JPS60219027A - Mat molding of vinylidene fluoride resin and manufacture thereof - Google Patents

Mat molding of vinylidene fluoride resin and manufacture thereof

Info

Publication number
JPS60219027A
JPS60219027A JP59074876A JP7487684A JPS60219027A JP S60219027 A JPS60219027 A JP S60219027A JP 59074876 A JP59074876 A JP 59074876A JP 7487684 A JP7487684 A JP 7487684A JP S60219027 A JPS60219027 A JP S60219027A
Authority
JP
Japan
Prior art keywords
resin
vinylidene fluoride
molded product
mat
molding
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
JP59074876A
Other languages
Japanese (ja)
Other versions
JPH0458497B2 (en
Inventor
Takeshi Nakahira
中平 武志
Masamichi Akatsu
正道 赤津
Hiroyuki Endo
弘之 遠藤
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.)
Kureha Corp
Original Assignee
Kureha Corp
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 Kureha Corp filed Critical Kureha Corp
Priority to JP59074876A priority Critical patent/JPS60219027A/en
Publication of JPS60219027A publication Critical patent/JPS60219027A/en
Publication of JPH0458497B2 publication Critical patent/JPH0458497B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/022Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the choice of material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C48/00Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
    • B29C48/03Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor characterised by the shape of the extruded material at extrusion
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2027/00Use of polyvinylhalogenides or derivatives thereof as moulding material
    • B29K2027/12Use of polyvinylhalogenides or derivatives thereof as moulding material containing fluorine

Abstract

PURPOSE:To provide the titled mat molding which enables mat to be manufactured uniformly without any adverse effect on secondary workability by molding a mixture of powder and granular resin of ethylene tetrafluoride based on resin of vinylidene fluoride at special temperature. CONSTITUTION:Resin of vinylidene fluoride such as homopolymer of vinylidene fluoride A and resin of ethylene tetrafluoride such as homopolymer of ethylene tetrafluoride B are mixed by a mixer and the mixture is extruded by an extruder into pellets. Next, it is molded at more than melting point temperature of the component A. As a result, a mat intended for having a sea/island-type construction of a sea substrate as component A and island particles as component B with an average particle diameter of 0.1-10mum is obtained. A mat having particles oriented in a special flowing direction is preferred.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は弗化ビニリデン系樹脂マット成形物及びその製
造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a vinylidene fluoride resin mat molded product and a method for producing the same.

〔従来の技術〕[Conventional technology]

樹脂成形物を艶消しすることは成形物より反射される光
を散乱させ、人間の眼に安らぎを与え、成形物の高級品
化をかもしだす効果をもたらす。
Matting a resin molded product scatters the light reflected from the molded product, gives comfort to the human eye, and has the effect of making the molded product a high-class product.

この様な艶消し加工、即ちマット加工としては従来、た
とえばエンボスされたゴムロールを通過させて成形物を
エンボスする方法、砂を常温の成形物に吹きつけて、成
形物の表面をエンボスする方法(サンドシラスト法)、
酸化チタン、二酸化珪素等の無機物を成形物に添加する
ことにより艶消しする方法等が知られている。
Conventional methods for such matte finishing, i.e., matte finishing, include a method in which the molded product is embossed by passing it through an embossed rubber roll, a method in which sand is blown onto the molded product at room temperature, and the surface of the molded product is embossed ( sandshirast method),
A method of matting a molded article by adding an inorganic substance such as titanium oxide or silicon dioxide to the molded article is known.

しかしながらこれらの方法はそれぞれ次の様な問題を有
する。即ちエンボスによる方法は成形物がフィルムであ
るとき、フィルムの厚さが不均一であると、ゴムロール
に接する部位と接しない部位が生じ、艶消しされる部位
とされない部位が生じてしまう。弗化ビニリデン系樹脂
は結晶性樹脂であり、しかもその結晶化度も約45俤程
度であるため、本質的に均一な厚さが得られにくい樹脂
であり、エンボス法では艶消しに斑を生じやすい。
However, each of these methods has the following problems. That is, in the embossing method, when the molded product is a film, if the thickness of the film is uneven, some parts will come into contact with the rubber roll and some parts will not, resulting in some parts being matted and some not. Vinylidene fluoride resin is a crystalline resin, and its crystallinity is about 45 degrees, so it is essentially difficult to obtain a uniform thickness, and the embossing method causes unevenness on the matte surface. Cheap.

またこの方法では一旦マット加工されたフィルムを他の
樹脂面に被覆して使用する場合、接着力を持たせる上で
加熱融着させる。が、これは接着剤を用いる方法は乾燥
工程を必要とし、工業上採用しにくいためである。しか
しながらこの様な二次加工を行なう過程でマット加工さ
れたフィルムのマットが消失するか、または斑を助長さ
せることとなるという欠点も有する。
In addition, in this method, when the matted film is used by covering another resin surface, it is heated and fused to provide adhesive strength. However, this is because the method using adhesive requires a drying process and is difficult to adopt industrially. However, it also has the disadvantage that during such secondary processing, the matte of the matted film may disappear or unevenness may be promoted.

別のマット加工法であるサントノラスト法は成形物の表
面に傷をつけることであり、外観上他のマット加工法に
較べて劣ったマット成形物を与える。
Another matte processing method, the Santonoraste method, involves scratching the surface of the molded product, resulting in a matte molded product that is inferior in appearance to other matte processing methods.

更に別のマット加工法である無機物を成形物に添加する
方法は、酸化チタンを始め吸水性の無機物を用いるとき
には、添加する無機物の脱気を十分に行わないと成形物
の表面が泡だらけとなる。
Another matte processing method, which involves adding inorganic substances to molded products, is that when water-absorbing inorganic materials such as titanium oxide are used, the surface of the molded product will be full of bubbles unless the added inorganic material is sufficiently degassed. Become.

また分散性の悪い無機物であると、分散が困難であり不
均一なマット加工となる欠点を有する。
In addition, inorganic substances with poor dispersibility have the disadvantage of being difficult to disperse and resulting in non-uniform matte finish.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

この発明はこの様な従来技術の現状に鑑み、弗化ビニリ
デン系樹脂をマット加工するに二次加工性に支障なく、
均一なマット加工を可能にするマット成形物及びその製
造方法を提供することにある。
In view of the current state of the prior art, the present invention has been developed to matt-process vinylidene fluoride resin without any problems in secondary processability.
An object of the present invention is to provide a mat molded product that enables uniform mat processing and a method for manufacturing the same.

〔発明の構成〕[Structure of the invention]

この発明は溶融成形された弗化ビニリデン系樹脂を海基
質とし、四弗化エチレン系樹脂を島粒子とする海鳥型構
造であり、島の平均粒子径が0.1〜10μmであると
きに目的とするマット成形物の得られることを知見した
ことに基づいている。
This invention has a seabird-shaped structure in which a melt-molded vinylidene fluoride resin is used as a sea substrate and a tetrafluoroethylene resin is used as island particles, and the purpose is when the average particle diameter of the islands is 0.1 to 10 μm. This is based on the knowledge that a matte molded product with the following properties can be obtained.

またこの様な成形物が、弗化ビニリデン系樹脂を主とし
、四弗化エチレン系樹脂粉粒体を従とする混合物を、弗
化ビニリデン系樹脂の融点以上の温度で成形することに
より得られることにも基づいている。
Moreover, such a molded product can be obtained by molding a mixture containing mainly vinylidene fluoride resin and powdered tetrafluoroethylene resin at a temperature higher than the melting point of the vinylidene fluoride resin. It is also based on that.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

本発明に云う弗化ビニリデン系樹脂とは弗化ビニリデン
ホモポリマーは勿論、ンツ化ビニリデンを構成単位とし
て70モルチ以上と、これと共重合可能な1種または2
種以上のモノマーを有する構成単位の残部とからなる共
重合体、或いはこれらの少なくともいずれかの重合体を
70重量%以上含有する組成物、更にこれらと同効の物
を指す。
The vinylidene fluoride resin referred to in the present invention is not only a vinylidene fluoride homopolymer, but also a vinylidene fluoride homopolymer containing 70 moles or more of vinylidene fluoride as a constituent unit, and one or two types copolymerizable with this resin.
It refers to a copolymer consisting of the remainder of the structural unit having more than one type of monomer, or a composition containing 70% by weight or more of at least one of these polymers, and also a product having the same effect as these.

また本発明に云う四弗化エチレン系樹脂とは四弗化エチ
レンホモポリマー、四弗化エチレンを構成単位として5
0モルチ以上と、これと共重合可能なモノマー、例えば
エチレン、六弗化プロピレン、パーフルオロビニルエー
テルノ如キモ/ −r −01種または2種以上を有す
る構成単位の残部とからなる共重合体、或いは四弗化エ
チレンの水素基の代わりに他の基、例えば三弗化エチレ
ン、パーフルオロアルキルエーテルテトラフルオロエチ
レン等を置換した重合体、更にこれらと同効の物を指す
In addition, the tetrafluoroethylene-based resin referred to in the present invention refers to a tetrafluoroethylene homopolymer, a polytetrafluoroethylene homopolymer, and a polytetrafluoroethylene homopolymer containing 5% tetrafluoroethylene as a constituent unit.
A copolymer consisting of a monomer copolymerizable with this, such as ethylene, hexafluorinated propylene, perfluorovinyl ether, etc./-r-0, and the remainder of a structural unit having one or more types of Alternatively, it refers to a polymer in which the hydrogen group of tetrafluoroethylene is replaced with another group, such as trifluoroethylene, perfluoroalkyl ether tetrafluoroethylene, etc., and also a product having the same effect as these.

本発明による樹脂成形物はこの様な四弗化エチレン系樹
脂を島粒子とし、溶融成形された弗化ビニリデン系樹脂
を海基質とする海島型構造を有している。海島型構造と
は高分子組成物の当業者には周知の用語であるが、海と
する樹脂中に島状にもう一方の樹脂が分散した組成物を
指していう。
The resin molded article according to the present invention has a sea-island structure in which the tetrafluoroethylene resin is used as island particles and the melt-molded vinylidene fluoride resin is used as the sea substrate. The sea-island structure is a term well known to those skilled in the art of polymer compositions, and refers to a composition in which a sea resin is dispersed in the form of islands of another resin.

本発明においては弗化ビニリデン系樹脂は溶融成形され
ていなければならないが、四弗化エチレン系樹脂は溶融
成形されていてもいなくてもよい3゜四弗化エチレン系
樹脂により形成される島粒子の平均粒子径は大き過ぎて
も小さ過ぎCもマット化されにくいので、0.1μm〜
10μmの範囲の平均粒径な有するものが用いられる。
In the present invention, the vinylidene fluoride resin must be melt-molded, but the tetrafluoroethylene resin is island particles formed from 3°tetrafluoroethylene resin, which may or may not be melt-molded. The average particle diameter of C is either too large or too small because C is difficult to matte, so it is 0.1 μm or more.
Those having an average particle size in the range of 10 μm are used.

好ましくは061〜5μm、より好ましくは0.1〜2
μmのものが用いられる。ここで平均粒子径とは電子顕
微鏡によりめた粒子の数100個の径をめ、その値の最
大値より25個、最小値より25個を除き、50個の粒
子の径の算術平均値である。粒子はマット成形物の1部
分のみが観測されない様に各部位を実質的に均等に観測
するものとし、各々の粒子の径は長径と短径の相加平均
とする。
Preferably 061-5 μm, more preferably 0.1-2
μm is used. Here, the average particle size is the arithmetic mean value of the diameters of 50 particles, excluding 25 from the maximum value and 25 from the minimum value, out of the diameters of 100 particles determined by an electron microscope. be. Each part of the particles is observed substantially equally so that only one part of the mat molded product is not observed, and the diameter of each particle is the arithmetic average of the major axis and the minor axis.

また本発明のマット成形物は特定一方向に流動配向した
状態である方がマット化される度合が高まり、好ましい
マット成形物となり、特定一方向に流動配向している度
合が高い程、好適に用いられる。特定一方向に流動配向
している度合は、例えば成形物が透明であるときには平
均複屈折率の大きさで判別され、平均複屈折率が3X1
0”−5以上のものが好ましく、1×10 以上のもの
が一層好ましく、lXl0−3以上のものが特に好まし
い。ここで平均複屈折率とはマット成形物の成形方法に
よっては成形物の部位により複屈折率が異なる場合があ
るので、成形物の平均の複屈折率を云う。複屈折率は成
形物の形状により、適宜選択された測定法によらねばな
らないが、例えばフィルムの場合にはフィルムの面に垂
直に偏光を入射させて測定される。成形物が不透明で複
屈折率により流動配向の度合を判別できないときには、
JIS 28741の60°鏡面光沢度の成形物への光
の入射方向による差で判別され、その差が0.2以上と
なるものが好ましく、より好ましくは0.3以上、より
一層好ましくは0.4以上となるものが用いられる。
In addition, when the matte molded product of the present invention is in a state where the fluid is oriented in one specific direction, the degree of matting increases and becomes a preferable matte molded product. used. The degree of fluid orientation in a specific direction is determined by the average birefringence when the molded product is transparent, for example, and the average birefringence is 3X1.
0"-5 or more is preferable, 1×10 or more is more preferable, and lXl0-3 or more is particularly preferable. Here, the average birefringence refers to the area of the matte molded product depending on the molding method. The birefringence index is the average birefringence of the molded product because the birefringence index may differ depending on the shape of the molded product.The birefringence index must be measured by an appropriately selected measurement method depending on the shape of the molded product, but for example, in the case of a film, It is measured by applying polarized light perpendicular to the plane of the film.When the molded product is opaque and the degree of flow orientation cannot be determined by the birefringence,
JIS 28741 60° specular gloss is determined by the difference depending on the direction of incidence of light on the molded product, and the difference is preferably 0.2 or more, more preferably 0.3 or more, and even more preferably 0. Those with a value of 4 or more are used.

以上の様な構成からなる本発明弗化ビニリデン系樹脂成
形物はマット化され、JIS z8741 による鏡面
光沢度が75チ以下のものが容易に得られ、好適な構成
の選択をすれば50チ以下のものが得られる。
The vinylidene fluoride resin molded product of the present invention having the above-mentioned structure is matte and can easily have a specular gloss of 75 inches or less according to JIS z8741, and if a suitable structure is selected, it can be 50 inches or less. You can get the following.

この様な成形物の形状はフィルム、糸、チューブ等を始
めとする任意のものであるが、特にフィルム状とし、他
の熱可塑性樹脂、代表的にはメタクリル酸エステル系樹
脂、特にメタクリル酸メチル系樹脂又はこれを接着面と
する積層体、例えばメタクリル酸メチル系樹脂と塩化ビ
ニル系樹脂との積層物、メタクリル酸メチル系樹脂と熱
可塑性ポリエステルとの積層物等と積層されて壁紙、パ
ネル板に代表される内装材、外装材等の建材として好適
に用いられる。
The shape of such a molded product may be arbitrary, including films, threads, tubes, etc., but it is especially film-like, and it is made of other thermoplastic resins, typically methacrylate ester resins, especially methyl methacrylate. based resin or a laminate using this as an adhesive surface, such as a laminate of methyl methacrylate resin and vinyl chloride resin, a laminate of methyl methacrylate resin and thermoplastic polyester, etc. to produce wallpaper, panel boards, etc. It is suitably used as building materials such as interior materials and exterior materials.

上記マット成形物は例えば弗化ビニリデン系樹脂を主と
し、四弗化エチレン系樹脂粉粒体を従とする混合物を、
弗化ビニリデン系樹脂の融点以上の温度で成形すること
によって得られる。ここで「弗化ビニリデン系樹脂を主
とし」とは、体積比において四弗化エチレン系樹脂に対
し、弗化ビニリデン系樹脂の方が多い割合を占めるとい
う意味である。また、四弗化エチレン系樹脂は粉状又は
粒状であり、その平均粒子径は高々10μmのものを用
い、各粒子は単独又は凝集した形でマット成形物中で島
を形成する。
The above-mentioned mat molded product is made of, for example, a mixture containing mainly vinylidene fluoride resin and secondary ethylene tetrafluoride resin powder.
It is obtained by molding at a temperature higher than the melting point of the vinylidene fluoride resin. Here, "mainly vinylidene fluoride resin" means that vinylidene fluoride resin occupies a larger volume ratio than tetrafluoroethylene resin. Further, the tetrafluoroethylene resin is in the form of powder or particles, and the average particle diameter is at most 10 μm, and each particle forms an island in the mat molded product, either singly or in agglomerated form.

特にマット成形物がフィルム状であり、透明性を損わな
い程度にマット化させる場合には、四弗化エチレン系樹
脂は弗化ビニリデン系樹脂100重量部に対し、高々2
0重量部、好ましくは10重量部以下、より好ましくは
8重量部以下とすることにより嚢価度が80チ以下のフ
ィルムが得られる。他方、四弗化エチレン系樹脂粉末が
少な過ぎるとマット化されに(いので、成形物の厚さに
よっても異なるが通常1重量部以上、好ましくは3重量
部以上が用いられる。
In particular, when the matte molded product is in the form of a film and is to be matted to an extent that does not impair transparency, the amount of ethylene tetrafluoride resin is at most 2 parts by weight per 100 parts by weight of vinylidene fluoride resin.
By setting the amount to 0 parts by weight, preferably 10 parts by weight or less, and more preferably 8 parts by weight or less, a film having a bag value of 80 inches or less can be obtained. On the other hand, if the amount of the tetrafluoroethylene resin powder is too small, it will not become matte (this may be difficult), so it is usually 1 part by weight or more, preferably 3 parts by weight or more, although it varies depending on the thickness of the molded product.

以下、実施例により本発明を更に詳細に説明する。Hereinafter, the present invention will be explained in more detail with reference to Examples.

実施例1,2および比較例1 ポリ弗化ビニリデンホモポリマー(ηinh 1dl/
i: 0.411/dl濃度のジメチルホルムアミr溶
液につき30Cで測定した値)100重量部と下記第1
表に示す量のポリ四弗化エチレンホモポリマーの微粉末
(JISB9921によりめた平均粒子径は0.3μm
)をヘンシェルミキサーで常温で10分間混合し、50
φ押出機で210Cで押出し堅レットを得た。このペレ
ットを50φ押出機で240Cで押出し、フラットダイ
スより30μ扉の厚さのフィルムを得た。フィルムの艶
消し状態はフィルム全体にわたり一様に得られ、JIS
Z8741に規定されているグロスメーターで光沢度に
より測定し、島の径は本文記載の通りにしてめ、それぞ
れ第1表に示す結果を得た。
Examples 1, 2 and Comparative Example 1 Polyvinylidene fluoride homopolymer (ηinh 1dl/
i: Value measured at 30C for a dimethylformamin r solution with a concentration of 0.411/dl) 100 parts by weight and the following 1st
Fine powder of polytetrafluoroethylene homopolymer in the amount shown in the table (average particle size determined by JISB9921 is 0.3 μm)
) in a Henschel mixer at room temperature for 10 minutes,
A hardlet was obtained by extruding at 210C in a φ extruder. This pellet was extruded at 240C using a 50φ extruder, and a film having a thickness of 30 μm was obtained using a flat die. The matte state of the film is uniformly obtained over the entire film, and the JIS
The gloss was measured using a gloss meter specified in Z8741, and the diameter of the islands was determined as described in the text, and the results shown in Table 1 were obtained.

第1表 実施例3.4および比較例2 前記比較例1並びに実施例1又は3で得たペレットをそ
れぞれ35φ押出機で245Cで押出し、メタクリル酸
メチル70モルチとアクリル酸ノチル30モルチとの共
重合体を74φ押出機で245Cで押出し、両者を2層
共押出用複合フラットダイスから押出して表層はポリ弗
化ビニリデンホモポリマーと四弗化エチレンホモポリマ
ーとの組成物、基材層はアクリル酸エステル系樹脂より
なる2層フィルムを得た。表層の厚さは5μ、基材層の
厚さは45μである。2層フィルムの表面の艶消し状態
は均一であり、実施例1と同様に測定して第2表に示す
結果を得た。
Table 1 Example 3.4 and Comparative Example 2 The pellets obtained in Comparative Example 1 and Example 1 or 3 were extruded at 245C using a 35φ extruder, and mixed with 70 mol of methyl methacrylate and 30 mol of notyl acrylate. The polymer was extruded at 245C with a 74φ extruder, and both were extruded through a composite flat die for two-layer coextrusion.The surface layer was a composition of polyvinylidene fluoride homopolymer and tetrafluoroethylene homopolymer, and the base layer was a composition of acrylic acid. A two-layer film made of ester resin was obtained. The thickness of the surface layer is 5μ, and the thickness of the base layer is 45μ. The surface of the two-layer film had a uniform matte state, and was measured in the same manner as in Example 1, and the results shown in Table 2 were obtained.

第2表 透明度、曇価度はJIS K6714の規定に従って測
定した。
Table 2 Transparency and haze were measured according to JIS K6714.

実施例5.6および比較例3 四弗化エチレン系樹脂としてエチレンと四弗化エチレン
との交互共重合体微粉末(JIS B9921によりめ
た平均粒子径は0.4am)をポリ弗化ヒニリデ710
0重量部に対しそれぞれ下記第3表に示す量で使用し、
ペレット作成の際の押出温度を305C、フィルム作成
の際の押出温度を310Cとし、厚さ20μmのフィル
ムを得た。
Example 5.6 and Comparative Example 3 A fine powder of an alternating copolymer of ethylene and tetrafluoroethylene (average particle size determined by JIS B9921: 0.4 am) was used as polyfluorinated ethylene resin 710 as a tetrafluoroethylene resin.
Used in the amounts shown in Table 3 below for 0 parts by weight,
The extrusion temperature during pellet production was 305C, and the extrusion temperature during film production was 310C to obtain a film with a thickness of 20 μm.

その他は実施例1と同様に行なった。その結果を第3表
に示す。
The rest was the same as in Example 1. The results are shown in Table 3.

第3表 実施例7,8および比較例4 実施例1のポリ四弗化エチレンホモポリマーの代わりに
エチレンと四弗化エチレンとの交互共重合体微粉末(平
均粒子径は実施例5と同じ)を下記第4表に示す量で用
いた他は実施例1と同様に行なった。その結果を第4表
に示す。
Table 3 Examples 7 and 8 and Comparative Example 4 Fine powder of alternating copolymer of ethylene and tetrafluoroethylene instead of the polytetrafluoroethylene homopolymer of Example 1 (average particle size is the same as Example 5) ) was used in the amounts shown in Table 4 below. The results are shown in Table 4.

〔発明の効果〕〔Effect of the invention〕

以上の実施例かられかる通り、本発明に係るマット成形
物は二次加工性に何等支障を来すこ゛となく均一なマッ
ト加工が可能である。
As can be seen from the above examples, the mat molded product according to the present invention can be processed into a uniform mat without causing any problems in secondary processability.

(ほか3名)(3 others)

Claims (4)

【特許請求の範囲】[Claims] (1)溶融成形された弗化ビニリデン系樹脂を海基質と
し、四弗化エチレン系樹脂を島粒子とする海島型構造で
あり、島の平均粒子径が0.1〜10μmである弗化ビ
ニリデン系樹脂マット成形物。
(1) Vinylidene fluoride has a sea-island structure with melt-molded vinylidene fluoride resin as the sea substrate and tetrafluoroethylene resin as island particles, and the average particle diameter of the islands is 0.1 to 10 μm. Resin mat molded product.
(2)特定一方向に流動配向したことを特徴とする特許
請求の範囲第1項記載の弗化ビニリデン系樹脂マット成
形物。
(2) The polyvinylidene fluoride resin mat molded product according to claim 1, characterized in that the molded product is fluidized in one specific direction.
(3)弗化ビニリデン系樹脂を主とし、四弗化エチレン
系樹脂粉粒体を従とする混合物を、弗化ビニyデン系樹
脂の融点以上の温度で成形する弗化ビニリデン系樹脂マ
ット成形物の製造方法。
(3) Vinylidene fluoride resin mat molding by molding a mixture mainly consisting of vinylidene fluoride resin and tetrafluoroethylene resin powder at a temperature higher than the melting point of the vinylidene fluoride resin. How things are manufactured.
(4)成形が押出成形でなされることを特徴とする特許
請求の範囲第3項記載の弗化ビ= IJデン系樹脂マッ
ト成形物の製造方法。
(4) The method for producing a bifluoride resin mat molded product according to claim 3, wherein the molding is performed by extrusion molding.
JP59074876A 1984-04-16 1984-04-16 Mat molding of vinylidene fluoride resin and manufacture thereof Granted JPS60219027A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59074876A JPS60219027A (en) 1984-04-16 1984-04-16 Mat molding of vinylidene fluoride resin and manufacture thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59074876A JPS60219027A (en) 1984-04-16 1984-04-16 Mat molding of vinylidene fluoride resin and manufacture thereof

Publications (2)

Publication Number Publication Date
JPS60219027A true JPS60219027A (en) 1985-11-01
JPH0458497B2 JPH0458497B2 (en) 1992-09-17

Family

ID=13559980

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59074876A Granted JPS60219027A (en) 1984-04-16 1984-04-16 Mat molding of vinylidene fluoride resin and manufacture thereof

Country Status (1)

Country Link
JP (1) JPS60219027A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006159524A (en) * 2004-12-03 2006-06-22 Du Pont Mitsui Fluorochem Co Ltd Fluoroplastic resin molding method and fluoroplastic resin molded product
JP2007320267A (en) * 2006-06-02 2007-12-13 Du Pont Mitsui Fluorochem Co Ltd Fluororesin molding method and fluororesin molding
WO2016204174A1 (en) * 2015-06-16 2016-12-22 日星電気株式会社 Heat-shrinkable tube and method for producing same

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5411155A (en) * 1977-06-24 1979-01-27 Ugine Kuhlmann Lublicated thermoplastics compound based on polyvinyl fluoride

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5411155A (en) * 1977-06-24 1979-01-27 Ugine Kuhlmann Lublicated thermoplastics compound based on polyvinyl fluoride

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006159524A (en) * 2004-12-03 2006-06-22 Du Pont Mitsui Fluorochem Co Ltd Fluoroplastic resin molding method and fluoroplastic resin molded product
JP4533115B2 (en) * 2004-12-03 2010-09-01 三井・デュポンフロロケミカル株式会社 Fluororesin molding method and fluororesin molding
KR101433495B1 (en) * 2004-12-03 2014-08-22 듀폰-미쯔이 플루오로케미칼 가부시끼가이샤 Fluoropolymer Molding Process And Fluoropolymer Molded Product
JP2007320267A (en) * 2006-06-02 2007-12-13 Du Pont Mitsui Fluorochem Co Ltd Fluororesin molding method and fluororesin molding
WO2016204174A1 (en) * 2015-06-16 2016-12-22 日星電気株式会社 Heat-shrinkable tube and method for producing same
JP6140376B2 (en) * 2015-06-16 2017-05-31 日星電気株式会社 Heat shrinkable tube and manufacturing method thereof
JPWO2016204174A1 (en) * 2015-06-16 2017-06-29 日星電気株式会社 Heat shrinkable tube and manufacturing method thereof
CN107683200A (en) * 2015-06-16 2018-02-09 日星电气有限公司 Heat-shrinkable tube and its manufacture method
US10661497B2 (en) 2015-06-16 2020-05-26 Nissei Electric Co., Ltd. Heat shrink tube and method for producing the same

Also Published As

Publication number Publication date
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