JP2003171565A - Resin composition containing inorganic fine particle and manufacturing method thereof - Google Patents

Resin composition containing inorganic fine particle and manufacturing method thereof

Info

Publication number
JP2003171565A
JP2003171565A JP2001373923A JP2001373923A JP2003171565A JP 2003171565 A JP2003171565 A JP 2003171565A JP 2001373923 A JP2001373923 A JP 2001373923A JP 2001373923 A JP2001373923 A JP 2001373923A JP 2003171565 A JP2003171565 A JP 2003171565A
Authority
JP
Japan
Prior art keywords
weight
inorganic fine
resin composition
particles
fine particles
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP2001373923A
Other languages
Japanese (ja)
Other versions
JP4048765B2 (en
Inventor
Hiroshi Nozawa
博 野澤
Mitsushige Tsuji
光慈 辻
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP2001373923A priority Critical patent/JP4048765B2/en
Publication of JP2003171565A publication Critical patent/JP2003171565A/en
Application granted granted Critical
Publication of JP4048765B2 publication Critical patent/JP4048765B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Processes Of Treating Macromolecular Substances (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a resin composition in which handling of a fine particle is easy and dispersibility of an inorganic fine particle is excellent. <P>SOLUTION: The resin composition comprises 80-99 parts by weight of a thermoplastic resin, i.e., a particle satisfying the following requirement: (A)-(C) and 1-20 parts by weight of an inorganic fine particle: requirement (A): that a weight average particle diameter is 500 μm or more, requirement (B): that a particle having a particle diameter of 200 μm or less is 1% by weight or more to less than 5% by weight and requirement (C): that a particle having a particle diameter of 500 μm or less is 15% by weight or more. In the method for manufacturing the resin composition, after the thermoplastic resin and the inorganic fine particle are mixed, the mixture is melted and kneaded. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、樹脂組成物に関す
るものである。さらに詳しくは、粉体としての取り扱い
が容易で、無機微粒子の分散性に優れる樹脂組成物に関
するものである。
TECHNICAL FIELD The present invention relates to a resin composition. More specifically, it relates to a resin composition which is easy to handle as a powder and has excellent dispersibility of inorganic fine particles.

【0002】[0002]

【従来の技術】従来から、熱可塑性樹脂を用いて得られ
るフィルムやシートは、食品をはじめとする種々の製品
の包装用材料として広く用いられている。熱可塑性樹脂
を用いて得られるフィルム自体の欠点としては包装適正
の悪化が挙げられ、この欠点はフィルムを重ねたときに
フィルム同士が密着すること、いわゆるフィルムのブロ
ッキングが原因と考えられており、この欠点を解消する
ために、フィルム中に無機微粒子を配合することが広く
行われている。
2. Description of the Related Art Conventionally, films and sheets obtained by using thermoplastic resins have been widely used as packaging materials for various products including foods. As a defect of the film itself obtained by using a thermoplastic resin, there is a deterioration in packaging suitability, and this defect is considered to be caused by so-called film blocking that the films adhere to each other when the films are stacked, In order to eliminate this drawback, it is widely practiced to incorporate inorganic fine particles into the film.

【0003】フィルム中に無機微粒子を配合する方法と
して広く用いられているのは、粒子状の熱可塑性樹脂を
無機微粒子と混合し、次いで溶融混練してペレット状の
樹脂組成物を製造し、ついでこれを成形してフィルムを
得る方法である。
A widely used method for incorporating inorganic fine particles into a film is to mix a particulate thermoplastic resin with the inorganic fine particles, and then melt-knead the mixture to produce a pellet-shaped resin composition. This is a method of molding this to obtain a film.

【0004】例えば、特開昭58−225142号公報
には、ロージン−ラムラーの式で表される粒度分布を有
し、100μ以下の粒子体を1重量%以上及び1200
μ以上の粒子体を1重量%以上それぞれ含まないプロピ
レン重合体に、2酸化珪素と脂肪酸塩との重量比が0.
01〜1の範囲で配合してなり、2酸化珪素の分散性の
向上に効果的であるオレフィン重合体組成物が記載され
ている。
For example, JP-A-58-225142 discloses a particle body having a particle size distribution represented by the Rosin-Rammler formula and having a particle size of 100 .mu.
The weight ratio of silicon dioxide to a fatty acid salt is 0.1% in a propylene polymer that does not contain 1% by weight or more of particles of .mu.
An olefin polymer composition is described which is blended in the range of 01 to 1 and is effective in improving the dispersibility of silicon dioxide.

【0005】特開平8−81591号公報には、平均粒
子径が500〜1300μmで300μm以下の微粒子
の割合が10重量%以下のオレフィン重合体粒子100
重量部に、平均粒子径が1.0〜4.0μm、見掛比重
が0.20〜0.60g/cm3の無機系微粉末0.0
5〜0.60重量部を配合し、溶融混練したことを特徴
とするポリオレフィン組成物が記載されている。
Japanese Unexamined Patent Publication (Kokai) No. 8-81591 discloses an olefin polymer particle 100 having an average particle diameter of 500 to 1300 μm and a proportion of fine particles of 300 μm or less of 10% by weight or less.
In parts by weight, an inorganic fine powder having an average particle diameter of 1.0 to 4.0 μm and an apparent specific gravity of 0.20 to 0.60 g / cm 3 is 0.0
A polyolefin composition is described which comprises 5 to 0.60 parts by weight and is melt-kneaded.

【0006】また、熱可塑性樹脂中の無機微粒子の濃度
が高濃度になるように熱可塑性樹脂に無機微粒子を混合
し、次いで溶融混練を行って、マスターバッチを製造
し、これを別に用意された熱可塑性樹脂に添加すること
も広く行われている。例えば、特開平8−92424号
公報には、平均粒子径が50〜500μで100μ以下
の微粒子の割合が10重量%以上のオレフィン重合体粒
子に無機系微粉末を配合し、溶融混練して得られ、アン
チブロッキング剤の濃度が3.0〜25.0重量%であ
り、アンチブロッキング剤の分散性が良好でフィルムの
外観、透明性、耐ブロッキング性、耐傷付き性の良好な
ポリオレフィンフィルム用マスターバッチが記載されて
いる。
The inorganic fine particles are mixed with the thermoplastic resin so that the concentration of the inorganic fine particles in the thermoplastic resin is high, and then the mixture is melt-kneaded to produce a masterbatch, which is prepared separately. Addition to thermoplastics is also widely practiced. For example, in JP-A-8-92424, an olefin polymer particle having an average particle diameter of 50 to 500 μ and a proportion of fine particles of 100 μ or less of 10 wt% or more is blended with an inorganic fine powder, and melt-kneaded to obtain. The concentration of the antiblocking agent is 3.0 to 25.0% by weight, the dispersibility of the antiblocking agent is good, and the film appearance, transparency, blocking resistance, and scratch resistance are good masters for polyolefin films. Batches are listed.

【0007】しかし、上記特開昭58−225142号
公報または特開平8−81591号公報に記載されてい
るようにオレフィン重合体粒子に二酸化ケイ素(シリ
カ)粉末である無機微粒子を混合した場合、一般的に無
機微粒子は混合中に凝集しやすいので、無機微粒子の凝
集体が生成することがある。特に、上記特開平8−92
424号公報に記載されているように高濃度のマスター
バッチを製造する時には凝集体が生成しやすい。そし
て、凝集体が製品であるフィルムやシートに混入する
と、フィルムやシートの外観を損ない、製品の価値が低
下することがある。
However, as described in JP-A-58-225142 or JP-A-8-81591, when olefin polymer particles are mixed with inorganic fine particles which are silicon dioxide (silica) powders, it is generally Since inorganic fine particles tend to aggregate during mixing, an aggregate of inorganic fine particles may be formed. Particularly, the above-mentioned JP-A-8-92.
As described in Japanese Patent No. 424, when a high-concentration masterbatch is produced, aggregates are likely to be formed. When the aggregates are mixed into the product film or sheet, the appearance of the film or sheet may be impaired and the product value may be reduced.

【0008】凝集体の生成を防ぐ方法としては、従来か
ら熱可塑性樹脂中の微粒子の量を増加させる方法、特定
の添加剤を用いる方法、特定の性状を示す無機微粒子を
用いる方法などが知られている。しかし、熱可塑性樹脂
中の微粒子の量を増加させる方法は飛散などが起こり、
微粒子の取り扱いが困難になり、粉塵爆発の危険性が増
加する。また、特定の添加剤を用いる方法や特定の性状
を示す無機微粒子を用いる方法は適用できる用途が限ら
れている。このような状況において、幅広い用途に適用
できる樹脂組成物の製造方法であって、無機微粒子の濃
度を高くすることができ、無機微粒子が凝集することな
く、その分散性に優れる樹脂組成物の製造方法が望まれ
ていた。
As methods for preventing the formation of aggregates, conventionally known methods include increasing the amount of fine particles in a thermoplastic resin, using a specific additive, and using inorganic fine particles having specific properties. ing. However, the method of increasing the amount of fine particles in the thermoplastic resin causes scattering,
The handling of fine particles becomes difficult and the risk of dust explosion increases. In addition, the use of the method using a specific additive or the method using inorganic fine particles having a specific property is limited. In such a situation, a method for producing a resin composition that can be applied to a wide range of uses, in which the concentration of the inorganic fine particles can be increased, the inorganic fine particles do not aggregate, and a resin composition having excellent dispersibility can be produced. A method was desired.

【0009】[0009]

【発明が解決しようとする課題】本発明の目的は、粉体
としての取り扱いが容易で、無機微粒子の分散性に優れ
る樹脂組成物を提供することにある。
An object of the present invention is to provide a resin composition which is easy to handle as a powder and has excellent dispersibility of inorganic fine particles.

【0010】[0010]

【課題を解決するための手段】本発明者らは、かかる実
情に鑑み、鋭意検討の結果、重量平均粒子径が特定の範
囲であり、粒子径が特定の値以下である粒子の割合が特
定の範囲であり、粒子径が特定の範囲である粒子の割合
が特定の範囲であり、混合割合が一定の範囲である熱可
塑性樹脂と混合割合が一定の範囲である無機微粒子を含
む樹脂組成物と、上記樹脂組成物の製造方法、および混
合量は特定の範囲である上記樹脂組成物と混合量が特定
の範囲である熱可塑性樹脂を混合し、押出成形して得ら
れるフィルムが上記課題を解決できることを見出し、本
発明の完成に至った。
DISCLOSURE OF THE INVENTION In view of such circumstances, the present inventors have made earnest studies and, as a result, have determined that the weight average particle diameter is in a specific range and the proportion of particles having a particle diameter of a specific value or less is specified. , The particle size is in a specific range, the ratio of particles is in a specific range, the mixing ratio is a thermoplastic resin and a mixing ratio is a resin composition containing inorganic fine particles in a certain range. And a method for producing the resin composition, and the mixing amount is a mixture of the resin composition and the thermoplastic resin having a mixing range of a specific range, the film obtained by extrusion molding the above problems The inventors have found that they can be solved and completed the present invention.

【0011】すなわち、本発明は、下記の要件(A)〜
(C)を満足する粒子である熱可塑性樹脂80〜99重
量部と無機微粒子1〜20重量部を含むことを特徴とす
る樹脂組成物、およびその樹脂組成物の製造方法に係る
ものである。 要件(A):重量平均粒子径が500μm以上である。 要件(B):粒子径が200μm以下である粒子が1重
量%以上5重量%未満である。 要件(C):粒子径が500μm以下である粒子が15
重量%以上である。 以下、本発明を詳細に説明する。
That is, the present invention provides the following requirements (A)-
The present invention relates to a resin composition containing 80 to 99 parts by weight of a thermoplastic resin which is particles satisfying (C) and 1 to 20 parts by weight of inorganic fine particles, and a method for producing the resin composition. Requirement (A): The weight average particle diameter is 500 μm or more. Requirement (B): 1% by weight or more and less than 5% by weight of particles having a particle diameter of 200 μm or less. Requirement (C): 15 particles having a particle diameter of 500 μm or less
It is more than weight%. Hereinafter, the present invention will be described in detail.

【0012】[0012]

【発明の実施の形態】本発明で用いられる熱可塑性樹脂
は、エチレン、プロピレン、スチレン、エステル類から
選ばれた少なくとも1種の単量体を重合して得られる重
合体であり、例えば、エチレンを主成分とする単量体を
重合して得られる重合体、プロピレンを主成分とする単
量体を重合して得られる重合体、スチレンを主成分とす
る単量体を重合して得られる重合体、エステル類を主成
分とする単量体を重合して得られる重合体等が挙げら
れ、好ましくはプロピレンを主成分とする単量体を重合
して得られる重合体である。これらの重合体は単独で用
いてもよく、少なくとも2種を併用しても良い。
BEST MODE FOR CARRYING OUT THE INVENTION The thermoplastic resin used in the present invention is a polymer obtained by polymerizing at least one monomer selected from ethylene, propylene, styrene and esters. A polymer obtained by polymerizing a monomer containing propylene as a main component, a polymer obtained by polymerizing a monomer containing propylene as a main component, and a polymer obtained by polymerizing a monomer containing styrene as a main component Examples thereof include a polymer and a polymer obtained by polymerizing a monomer having an ester as a main component, and a polymer obtained by polymerizing a monomer having a propylene as a main component is preferable. These polymers may be used alone or in combination of at least two kinds.

【0013】エチレンを主成分とする単量体を重合して
得られる重合体としては、エチレン単独重合体、エチレ
ン−プロピレン共重合体、エチレンと炭素原子数4〜1
2のα−オレフィンの共重合体等が挙げられる。
Polymers obtained by polymerizing a monomer containing ethylene as a main component include ethylene homopolymers, ethylene-propylene copolymers, ethylene and 4 to 1 carbon atoms.
Examples thereof include a copolymer of 2 α-olefins.

【0014】エチレン−プロピレン共重合体のプロピレ
ン含量は、エチレン−プロピレン共重合体の全重量に対
して0.1重量%〜10重量%のものが挙げられる。
The propylene content of the ethylene-propylene copolymer may be 0.1 to 10% by weight based on the total weight of the ethylene-propylene copolymer.

【0015】炭素原子数4〜12のα−オレフィンとし
ては、例えば、ブテン−1、ヘキセン−1、オクテン−
1等が挙げられ、α−オレフィン含量は、エチレンと炭
素原子数4〜12のα−オレフィンの共重合体の全重量
に対して0.1重量%〜50重量%のものが挙げられ
る。エチレンと炭素原子数4〜12のα−オレフィンの
共重合体としては、例えば、エチレン−ブテン−1共重
合体、エチレン−ヘキセン−1共重合体、エチレン−オ
クテン−1共重合体等が挙げられる。
Examples of the α-olefin having 4 to 12 carbon atoms include butene-1, hexene-1, octene-
1 and the like, and the α-olefin content is 0.1 to 50% by weight based on the total weight of the copolymer of ethylene and the α-olefin having 4 to 12 carbon atoms. Examples of the copolymer of ethylene and an α-olefin having 4 to 12 carbon atoms include ethylene-butene-1 copolymer, ethylene-hexene-1 copolymer, ethylene-octene-1 copolymer and the like. To be

【0016】エチレンを主成分とする単量体を重合して
得られる重合体として好ましくは、エチレン単独重合
体、エチレン−プロピレン共重合体、エチレン−ブテン
−1共重合体、エチレン−ヘキセン−1共重合体であ
る。
The polymer obtained by polymerizing a monomer containing ethylene as a main component is preferably ethylene homopolymer, ethylene-propylene copolymer, ethylene-butene-1 copolymer, ethylene-hexene-1. It is a copolymer.

【0017】エチレンを主成分とする単量体を重合して
得られる重合体の製造方法は、特に制限されるものでは
なく、公知の重合触媒を用いる公知の重合方法が挙げら
れる。公知の重合触媒としては、例えば、チーグラー触
媒、メタロセン触媒等が挙げられ、公知の重合方法とし
ては、例えば、高圧重合法、溶液重合法、スラリー重合
法、気相重合法等が挙げられ、これらの重合方法は回分
式であっても良く、連続式であっても良い。
The method for producing a polymer obtained by polymerizing a monomer containing ethylene as a main component is not particularly limited, and a known polymerization method using a known polymerization catalyst can be mentioned. Known polymerization catalysts include, for example, Ziegler catalysts, metallocene catalysts and the like, and known polymerization methods include, for example, high pressure polymerization method, solution polymerization method, slurry polymerization method, gas phase polymerization method, etc. The polymerization method may be batchwise or continuous.

【0018】プロピレンを主成分とする単量体を重合し
て得られる重合体としては、プロピレン単独重合体、プ
ロピレン−エチレン共重合体、プロピレンと炭素原子数
4〜12のα−オレフィンの共重合体、プロピレンとエ
チレンと炭素原子数4〜12のα−オレフィンの三元共
重合体等が挙げられる。
Examples of the polymer obtained by polymerizing a monomer containing propylene as a main component include a propylene homopolymer, a propylene-ethylene copolymer, and a copolymer of propylene and an α-olefin having 4 to 12 carbon atoms. Examples thereof include a ternary copolymer of propylene, ethylene, and an α-olefin having 4 to 12 carbon atoms.

【0019】プロピレン−エチレン共重合体におけるエ
チレン含量は、プロピレン−エチレン共重合体の全重量
に対して0.1重量%〜10重量%のものを用いること
ができる。
The ethylene content in the propylene-ethylene copolymer may be 0.1 to 10% by weight based on the total weight of the propylene-ethylene copolymer.

【0020】プロピレンと炭素原子数4〜12のα−オ
レフィンの共重合体において、炭素原子数4〜12のα
−オレフィンとしては、前記のエチレンを主成分とする
単量体を重合して得られる重合体において用いられる炭
素原子数4〜12のα−オレフィンが挙げられ、α−オ
レフィン含量は、プロピレンと炭素原子数4〜12のα
−オレフィンの共重合体の全重量に対して0.1重量%
〜30重量%が挙げられる。プロピレンと炭素原子数4
〜12のα−オレフィンの共重合体としては、例えば、
プロピレン−ブテン−1共重合体、プロピレン−ヘキセ
ン−1共重合体等が挙げられる。
In the copolymer of propylene and α-olefin having 4 to 12 carbon atoms, α having 4 to 12 carbon atoms
Examples of the olefin include α-olefin having 4 to 12 carbon atoms used in the polymer obtained by polymerizing the above-mentioned monomer containing ethylene as a main component, and the α-olefin content is propylene and carbon. Α with 4 to 12 atoms
0.1% by weight, based on the total weight of the olefin copolymer
˜30% by weight. Propylene and 4 carbon atoms
Examples of the α-olefin copolymer of
Examples thereof include a propylene-butene-1 copolymer and a propylene-hexene-1 copolymer.

【0021】プロピレンとエチレンと炭素原子数4〜1
2のα−オレフィンの三元共重合体において、エチレン
含量は、三元共重合体の全重量に対して0.1重量%〜
10重量%のものを用いることができる。炭素原子数4
〜12のα−オレフィンとしては、前記のエチレンを主
成分とする単量体を重合して得られる重合体において用
いられる炭素原子数4〜12のα−オレフィンが挙げら
れ、α−オレフィン含量は、三元共重合体の全重量に対
して0.1重量%〜30重量%が挙げられる。プロピレ
ンとエチレンと炭素原子数4〜12のα−オレフィンの
三元共重合体としては、例えば、プロピレン−エチレン
−ブテン−1共重合体、プロピレン−エチレン−ヘキセ
ン−1共重合体等が挙げられる。
Propylene, ethylene and 4 to 1 carbon atoms
The ethylene content of the α-olefin terpolymer of 2 is 0.1% by weight to the total weight of the terpolymer.
10% by weight can be used. 4 carbon atoms
Examples of the α-olefin having 12 to 12 include α-olefins having 4 to 12 carbon atoms which are used in a polymer obtained by polymerizing the above-mentioned monomer containing ethylene as a main component, and the α-olefin content is , 0.1 to 30% by weight based on the total weight of the terpolymer. Examples of the terpolymer of propylene, ethylene and α-olefin having 4 to 12 carbon atoms include propylene-ethylene-butene-1 copolymer and propylene-ethylene-hexene-1 copolymer. .

【0022】プロピレンを主成分とする単量体を重合し
て得られる重合体として好ましくは、プロピレン単独重
合体、プロピレン−エチレン共重合体、プロピレン−ブ
テン−1共重合体、プロピレン−エチレン−ブテン−1
共重合体である。
The polymer obtained by polymerizing a monomer containing propylene as a main component is preferably propylene homopolymer, propylene-ethylene copolymer, propylene-butene-1 copolymer, propylene-ethylene-butene. -1
It is a copolymer.

【0023】プロピレンを主成分とする単量体を重合し
て得られる重合体の製造方法は、特に制限されるもので
はなく、公知の重合触媒を用いる公知の重合方法が挙げ
られる。公知の重合触媒としては、例えば、チーグラー
触媒、メタロセン触媒等が挙げられ、公知の重合方法と
しては、例えば、溶液重合法、スラリー重合法、気相重
合法等が挙げられ、これらの重合方法は回分式であって
も良く、連続式であっても良い。
The method for producing a polymer obtained by polymerizing a monomer containing propylene as a main component is not particularly limited, and a known polymerization method using a known polymerization catalyst can be mentioned. Known polymerization catalysts include, for example, Ziegler catalysts, metallocene catalysts, etc., and known polymerization methods include, for example, solution polymerization method, slurry polymerization method, gas phase polymerization method, and the like. It may be a batch system or a continuous system.

【0024】本発明で用いられる熱可塑性樹脂は粒子で
あり、その重量平均粒子径は500μm以上であり、好
ましくは500〜1000μmである。粒子である熱可
塑性樹脂の重量平均粒子径が500μm未満の場合、粉
塵爆発の危険が発生するなど、粉体としての取り扱いが
困難となることがある。なお、熱可塑性樹脂の粒子径
は、レーザー回折式粒度分布測定装置などを用いて測定
することができる。
The thermoplastic resin used in the present invention is particles, and the weight average particle diameter thereof is 500 μm or more, preferably 500 to 1000 μm. When the weight average particle diameter of the thermoplastic resin particles is less than 500 μm, it may be difficult to handle as a powder, such as a danger of dust explosion. The particle size of the thermoplastic resin can be measured using a laser diffraction type particle size distribution measuring device or the like.

【0025】本発明で用いられる粒子である熱可塑性樹
脂において、粒子径が200μm以下である粒子は、熱
可塑性樹脂の全重量に対して、1重量%以上5重量%未
満である。粒子径が200μm以下である粒子が1重量
%未満の場合、無機微粒子の分散が不充分なことがあ
り、5重量%以上の場合、粉塵爆発の危険が発生するな
ど、粉体としての取り扱いが困難となることがある。
In the thermoplastic resin used in the present invention, the amount of particles having a particle diameter of 200 μm or less is 1% by weight or more and less than 5% by weight based on the total weight of the thermoplastic resin. If the amount of particles having a particle size of 200 μm or less is less than 1% by weight, the dispersion of the inorganic fine particles may be insufficient. If the amount of particles is 5% by weight or more, there is a danger of dust explosion. It can be difficult.

【0026】本発明で用いられる粒子である熱可塑性樹
脂において、粒子径が500μm以下である粒子は、熱
可塑性樹脂の全重量に対して、15重量%以上であり、
好ましくは15〜40重量%である。ここでいう粒子径
が500μm以下である粒子は、前述した粒子径が20
0μm以下である粒子も含んでいる。粒子径が500μ
m以下である粒子が15重量%未満の場合、無機微粒子
の分散が不充分なことがある。
In the thermoplastic resin which is a particle used in the present invention, the amount of particles having a particle diameter of 500 μm or less is 15% by weight or more based on the total weight of the thermoplastic resin,
It is preferably 15 to 40% by weight. Particles having a particle diameter of 500 μm or less as referred to herein have a particle diameter of 20 described above.
It also includes particles having a size of 0 μm or less. Particle size is 500μ
When the amount of particles of m or less is less than 15% by weight, the inorganic fine particles may be insufficiently dispersed.

【0027】本発明で用いられる無機微粒子は、特に限
定されるものではないが、平均粒子径が1〜10μmで
あり、見掛け比重が0.1〜1g/ccであるものがフ
ィルムの外観や耐ブロッキング性、耐傷つき性の面から
好ましく用いられる。
The inorganic fine particles used in the present invention are not particularly limited, but those having an average particle diameter of 1 to 10 μm and an apparent specific gravity of 0.1 to 1 g / cc have the appearance and resistance of the film. It is preferably used in terms of blocking property and scratch resistance.

【0028】本発明で用いられる無機微粒子として、具
体的には、二酸化ケイ素、アルミノシリケート、タルク
等のケイ酸マグネシウム、カオリン等のケイ酸アルミニ
ウム、ホウ酸アルミニウム、炭酸カルシウム等が挙げら
れる。この中でも、特に二酸化ケイ素については本発明
の効果が大きいので好ましく用いられる。
Specific examples of the inorganic fine particles used in the present invention include magnesium silicates such as silicon dioxide, aluminosilicate and talc, aluminum silicates such as kaolin, aluminum borate, calcium carbonate and the like. Among these, silicon dioxide is particularly preferably used because the effect of the present invention is great.

【0029】本発明で用いられる粒子である熱可塑性樹
脂と無機微粒子の混合量は、粒子である熱可塑性樹脂の
混合量が80〜99重量部であり、無機微粒子の混合量
が1〜20重量部である。好ましくは、粒子である熱可
塑性樹脂の混合量が90〜98重量部であり、無機微粒
子の混合量が2〜10重量部である。
Regarding the mixing amount of the thermoplastic resin which is the particles and the inorganic fine particles used in the present invention, the mixing amount of the thermoplastic resin which is the particles is 80 to 99 parts by weight, and the mixing amount of the inorganic fine particles is 1 to 20 parts by weight. It is a department. Preferably, the mixing amount of the thermoplastic resin as particles is 90 to 98 parts by weight, and the mixing amount of the inorganic fine particles is 2 to 10 parts by weight.

【0030】粒子である熱可塑性樹脂の混合量が80重
量部未満の場合(即ち、無機微粒子の混合量が20重量
部を超えた場合)、無機微粒子の分散性が不充分なこと
がある。また、粒子である熱可塑性樹脂の混合量が99
重量部を超えた場合(即ち、無機微粒子の混合量が1重
量部未満の場合)、フィルムなどの製品に用いる場合に
大量に添加しなければ耐ブロッキング性が改良されず、
製品としての価値が低いものとなることがある。
When the mixing amount of the thermoplastic resin particles is less than 80 parts by weight (that is, when the mixing amount of the inorganic fine particles exceeds 20 parts by weight), the dispersibility of the inorganic fine particles may be insufficient. In addition, the mixing amount of the thermoplastic resin particles is 99
If the amount exceeds 100 parts by weight (that is, the amount of the inorganic fine particles is less than 1 part by weight), the blocking resistance is not improved unless added in a large amount when used in products such as films,
The value as a product may be low.

【0031】本発明で用いられる混合方法は、特に制限
されるものではなく、公知の混合方法が挙げられ、公知
の混合装置を用いる方法である。混合に用いられる装置
としては、例えば、タンブラーミキサー、スーパーミキ
サー、ヘンシェルミキサー、スクリューブレンダー、リ
ボンブレンダー等が挙げられる。
The mixing method used in the present invention is not particularly limited and may be a known mixing method, which is a method using a known mixing device. Examples of the apparatus used for mixing include a tumbler mixer, a super mixer, a Henschel mixer, a screw blender and a ribbon blender.

【0032】本発明の樹脂組成物は、必要な場合には金
属石けん、塩素補足剤、酸化防止剤、紫外線吸収剤、光
安定剤、帯電防止剤、滑剤、難燃剤、核剤、顔料などの
添加剤を本発明の効果を維持できる程度において加えて
もよい。
The resin composition of the present invention contains, if necessary, metallic soap, chlorine scavenger, antioxidant, ultraviolet absorber, light stabilizer, antistatic agent, lubricant, flame retardant, nucleating agent, pigment and the like. Additives may be added to the extent that the effects of the present invention can be maintained.

【0033】本発明の樹脂組成物の製造方法は、特に制
限されるものではないが、好ましくは熱可塑性樹脂と無
機微粒子を混合した後に、溶融混練する方法である。溶
融混練方法としては、溶融混練方法に関しては熱可塑性
樹脂の融点以上の温度で溶融混練する方法であれば特に
限定されない。溶融混練に用いられる装置としては、特
に制限されるものではなく、公知の溶融混練の装置が挙
げられ、例えば、一軸の溶融押出機、二軸以上の多軸の
溶融押出機、バンバリーミキサー等が挙げられ、好まし
くは二軸以上の多軸押出機である。
The method for producing the resin composition of the present invention is not particularly limited, but is preferably a method in which a thermoplastic resin and inorganic fine particles are mixed and then melt-kneaded. The melt-kneading method is not particularly limited as long as it is a method of melt-kneading at a temperature equal to or higher than the melting point of the thermoplastic resin. The device used for melt kneading is not particularly limited, and examples thereof include known melt kneading devices, and examples thereof include a uniaxial melt extruder, a biaxial or more multiaxial melt extruder, and a Banbury mixer. Among them, a multi-screw extruder having two or more screws is preferable.

【0034】本発明の組成物は、押出成形、射出成形、
発泡成形、中空成形など幅広い用途に好適に用いること
ができる。中でも押出成形には好適に用いられる。
The composition of the present invention can be prepared by extrusion molding, injection molding,
It can be suitably used for a wide range of applications such as foam molding and blow molding. Above all, it is preferably used for extrusion molding.

【0035】本発明の樹脂組成物とその他の熱可塑性樹
脂の混合物も押出成形、射出成形、発泡成形、中空成形
など幅広い用途に好適に用いることができる。特に押出
成形には好適に用いられ、無機微粒子の分散が良好なフ
ィルムが得られる。
Mixtures of the resin composition of the present invention and other thermoplastic resins can also be suitably used in a wide variety of applications such as extrusion molding, injection molding, foam molding and blow molding. Particularly, it is suitably used for extrusion molding, and a film in which inorganic fine particles are well dispersed can be obtained.

【0036】[0036]

【実施例】以下、実施例および比較例により本発明を説
明するが、本発明はこれら実施例に限定されるものでは
ない。
The present invention will be described below with reference to examples and comparative examples, but the present invention is not limited to these examples.

【0037】(1)MFR:JIS K7210に従
い、温度230℃、荷重2.16kgfで測定した。 (2)エチレン含量:高分子ハンドブック(1995
年、紀伊国屋書店発行)の第616頁に記載されている
方法により、赤外分光法で測定を行い求めた。 (3)粒子径および重量平均粒子径:SYMPATEC
社製流下式レーザー回折式粒度分布測定装置(HELO
S & GRADIS)を用い、重量粒度分布の積分曲
線を用いて求めた。 (4)フィルム外観:フィルムを5枚重ねたものについ
て200cm2あたり、目視により確認できるフィッシ
ュアイの個数を計測し、40個以上のものを「不良」、
40個以下の物を「良好」とした。
(1) MFR: Measured according to JIS K7210 at a temperature of 230 ° C. and a load of 2.16 kgf. (2) Ethylene content: Polymer Handbook (1995
, Published by Kinokuniya Publishing Co., Ltd.), page 616, and measured by infrared spectroscopy. (3) Particle size and weight average particle size: SYMPATEC
Flow-through type laser diffraction particle size analyzer (HELO)
S & GRADIS) and an integral curve of the weight particle size distribution. (4) Appearance of film: The number of visually recognizable fish eyes per 200 cm 2 of five stacked films was measured, and 40 or more were “defective”,
The thing of 40 or less was made into "good."

【0038】(実施例)熱可塑性樹脂としてMFRが8
g/10分、重量平均粒子径が770μm、粒子径が2
00μm以下である粒子の重量割合が1.3重量%、粒
子径が500μm以下である粒子の重量割合が16.0
重量%であるプロピレン−エチレン共重合体(エチレン
含有量=4重量%)を、無機微粒子としてサイリシア3
50(富士シリシア化学製、レーザー法による平均粒子
径3.9μm、見かけ比重0.15g/cc)を用い
た。熱可塑性樹脂98重量部を20Lヘンシェルミキサ
ー(川田製作所製)内で80℃まで予熱し、無機微粒子
2重量部と酸化防止剤イルガノックス1010(チバ・
スペシャリティ・ケミカル社製)0.05重量部、イル
ガフォス168(チバ・スペシャリティ・ケミカル社
製)0.10重量部を加え、535rpm、80℃で1
分間混合した。この混合物をΦ30mm二軸混練機(T
EX30:日鋼製作所製)で230℃で混練した。製造
時の粉体の取り扱い性は良好であった。上記で混練して
得られた樹脂組成物5重量部に、無機微粒子を含まない
プロピレン−エチレン−ブテン−1共重合体(MFR=
7g/10分)95重量部を加え、250℃でTダイを
用いて厚さ30μmのフィルムを製膜した。得られたフ
ィルムの外観は良好であった。
(Example) A thermoplastic resin having an MFR of 8
g / 10 minutes, weight average particle size is 770 μm, particle size is 2
The weight ratio of particles having a diameter of 00 μm or less is 1.3% by weight, and the weight ratio of particles having a particle diameter of 500 μm or less is 16.0.
The propylene-ethylene copolymer (ethylene content = 4% by weight) which is the weight% is used as inorganic fine particles in Sylysia 3
50 (manufactured by Fuji Silysia Chemical Ltd., average particle size by laser method 3.9 μm, apparent specific gravity 0.15 g / cc) was used. 98 parts by weight of the thermoplastic resin is preheated to 80 ° C. in a 20 L Henschel mixer (manufactured by Kawada Seisakusho), and 2 parts by weight of inorganic fine particles and the antioxidant Irganox 1010 (Ciba.
0.05 parts by weight of Specialty Chemicals Co., Ltd. and 0.10 parts by weight of Irgafos 168 (made by Ciba Specialty Chemicals Co., Ltd.) were added, and 1 at 535 rpm and 80 ° C.
Mix for minutes. Φ30mm biaxial kneader (T
EX30: manufactured by Nikko Seisakusho) was kneaded at 230 ° C. The handleability of the powder during manufacture was good. Into 5 parts by weight of the resin composition obtained by kneading as described above, a propylene-ethylene-butene-1 copolymer containing no inorganic fine particles (MFR =
(7 g / 10 min) 95 parts by weight was added, and a film having a thickness of 30 μm was formed at 250 ° C. using a T die. The appearance of the obtained film was good.

【0039】(比較例1)実施例において、熱可塑性樹
脂をMFRが8g/10分、重量平均粒子径が1320
μm、粒子径が200μm以下である粒子の重量割合が
0.2重量%、粒子径が500μm以下である粒子の重
量割合が1.4重量%であるプロピレン−エチレン共重
合体(エチレン含有量=4重量%)に変更した以外は実
施例と同様に行った。製造時の粉体の取り扱い性は良好
であったが、得られたフィルムの外観は無機微粒子の凝
集物が多く、不良であった。
(Comparative Example 1) In the example, the thermoplastic resin has an MFR of 8 g / 10 minutes and a weight average particle diameter of 1320.
A propylene-ethylene copolymer in which the weight ratio of particles having a particle diameter of 200 μm or less is 0.2% by weight, and the weight ratio of particles having a particle diameter of 500 μm or less is 1.4% by weight (ethylene content = 4% by weight) was changed to the same as the example. The handleability of the powder at the time of production was good, but the appearance of the obtained film was poor because there were many aggregates of inorganic fine particles.

【0040】(比較例2)実施例において、熱可塑性樹
脂をMFRが8g/10分、重量平均粒子径600μ
m、粒子径が200μm以下である粒子の重量割合が
0.8重量%、粒子径が500μm以下である粒子の重
量割合が26.6重量%であるプロピレン−エチレン共
重合体(エチレン含有量=4重量%)に変更した以外は
実施例と同様に行った。製造時の粉体の取り扱い性は良
好であったが、得られたフィルムの外観は無機微粒子の
凝集物が多く、不良であった。
(Comparative Example 2) In the example, the thermoplastic resin was used, the MFR was 8 g / 10 min, and the weight average particle diameter was 600 μ.
m, the weight ratio of particles having a particle diameter of 200 μm or less is 0.8% by weight, and the weight ratio of particles having a particle diameter of 500 μm or less is 26.6% by weight (ethylene content = ethylene content). 4% by weight) was changed to the same as the example. The handleability of the powder at the time of production was good, but the appearance of the obtained film was poor because there were many aggregates of inorganic fine particles.

【0041】(比較例3)実施例において、熱可塑性樹
脂をMFRが8g/10分、重量平均粒子径が410μ
m、粒子径が200μm以下である粒子の重量割合が
7.1重量%、粒子径が500μm以下である粒子の重
量割合が58.4重量%のプロピレン−エチレン共重合
体(エチレン含有量=4重量%)に変更した以外は実施
例と同様に行った。得られたフィルムの外観は良好であ
ったが、製造時の粉体の取り扱いが困難であった。
(Comparative Example 3) In the example, the thermoplastic resin was used in which the MFR was 8 g / 10 minutes and the weight average particle size was 410 μm.
m, the weight ratio of particles having a particle diameter of 200 μm or less is 7.1% by weight, and the weight ratio of particles having a particle diameter of 500 μm or less is 58.4% by weight (ethylene content = 4. The same procedure as in Example was performed except that the content was changed to (wt%). Although the appearance of the obtained film was good, it was difficult to handle the powder during production.

【0042】[0042]

【表1】 [Table 1]

【0043】実施例の樹脂組成物が製造時の粉体の取り
扱い性と、その樹脂組成物を用いて得られるフィルムの
外観の両方に優れているのに対して、比較例1および2
の樹脂組成物を用いて得られたフィルムの外観は不充分
であり、比較例3の樹脂組成物は製造時の粉体の取り扱
いが困難であることがわかる。
The resin compositions of Examples are excellent in both handling of powder during production and appearance of films obtained by using the resin compositions, whereas Comparative Examples 1 and 2
The appearance of the film obtained by using the resin composition of No. 1 is insufficient, and it can be seen that the resin composition of Comparative Example 3 is difficult to handle the powder at the time of production.

【0044】[0044]

【発明の効果】以上、詳述したとおり、本発明により、
粉体としての取り扱いが容易で、無機微粒子の分散性に
優れる樹脂組成物を得ることができる。
As described above in detail, according to the present invention,
A resin composition which is easy to handle as a powder and has excellent dispersibility of inorganic fine particles can be obtained.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 4F070 AA15 AA16 AA71 AB09 AC23 AD04 FA01 FA03 FB07 FC02 4J002 AA011 BB021 BB031 BB051 BB111 BB121 BB141 BB151 BC021 DE236 DJ016 DJ036 DJ046 DK006 FA081 GG02   ─────────────────────────────────────────────────── ─── Continued front page    F-term (reference) 4F070 AA15 AA16 AA71 AB09 AC23                       AD04 FA01 FA03 FB07 FC02                 4J002 AA011 BB021 BB031 BB051                       BB111 BB121 BB141 BB151                       BC021 DE236 DJ016 DJ036                       DJ046 DK006 FA081 GG02

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】下記の要件(A)〜(C)を満足する粒子
である熱可塑性樹脂80〜99重量部と無機微粒子1〜
20重量部を含むことを特徴とする樹脂組成物。 要件(A):重量平均粒子径が500μm以上である。 要件(B):粒子径が200μm以下である粒子が1重
量%以上5重量%未満である。 要件(C):粒子径が500μm以下である粒子が15
重量%以上である。
1. A thermoplastic resin which is particles satisfying the following requirements (A) to (C): 80 to 99 parts by weight and inorganic fine particles:
A resin composition comprising 20 parts by weight. Requirement (A): The weight average particle diameter is 500 μm or more. Requirement (B): 1% by weight or more and less than 5% by weight of particles having a particle diameter of 200 μm or less. Requirement (C): 15 particles having a particle diameter of 500 μm or less
It is more than weight%.
【請求項2】無機微粒子が二酸化ケイ素であることを特
徴とする請求項1記載の樹脂組成物。
2. The resin composition according to claim 1, wherein the inorganic fine particles are silicon dioxide.
【請求項3】熱可塑性樹脂がプロピレンを主成分とする
単量体を重合して得られる重合体であることを特徴とす
る請求項1記載の樹脂組成物。
3. The resin composition according to claim 1, wherein the thermoplastic resin is a polymer obtained by polymerizing a monomer containing propylene as a main component.
【請求項4】熱可塑性樹脂と無機微粒子を混合した後、
溶融混練することを特徴とする請求項1〜3のいずれか
に記載の樹脂組成物の製造方法。
4. After mixing the thermoplastic resin and the inorganic fine particles,
Melt kneading, The manufacturing method of the resin composition in any one of Claims 1-3 characterized by the above-mentioned.
JP2001373923A 2001-12-07 2001-12-07 Resin composition containing inorganic fine particles and method for producing the same Expired - Fee Related JP4048765B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001373923A JP4048765B2 (en) 2001-12-07 2001-12-07 Resin composition containing inorganic fine particles and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001373923A JP4048765B2 (en) 2001-12-07 2001-12-07 Resin composition containing inorganic fine particles and method for producing the same

Publications (2)

Publication Number Publication Date
JP2003171565A true JP2003171565A (en) 2003-06-20
JP4048765B2 JP4048765B2 (en) 2008-02-20

Family

ID=19182561

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001373923A Expired - Fee Related JP4048765B2 (en) 2001-12-07 2001-12-07 Resin composition containing inorganic fine particles and method for producing the same

Country Status (1)

Country Link
JP (1) JP4048765B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006117816A (en) * 2004-10-22 2006-05-11 Mitsui Chemicals Inc Thermoplastic resin composition and porous film and laminate produced by using the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006117816A (en) * 2004-10-22 2006-05-11 Mitsui Chemicals Inc Thermoplastic resin composition and porous film and laminate produced by using the same

Also Published As

Publication number Publication date
JP4048765B2 (en) 2008-02-20

Similar Documents

Publication Publication Date Title
EP0796884B1 (en) Masterbatch formulation for polyolefin applications
JP3396303B2 (en) Masterbatch for polyolefin film and composition for polyolefin film
JPH01149845A (en) Filler reinforced resin composition
JP2008208210A (en) Polypropylene film
JP3678338B2 (en) Propylene resin composition
JP3320031B2 (en) High concentration talc masterbatch
JPH08225655A (en) Antiblocking agent masterbatch and stretched polyolefinic resin film made by using the same
JPS621622B2 (en)
JP3879500B2 (en) Method for producing resin composition containing inorganic fine particles
JPS61281143A (en) Resin composition for extrusion molding
JP4048765B2 (en) Resin composition containing inorganic fine particles and method for producing the same
JPH10265215A (en) Talc and propylene polymer composition containing the same
JP3386878B2 (en) Polypropylene resin composition for mat-like unstretched film
JP4661155B2 (en) Resin composition containing inorganic fine particles
JP4379969B2 (en) Polyethylene composition and film thereof
JP2996771B2 (en) Polypropylene composition
JPH08208908A (en) Polypropylene resin composition
JP2001072812A (en) Polypropylene resin composition and film comprising the same
JPH11181185A (en) Polypropylene resin composition
JP3005323B2 (en) Polypropylene composition
JPS5869238A (en) Filled composite polypropylene resin particle
JPH07228733A (en) Polypropylene composition and stretched film obtained therefrom
WO2005007736A1 (en) Low glow olefin
JP2567248B2 (en) Resin composition for film molding
JP3035010B2 (en) Talc-containing propylene polymer composition

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20041126

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20070131

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070213

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20070412

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20070412

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20071106

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20071119

R151 Written notification of patent or utility model registration

Ref document number: 4048765

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101207

Year of fee payment: 3

RD05 Notification of revocation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: R3D05

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101207

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20101207

Year of fee payment: 3

RD05 Notification of revocation of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: R3D05

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111207

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20111207

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121207

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121207

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20131207

Year of fee payment: 6

LAPS Cancellation because of no payment of annual fees