepared by the above-mentioned step (S1) can be used as a precursor for preparing the polyolefin-polystyrene-based multi-block copolymer of the present invention by the anionic polymerization of the step (S2) described below.

Step (S2)

The step (S2) is carried out following the step (S1) and in the presence of the alkyl lithium compound including the silicon atom and the triamine compound, the polystyrene block is formed by anionic polymerization of the polyolefin block and the styrene-based monomer To prepare the steps of polyolefin-polystyrene-based multi-block copolymer.

In the step (S2), the styrene-based monomer can be continuously inserted between the zinc-carbon bonds of the (polyolefin group) ₂ Zn contained in the compound formed by the above-mentioned step (S1), and at the same time, exist in the step (S1). The styryl group at the terminal of the compound formed by (S1) may participate as a copolymerization point with the styrenic monomer to be attached to the polystyrene chain. Furthermore, the multi-block copolymers prepared via the above procedure can be easily interrupted by the reaction of terminal groups with water, oxygen, or organic acids, whereby the multi-block copolymers are converted into industrially useful polymers Olefin-polystyrene based multiblock copolymers.

The styrenic monomer may be a styrenic monomer having 6 to 20 carbon atoms. More specifically, the styrene-based monomer may be a styrene-based monomer including ethylene substituted with an aryl group having 6 to 20 carbon atoms, ethylene substituted with a phenyl group, and the like, for example, styrene.

The alkyllithium compound including a silicon atom may be a compound represented by the following formula 8.

[Formula 8] (CH ₃ ) ₃ Si(CH ₂ )Li

The alkyllithium compound including the silicon atom is widely used as a material for an anionic polymerization initiator, and is easily used in the present invention.

The triamine compound may be a compound represented by the following formula 9.

[Formula 9]

The triamine compound is a compound for improving reactivity as a base or as a nucleophile of the alkyllithium compound by good coordination with lithium, which is readily available and inexpensive.

The present invention novelly uses compounds of formula 8 and 9 (eg, Me ₃ SiCH ₂ Li·(PMDETA)) as an initiator in step (S2), and thus, can inhibit polystyrene homopolymer, polyolefin homopolymer, and the production of polyolefin-polystyrene diblock copolymers, and maximizing the production of polyolefin-polystyrene-based multiblock copolymers, which are the subject of the present invention.

The alkyllithium compound including a silicon atom and represented by the formula 8 and the triamine compound represented by the formula 9 may be mixed and introduced into an aliphatic hydrocarbon solvent, or the alkyllithium compound including a silicon atom and represented by the formula 8 and the triamine compound represented by Formula 9 can be introduced sequentially.

The anionic polymerization reaction temperature of step (S2) may vary depending on reactants, reaction conditions, etc., but may be specifically 40 to 170°C, more specifically 60 to 150°C, or 90 to 100°C.

The anionic polymerization reaction of step (S2) can be carried out in a batch, semi-continuous, or continuous manner, and can also be carried out in two or more steps with different reaction conditions.

The anionic polymerization reaction time of step (S2) may vary depending on reactants, reaction conditions, etc., but may be specifically 0.5 to 10 hours, 1 to 8 hours, 2 to 7 hours, or 4 to 6 hours. Within the above range, it is favorable to convert all the introduced styrene-based monomers into multi-block copolymers.

As mentioned above, in the production method of the present invention, the organic zinc compound represented by the above-mentioned formula 4 is used, and the polyolefin chain is grown through an olefin polymerization reaction, and then a styrene anionic polymerization reaction is carried out continuously to prepare a polyolefin-polystyrene-based polyolefin. A block copolymer, whereby a polyolefin-polystyrene-based multi-block copolymer having improved physical properties compared to the prior art can be efficiently prepared, and thus, can be easily used in industry.

The method of preparing the polyolefin-polystyrene-based multiblock copolymer according to the example of the present invention is different from the typical method of preparing the polyolefin-polystyrene-based multiblock copolymer, in which styrene and diene are anionically polymerized The reaction is followed by a two-step hydrogenation procedure, and is characterized in that the polyolefin-polystyrene-based multi-block copolymer is prepared in such a manner that the double bonds in the main chain of the copolymer are not hydrogenated. Accordingly, the polyolefin-polystyrene-based multi-block copolymer contained in the thermoplastic resin composition of the present invention is characterized in that the polyolefin-polystyrene-based multi-block copolymer does not contain unsaturation and is used in Unsaturated bonds present during the hydrogenation procedure of the double bonds of the main chain.

Meanwhile, the thermoplastic resin composition having the above-mentioned composition according to an embodiment of the present invention may include appropriate contents of each component in order to meet the use and physical properties required thereby. For example, in the present invention, the weight ratio of the (1) polypropylene and the (2) polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition may be 10:90 to 90:10, The specific weight ratio is 20:80 to 80:20, and more specifically, the weight ratio is 40:60 to 60:40.

When the content of the polyolefin-polystyrene-based multi-block copolymer contained in the thermoplastic resin composition is too small, the impact strength may be deteriorated, and when the polyolefin-polystyrene-based multi-block copolymer is contained When the content of the thermoplastic resin composition is excessive, the fluidity of the thermoplastic resin composition may be deteriorated. The mixing ratio may be controlled in consideration of the importance of the physical properties of the polypropylene and the polyolefin-polystyrene-based multi-block copolymer.

The thermoplastic resin composition according to the embodiment of the present invention may optionally further include inorganic fillers and the polypropylene and the polyolefin-polystyrene-based multi-block copolymer to improve the mechanical properties of the thermoplastic resin composition.

The inorganic filler may be a powder-type filler, a flake-type filler, a fibrous filler, or a balloon-type filler, and any one of them or a mixture of two or more thereof may be used. Specifically, the powdered filler may be natural silicic acid or silicates (eg, talc fines, kaolin, calcined clay, or sericite), carbonates (eg, precipitated calcium carbonate, ground calcium carbonate, or carbonic acid) magnesium), hydroxides (eg, aluminum hydroxide or magnesium hydroxide), oxides (eg, zinc oxide, magnesium oxide, or titanium oxide), artificial silicic acid or silicates (eg, hydrated calcium silicate, hydrated aluminum silicate, hydrous silicic acid or silicic anhydride), and silicon carbide. In addition, the flake-type filler may be mica or the like. The fibrous filler can be alkali magnesium sulfate whisker, calcium titanate whisker, aluminum borate whisker, sepiolite, processed mineral fiber (PMF), potassium titanate and the like. In addition, the balloon-type filler may be a glass balloon or the like. In the above, the inorganic filler may be talc.

In addition, the inorganic filler may be surface-treated to improve the strength properties and moldability of the thermoplastic resin composition.

Specifically, the inorganic filler can be physically modified by using a surface treatment agent (eg, silane coupling agent, high-carbon fatty acid, fatty acid metal salt, unsaturated organic acid, organic titanate, resin acid, or polyethylene glycol). or chemical surface treatment.

In addition, the average particle diameter (D ₅₀ ) of the inorganic filler may be 1 μm to 20 μm, specifically 3 μm to 15 μm, and more specifically 5 μm to 10 μm. When the average particle size of the inorganic filler is too small, when it is mixed with polypropylene and polyolefin-polystyrene-based multi-block copolymer, it will be difficult to achieve uniform dispersion due to the aggregation of inorganic filler particles. As a result, the thermoplastic resin is improved. The effect of the mechanical properties of the composition will be insignificant. In addition, when the average particle diameter of the inorganic filler is too large, the dispersibility of the inorganic filler itself may be deteriorated, and the physical properties may be deteriorated.

In the present invention, the average particle size (D ₅₀ ) of the inorganic filler can be defined as the particle size at 50% of the particle size distribution. In the present invention, the average particle size (D ₅₀ ) of the inorganic filler can be measured by, for example, a scanning electron microscope (SEM) or a field emission scanning electron microscope (FE-SEM) by electron microscopy, or measured by diffraction. Specifically, when measured by laser diffraction, the inorganic filler can be dispersed in a dispersion medium and then introduced into a commercially available laser diffraction particle size measurement device (eg, Microtrac MT 3000) for measurement in the measurement device The mean particle size at 50% of the particle size distribution ( _D50 ).

Based on 100 parts by weight of the thermoplastic resin composition, the content of the above-mentioned inorganic filler may be 0.1 parts by weight to 40 parts by weight. Based on 100 parts by weight of the thermoplastic resin composition, when the content of the inorganic filler in the thermoplastic resin composition is less than 0.1 part by weight, the improvement effect of including the inorganic filler is not significant, and when it exceeds 40 parts by weight, The workability of the thermoplastic resin composition deteriorates. More specifically, based on the total weight of the thermoplastic resin composition, the content of the inorganic filler may be 0.1 wt % to 20 wt %.

The thermoplastic resin compositions according to the embodiments of the present invention meeting the above composition and content conditions can be prepared by adding polypropylene and optional inorganic fillers to polyolefin-polystyrene-based multi-block copolymers, followed by heat treatment. be made of. Here, the type and content of the polypropylene are the same as the aforementioned.

This mixing procedure can be carried out according to typical methods. Specifically, the mixing can be performed using a high-speed mixer or a ribbon mixer.

In addition, as required by the mixing procedure, additives (eg, antioxidants, heat stabilizers, UV stabilizers, antistatic agents, etc.) may be additionally included, and in order to improve coatability, they may be selectively included in an appropriate content range In addition, additives with small amounts of adhesive resins or polar groups are used.

Furthermore, the heat treatment procedure can be carried out at temperatures above the melting point of polypropylene and 210°C or lower. This heat treatment procedure can be carried out using various bending equipment (eg, twin screw extruders, single screw extruders, tumbling mills, kneaders, or banbury mixers).

The thermoplastic resin compositions according to the examples of the present invention produced according to the above-described production method can have excellent elongation and tensile strength and exhibit high fluidity.

Specifically, the thermoplastic resin composition may meet the following physical properties (A) to (E).

(A) Tensile strength from 10 to 35MPa,

(B) 20 to 1500% elongation,

(C) Yield strength from 5 to 25 MPa,

(D) Melt flow rate (MFR, 230°C and 2.16 kg) from 0.5 to 200 g/10 min, and

(E) Melt flow rate (MFR, 190 °C and 2.16 kg) from 2 to 100 g/10 min.

(A) The tensile strength may be 10 to 35 MPa, specifically 15 to 30 MPa, more specifically 17 to 30 MPa.

(B) The elongation may be 20 to 1500%, specifically 30 to 1400%, more specifically 50 to 1300%.

(C) The yield strength may be 5 to 25 MPa, specifically 7 to 22 MPa, more specifically 9 to 20 MPa.

Tensile strength, elongation, and yield strength can be measured according to ASTM D638 (50 mm/min) and represent tensile strength at rupture, elongation at rupture, and strength at yield point, respectively.

(D) The melt flow rate (MFR, 230°C and 2.16 kg) may be 0.5 to 200 g/10 min, specifically 3 to 150 g/10 min, and more specifically 7 to 130 g/10 min.

(E) The melt flow rate (MFR, 190°C and 2.16 kg) may be 2 to 100 g/10 min, specifically 2 to 80 g/10 min, and more specifically 2 to 50 g/10 min.

The melt flow rate was measured according to ASTM-D 1238 at 230°C and 2.16 kg load and 190°C and 2.16 kg load, respectively.

Thermoplastic resin compositions according to embodiments of the present invention can be used for slush molding in various fields and applications for packaging, construction, household goods, etc. (eg, materials for automobiles, wires, toys, fabrics, or medicines). Extrusion molding, or injection molding. In particular, the thermoplastic resin composition has excellent toughness and impact strength at low temperature and room temperature, and also has excellent physical properties such as heat resistance and rigidity, and thus, can be used for interior and exterior parts of automobiles.

According to another embodiment of the present invention, mouldings and automotive parts produced by using thermoplastic compositions meeting the above-mentioned physical property requirements are proposed.

The mouldings can be in particular blow mouldings, inflatable mouldings, cast mouldings, extrusion laminate mouldings, extrusion mouldings, foam mouldings, injection mouldings, sheets, films , fibers, monofilaments, non-woven fabrics, etc.

In addition, the automobile parts may be interior/exterior parts for automobiles, and the like.

example

Hereinafter, the present invention will be described in detail with reference to examples. However, the following examples are only used to illustrate the present invention and are not intended to limit the scope of the present invention.

< Preparation of transition metal compounds >

Preparation example 1

(i) Preparation of ligand compounds

Isopropyllithium (0.45 mL, 0.36 mmol, 0.79 M in pentane) was slowly added to 2-naphthyl-1,10-phenanthroline (0.789 g, 2.58 mmol). After stirring at room temperature for 3 hours, degassed _H2O (3 mL) was added. The aquifer was removed by syringe under _N2 . The solvent was removed using a vacuum line and the residue was dissolved in degassed ethanol (15 mL) and THF (5 mL). Under _N2 , the solution was transferred to a bomb reactor containing Pd/C (0.242 mmol, 10 mol %). After charging _H2 gas to 5 bar, the mixture was stirred at room temperature for 12 hours. The _H2 gas was released and the catalyst residue was filtered on celite and removed. The solvent was removed and the residue was purified by silica gel column chromatography using ethyl acetate/hexane (1/3, v/v). A pale yellow viscous solid was obtained (0.085 g, 73%). ¹ H NMR and ¹³ C NMR spectra are shown in FIG. 1 .

- ¹ H NMR (C ₆ D ₆ ): δ 8.58(d, J = 7.8 Hz, H), 7.75(d, J = 9.0 Hz, H), 7.70(d, J = 9.6 Hz, H), 7.66( d, J = 7.2 Hz, H), 7.63(d, J = 6.6 Hz, H), 7.32(m, 4H), 7.18(d, J = 8.4 Hz, H), 6.99(d, J = 7.8 Hz, H), 6.39(s, H, NH), 2.93(m, H), 2.79(m, H), 2.70(dt, J = 4.8 Hz, H), 1.70(m, H), 1.63(m, H) ), 1.47(m, H), 0.81(d, J = 7.2 Hz, 3H, CH(CH ₃ ) ₂ ), 0.76(d, J = 7.2 Hz, 3H, CH(CH ₃ ) ₂ ) ppm.

^-13 C { ¹ H} nmr (C ₆ D ₆ ): Δ 18.34, 18.77, 24.43, 26.78, 32.52, 56.73, 112.78, 116.67, 122.62, 125.59, 126.51, 126.614, 128.14, 129.03, 129.03, 129.03 129.28, 132.20, 134.71, 136.41, 137.64, 139.79, 141.75, 155.92 ppm.

- m/z calculated for ([M ⁺ ]C ₂₅ H ₂₄ N ₂ ) 352.4800. Experimental value: 352.1942.

(ii) Preparation of transition metal compounds

[Formula 1-3]

MeMgBr (1.24 mL, 3.11 M in diethyl ether) was added dropwise to a stirred suspension (0.300 g, 0.938 mmol) of HfCl4 in toluene ( ₈ mL) at -78 °C. After stirring for 1 hour in the temperature range -40°C and -35°C, the solution was cooled again to -78°C. A solution of the ligand compound (0.366 g, 1.00 mmol) in toluene (4 mL) (0.24 g, 0.94 mmol) was added dropwise. The resulting solution was stirred at a controlled temperature range between -40°C and -35°C for 2 hours and then at room temperature overnight. The solvent was removed using a vacuum line, and the residue was extracted with toluene (50 mL). A dark brown powder (0.226 g, 47%) was obtained by pulverization in hexane. ¹ H NMR and ¹³ C NMR spectra are shown in FIG. 2 .

- ¹ H NMR (C ₆ D ₆ ): δ 8.66(d, J = 7.8 Hz, H), 8.50(d, J = 7.8 Hz, H), 7.92(d, J = 9.0 Hz, H), 7.83( d, J = 7.2 Hz, H), 7.76(d, J = 8.4 Hz, H), 7.62(d, J = 7.8 Hz, H), 7.40(td, J = 7.2 Hz, H), 7.32(m, H), 7.14(d, J = 7.8 Hz, H), 6.77(d, J = 7.2 Hz, H), 4.02(m, H), 2.80(m, H), 2.62(dt, J = 6.0 Hz, H), 2.55(m, H), 1.88(m, H), 1.72(m, H), 1.09 and 1.04(d, J = 6.6 Hz, 6H, CH(CH ₃ ) ₂ ), 0.82(s, 3H , HfCH ₃ ), 0.81(s, 3H, HfCH ₃ ) ppm.

^-13 C { ¹ H} nmr (C ₆ D ₆ ): Δ 18.55, 21.28, 23.07, 25.44, 32.58, 60.98, 63.06, 66.88, 112.37, 119.64, 124.55, 125.48, 126.97, 129.97, 129.97 130.26, 131.25, 133.82, 135.51, 140.97, 141.44, 143.94, 150.14, 164.58, 209.13 ppm.

-Analytical calculation (C ₂₇ H ₂₈ HfN ₂ ): C, 58.01; H, 5.05; N, 5.01%.

- Experimental values: C, 57.91; H, 5.01; N, 5.11%.

< Preparation of auxiliary catalyst >

In the glove box, excess K ⁺ [B(C ₆ F ₅ ) ₄ ] ^- (0.633 g, 0.881 mmol, considered pure) was combined with [(C ₁₈ H ₃₇ ) ₂ N(H)Me] ⁺ [Cl] ^- (0.404 g, 0.705 mmol) in toluene (anhydrous, 10 mL) was reacted for 1 hour at room temperature. After filtration on celite, the solvent was removed using a vacuum line. The residue was dissolved in methylcyclohexane (4 mL) and filtered again on celite. The solvent was removed to give a yellow oil compound which was used without further purification (0.797 g, 93%).

- ¹ H NMR (C ₆ D ₆ ): δ 3.15(br, H, NH), 1.97(m, 2H, NCH ₂ ), 1.80(m, H, NCH ₂ ), 1.51(d, J = 6.0 Hz, 3H, NCH ₃ ), 1.45-1.29(m, 48H), 1.26(quintet, J = 7.2 Hz, 4H), 1.13(quintet, J = 7.2 Hz, 4H), 0.94(t, J = 7.8 Hz, 6H) , 0.88(quintet, J = 7.8 Hz, 4H), 0.81(m, 4H) ppm.

- ¹⁹ F NMR (C ₆ D ₆ ): δ -132.09, -161.75, -165.98.

< Preparation of Organozinc Compounds >

Borane dimethyl sulfide (1.6 mL, 3.2 mmol) was slowly introduced into the stirring triethylborane (0.6 g) and reacted for 90 minutes thereafter. The mixture was slowly introduced into divinylbenzene (3.8 g) dissolved in dry diethyl ether (10 mL) cooled to -20°C and then stirred overnight. The solvent was removed with a vacuum pump and then diethylzinc (0.8 g) was added. The reaction was carried out at 0°C for 5 hours while the triethylborane formed was removed by distillation under reduced pressure. Excess divinylbenzene and diethylzinc were removed by distillation at reduced pressure at 40°C. Methylcyclohexane (150 mL) was added to redissolve the product, and then the obtained solid compound (by-product) was filtered using diatomaceous earth and removed to obtain the organozinc compound represented by the above formula.

< Polyolefin - Preparation of polystyrene-based multiblock copolymers >

Executed Preparation Example 1

The Parr reactor (1 gallon) was vacuum dried at 120°C for 2 hours. A solution of Oc3Al (trioctylaluminum, 1466.4 mg, 1,000 μmol _- Al) in methylcyclohexane (1,200 g) was added to the reactor. The mixture was stirred at 120°C for 1 hour using a heating jacket, then the solution was removed using a cannula.

The reactor was filled with methylcyclohexane (600 g) containing Oc3Al (715.6 mg, 488 μmol _- Al/25 wt% in hexane) as scavenger and 1-hexene (280 g) as scavenger Olefin monomer and temperature set to 90°C. A solution of the organozinc compound (3,000 μmol) in methylcyclohexane (3.85 g) was charged as a chain transfer agent, and then injected with a solution containing a mixture of [(C ₁₈ H ₃₇ ) ₂ N(H)Me] ⁺ [B( A methylcyclohexane solution (1.68 g) of the transition metal compound of Preparation 1 (9.0 μmol-Hf) activated with _{C6F5 )4 ]} ^- (9.0 μmol) in methylcyclohexane. The polymerization was carried out for 40 minutes while maintaining the pressure in the reactor at 25 bar by opening the valve of the ethylene tank. The temperature was adjusted in the range of 90 to 120°C, and the remaining ethylene gas was discharged.

When the temperature reached 90°C, Me3SiCH2 Li (244.8 mg, 2.6 mmol) and PMDETA ( _{495.1 mg} , 2.86 mmol) in methylcyclohexane (3.85 g) _were added. ₂ Li·(PMDETA) solution. During stirring, the temperature was maintained at 90°C for 30 minutes before styrene (88.0 g) was injected. The temperature was adjusted in the range of 90 to 100°C using a heating jacket.

Complete conversion of the styrene was confirmed ^by1H NMR analysis of an aliquot. After complete conversion of styrene, 2-ethylhexanoic acid and ethanol were injected continuously. The resulting polymer mass (300 g) was dried in a vacuum oven at 80°C overnight.

Executed preparation example 2

In the same manner as in Preparation 1 carried out, but using methylcyclohexane (1,200 g) containing MMAO-3A (1,000 μmol-Al/in hexane) as a scavenger, and 1-hexene (560 g) g) As an olefin monomer, an organozinc compound (3,100 μmol) in methylcyclohexane (3.85 g) as a chain transfer agent, containing via [(C ₁₈ H ₃₇ ) ₂ N(H)Me] ⁺ [B (C ₆ F ₅ ) ₄ ] ^- (12.0 μmol) activated transition metal compound (12.0 μmol-Hf) in methylcyclohexane solution of transition metal compound (12.0 μmol-Hf) in methylcyclohexane (3.6 g), and styrene (104.0 g) was used in the reactor in various amounts and the ethylene tank was valved so that the pressure in the reactor was 20 bar, the resulting polymer mass (360 g) was dried in a vacuum oven at 80°C overnight .

Comparative preparation example 1

Commercially available SEBS, G1651 from Kraton Company was used.

Comparative Preparation Example 2

Commercially available SEBS, G1650 from Kraton Company was used.

[Table 1]

Experimental example 1

The polyolefin-polystyrene-based multi-block copolymers of the preparation examples used for implementation were measured for the physical properties of each of the copolymers according to the following conditions and methods, and the results are shown in Table 2 below.

(1) Measurement of ethylene, α-olefin, and styrene content

This measurement is performed via a nuclear magnetic resonance apparatus (NMR). ^1H NMR was measured using a Bruker 600MHz AVANCE III HD NMR apparatus at ns=16, d1=3s, solvent=TCE-d2, and 373K, and the TCE-d2 solvent peak was corrected to 6.0 ppm. The _CH3 of 1-propene was confirmed to be at 1 ppm and the peak (triplet) associated with _CH3 of the butyl branch of 1-hexene was confirmed to be close to 0.96 ppm to calculate the content. In addition, the styrene content was calculated using the aromatic peak near 6.5 to 7.5 ppm.

(2) Weight average molecular weight (Mw, g/mol) and polydispersity index (PDI)

The weight-average molecular weight (Mw, g/mol) and the number-average molecular weight (Mn, g/mol) were measured by permeation chromatography (GPC), respectively, and the polydispersity index was calculated by dividing the weight-average molecular weight by the number-average molecular weight (PDI).

- String: PL Olexis

- Solvent: TCB (Trichlorobenzene)

- Flow rate: 1.0 ml/min

- Sample concentration: 1.0 mg/ml

- Injection volume: 200 ㎕

- Column temperature: 160°C

- Detector: Agilent High Temperature RI Detector

- Standard: Polystyrene

- Calculate molecular weight with Universal correction using the Mark-Houwink equation (K = 40.8 × 10 ^-5 , α = 0.7057)

(3) Compound viscosity

Complex viscosity was measured using TA Instruments' Advanced Rheometric Expansion System Specification. Using parallel plates with a diameter of 25.0 mm, the samples had a spacing of 2.0 mm at 160°C. The measurements were made in dynamic strain frequency sweep mode, using 5% strain and frequencies from 0.05 rad/s to 500 rad/s, in a set of 10 points measuring 41 points.

The composite viscosity at frequencies of 0.5 rad/s and 125 rad/s is shown in Table 2 below.

[Table 2]

example 1 - Preparation of thermoplastic resin composition

To 20 parts by weight of the polyolefin-polystyrene-based multi-block copolymer prepared in Preparation Example 1 carried out above, 80 parts by weight of a melt flow index (230° C., 2.16 kg) of 30 g/10 min was added. High crystallinity impact copolymer polypropylene (CB5230, product of Korea Petrochemical Ind. Co., LTD) was then solution blended in xylene using a reactor to obtain a thermoplastic resin composition compound. At this time, the temperature was 200°C to 230°C, the rotational speed of the impeller was 400 rpm, and the blending time was 4 hours. After blending was complete, the compound was recovered and then dried in a 100°C vacuum oven overnight.

example 2 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 1, except that the content of the polyolefin-polystyrene-based multi-block copolymer prepared in Preparation Example 1 and the content of the high-crystallinity impact-resistant polypropylene were carried out respectively. Change to 50 parts by weight and 50 parts by weight.

example 3 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 1, except that the polyolefin-polystyrene-based multi-block copolymer prepared in Preparative Example 2 was used in place of the polyolefin prepared in Preparative Example 1. - Polystyrene-based multiblock copolymers.

example 4 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 1, except that the polyolefin-polystyrene-based multi-block copolymer prepared in Preparative Example 2 was used in place of the polyolefin prepared in Preparative Example 1. - Polystyrene-based multiblock copolymers.

Comparative example 1 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 1, except that the polyolefin-polystyrene-based multiblock copolymer prepared in Comparative Preparation Example 1 was used in place of the polyolefin prepared in Practical Preparation Example 1 - Polystyrene-based multiblock copolymers.

Comparative example 2 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 2, except that the polyolefin-polystyrene-based multi-block copolymer prepared in Comparative Preparation Example 1 was used in place of the polyolefin prepared in Practical Preparation Example 1 - Polystyrene-based multiblock copolymers.

Comparative example 3 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 1, except that the polyolefin-polystyrene-based multi-block copolymer prepared in Comparative Preparation Example 2 was used in place of the polyolefin prepared in Practical Preparation Example 1 - Polystyrene-based multiblock copolymers.

Comparative example 4 - Preparation of thermoplastic resin composition

A thermoplastic resin composition compound was prepared in the same manner as in Example 2, except that the polyolefin-polystyrene-based multi-block copolymer prepared in Comparative Preparation Example 2 was used in place of the polyolefin prepared in Implementation Example 1 - Polystyrene-based multiblock copolymers.

Experimental example 2

1) Tensile strength, elongation, and compound viscosity

The thermoplastic resin composition compounds of Examples 1 to 4 and Comparative Examples 1 to 4 were extruded and pelletized, respectively, and then the tensile strength at break and the elongation at break were measured according to ASTM D638 (50 mm/min). , and the yield strength at rupture.

2) Melt Flow Rate (MFR)

Melt flow rate was measured according to ASTM-D 1238 at 230°C and 2.16 kg load and 190°C and 2.16 kg load.

[table 3]

*The MFR (230°C, 2.16 kg) of Example 3 is too high to measure.

As can be seen in Table 5 above, the polyolefin-polystyrene-based multi-block copolymer of Preparative Example 1 performed or the polyolefin-polystyrene-based multi-block polyphenylene of Preparative Example 2 performed is also included in addition to polypropylene The thermoplastic resin composition of the ethylene-based multi-block copolymer maintains excellent tensile strength, elongation, and yield strength and exhibits improved fluidity, and thus, is advantageous for injection and double injection and exhibits suitability for use in automotive interior materials and other excellent mechanical and physical properties. The thermoplastic resin composition of Example 3, including the polyolefin-polystyrene-based multi-block copolymer of Preparation Example 2, had an extremely high MFR value at 230° C. and 2.16 kg, which could not be measured in experiments, but at 190 °C and 2.16 kg exhibit excellent MFR values. Accordingly, it has been analyzed that the thermoplastic resin composition of Example 3 can exhibit excellent injection properties by appropriately lowering the injection temperature when applying real injection.

In addition, when the thermoplastic resin compositions were compared with each other, when the polystyrene-based multi-block copolymer of the implemented preparation example 1 was used in the same content as the SEBS of the comparative preparation example 1 or the SEBS of the comparative preparation example 2, an example was confirmed. The thermoplastic resin composition of 1 was significantly better than the thermoplastic resin compositions of Comparative Preparation Examples 1 and 3, while the thermoplastic resin composition of Example 2 was significantly better than Comparative Examples 2 and 4 in terms of tensile strength and yield strength and melt flow rate thermoplastic resin composition.

[Fig. 1] ¹ H NMR and ¹³ showing the ligand compound used in the preparation of the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition according to the example of the present invention. C NMR spectrum; and

[ Fig. 2 ] Shows ¹ H NMR and ¹³ C of the transition metal compound used in the preparation of the polyolefin-polystyrene-based multi-block copolymer included in the thermoplastic resin composition according to the example of the present invention NMR spectroscopy.

Claims (9)

A thermoplastic resin composition comprising: (1) Polypropylene; and (2) Polyolefin-polystyrene-based multiblock copolymers that meet the following conditions (a) and (b): (a) Complex viscosity (η*) at a temperature of 160°C and a frequency (ω) of 0.5 rad/s: 40,000 to 350,000 Pa·s, (b) Compound viscosity at a temperature of 160°C and a frequency of 125 rad/s: 900 to 3,500 Pa·s. The thermoplastic resin composition of claim 1, wherein the compound viscosity at a temperature of 160°C and a frequency of 0.5 rad/s is 45,000 to 300,000 Pa·s, and the compound viscosity at a temperature of 160°C and a frequency of 125 rad/s 1,000 to 3,300 Pa·s. The thermoplastic resin composition of claim 1, wherein the polyolefin-polystyrene-based multi-block copolymer has a weight average molecular weight of 50,000 g/mol to 400,000 g/mol. The thermoplastic resin composition of claim 1, wherein the polyolefin-polystyrene-based multi-block copolymer has a molecular weight distribution of 1.5 to 3.0. The thermoplastic resin composition of claim 1, wherein the polyolefin-polystyrene-based multi-block copolymer is one or more selected from the group consisting of: polystyrene-poly(ethylene-co- propylene)-polystyrene block copolymer, polystyrene-poly(ethylene-co-1-butene)-polystyrene block copolymer, polystyrene-poly(ethylene-co-1-pentene) - polystyrene block copolymer, polystyrene-poly(ethylene-co-1-hexene)-polystyrene block copolymer, polystyrene-poly(ethylene-co-1-heptene)-polystyrene Styrenic block copolymers, and polystyrene-poly(ethylene-co-1-octene)-polystyrene block copolymers. The thermoplastic resin composition of claim 1, wherein the polyolefin-polystyrene-based multi-block copolymer comprises 10% to 30% by weight of the polystyrene-based block. The thermoplastic resin composition according to claim 1, wherein the polyolefin-polystyrene-based multi-block copolymer is prepared in such a manner that the double bonds in the main chain of the copolymer are not hydrogenated. The thermoplastic resin composition of claim 1, wherein the weight ratio of the (1) polypropylene and the (2) polyolefin-polystyrene-based multi-block copolymer is 10:90 to 90:10. The thermoplastic resin composition of claim 1, wherein the thermoplastic resin composition is a thermoplastic resin composition meeting the following physical properties (A) to (E): (A) Tensile strength of 10 to 35MPa, (B) Elongation from 20 to 1500%, (C) Yield strength of 5 to 25MPa, (D) Melt flow rate (MFR, 230°C and 2.16 kg) of 0.5 to 200 g/10 min, and (E) Melt flow rate (MFR, 190 °C and 2.16 kg) from 2 to 100 g/10 min.

Images