JP5357825B2 - Ethylene-based copolymer and composition - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a composition having good foamability and moldability; and a copolymer included in the composition to improve foamability and moldability in a small amount to be added. <P>SOLUTION: The copolymer includes structure units derived from ethylene A, &alpha;-olefin B, and VNBC, is synthesized using a metallocene catalyst, wherein the structure unit derived from B is 5-45 mol.%, the structure unit derived from VNB is 0.1-0.8 mol.%, and melt flow rate [MFR(g/10 minutes)] is 0.3-10, as measured at 190&deg;C under load of 2.16 Kg; and satisfies the formula (A): 13&gt; degree of strain hardening during measurement of elongation viscosity (&chi;<SB POS="POST">max</SB>) &gt;3... (A). <P>COPYRIGHT: (C)2012,JPO&amp;INPIT

Description

  The present invention relates to an ethylene-based copolymer, a composition containing the copolymer, and a foam using the same. More specifically, a copolymer capable of modifying foamability and moldability and the appearance and physical properties of a foamed molded product with a small addition amount, a composition providing a foam having a flexible and good appearance, and foam obtained therefrom About the body.

Up to now, foaming of thermoplastic resin has been relatively easy to foam, so amorphous resins such as polystyrene have been used in many cases. However, recently, linear resins are required due to demands for heat resistance and impact resistance. The development of foams using high-density polyethylene in the form of foam is being actively conducted. On the other hand, polyurethane (for example, see Patent Document 1) is often used as the soft foam, but because of the problem that the load on the environment is large because an organic solvent, a crosslinking agent, a catalyst, and the like are added during foam molding. Therefore, development of a flexible foam using polyolefin is strongly desired.
Most of the foaming in the olefinic resin is performed by expanding a non-volatile gas in the molten mixture. However, since the olefinic resin is generally crystalline, when the temperature of the resin is increased, the melt viscosity and the melt strength are rapidly increased. As a result, the gas cannot be retained, dissipates from the resin and the expansion ratio does not increase, and the appearance of the product surface deteriorates due to foam breakage. Linear high-density polyethylene has a relatively high crystallization temperature, and viscoelasticity is greatly changed by a slight temperature change. Therefore, there is a problem that an appropriate processing temperature range for foam molding is extremely narrow. Conversely, if the foaming temperature is lowered to increase the melt viscosity or melt strength of the resin, or the degree of crosslinking is increased by using electron beam crosslinking or a crosslinking agent, it becomes difficult to foam sufficiently and uniformly.

  For this reason, as a method for obtaining a high foaming ratio polyethylene foam having excellent heat resistance and impact resistance and a good appearance, (1) a method of mixing a branched low density polyethylene and a linear low density polyethylene (For example, refer patent document 2) (2) The method (For example, refer patent document 3) of mixing polyolefin wax with polyethylene with high melt tension is proposed.

  However, in the method of Patent Document 2, it is necessary to add a large amount of branched low-density polyethylene and linear low-density polyethylene, and as a result, heat resistance and other physical properties are greatly reduced. Moreover, in the method proposed in Patent Document 3, problems such as shrinkage of the foam and a decrease in mechanical strength due to a decrease in the closed cell ratio occur, and it is difficult to obtain a foam having a high expansion ratio.

  Therefore, there is a strong demand for the development of a modifier that can improve the moldability and the appearance and physical properties of the foamed molded product without deteriorating the properties of polyolefin resin such as polyethylene.

JP 2006-131754 A JP-A-2005-154729 JP 2006-199872 A

  The present invention is intended to solve the problems associated with the prior art as described above, and a copolymer capable of improving sufficiently high foamability and moldability by addition of a small amount thereof, and a composition containing the copolymer An object of the present invention is to provide a highly foamed molded article having a soft and good appearance, obtained by foaming a product.

  As a result of intensive studies to achieve the above-mentioned problems, the present inventors have found that an ethylene-based copolymer obtained by copolymerizing a specific diene using a metallocene catalyst can increase the polyolefin content by adding a small amount. The foamability and moldability were improved, and the foamed molded product obtained from the composition was found to have a flexible and good appearance, and the present invention was completed.

That is, the ethylene copolymer (X) of the present invention is derived from ethylene [A], α-olefin [B] having 3 to 20 carbon atoms, and 5-vinyl-2-norbornene (VNB) [C]. A copolymer containing a structural unit and synthesized using a metallocene catalyst, wherein (1) the structural unit derived from an α-olefin [B] having 3 to 20 carbon atoms is contained in 100 mol% of all the structural units. 5 to 45 mol%, and (2) the structural unit derived from VNB is 0.1 to 0.8 mol% in 100 mol% of all structural units, and (3) 190 ° C, 2.16 kg load The melt flow rate [MFR (g / 10 min)] measured in (3) is 0.3 to 10, and (4) satisfies the following formula (A).
13> degree of strain hardening in elongational viscosity measurement (χ _max )> 3 (A)
It is a preferable embodiment in terms of productivity that the copolymer of the present invention is synthesized using a catalyst having a structure represented by the following formula (iii ′).

In the formula (III ′), R ′ is a hydrogen atom, a hydrocarbyl group having 1 to 20 carbon atoms, R ″ is a hydrocarbyl group having 1 to 20 carbon atoms or a hydrogen atom, M is titanium, Y Is —NR ^* —, Z ^* is —SiR ^* ₂ —, and each R ^* is independently a hydrogen atom or a hydrocarbyl group having 1 to 20 carbon atoms, and of p and q When one is 0, the other is 1, p is 0 and q is 1, M is in the +2 oxidation state and X ′ is 1,4-diphenyl-1,3-butadiene or 1 , 3-pentadiene, when p is 1 and q is 0, M is in the +3 oxidation state and X is 2- (N, N-dimethylamino) benzyl.

The composition of the present invention is characterized by containing the copolymer.
The composition of the present invention comprises 60 to 95 parts by weight of a polyolefin resin and / or elastomer (Y) having an MFR of 0.1 to 30 g / 10 minutes measured at 190 ° C. and a load of 2.16 kg, and the ethylene-based copolymer. It is preferable that union (X) contains 40 to 5 parts by weight.

The composition containing the copolymer of the present invention has good foamability and moldability. By foaming the composition, a foamed molded article having excellent heat resistance and impact resistance and good appearance is obtained. be able to. The molded body is suitably used for various applications such as a buffer material, a heat insulating material, and a sound absorbing material.

Hereinafter, the present invention will be specifically described.
[Ethylene copolymer (X)]
The ethylene copolymer (X) of the present invention has a structure derived from ethylene [A], an α-olefin [B] having 3 to 20 carbon atoms, and 5-vinyl-2-norbornene (VNB) [C]. A copolymer containing a unit and synthesized using a metallocene catalyst, wherein (1) a structural unit derived from an α-olefin [B] having 3 to 20 carbon atoms is 100 mol% in all structural units, 5 to 45 mol%, and (2) the structural unit derived from VNB is 0.1 to 0.8 mol% in 100 mol% of all structural units, and (3) at 190 ° C. and a load of 2.16 kg. The measured melt flow rate [MFR (g / 10 min)] is 0.3 to 10, and (4) satisfies the following formula (A).

13> degree of strain hardening in elongational viscosity measurement (χ _max )> 3 (A)

  In addition, in this specification, said (1)-(4) is also described as requirements (1)-(4), respectively. The copolymer of the present invention comprises ethylene [A], α-olefin [B] having 3 to 20 carbon atoms, and 5-vinyl-2-norbornene (VNB) as monomers, and a structural unit derived from the raw material. It is a copolymer having.

  In the present specification, ethylene [A] is component [A], α-olefin [B] having 3 to 20 carbon atoms is component [B], and 5-vinyl-2-norbornene (VNB) [C] is Also referred to as component [C].

[Component [A]]
In the copolymer of the present invention, the structural unit derived from ethylene [A] is 55 to 95 mol%, preferably 60 to 90 mol%, in 100 mol% of all structural units.

[Component [B]]
Specific examples of the α-olefin [B] having 3 to 20 carbon atoms include propylene, 1-butene, 1-pentene, 1-hexene, 4-methyl-1-pentene, 1-heptene, 1- Examples include octene, 1-decene, 1-dodecene, 1-tetradecene, 1-hexadecene, and 1-eicocene. Of these, α-olefins having 3 to 8 carbon atoms such as propylene, 1-butene, 1-hexene and 1-octene are particularly preferable. Such an α-olefin is preferable because the raw material cost is relatively low and the resulting copolymer exhibits excellent mechanical properties.

  In addition, the copolymer of this invention contains the structural unit derived from an at least 1 sort (s) of C3-C20 alpha-olefin [B], and has 2 or more types of C3-C20 alpha-. A structural unit derived from olefin [B] may be included.

  The copolymer of the present invention contains, in addition to the above-mentioned component [A], component [B], and component [C], a structural unit derived from a non-conjugated diene containing 0.1 to It may contain 5.0 mol%. Examples of the non-conjugated diene component include the following aliphatic polyenes and alicyclic polyenes.

  Specific examples of the aliphatic polyene include 1,4-hexadiene, 1,5-heptadiene, 1,6-octadiene, 1,7-nonadiene, 1,8-decadiene, 1,12-tetradecadiene, 3- Methyl-1,4-hexadiene, 4-methyl-1,4-hexadiene, 5-methyl-1,4-hexadiene, 4-ethyl-1,4-hexadiene, 3,3-dimethyl-1,4-hexadiene, 5-methyl-1,4-heptadiene, 5-ethyl-1,4-heptadiene, 5-methyl-1,5-heptadiene, 6-methyl-1,5-heptadiene, 5-ethyl-1,5-heptadiene, 4-methyl-1,4-octadiene, 5-methyl-1,4-octadiene, 4-ethyl-1,4-octadiene, 5-ethyl-1,4-octadiene, 5-methyl-1,5-octadiene, 6-methyl-1,5-octadiene, 5-ethyl-1,5-octadiene, 6-ethyl-1,5-octadiene, 6-methyl-1,6-octadiene, 7-methyl-1,6-octadiene, 6-ethyl-1,6-octadiene, 6-propiene -1,6-octadiene, 6-butyl-1,6-octadiene, 7-methyl-1,6-octadiene, 4-methyl-1,4-nonadiene, 5-methyl-1,4-nonadiene, 4-ethyl -1,4-nonadiene, 5-ethyl-1,4-nonadiene, 5-methyl-1,5-nonadiene, 6-methyl-1,5-nonadiene, 5-ethyl-1,5-nonadiene, 6-ethyl -1,5-nonadiene, 6-methyl-1,6-nonadiene, 7-methyl-1,6-nonadiene, 6-ethyl-1,6-nonadiene, 7-ethyl-1,6-nonadiene, 7-methyl -1,7-nonadiene, 8-methyl-1,7-nonadiene, 7-ethyl-1,7-nonadiene, 5-methyl-1,4-decadiene, 5-ethyl-1,4-decadiene, 5-methyl -1,5-decadiene, 6-methyl-1,5-decadiene, 5-ethyl-1,5-decadiene, 6-ethyl-1,5-decadiene, 6-methyl-1,6-decadiene, 6-ethyl -1,6-decadiene, 7-methyl-1,6-decadiene, 7-ethyl-1,6-decadiene, 7-methyl-1,7-decadiene, 8-methyl-1, 7-decadiene, 7-ethyl-1,7-decadiene, 8-ethyl-1,7-decadiene, 8-methyl-1,8-decadiene, 9-methyl-1,8-decadiene, 8-ethyl-1, Examples include 8-decadiene, 6-methyl-1,6-undecadiene, 9-methyl-1,8-undecadiene, and the like. In the present invention, these aliphatic polyenes can be used singly or in combination of two or more. Preferably, 7-methyl-1,6-octadiene is used.

  The alicyclic polyene is composed of an alicyclic portion having one carbon / carbon double bond (unsaturated bond) and a chain portion having an internal olefin bond (carbon / carbon double bond). Specific examples thereof include 5-ethylidene-2-norbornene (ENB), 5-propylidene-2-norbornene, 5-butylidene-2-norbornene, and the like. 5-ethylidene-2-norbornene (ENB) ) Is preferably used. Specific examples of the other alicyclic polyenes include 2-methyl-2,5-norbornadiene and 2-ethyl-2,5-norbornadiene.

[Requirement (1)]
In the copolymer of the present invention, the structural unit derived from the α-olefin [B] having 3 to 20 carbon atoms is 5 to 45 mol%, preferably 10 to 40 mol in 100 mol% of all structural units. %.

  When the structural unit (mol%) derived from the component [B] is in the above range, it is preferable from the viewpoint of the flexibility and impact resistance of the foam obtained from the composition containing the copolymer of the present invention. .

The molar ratio can be determined by ¹ H-NMR.
[Requirement (2)]
In the copolymer of the present invention, the structural unit derived from VNB [C] is 0.1 to 0.8 mol%, preferably 0.1 to 0.6 mol%, in 100 mol% of all structural units. More preferably, it is 0.1 to 0.5 mol%.

  When the structural unit (mol%) derived from the component [C] is in the above range, it is preferable from the viewpoint of the expansion ratio and appearance of the foam obtained from the composition containing the copolymer of the present invention.

The molar ratio can be determined by ¹ H-NMR.
Specifically, the ¹ H-NMR spectrum of the copolymer is obtained under the following conditions, and the amount of structural units derived from ethylene, the amount of structural units derived from propylene, and the amount of structural units derived from VNB in each polymer. Can be obtained from the integrated intensity.
Apparatus: ECX400P type nuclear magnetic resonance apparatus (manufactured by JEOL Ltd.)
Measurement condition frequency: 400 MHz
Pulse width: 6.00 μsec (45 °)
Repeat time: 7.0 seconds Integration count: 512 times Measurement solvent: ODCB-d ₄
Measurement temperature: 120 ° C

[Requirement (3)]
The copolymer of the present invention has a melt flow rate [MFR (g / 10 min)] measured at 190 ° C. and a load of 2.16 Kg of 0.3 to 10, preferably 0.3 to 8, more preferably 0.4-6.

When the MFR is within the above range, the moldability of the composition containing the copolymer of the present invention is good, and it is preferable from the viewpoint of the appearance of the foam.
The MFR can be measured according to ASTM D1238.

[Requirement (4)]
The copolymer of the present invention satisfies the following formula (A), and preferably satisfies the following formula (A ′).
13> degree of strain hardening in elongational viscosity measurement (χ _max )> 3 (A)
11> degree of strain hardening in elongational viscosity measurement (χ _max )> 3.5 (A ′)

In general, deformation having a free surface such as spinning molding, film molding, blow molding, and foam molding is dominated by elongational deformation. The behavior of the polymer melt under elongation deformation is evaluated by measuring the viscosity under uniaxial elongation deformation with the simplest deformation mode. With respect to the uniaxial elongation viscosity of the polymer melt, a strain hardening property is observed in which the elongation viscosity increases as compared with the elongation viscosity in the linear region due to an increase in applied strain. The degree of strain hardening in the measurement of elongational viscosity is an important index for molding processing under elongation deformation, and those with a large degree of strain hardening have a uniform cell thickness during blow molding, as well as cell cells during foam molding. It is known that it has a function of growing uniformly, and the degree of strain hardening is represented by the following formula (A).
Strain hardening degree (χ _max ) = η _Emax / η _lin (A)
η _Emax ; maximum reached extensional viscosity, η _lin ; linear viscosity

Here, η _Emax is the maximum value of the extension viscosity until the strain amount becomes 3, and η _lin is a strain in a time-extension viscosity curve (logarithmic plot) obtained by uniaxial extension viscosity measurement under a constant strain rate. The viscosity immediately before curing is approximated by a straight line, and is the viscosity on the approximate straight line up to the time when the extensional viscosity becomes the maximum value.

  The degree of strain hardening has a long relaxation time and increases with the introduction of a high molecular weight component or a branched component. It is a useful indicator of quantity.

With respect to the method for measuring the strain hardening degree, the same value can be obtained by any method as long as the uniaxial elongation viscosity can be measured. In the present invention, however, a viscoelastic device (Anton) equipped with a uniaxial elongation jig (Sentmanat Extended Rheometer) is used. This was measured using a viscoelasticity tester (model MCR301) manufactured by Pearl. Moreover, it is preferable to mix | blend a suitable quantity (for example, 1000 ppm) of antioxidant previously with a measurement sample. As a sample for measuring extensional viscosity, a sheet having a thickness of 2 mm obtained by pressing the copolymer at 210 ° C. was cut into a width of 10 mm and a length of 20 mm. Using this sample, the elongational viscosity was measured at 210 ° C. and a strain rate of 0.1 sec ⁻¹ , and the strain hardening degree was determined by the above calculation method.

  The copolymer of the present invention is a copolymer synthesized using a metallocene catalyst as described above. In the present invention, the metallocene catalyst is represented by the following formula (I), (II) or (III). The catalysts represented are preferred.

  The compound represented by formula (I) will be described.

In formula (I), each R is independently a group or hydrogen atom selected from hydrocarbyl, halohydrocarbyl, silyl, germyl, and combinations thereof, and the number of atoms other than hydrogen contained in the group is 20 or less. It is.
M is titanium, zirconium or hafnium.
Y is -O-, -S-, -NR ^* -or -PR ^* -.

R ^* is a hydrogen atom, hydrocarbyl group, hydrocarbyloxy group, silyl group, halogenated alkyl group or halogenated aryl group, and when R ^* is not hydrogen, R ^* represents up to 20 non-hydrogen atoms. contains.

  Z is a divalent group containing boron or a group 14 element and containing nitrogen, phosphorus, sulfur or oxygen, and the divalent group has 60 or less atoms other than hydrogen atoms. is there.

  X is an anionic ligand having 60 or less atoms independently when a plurality of X are present (except for a cyclic ligand in which π electrons are delocalized).

X ′ is a neutral linking compound having 20 or less atoms, independently when there are a plurality of X ′.
p is 0, 1 or 2.
q is 0 or 1.

  However, when p is 2 and q is 0, M is in the +4 oxidation state, X is halide, hydrocarbyl, hydrocarbyloxy, di (hydrocarbyl) amide, di (hydrocarbyl) phosphide, hydrocarbyl sulfide, silyl group, An anionic ligand selected from a halo-substituted derivative, a di (hydrocarbyl) amino-substituted derivative, a hydrocarbyloxy-substituted derivative and a di (hydrocarbyl) phosphino-substituted derivative, wherein the number of atoms other than hydrogen atoms of X is 20 or less is there. When p is 1 and q is 0, M is in the +3 oxidation state, X is allyl, 2- (N, N′-dimethylaminomethyl) phenyl and 2- (N, N′-dimethyl) aminobenzyl. Or M is in an oxidation state of +4, and X is a divalent conjugated diene derivative to form metallacyclopentene with M. When p is 0 and q is 1, M is in the +2 oxidation state, X ′ is a neutral conjugated or nonconjugated diene which may be substituted with one or more hydrocarbyl groups, and has 40 carbon atoms. It is contained in a number of 1 or less and forms a π complex with M.

  The compound represented by formula (II) will be described.

In formula (II), R ¹ and R ² are a hydrogen atom or an alkyl group having 1 to 6 carbon atoms, and at least one of R ¹ and R ² is not a hydrogen atom.
R ^{3 to} R ⁶ are each independently a hydrogen atom or an alkyl group having 1 to 6 carbon atoms.
R ^{1 to} R ⁶ may be bonded to each other to form a ring.
M is titanium.
Y is -O-, -S-, -NR ^* -or -PR ^* -.
Z ^* is _{^{SiR * 2, CR * 2,}} SiR * 2 SiR * 2, CR * 2 CR * 2, CR * = CR *, CR * 2 SiR * 2 , or GeR ^* _2.

Each R ^* is independently a hydrogen atom, hydrocarbyl group, hydrocarbyloxy group, silyl group, halogenated alkyl group or halogenated aryl group, and when R ^* is not hydrogen, R ^* is up to 20 hydrogen atoms; Contains atoms other than. Z two binding of the ^* R ^* (when R ^* is not hydrogen) may also form a ring, R ^* binding to R ^* and Y bonded to Z ^* may form a ring.
p is 0, 1 or 2.
q is 0 or 1.

  However, when p is 2, q is 0, M is in a +4 oxidation state, and X is independently a methyl group or a benzyl group. When p is 1, q is 0, M is in an oxidation state of +3, X is a 2- (N, N′-dimethyl) aminobenzyl group, or q is 0, and M is In the +4 oxidation state, X is 1,3-butadienyl. When p is 0, q is 1, M is in the +2 oxidation state, and X is 1,4-diphenyl-1,3-butadiene, 2,4-hexadiene, or 1,3-pentadiene.

  The compound represented by formula (III) will be described.

In formula (III), R ′ is a hydrogen atom, a hydrocarbyl group, a di (hydrocarbylamino) group, or a hydrocarbyleneamino group, and when R ′ has a carbon atom, the number of carbon atoms is 20 or less.
In formula (III), R ″ is a hydrocarbyl group having 1 to 20 carbon atoms or a hydrogen atom.
In the formula (III), M is titanium.
In formula (III), Y, -O -, - S -, - NR * -, - PR * -, - NR 2 *, or -PR ₂ ^*.
Wherein (III), Z ^{* _{is, -SiR * 2 -, - CR}} * 2 -, - SiR * 2 SiR * 2 -, - CR * 2 CR * 2 -, - CR * = CR * -, - CR ^* ₂ SiR ^* _2- or -GeR ^* _2- .

Each of R ^* is independently a hydrogen atom or a group containing at least one selected from the group consisting of hydrocarbyl, hydrocarbyloxy, silyl, alkyl halide, and aryl halide, when there are a plurality of R ^* , R ^* includes atoms from 2 to 20, and two R ^{* s} (if R ^* is not a hydrogen atom) that Z ^* optionally may form a ring, and R ^* and Y of Z ^* R ^* in the above may form a ring.

  In formula (III), X is a monovalent anionic ligand having 60 or less atoms, excluding a cyclic ligand in which π electrons are delocalized. X ′ is a neutral linking group having 20 or less atoms. X ″ is a divalent anionic ligand having 60 or less atoms. P is 0, 1 or 2. q is 0 or 1. r is 0 or 1.

When p is 2, q and r are 0 and M is an oxidation state of +4 (except when Y is -NR ^* ₂ or -PR ^* ₂ ), or M is an oxidation state of +3 (provided that , Y is —NR ^* ₂ or —PR ^* ₂ , and X is a halide group, hydrocarbyl group, hydrocarbyloxy group, di (hydrocarbyl) amide group, di (hydrocarbyl) phosphide group, hydrocarbyl sulfide group, and silyl Groups, as well as groups in which these groups are halogen substituted, groups in which these groups are di (hydrocarbyl) amino substituted, groups in which these groups are hydrocarbyloxy substituted and groups in which these groups are di (hydrocarbyl) phosphino substituted An anionic ligand selected from the group consisting of the above groups, wherein the group comprises atoms having atomic numbers from 2 to 30.

  When r is 1, p and q are 0, M is in the +4 oxidation state, and X ″ is a dianionic selected from the group consisting of a hydrocarbazyl group, an oxyhydrocarbyl group, and a hydrocarbylene dioxy group A ligand, wherein X ″ has atoms of atomic numbers 2 to 30. When p is 1, q and r are 0, M is the oxidation state of +3, X is allyl, 2- (N, N-dimethylamino) phenyl, 2- (N, N-dimethylaminomethyl) ) An anionic stabilizing ligand selected from the group consisting of phenyl and 2- (N, N-dimethylamino) benzyl. When p and r are 0, q is 1, M is in the +2 oxidation state, and X ′ is a neutral conjugated diene or neutral diconjugated, optionally substituted with one or more hydrocarbyl groups It is a diene, and the X ′ has a carbon atom number of 40 or less and forms a bond with M by π-π interaction.

In a more preferred embodiment, in formula (III), when p is 2 and q and r are 0, M is in the +4 oxidation state, and each X is independently methyl, benzyl, or halide. Yes, when p and q are 0, r is 1, M is in the +4 oxidation state, X ″ is a 1,4-butadienyl group that forms a metallacyclopentene ring with M, and p is 1 Q and r are 0, M is in the +3 oxidation state, X is 2- (N, N-dimethylamino) benzyl, and when p and r are 0, q is 1 Where M is the +2 oxidation state and X ′ is 1,4-diphenyl-1,3-butadiene or 1,3-pentadiene.
Of the formula (III), a compound represented by the following formula (III ′) is particularly preferable.

In the above formula (III ′), R ′ is a hydrogen atom and a hydrocarbyl group having 1 to 20 carbon atoms, R ″ is a hydrocarbyl group or hydrogen atom having 1 to 20 carbon atoms, M is titanium, Y Is —NR ^* —, Z ^* is —SiR ^* ₂ —, and each R ^* is independently a hydrogen atom or a hydrocarbyl group having 1 to 20 carbon atoms, and of p and q When one is 0, the other is 1, p is 0 and q is 1, M is in the +2 oxidation state and X ′ is 1,4-diphenyl-1,3-butadiene or 1 , 3-pentadiene, when p is 1 and q is 0, M is in the +3 oxidation state and X is 2- (N, N-dimethylamino) benzyl.

Examples of the hydrocarbyl group having 1 to 20 carbon atoms include linear alkyl groups such as a methyl group, an ethyl group and a butyl group, and branched alkyl groups such as a t-butyl group and a neopentyl group. Examples include linear alkyloxy groups such as oxy group, ethyloxy group, and butyloxy group, and branched alkyloxy groups such as t-butyloxy group and neopentyloxy group. And chlorinated, brominated or fluorinated groups or branched alkyl groups. Examples of the halogenated aryl group include a chlorinated phenyl group and a chlorinated naphthyl group.
In the above formula (III ′), R ″ is preferably a hydrogen atom or methyl, and is preferably methyl.

Particularly preferred catalysts are (t-butylamido) dimethyl (η ⁵ -2-methyl-s-indasen-1-yl) silane titanium (II) 2,4-hexadiene (IV), (t-butylamido) -dimethyl (η ^5-methyl -s- indacene-1-yl) silane - titanium (IV) dimethyl (V), (t-butylamido) - dimethyl (eta ^{5-2,3-dimethyl} indenyl) silane titanium (II) 1 , 4-diphenyl-1,3-butadiene (VI), (t-butyl-amido) -dimethyl (η ⁵ -2,3-dimethyl-s-indasen-1-yl) silane titanium (IV) dimethyl (VII) , (T-Butylamido) -dimethyl (η ⁵ -2-methyl-s-indasen-1-yl) silane titanium (II) 1,3-pentadiene (VIII) .
Among them, (t-butylamido) -dimethyl (η ⁵ -2-methyl-s-indacene-1-yl) silanetitanium (II) 1,3-pentadiene (VIII) is particularly preferable.

In particular, when a catalyst having a structure represented by the above formula (VIII) is used, the polymerization reaction for obtaining the copolymer of the present invention is excellent in the copolymer property of 5-vinyl-2-norbornene (VNB), For example, a double bond at the VNB end can be efficiently incorporated and branching can be introduced at a high rate. In addition, since the molecular weight distribution and composition distribution of the obtained copolymer are narrow and a copolymer having a very uniform molecular structure can be prepared, gel-like irregularities on the surface of the molded body, which are concerned with branch formation, are also a concern. Formation is significantly suppressed. As a result, a molded body containing such a copolymer does not contain gel-like particles, so that the surface appearance is excellent, and because the shape retention is excellent, the production stability is also good.
These catalysts can be prepared using well-known synthetic techniques. For example, it is disclosed in International Publication WO98 / 49212.

<Method for producing copolymer>
When synthesizing the copolymer of the present invention, a metallocene catalyst, preferably a catalyst having the structure exemplified above is used. More specifically, the above catalyst is used as a main catalyst, an organoaluminum compound such as a boron compound and / or a trialkyl compound is used as a cocatalyst, an aliphatic hydrocarbon such as hexane is used as a solvent, and a continuous process using a reactor with a stirrer or A batch method is mentioned.

  Examples of boron compounds include trimethylammonium tetrakis (pentafluorophenyl) borate, di (hydrogenated tallow alkyl) methylammonium tetrakis (pentafluorophenyl) borate, triethylammonium tetrakis (pentafluorophenyl) borate, tripropylammonium tetrakis (penta Fluorophenyl) borate, tri (n-butyl) ammonium tetrakis (pentafluorophenyl) borate, tri (sec-butyl) ammonium tetrakis (pentafluorophenyl) borate, N, N-dimethylanilinium tetrakis (pentafluorophenyl) borate, N, N-dimethylanilinium n-butyltris (pentafluorophenyl) borate, N, N-dimethylanilinium base Diltris (pentafluorophenyl) borate, N, N-dimethylanilinium tetrakis (4- (t-butyldimethylsilyl) -2,3,5,6-tetrafluorophenyl) borate, N, N-dimethylanilinium tetrakis ( 4- (triisopropylsilyl) -2,3,5,6-tetrafluorophenyl) borate, N, N-dimethylanilinium pentafluorophenoxytris (pentafluorophenyl) borate, N, N-diethylanilinium tetrakis (penta Fluorophenyl) borate, N, N-dimethyl-2,4,6-trimethylanilinium tetrakis (pentafluorophenyl) borate, trimethylammonium tetrakis (2,3,4,6-tetrafluorophenyl) borate, triethylammonium Trakis (2,3,4,6-tetrafluorophenyl) borate, tripropylammonium tetrakis (2,3,4,6-tetrafluorophenyl) borate, N, N-dimethylanilinium tetrakis (2,3,4, 6-tetrafluorophenyl) borate, N, N-diethylanilinium tetrakis (2,3,4,6-tetrafluorophenyl) borate, and N, N-dimethyl-2,4,6-trimethylanilinium tetrakis (2 , 3,4,6-tetrafluorophenyl) borate; dialkylammonium salts such as di- (i-propyl) ammonium tetrakis (pentafluorophenyl) borate, tri (n-butyl) ammonium tetrakis (2,3,4, 6-tetrafluorophenyl) borate, dimethyl (t-butyl) E) ammonium tetrakis (2,3,4,6-tetrafluorophenyl) borate, and dicyclohexylammonium tetrakis (pentafluorophenyl) borate; trisubstituted phosphonium salts such as triphenylphosphonium tetrakis (pentafluorophenyl) borate, Tri (o-tolyl) phosphonium tetrakis (pentafluorophenyl) borate and tri (2,6-dimethylphenyl) phosphonium tetrakis (pentafluorophenyl) borate; disubstituted oxonium salts such as diphenyloxonium tetrakis (pentafluoro Phenyl) borate, di- (o-tolyl) oxonium tetrakis (pentafluorophenyl) borate, and di (2,6-dimethylphenyl) oxonium tetrakis (Pentafluorophenyl) borate; disubstituted sulfonium salts such as diphenylsulfonium tetrakis (pentafluorophenyl) borate, di (o-tolyl) sulfonium tetrakis (pentafluorophenyl) borate, and bis (2,6-dimethylphenyl) ) Sulfonium tetrakis (pentafluorophenyl) borate and the like.

  Examples of the organoaluminum compound include triisobutylaluminum (hereinafter also referred to as “TIBA”). The reaction temperature can be raised to 100 ° C. because the catalyst is not deactivated even at high temperatures. The polymerization pressure is in the range of more than 0 to -8 MPa (gauge pressure), preferably more than 0 to -5 MPa (gauge pressure). The reaction time (average residence time when copolymerization is carried out in a continuous process) varies depending on conditions such as catalyst concentration and polymerization temperature, but is usually 0.5 minutes to 5 hours, preferably 10 minutes to 3 hours. Further, in the copolymerization, a molecular weight regulator such as hydrogen can be used.

  The molar (feed) ratio ([A] / [B]) of ethylene [A] to the α-olefin [B] is 25/75 to 90/10, preferably 30/70 to 80/20.

  The molar (feed) ratio ([A] / [C]) of ethylene [A] and 5-vinyl-2-norbornene (VNB) [C] is 70/30 to 99.9 / 0.1, preferably 80/20 to 99.5 / 0.5.

  Polymerization using the above catalyst is preferable because a non-conjugated polyene having a double bond is copolymerized at a high conversion rate, and an appropriate amount of branching can be introduced into the resulting copolymer.

  In the copolymer of the present invention thus obtained, the structural unit derived from the α-olefin [B] having 3 to 20 carbon atoms is 5 to 45 mol% in 100 mol% of all structural units, Preferably it is 10-40 mol%. Moreover, the structural unit derived from VNB is 0.1-0.8 mol% in 100 mol% of all structural units, Preferably it is 0.1-0.6 mol%.

  Polymerization using the above catalyst is preferable because VNB is copolymerized at a high conversion and a large amount of branching can be introduced into the resulting copolymer.

[Polyolefin resin (Y)]
The polyolefin resin used in the present invention has an MFR measured at 190 ° C. and a load of 2.16 kg of 0.1 to 30 g / 10 minutes, preferably 1.0 to 30 g / 10 minutes, more preferably 5.0. It is preferably ˜25 g / 10 minutes.

When the MFR is within the above range, the moldability of the composition containing the ethylene copolymer (X) of the present invention is good, and it is preferable from the viewpoint of the appearance of the foam. The MFR can be measured according to ASTM D1238.
Examples of the polyolefin resin (Y) include polyethylene, polypropylene, polybutene, and an ethylene-α olefin copolymer, among which linear low-density polyethylene is particularly preferable, and the density [d (kg / m ³ )] is 925 to 925. A range of 965 kg / m ³ is preferably used. In this range, it is suitable from the viewpoints of moldability during foaming and heat resistance of the foamed molded product. The density can be measured according to JIS K6760 (1995).

<Composition>
In the composition of the present invention, the mixing ratio of the ethylene copolymer (X) and the polyolefin resin (Y) is (X) / (Y) = 40/60 to 5/95, preferably 35/65 to 10 /. 90, more preferably 35/65 to 15/85. When the ratio of the ethylene-based copolymer (X) exceeds 40% by weight, the molding processability is deteriorated. When the ratio is less than 5% by weight, the strain hardening degree becomes small, so it is difficult to increase the expansion ratio. At the same time, the appearance of the foam-molded product deteriorates.
The composition of the present invention may contain components other than the copolymer and the polyolefin resin. Other components include, for example, anti-aging agents (stabilizers), antistatic agents, antifogging agents, antiblocking agents, inorganic fillers such as glass fibers, reinforcing agents, organic fillers or reinforcing agents, softening agents. A known additive such as a flame retardant can be blended.

  The composition of the present invention comprises the copolymer of the present invention and other components, for example, a batch mixer such as an internal mixer, a kneader, a roll kneader, or a continuous mixer such as a short / double screw extruder. Done by machine. In order to obtain a resin composition with stable quality, the mixing temperature is preferably 150 ° C to 250 ° C.

  As a method for producing an extruded foam using the ethylene copolymer composition of the present invention, any method may be used as long as the foam is obtained. For example, the ethylene copolymer composition and the above-described method may be used. Supply the air conditioning agent such as talc and shrinkage inhibitor added to the extruder according to the heat, melt and knead, and supply the foaming agent to make the foamable molten resin mixture. Examples of the method include adjusting the internal pressure of the die, the discharge amount, and the like, and extruding into a low pressure region from a die attached to the tip of the extruder for foaming. Also, extrusion foams of various shapes such as round bar foams, sheet foams, plate foams, etc. are manufactured by selecting a die attached to the tip of the extruder according to the desired foam shape. be able to. For example, if a strand die is attached, a round bar-like foam can be obtained; if an annular die is attached, a sheet-like foam can be obtained; and if a slit die is attached, a plate-like foam can be produced. .

  The extruded foam in the present invention is prepared by supplying the above composition, additive, foaming agent, etc. to an extruder, heating and kneading to obtain a foamable molten resin mixture, and then adjusting the extruder resin temperature within an appropriate range. Then, it can be formed by extruding from an extruder to a low pressure region. That is, it is considered that the foamable molten resin mixture whose extrusion resin temperature is adjusted within an appropriate range has a melt tension that resists the foaming force of the foaming agent and foams uniformly.

The specific extrusion resin temperature is based on the melting point of the polyolefin resin (Y), and the extrusion resin temperature of the foamable molten resin is [the melting point of the olefin resin (Y) −10 ° C.] to [the olefin resin (Y). It is preferable to adjust within the range of [melting point of the olefin resin (Y) −5 ° C.] to [melting point of the olefin resin (Y) + 5 ° C.]. Is preferred. When the extrusion resin temperature is lower than [the melting point of the above-mentioned olefin resin (Y) −10 ° C.], crystallization occurs at the die portion, and it becomes difficult to obtain a foam. On the other hand, when the extrusion temperature is higher than [the melting point of the olefin resin (Y) + 10 ° C.], the foam of the resulting foam breaks and becomes non-uniform.

Examples of the foaming agent in extrusion foam molding include inorganic gas foaming agents such as carbon dioxide, nitrogen, argon, and air; propane, butane, pentane, hexane, cyclobutane, cyclohexane, trichlorofluoromethane, dichlorodifluoromethane, and the like. Volatile foaming agents: azodicarbonamide, barium azodicarboxylate, N, N-dinitrosopentamethylenetetramine, 4,4'-oxybis (benzenesulfonylhydrazide) that is liquid or solid at room temperature and generates gas when heated ), Chemical foaming agents such as diphenylsulfone-3,3′-disulfonylhydrazide, p-toluenesulfonyl semicarbazide, trihydrazinotriazine, biurea, zinc carbonate, and the like. The ethylene-based copolymer (X) and polyolefin resin (Y) of the present invention Preferably 1-20 parts by weight with respect to total 100 parts by weight, particularly preferably in the range of 5 to 15 parts by weight. The expansion ratio is preferably 5 to 50 times. The resin composition of the present invention is excellent in low-temperature extrusion processability, heat resistance and foam moldability, and retains the excellent properties inherent in high-density linear polyolefin-based resins. An uncrosslinked polyolefin resin foam having excellent surface characteristics and closed cells and a high expansion ratio can be obtained.

  Since the foam of the present invention is excellent in heat resistance and flexibility and has a high expansion ratio, it is suitably used for various applications such as a cushioning material, a heat insulating material, and a sound absorbing material.

EXAMPLES Next, although an Example is shown and this invention is demonstrated further in detail, this invention is not limited by these.
Each physical property of the obtained copolymer was measured according to the following.

[Molar amount of structural unit derived from α-olefin [B] having 3 to 20 carbon atoms]
^It calculated | required by the intensity | strength measurement by a < ¹ > H-NMR spectrum meter.

[Molar amount of structural unit derived from VNB [C]]
^It calculated | required by the intensity | strength measurement by a < ¹ > H-NMR spectrum meter.

[Melt flow rate [MFR] (g / 10 min)]
Melt flow rate measured at 190 ° C. and 2.16 kg load [MFR (g / 10 min)]

[Strain hardening in elongational viscosity measurement]
The degree of strain hardening in the measurement of elongational viscosity is an important index for molding processing under elongation deformation, and those with a large degree of strain hardening have a uniform cell thickness during blow molding, as well as cell cells during foam molding. It is known that it has a function of growing uniformly, and the degree of strain hardening is represented by the following formula (A).
Strain hardening degree (χ _max ) = η _Emax / η _lin (A)
η _Emax ; maximum reached elongation viscosity, η _lin ; linear viscosity Here, η _Emax is the maximum value of elongation viscosity until the strain amount becomes 3, and η _lin is obtained by uniaxial elongation viscosity measurement under a constant strain rate. In the time-extension viscosity curve (logarithmic plot), the viscosity immediately before the strain hardening is approximated by a straight line, and the viscosity is on the approximate straight line up to the time when the elongational viscosity becomes the maximum value.

  The degree of strain hardening has a long relaxation time and increases with the introduction of a high molecular weight component or a branched component. It is a useful indicator of quantity.

As for the method for measuring the strain hardening degree, the same value can be obtained by any method as long as the uniaxial elongation viscosity can be measured. Here, however, the viscoelastic device (Anton Paar) equipped with a uniaxial extension jig (Sentmanat Extended Rheometer) It measured using the viscoelasticity testing machine made from a company (model MCR301). As a sample for measuring extensional viscosity, a sheet having a thickness of 2 mm obtained by pressing the copolymer at 210 ° C. was cut into a width of 10 mm and a length of 20 mm. Using this sample, the elongational viscosity was measured at 210 ° C. and a strain rate of 0.1 sec ⁻¹ , and the strain hardening degree was calculated by the above calculation method.

[Example 1]
Continuously using a polymerization vessel having a volume of 300 L equipped with a stirring blade, a ternary composed of component [A]: ethylene, component [B]: propylene, component [C]: 5-vinyl-2-norbornene (VNB) The polymerization reaction of the copolymer was performed at 90 ° C.

As a polymerization solvent, hexane (feed amount 30.4 Kg / h) was used, ethylene feed amount 7.6 Kg / h, propylene feed amount 3.7 Kg / h, VNB feed amount 90 g / h, and hydrogen (H ₂ ) The feed amount was continuously supplied to the polymerization reactor at 85 NL / h. (T-Butylamido) -dimethyl (η ⁵ -2-methyl-s-indacene-1-yl) is a catalyst having a structure represented by the above formula (VIII) as a main catalyst while maintaining the polymerization pressure at 1.6 MPa. ) Using silane titanium (II) 1,3-pentadiene, it was continuously fed to the polymerization vessel so as to be 0.04 mmol / h. Further, (C ₆ H ₅ ) ₃ CB (C ₆ F ₅ ) ₄ is 0.15 mmol / h as a cocatalyst, and triisobutylaluminum (hereinafter also referred to as “TIBA”) is 25 mmol / h as an organoaluminum compound. Each was continuously fed to the polymerization vessel.

  In this way, a polymer solution containing 14.9% by weight of a copolymer composed of ethylene, propylene, and VNB was obtained. A small amount of methanol was added to the polymerization solution extracted from the lower part of the polymerization vessel to stop the polymerization reaction. The polymer was separated from the solvent by a steam stripping treatment, and then dried under reduced pressure at 80 ° C. overnight. The physical properties of the obtained copolymer are shown in Table 1.

[Example 2]
The synthesis was performed in the same manner as in Example 1 except that the feed amounts of ethylene, propylene and VNB were changed. The physical properties of the obtained copolymer are shown in Table 1.

Example 3
The synthesis was performed in the same manner as in Example 1 except that the feed amounts of ethylene, propylene and VNB were changed. The physical properties of the obtained copolymer are shown in Table 1.

Example 4
Using a 300 L capacity polymerization vessel equipped with a stirring blade, component [A]: ethylene, component [B]: propylene, component [C]: 5-vinyl-2-norbornene (VNB), and 5- A polymerization reaction of a quaternary copolymer composed of ethylidene-2-norbornene (ENB) was carried out at 95 ° C.

As a polymerization solvent, hexane (feed amount 26.6 kg / h) is used, ethylene feed amount is 5.5 kg / h, propylene feed amount is 4.9 kg / h, VNB feed amount is 96 g / h, ENB feed amount is 929 g / h and a hydrogen (H ₂ ) feed amount of 120 NL / h were continuously fed to the polymerization reactor.
The other conditions were synthesized in the same manner as in Example 1. The physical properties of the obtained copolymer are shown in Table 1.

[Comparative Example 1]
The synthesis was performed in the same manner as in Example 1 except that the feed amounts of ethylene and propylene were changed to 7.5 kg / h and 3.2 kg / h, respectively, and the feed of VNB was cut. The physical properties of the obtained copolymer are shown in Table 1.

[Comparative Example 2]
Synthesis was performed in the same manner as in Example 4 except that the feed amounts of ethylene, propylene, VNB and ENB were changed. The physical properties of the obtained copolymer are shown in Table 1.

[Comparative Example 3]
Ethylene / propylene / 5-ethylidene-2-norbornene terpolymer [trade name: Mitsui Elastomer K-9720 (trademark), manufactured by Mitsui Chemicals, Inc., ethylene content 88 mol%, ENB content 2.8 mol%, MFR ( 190 ° C., 2.16 kg load) 2 g / 10 min]
Hereafter, the measuring method of each physical property of a composition is shown.

[Closed cell ratio]
The closed cell ratio of the foamed molded product: S (%) was measured using an air comparison type hydrometer manufactured by Toyo Seiki Seisakusho (M-1 type) in accordance with Procedure C described in ASTM D2856-70. The actual volume of the foam (the sum of the volume of closed cells and the volume of the resin part): a value calculated from the following formula from Vx (L).
S (%) = (Va−Vx) × 100 / (Va−W / ρ)
Va: Apparent volume (L) calculated from the outer dimensions of the foam specimen used for the measurement
W: Weight of test piece ρ: Density of resin constituting the test piece (g / L)

  The density ρ (g / L) of the resin constituting the test piece and the weight W (g) of the test piece are obtained by performing an operation of defoaming the foam test piece with a pressure press and then cooling it. It can be obtained from the obtained test piece.

[Foaming ratio]
A cylindrical foam having a diameter of 5 cm and a length of 10 cm is cut out from the foamed molded product, the weight W2 (g) is measured, and the apparent density is calculated according to the following formula according to JIS K6767.
Apparent density (g / cm ³ ) = W2 / (2.5 × 2.5 × π × 10)
The expansion ratio was calculated from the following equation based on the apparent density.
Expansion ratio = 1 / apparent density

(Foam shape)
The appearance of the foam molded product and the state of bubbles in the cross section were visually evaluated.
○: Smooth surface foam shape, ×: Concave foam shape

Example 5
Example 1 [ethylene copolymer (X)] obtained and commercially available high-density polyethylene [polyolefin resin (Y)] (trade name Nipolon 2500, MFR = 8.0 g / 10 min, manufactured by Tosoh Corporation) Density 961 kg / m ³ ) 15:85 (ethylene copolymer (X): polyolefin resin (Y), weight ratio)
1 part by weight of stearic acid monoglyceride (melting point: 65 ° C., “S-100”, manufactured by Riken Vitamin Co., Ltd.) and 100% by weight of the composition mixed at a ratio of 1 part by weight of “Finecell Master SSC-PO208K” manufactured by Co., Ltd. was added to 100 parts by weight of the composition, and this was put into an extruder to obtain a polyethylene resin melt. And the said polyethylene-type resin composition is used for the foaming extrusion equipment of the single screw extruder (diameter 50mm, L / D = 36, Nippon Steel Works Co., Ltd.) which has the barrel hole for volatile liquid injection in the middle of a barrel. After supplying the product at 10 Kg / h and performing melt-kneading, the butane, which is a volatile liquid, is used as a foaming agent, and is injected from the barrel hole at 700 g / h to disperse the butane, and the surface of the foamed molded product is uneven. A rod-shaped foamed molded product was extruded by a round bar die (diameter 13 mmΦ) set at 135 ° C., which is the lowest resin temperature at which no occurrence of slag occurs. Air was blown to the outside of the rod-like foamed molded article and taken up at 5.0 m / min to obtain a foamed molded article.

  About the foaming molding produced with the said manufacturing method, foaming magnification, foam shape, and bubble shape were evaluated. Table 2 shows the physical properties of the obtained foam. Table 2 also shows the types and blending amounts of the ethylene copolymer (X) and the polyolefin resin (Y).

Example 6
Example 5 except that the polyolefin resin (Y) was changed to linear low-density polyethylene (trade name Nipolon Z ZF260, MFR = 2.0 g / 10 min, density 936 kg / m ³ , manufactured by Tosoh Corporation). As well as. Table 2 shows the physical properties of the obtained foam.

Example 7
The same procedure as in Example 5 was carried out except that the ethylene copolymer (X) was changed to Example 2. Table 2 shows the physical properties of the obtained foam.

Example 8
The same procedure as in Example 5 was performed except that the ethylene copolymer (X) was changed to Example 3. Table 2 shows the physical properties of the obtained foam.

Example 9
The same procedure as in Example 5 was carried out except that the ethylene copolymer (X) was changed to Example 4. Table 2 shows the physical properties of the obtained foam.

Example 10
It carried out similarly to Example 5 except having changed the mixing ratio of ethylene-type copolymer (X) and polyolefin-type resin (Y). Table 2 shows the physical properties of the obtained foam.

[Comparative Example 4]
The same operation as in Example 5 was carried out except that only the polyolefin resin (Y) was used and the ethylene copolymer (X) was not mixed. Table 2 shows the physical properties of the obtained foam.

[Comparative Example 5]
The same procedure as in Example 5 was carried out except that the ethylene copolymer (X) was changed to Comparative Example 1. Table 2 shows the physical properties of the obtained foam.

[Comparative Example 6]
The same procedure as in Example 5 was carried out except that the ethylene copolymer (X) was changed to Comparative Example 2. Table 2 shows the physical properties of the obtained foam.

[Comparative Example 7]
The same procedure as in Example 5 was carried out except that the ethylene copolymer (X) was changed to Comparative Example 3. Table 2 shows the physical properties of the obtained foam.

The foamed molded article of the present invention is obtained by foaming an ethylene-based resin composition exhibiting sufficiently high foamability, and has a good foam appearance and is excellent in heat resistance and impact resistance. Therefore, this molded object can be used suitably for various uses, such as a shock absorbing material, a heat insulating material, and a sound-absorbing material.

Claims (4)

An ethylene system synthesized using a metallocene catalyst comprising a structural unit derived from ethylene [A], an α-olefin [B] having 3 to 20 carbon atoms and 5-vinyl-2-norbornene (VNB) [C] It contains 40 to 5 parts by weight of copolymer (X) and 60 to 95 parts by weight of polyolefin resin (Y) having an MFR of 0.1 to 30 g / 10 minutes measured at 190 ° C. under a load of 2.16 kg. A polyolefin resin composition characterized by comprising:
The polyolefin resin composition, wherein the ethylene copolymer (X) satisfies the following (1) to (4).
(1) The structural unit derived from the α-olefin [B] having 3 to 20 carbon atoms is 5 to 45 mol% in 100 mol% of all structural units,
(2) The structural unit derived from VNB [C] is 0.1 to 0.8 mol% in 100 mol% of all structural units,
(3) The melt flow rate [MFR (g / 10 min)] measured at 190 ° C. and a load of 2.16 kg is 0.3 to 10,
(4) The following formula (A) is satisfied.
13> degree of strain hardening in elongational viscosity measurement (χ _max )> 3 (A) The polyolefin resin composition according to claim 1, wherein the ethylene copolymer (X) is synthesized using a catalyst having a structure represented by the following formula ( III ') .
In the formula (III ′), R ′ is a hydrogen atom, a hydrocarbyl group having 1 to 20 carbon atoms, R ″ is a hydrocarbyl group having 1 to 20 carbon atoms or a hydrogen atom, M is titanium, Y Is —NR ^* —, Z ^* is —SiR ^* ₂ —, and each R ^* is independently a hydrogen atom or a hydrocarbyl group having 1 to 20 carbon atoms, and of p and q When one is 0, the other is 1, p is 0 and q is 1, M is in the +2 oxidation state and X ′ is 1,4-diphenyl-1,3-butadiene or 1 , 3-pentadiene, when p is 1 and q is 0, M is in the +3 oxidation state and X is 2- (N, N-dimethylamino) benzyl. The polyolefin-based resin composition according to claim 1 or 2 , further comprising a foaming agent. A foam obtained by foaming the resin composition according to claim 3 , wherein the foaming ratio is 5 to 50 times.