JP3527538B2 - Core resin composition and method for producing hollow molded article using the same - Google Patents
Core resin composition and method for producing hollow molded article using the sameInfo
- Publication number
- JP3527538B2 JP3527538B2 JP13357494A JP13357494A JP3527538B2 JP 3527538 B2 JP3527538 B2 JP 3527538B2 JP 13357494 A JP13357494 A JP 13357494A JP 13357494 A JP13357494 A JP 13357494A JP 3527538 B2 JP3527538 B2 JP 3527538B2
- Authority
- JP
- Japan
- Prior art keywords
- core
- resin composition
- weight
- oxyalkylene group
- water
- 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.)
- Expired - Lifetime
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C33/00—Moulds or cores; Details thereof or accessories therefor
- B29C33/44—Moulds or cores; Details thereof or accessories therefor with means for, or specially constructed to facilitate, the removal of articles, e.g. of undercut articles
- B29C33/52—Moulds or cores; Details thereof or accessories therefor with means for, or specially constructed to facilitate, the removal of articles, e.g. of undercut articles soluble or fusible
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Moulds For Moulding Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、中子用樹脂組成物及び
それを用いた中空成形品の製造法に関し、更に詳しくは
吸湿等により剛性が経時的に低下することが無く、耐熱
性、水溶解速度及び水溶解除去性に優れ、中空成形品の
仕上がり精度が良好な中子用樹脂組成物及びそれを用い
た中空成形品の製造法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a resin composition for cores and a method for producing a hollow molded article using the same, more specifically, the rigidity does not decrease with time due to moisture absorption, heat resistance, The present invention relates to a resin composition for cores, which has an excellent rate of water dissolution and water removability and a good finish accuracy of a hollow molded article, and a method for producing a hollow molded article using the same.
【0002】[0002]
【従来の技術】中空成形品を得るために水溶性樹脂によ
り中子を作ることは、種々提案されている。2. Description of the Related Art Various proposals have been made for forming a core from a water-soluble resin in order to obtain a hollow molded article.
【0003】例えば、特開平3−230927号公報及
び特開平3−227609号公報には、水溶性樹脂とし
てポリアクリルアミド、ポリアクリル酸、ポリメタクリ
ル酸、ポリイタコン酸、ポリビニルアルコール(以下P
VAと略す)、ポリエチレンオキサイド、ポリビニルピ
ロリドン、ポリビニルメチルエーテル、アルカリ性水溶
液可溶のイソプレン系樹脂、エチレンアクリレート−ア
クリル酸共重合体などを用いることが開示されている。For example, JP-A-3-230927 and JP-A-3-227609 disclose, as water-soluble resins, polyacrylamide, polyacrylic acid, polymethacrylic acid, polyitaconic acid, polyvinyl alcohol (hereinafter P.
(Abbreviated as VA), polyethylene oxide, polyvinylpyrrolidone, polyvinyl methyl ether, isoprene-based resin soluble in alkaline aqueous solution, ethylene acrylate-acrylic acid copolymer, and the like are disclosed.
【0004】又、特開平6−39844号公報には、射
出成形などにより容易に中子に成形可能な水溶性の樹脂
組成物として、重合度200〜2000の酢酸ビニル系
重合体をケン化度65〜95モル%でケン化して得られ
る重合体100重量部、可塑剤0.5〜50重量部及び
無機フィラー0〜100重量部からなる中子用樹脂組成
物が開示されている。Further, in JP-A-6-39844, a vinyl acetate polymer having a degree of polymerization of 200 to 2000 is saponified as a water-soluble resin composition which can be easily molded into a core by injection molding or the like. A resin composition for cores is disclosed which comprises 100 parts by weight of a polymer obtained by saponification at 65 to 95 mol%, 0.5 to 50 parts by weight of a plasticizer, and 0 to 100 parts by weight of an inorganic filler.
【0005】尚、本発明で用いているオキシアルキレン
基含有ビニルアルコール系ポリマー自体については、米
国特許第1971662号明細書、同第2844570
号明細書及び同第2990398号明細書(PVAにエ
チレンオキサイドを付加反応させたオキシエチレン基含
有PVA)、米国特許第3033841号明細書及び同
4369281号明細書(ポリアルキレングリコール共
存下に酢酸ビニルをグラフト重合させた重合物をケン化
したオキシアルキレン基含有PVA)、米国特許第46
18648号明細書及び同第4675360号明細書
(ビニルアルコールとポリ(アルキレンオキシ)アクリ
レートとの共重合体)、特開昭59−155408号公
報(オキシアルキレン基を含有する不飽和単量体と酢酸
ビニルとの共重合体をケン化した変性PVA)、特開平
1−158016号公報(オキシアルキレン基含有ビニ
ルアルコール系重合体フィルムからなる耐水性柔軟フィ
ルム)、特開平3−203932号公報(オキシアルキ
レン基含有ビニルアルコール系共重合体を実質的に無水
の条件下で溶融成形する方法)などの文献があるが、こ
のオキシアルキレン基含有ビニルアルコール系ポリマー
を射出成形に際しての中子に利用することについては何
等の記載も示唆もなく、ましてや無機系フィラーを配合
して中子として利用することに関して全く記載はない。Regarding the oxyalkylene group-containing vinyl alcohol-based polymer itself used in the present invention, US Pat. Nos. 1,917,662 and 2,844,570 are cited.
And No. 2990398 (oxyethylene group-containing PVA obtained by addition reaction of ethylene oxide with PVA), US Pat. Nos. 3,033,841 and 4,369,281 (with vinyl acetate in the presence of polyalkylene glycol). Oxyalkylene group-containing PVA obtained by saponifying a graft-polymerized polymer, US Pat. No. 46.
18648 and 4675360 (copolymer of vinyl alcohol and poly (alkyleneoxy) acrylate), JP-A-59-155408 (unsaturated monomer containing oxyalkylene group and acetic acid). Modified PVA obtained by saponifying a copolymer with vinyl), JP-A-1-158016 (water-resistant flexible film composed of vinyl alcohol-based polymer film containing oxyalkylene group), JP-A-3-203932 (oxyalkylene). There is a document such as a method of melt-molding a group-containing vinyl alcohol-based copolymer under substantially anhydrous conditions), but regarding the use of this oxyalkylene group-containing vinyl alcohol-based polymer as a core in injection molding. There is no description or suggestion, let alone blended with an inorganic filler and used as a core No mention at all in relation to Rukoto.
【0006】[0006]
【発明が解決しようとする課題】上述の様に中子用の水
溶性樹脂として種々のものが使用されているが、中空成
形品の仕上がり精度と水溶解除去性のバランスのとれた
中子を作ることは非常に困難であった。又、中子を作製
後直ちに中空成形用に使用されることは稀で、一定期間
外部に放置されることが多々あり、その結果、特開平6
−39844号公報開示技術では、吸湿等により剛性の
低下を招き中空成形品の仕上がり精度が低下するという
問題点があった。Although various types of water-soluble resins for cores are used as described above, a core having a well-balanced finish accuracy and water-dissolving removability of a hollow molded product is used. It was very difficult to make. Further, it is rarely used for hollow molding immediately after the core is produced, and it is often left outside for a certain period of time.
In the technology disclosed in Japanese Patent Laid-Open No. 39844, there is a problem that the rigidity is lowered due to moisture absorption and the like, and the finish accuracy of the hollow molded article is lowered.
【0007】吸湿等による剛性の経時的な低下が無く、
耐熱性、水溶解速度及び水溶解除去性に優れ、且つ仕上
がり精度が良好な中空成形品を得ることが出来る中子用
樹脂組成物及びそれを用いた中空成形品の製造法の出現
が望まれていた。There is no decrease in rigidity over time due to moisture absorption,
It is desired to develop a resin composition for cores which is excellent in heat resistance, water dissolution rate and water dissolution removal property, and which can obtain a hollow molded article having good finishing accuracy, and a method for producing a hollow molded article using the same. Was there.
【0008】[0008]
【課題を解決する為の手段】しかるに本発明者等はかか
る問題点を解決する為鋭意検討を行った結果、オキシア
ルキレン基を含有したPVA系樹脂(A)にアスペクト
比が20以上である無機系フィラー(B)を1〜60重
量%配合することにより、吸湿等による剛性の経時的な
低下が無く、耐熱性、水溶解速度及び水溶解除去性に優
れ、中空成形品の仕上がり精度が良好な中子用樹脂組成
物及びそれを用いた中空成形品の製造法が得られること
と見いだし本発明の完成に至った。However, as a result of intensive investigations by the present inventors in order to solve such problems, as a result, the PVA-based resin (A) containing an oxyalkylene group has an aspect ratio.
By blending 1 to 60% by weight of the inorganic filler (B) having a ratio of 20 or more, rigidity does not decrease with time due to moisture absorption, etc., and heat resistance, water dissolution rate and water dissolution removal property are excellent, and hollow. It was found that a resin composition for cores having a good finished precision of a molded product and a method for producing a hollow molded product using the same can be obtained, and the present invention has been completed.
【0009】以下、本発明を詳細に説明する。本発明で
用いられるオキシアルキレン基含有PVA系樹脂(A)
は、典型的には、脂肪酸ビニルエステルと、下記一般式
化1で示させるポリオキシエチレン(メタ)アリルエー
テル、ポリオキシプロピレン(メタ)アリルエーテルな
どのポリオキシアルキレン(メタ)アリルエーテルや下
記一般式化2で示されるポリオキシエチレンビニルエー
テル、ポリオキシプロピレンビニルエーテル等のポリア
ルキレンビニルエーテルを共重合して、ついで得られる
共重合体をケン化して得られる。中でも酢酸ビニル系共
重合体をケン化して得られるオキシアルキレン基を含有
したPVA系樹脂(A)が経済的に最も好ましい。The present invention will be described in detail below. Oxyalkylene group-containing PVA resin (A) used in the present invention
Is typically a fatty acid vinyl ester and a polyoxyalkylene (meth) allyl ether such as polyoxyethylene (meth) allyl ether or polyoxypropylene (meth) allyl ether represented by the following general formula 1 or the following general formula It can be obtained by copolymerizing a polyalkylene vinyl ether such as polyoxyethylene vinyl ether and polyoxypropylene vinyl ether represented by Formula 2, and then saponifying the resulting copolymer. Among them, the PVA-based resin (A) containing an oxyalkylene group, which is obtained by saponifying a vinyl acetate-based copolymer, is economically most preferable.
【0010】オキシアルキレン基含有PVA系ポリマー
を得るときの重合方法としては通常溶液重合法が採用さ
れ、場合により懸濁重合法、エマルジョン重合法などを
採用することもできる。ケン化反応としては、アルカリ
ケン化法、酸ケン化法などが採用される。As the polymerization method for obtaining the oxyalkylene group-containing PVA-based polymer, a solution polymerization method is usually adopted, and a suspension polymerization method, an emulsion polymerization method or the like can be adopted depending on the case. As the saponification reaction, an alkali saponification method, an acid saponification method or the like is adopted.
【0011】上記オキシアルキレン基含有PVA系ポリ
マーのオキシアルキレン基含有量は、1〜60重量%、
好ましくは2〜50重量%、特に好ましくは3〜40重
量%であり、1重量%未満であると押出成形性の低下、
水溶解速度及び水溶解除去性の低下等の点で問題があ
り、60重量%より多くなると中子の精密成形性の低
下、熱剛性の低下等の点で問題がある。ポリオキシアル
キレン基の平均縮合度は3〜100であり、平均縮合度
が3未満のものは、押出成形性の点で劣り、又オキシア
ルキレン基を導入する際の工業的生産性の低下、水溶解
速度及び水溶解除去性の低下等の問題点があり、平均縮
合度が100より多くなると押出成形性の低下等の問題
点が生じ、好ましくは3〜50、特に好ましくは5〜3
0である。尚、ここで言う平均縮合度とは、下記化1、
化2で示される化学式中のnを示す。The oxyalkylene group content of the oxyalkylene group-containing PVA polymer is 1 to 60% by weight,
It is preferably from 2 to 50% by weight, particularly preferably from 3 to 40% by weight, and when it is less than 1% by weight, extrusion moldability is deteriorated.
There is a problem in that the water-dissolving rate and the water-dissolving removability are lowered, and if it is more than 60% by weight, there is a problem in that the precision moldability of the core is lowered and the thermal rigidity is lowered. The polyoxyalkylene group has an average degree of condensation of 3 to 100, and those having an average degree of condensation of less than 3 are inferior in extrusion moldability, and also have low industrial productivity when introducing the oxyalkylene group and water. There are problems such as a decrease in dissolution rate and water-dissolving removability, and when the average degree of condensation is more than 100, problems such as a decrease in extrusion moldability occur, preferably 3 to 50, particularly preferably 5 to 3.
It is 0. The average degree of condensation referred to herein means the following chemical formula 1,
N in the chemical formula shown in Chemical formula 2 is shown.
【0012】[0012]
【化1】
但し、R0,R1,R2,R3は水素又はアルキル基を示
す。[Chemical 1] However, R 0 , R 1 , R 2 and R 3 represent hydrogen or an alkyl group.
【化2】 (X=H又は−C−R3又はR3) 但し、R1 ,R2 ,R3 は水素又はアルキル基を示す。[Chemical 2] (X = H or -C-R 3, or R 3) where, R 1, R 2, R 3 represents hydrogen or an alkyl group.
【0013】オキシアルキレン基を含有したPVA系樹
脂(A)に於ける脂肪酸ビニルエステル単位のケン化度
は60〜100モル%であり、60モル%未満では水溶
解除去性の低下、中空成形品の仕上がり精度の低下(熱
変形温度の低下)、熱安定性の低下、成形性の低下、無
機系フィラーとの親和性の低下、剛性の低下等で問題が
あり、好ましくは80〜100モル%が適当である。
又、重量平均重合度は100〜2000であり、100
未満であると中子の強度が不足し、2000より大きく
なると溶融粘度が大きく中空成形品の仕上がり精度の低
下、無機系フィラーの分散不良等の点で問題があり、好
ましくは100〜1000、無機系フィラー(B)配合
後の樹脂組成物の溶融粘度への影響及び該樹脂組成物を
中子として成形した場合の中子表面の平滑性(ガラス繊
維等のフィラー浮き)への影響より特に好ましくは10
0〜600である。The degree of saponification of the fatty acid vinyl ester units in the PVA-based resin (A) containing an oxyalkylene group is 60 to 100 mol%. There is a problem such as a decrease in finishing accuracy (a decrease in heat distortion temperature), a decrease in thermal stability, a decrease in moldability, a decrease in affinity with an inorganic filler, a decrease in rigidity, etc., preferably 80 to 100 mol% Is appropriate.
The weight average degree of polymerization is 100 to 2000,
If the amount is less than 2000, the strength of the core becomes insufficient, and if it exceeds 2000, there is a problem in that the melt viscosity is large and the finish accuracy of the hollow molded product is deteriorated, and the inorganic filler is poorly dispersed. It is particularly preferable because of the influence on the melt viscosity of the resin composition after blending the base filler (B) and the influence on the smoothness of the surface of the core (floating of the filler such as glass fiber) when the resin composition is molded as a core. Is 10
0 to 600.
【0014】又、共重合成分として、ポリオキシアルキ
レン(メタ)アリルエーテル以外に、α−オレフィン
(エチレン、プロピレン、長鎖α−オレフィン等)、エ
チレン性不飽和カルボン酸系モノマー(アクリレート、
メタクリレート、アクリロニトリル、メタクリロニトリ
ル、塩化ビニル、ビニルエーテル等)を30モル%程度
以下であれば含んでいてもよい。Further, as a copolymerization component, in addition to polyoxyalkylene (meth) allyl ether, α-olefins (ethylene, propylene, long-chain α-olefins, etc.), ethylenically unsaturated carboxylic acid type monomers (acrylates,
Methacrylate, acrylonitrile, methacrylonitrile, vinyl chloride, vinyl ether, etc.) may be contained in an amount of about 30 mol% or less.
【0015】オキシアルキレン基含有PVA系樹脂
(A)は上記の他、脂肪酸ビニルエステルと、ポリオキ
シエチレン(メタ)アクリレート、ポリオキシプロピレ
ン(メタ)アクリレート、ポリオキシエチレン(メタ)
アクリルアミド、ポリオキシプロピレン(メタ)アクリ
ルアミド、ポリオキシエチレン(1−(メタ)アクリル
アミド−1,1−ジメチルプロピル)エステル、ポリオ
キシエチレンアリルアミン、ポリオキシプロピレンアリ
ルアミン等のポリオキシアルキレンアリルアミン、ポリ
オキシエチレンビニルアミン、ポリオキシプロピレンビ
ニルアミン等のポリオキシアルキレンビニルアミン等を
共重合し、ついでケン化することによっても得ることが
出来る。The oxyalkylene group-containing PVA-based resin (A) is, in addition to the above, a fatty acid vinyl ester, polyoxyethylene (meth) acrylate, polyoxypropylene (meth) acrylate, and polyoxyethylene (meth).
Polyoxyalkylene allylamine such as acrylamide, polyoxypropylene (meth) acrylamide, polyoxyethylene (1- (meth) acrylamide-1,1-dimethylpropyl) ester, polyoxyethylene allylamine, polyoxypropylene allylamine, polyoxyethylene vinyl It can also be obtained by copolymerizing amine, polyoxyalkylene vinyl amine such as polyoxypropylene vinyl amine, and then saponifying.
【0016】オキシアルキレン基を含有したPVA系樹
脂(A)は、上記の方法以外にPVAに対するアルキレ
ンオキシドの反応、或いはポリオキシアルキレングリコ
ールに対する脂肪酸ビニルエステルの重合及びそれに引
き続くケン化によっても得ることが出来る。The PVA-based resin (A) containing an oxyalkylene group can be obtained by a reaction of alkylene oxide with PVA or polymerization of fatty acid vinyl ester with polyoxyalkylene glycol and subsequent saponification, in addition to the above method. I can.
【0017】本発明の中子用樹脂組成物に用いられる無
機系フィラーの配合量としては、1〜60重量%、好ま
しくは10〜55重量%、特に好ましくは20〜50重
量%である。1重量%未満であると耐熱剛性、水溶解速
度及び水溶解除去性、吸湿に対する剛性の経時安定性等
が不足し、又60重量%より多くなると押出成形性、中
空成形品の仕上がり精度及び表面平滑性等が低下し適当
でない。The amount of the inorganic filler used in the core resin composition of the present invention is 1 to 60% by weight, preferably 10 to 55% by weight, and particularly preferably 20 to 50% by weight. If it is less than 1% by weight, heat resistance rigidity, water dissolution rate and water dissolution removability, stability with time of rigidity against moisture absorption, etc. are insufficient, and if it is more than 60% by weight, extrusion moldability, finish accuracy and surface of hollow molded product are obtained. It is not suitable because the smoothness etc. decreases.
【0018】又、無機系フィラー(B)としては、吸水
時の寸法、重量変化及び強度、弾性率、耐熱性、温水溶
解除去性改善の面よりタルク、クレー、シリカ、ケイ藻
土、カオリン、雲母、アスベスト、石膏、グラファイ
ト、ガラス繊維、ガラスバルーン、ガラスビーズ、硫酸
カルシウム、硫酸バリウム、硫酸アンモニウム、亜硫酸
カルシウム、炭酸カルシウム、ウイスカー状炭酸カルシ
ウム、炭酸マグネシウム、ドーソナイト、ドロマイト、
チタン酸カリウム、カーボンブラック、アルミナ繊維、
アラミド繊維、ボロン繊維、加工鉱物繊維、炭素繊維、
炭素中空球、ベントナイト、モンモリロナイト、銅紛等
の中から任意のものを少なくとも1種用いることができ
るが、強度、弾性率、耐熱性、水溶解速度及び水溶解除
去性、中空成形品の仕上がり精度を更に改良するという
見地より、アスペクト比が20以上の無機系フィラー
(B)を採用することが必要で、平均繊維径又は平均フ
レーク径は1〜30μであることが好ましく、前記条件
を満たす形状のタルク、雲母、ガラス繊維、ウイスカー
状炭酸カルシウムが本発明に於ける無機系フィラー
(B)として特に好ましい。又、無機系フィラーの長径
としては50mm未満、好ましくは25mm未満、更に
好ましくは10mm未満であり、長径が50mm以上に
なると無機系フィラーが、配合の際の混練り時や射出成
形時に破砕する恐れがあり好ましくない。Further, as the inorganic filler (B), talc, clay, silica, diatomaceous earth, kaolin, from the viewpoints of size, weight change and strength upon absorption of water, strength, elastic modulus, heat resistance, and improvement in hot water dissolution and removal property, Mica, asbestos, gypsum, graphite, glass fiber, glass balloons, glass beads, calcium sulfate, barium sulfate, ammonium sulfate, calcium sulfite, calcium carbonate, whisker-like calcium carbonate, magnesium carbonate, dawsonite, dolomite,
Potassium titanate, carbon black, alumina fiber,
Aramid fiber, boron fiber, processed mineral fiber, carbon fiber,
At least one selected from carbon hollow spheres, bentonite, montmorillonite, copper powder, etc. can be used, but strength, elastic modulus, heat resistance, water dissolution rate and water dissolution removal property, finish accuracy of hollow molded product From the standpoint of further improving the inorganic filler having an aspect ratio of 20 or more
It is necessary to adopt (B), and the average fiber diameter or average fiber
The rake diameter is preferably 1 to 30 μm , and talc, mica, glass fiber, and whisker-like calcium carbonate having a shape satisfying the above conditions are particularly preferable as the inorganic filler (B) in the present invention. The major axis of the inorganic filler is less than 50 mm, preferably less than 25 mm, more preferably less than 10 mm. If the major axis is 50 mm or more, the inorganic filler may be crushed during kneading during compounding or injection molding. Is not preferred.
【0019】本発明で使用される雲母のフレークとして
は、白雲母、金雲母の他にバイオタイト、レビドライ
ト、パラゴナイト、マーガライト、セリセイト、合成フ
ロロフロゴパイトなどが使用され、又ガラス繊維として
は、無アルカリガラス(Eガラス)、化学用ガラス(C
ガラス)の他に含アルカリガラス(Aガラス)などが使
用される。ウイスカー状炭酸カルシウムとしては、例え
ばウイスカル(丸尾カルシウム株式会社製)が使用され
る。Examples of the mica flakes used in the present invention include muscovite and phlogopite, as well as biotite, levidrite, paragonite, margarite, sericite, synthetic phlolovogrogite, and the like. , Non-alkali glass (E glass), chemical glass (C
In addition to (glass), alkali-containing glass (A glass) and the like are used. As the whisker-like calcium carbonate, for example, whiskers (manufactured by Maruo Calcium Co., Ltd.) are used.
【0020】オキシアルキレン基含有PVA系樹脂
(A)に無機系フィラー(B)を配合する方法として
は、無機系フィラー(B)とオキシアルキレン基含有P
VA系樹脂(A)を、そのまま射出成形機又は押出成形
機に供給して、混合及び成形を同時に行う方法、或いは
オキシアルキレン基含有PVA系樹脂(A)と無機系フ
ィラー(B)の混合物を押出成形機に供給してペレット
化する方法などが採用される。The inorganic filler (B) is mixed with the oxyalkylene group-containing PVA-based resin (A) by the inorganic filler (B) and the oxyalkylene group-containing P.
A method in which the VA resin (A) is directly supplied to an injection molding machine or an extrusion molding machine to perform mixing and molding, or a mixture of the oxyalkylene group-containing PVA resin (A) and the inorganic filler (B). A method of supplying to an extruder and pelletizing is adopted.
【0021】中子の成形は、上記の無機系フィラー
(B)を配合したオキシアルキレン基含有PVA系樹脂
(A)を溶融成形することによりなされる。溶融成形法
としては、射出成形法、ブロー成形法、押出成形法、ト
ランスファー成形法などが挙げられる。溶融成形に際し
ては、滑剤、着色剤、酸化防止剤等の安定剤など種々の
添加剤や他のポリマーを必要に応じて配合してもよい。
射出成形法を採用する場合は、例えば、シリンダー温度
150〜250℃程度、金型温度30〜100℃程度、
射出圧力500〜2000Kg/cm2 程度の条件が採
用される。押出成形法を採用する場合は、例えば、ダイ
温度を150〜250℃程度に設定し、スクリュー圧縮
部温度を吐出部温度より5〜30℃高い温度に設定して
行うことが望ましい。The core is molded by melt-molding the oxyalkylene group-containing PVA resin (A) containing the above-mentioned inorganic filler (B). Examples of the melt molding method include an injection molding method, a blow molding method, an extrusion molding method, and a transfer molding method. At the time of melt molding, various additives such as a lubricant, a colorant, a stabilizer such as an antioxidant, and other polymers may be blended as necessary.
When the injection molding method is adopted, for example, the cylinder temperature is about 150 to 250 ° C, the mold temperature is about 30 to 100 ° C,
The conditions of injection pressure of about 500 to 2000 Kg / cm 2 are adopted. When the extrusion molding method is adopted, it is desirable to set the die temperature to about 150 to 250 ° C. and the screw compression temperature to 5 to 30 ° C. higher than the discharge temperature, for example.
【0022】そして本発明においては、このようにして
得た中子を金型に挿入し、中子の周囲に成形用材料を射
出成形する。成形用材料としては、各種の熱可塑性樹
脂、熱硬化性樹脂が挙げられる。Then, in the present invention, the core thus obtained is inserted into a mold, and a molding material is injection molded around the core. Examples of the molding material include various thermoplastic resins and thermosetting resins.
【0023】射出成形後は、中子を、冷水、常温の水、
温水、熱水、水蒸気など水で溶解除去して中空成形品を
製造する。中空成形品の例としては、屈曲部を有する中
空成形物(インテークマニホールド)、複雑形状の中空
多岐管、異径管、複雑形状の中空部品(バンパー、刃物
や台所用品などの柄、ゴルフクラブヘッド)、電子部品
・機械部品(プロペラ、翼、羽根車)などが挙げられ
る。After injection molding, the core is cooled with cold water, normal temperature water,
A hollow molded article is manufactured by dissolving and removing with hot water, hot water, water such as steam. Examples of hollow molded products are hollow molded products having bent parts (intake manifold), complex shaped hollow manifolds, different diameter pipes, complex shaped hollow parts (bumpers, handles such as blades and kitchen utensils, golf club heads). ), Electronic parts and mechanical parts (propellers, blades, impellers), and the like.
【0024】[0024]
【作用】オキシアルキレン基を含有したポリビニルアル
コール系樹脂(A)にアスペクト比が20以上である無
機系フィラー(B)を1〜60重量%配合することによ
り、かかる樹脂組成物からなる中子の剛性が吸湿等によ
り経時的に低下することが無く、耐熱性、水溶解速度及
び水溶解除去性に優れ、且つ仕上がり精度が良好な中空
成形品を得ることが出来る中子用樹脂組成物及びそれを
用いた中空成形品の製造法が得られ大変有用である。By blending 1 to 60% by weight of the organic filler (B) having an aspect ratio of 20 or more with the polyvinyl alcohol resin (A) containing an oxyalkylene group, such a resin composition can be obtained. For cores, the rigidity of the core made of is not deteriorated with time due to moisture absorption, etc., and is excellent in heat resistance, water dissolution rate, water dissolution removal property, and good finish accuracy. A resin composition and a method for producing a hollow molded article using the same are obtained, which is very useful.
【0025】[0025]
【実施例】以下、実施例を挙げて本発明を更に具体的に
説明する。尚、実施例中「%」とあるのは、断りのない
限り重量基準を意味する。
実施例1オキシアルキレン基含有PVA(A)
重量平均重合度:350
ポリオキシエチレンモノアリルエーテル(化1でXが
H)(オキシエチレンの平均縮合度は20)単位の共重
合割合:2.0モル%
ポリマー全体に占めるオキシアルキレン単位の割合:2
0重量%
酢酸ビニル成分のケン化度:90モル%EXAMPLES The present invention will be described in more detail below with reference to examples. In the examples, "%" means weight basis unless otherwise specified. Example 1 Oxyalkylene group-containing PVA (A) Weight average degree of polymerization: 350 Polyoxyethylene monoallyl ether (X in formula 1 is H) (Copolymerization ratio of oxyethylene is 20) Average unit: 2.0 Mol% Ratio of oxyalkylene units in the whole polymer: 2
0% by weight Saponification degree of vinyl acetate component: 90 mol%
【0026】無機系フィラー(B) ガラス繊維 平均繊維径(μ):10 アスペクト比 :300 Inorganic filler (B) Glass fiber Average fiber diameter (μ): 10 Aspect ratio: 300
【0027】上記の樹脂を表1に示す配合比率で単軸押
出機(L/D=28、40mmφ)に供給して供給部=
180℃、圧縮部=210℃、計量部=210℃で押出
すことによりペレット状の樹脂組成物を得た。本発明の
中子用樹脂組成物の中子としての適性を評価する為、該
成形用ペレットを射出成形機に供給して、シリンダー最
高温度220℃、金型温度60℃、射出圧900Kg/
cm2 の条件で射出成形し、以下に示す形状の試験片を
作製し、下記の条件により熱変形温度、水溶解時間及び
25℃、65%RH下で10日間放置後の曲げ強度の保
持率の評価を行った。The above resin was supplied to a single-screw extruder (L / D = 28, 40 mmφ) at the compounding ratio shown in Table 1, and the supply section =
Pelletized resin composition was obtained by extruding at 180 ° C., compression part = 210 ° C., and metering part = 210 ° C. In order to evaluate the suitability of the core resin composition of the present invention as a core, the molding pellets are supplied to an injection molding machine, the cylinder maximum temperature is 220 ° C., the mold temperature is 60 ° C., and the injection pressure is 900 Kg /
The test piece having the shape shown below was prepared by injection molding under the condition of cm 2, and the heat distortion temperature, the water dissolution time, and the bending strength retention rate after standing for 10 days at 25 ° C. and 65% RH under the following conditions: Was evaluated.
【0028】(試験片)
熱変形温度測定用:ASTM D648による厚み1
2.7mm、幅12.7mm、長さ127mmの試験
片。
水溶解時間測定用:厚み3.2mm、径50mmの円盤
状試験片。
曲げ試験用 :ASTM D790による厚み6.
4mm、幅12.7mm、長さ152.4mmの試験
片。(Test piece) For heat distortion temperature measurement: Thickness 1 according to ASTM D648
A test piece of 2.7 mm, width of 12.7 mm, and length of 127 mm. For water dissolution time measurement: a disc-shaped test piece having a thickness of 3.2 mm and a diameter of 50 mm. For bending test: Thickness according to ASTM D790 6.
4 mm, width 12.7 mm, length 152.4 mm test piece.
【0029】(試験条件)
熱変形温度:株式会社安田精機製作所製ヒートデストー
ションテスター使用。荷重18.6Kg、昇温速度2℃
/min.
(判定基準) ○:60℃以上
△:50℃以上60℃未満
×:50℃未満
水溶解時間: 水温25℃、水量2lのウオーターバス
に試験片を浸漬し、回転数300rpmで撹拌を行っ
た。
(判定基準) ○:100分以上200分未満
△:200分以上250分未満
×:250分以上
曲げ試験 :株式会社島津製作所オートグラフAG−5
000A使用。使用ロードセル500Kg、支点スパン
101.6mm
曲げ速度2.5mm/min.
(判定基準)20℃、65%RH下で10日間放置後の
曲げ強度の保持率で判定
○:86%以上
△:80%以上85%未満
×:80%未満(Test Conditions) Heat Deformation Temperature: Heat distortion tester manufactured by Yasuda Seiki Co., Ltd. was used. Load 18.6Kg, heating rate 2 ℃
/ Min. (Judgment Criteria) ◯: 60 ° C. or more Δ: 50 ° C. or more and less than 60 ° C. ×: less than 50 ° C. Water dissolution time: The test piece was immersed in a water bath having a water temperature of 25 ° C. and a water volume of 2 l, and stirred at a rotation speed of 300 rpm. . (Judgment Criteria) ○: 100 minutes or more and less than 200 minutes △: 200 minutes or more and less than 250 minutes X: 250 minutes or more Bending test: Shimadzu Corporation Autograph AG-5
Use 000A. Used load cell 500 kg, fulcrum span 101.6 mm Bending speed 2.5 mm / min. (Judgment Criteria) Judgment based on the retention rate of bending strength after leaving at 20 ° C. and 65% RH for 10 days ○: 86% or more △: 80% or more and less than 85% ×: less than 80%
【0030】又、上記の無機系フィラーを配合したオキ
シアルキレン基含有PVAのペレットを射出成形機に供
給して下記の条件で射出成形し、図1の(イ)に示した
枝管付き円筒状の中子を成形した。
溶融温度:200〜230℃
射出圧力:1次1000kg/cm2
2次 800kg/cm2
1サイクル:28秒The oxyalkylene group-containing PVA pellets containing the above-mentioned inorganic filler were fed to an injection molding machine and injection-molded under the following conditions to give a cylindrical shape with a branch pipe shown in FIG. The core was molded. Melt temperature: 200 to 230 ° C. Injection pressure: Primary 1000 kg / cm 2 2 primary 800 kg / cm 2 1 cycle: 28 seconds
【0031】次に、上記で得た中子を金型内にセット
し、下記の条件で中子の周囲にポリプロピレン(樹脂温
度:250℃)を射出成形した。
溶融温度:240 〜250℃
射出圧力:1次 600kg/cm2
2次 600kg/cm2
1サイクル:30秒Next, the core obtained above was set in a mold, and polypropylene (resin temperature: 250 ° C.) was injection-molded around the core under the following conditions. Melting temperature: 240 to 250 DEG ° C. Injection pressure: Primary 600 kg / cm 2 2 primary 600 kg / cm 2 1 cycle: 30 seconds
【0032】射出成形後、金型から射出成形品を取り出
し、温度20℃の水中に静置して中子の溶解除去を行
い、以下の方法で溶解時間及び中空成形品の寸法精度を
求めた。又、中子作製後20℃、65%RHで10日間
放置した後の中子についても同様に射出成形を行い、溶
解時間及び中空成形品の寸法精度を求めた。After the injection molding, the injection-molded product was taken out of the mold and allowed to stand in water at a temperature of 20 ° C. to dissolve and remove the core, and the melting time and the dimensional accuracy of the hollow-molded product were determined by the following methods. . Further, injection molding was similarly performed on the core after leaving the core at 20 ° C. and 65% RH for 10 days, and the melting time and the dimensional accuracy of the hollow molded product were determined.
【0033】溶解除去時間(20℃、静置):中子の周
囲にポリプロピレンを射出成形して得た成形品1個を、
温度20℃の水50リットルの入った水槽中に浸漬し、
中子が完全に溶解するまでの時間を測定した。このよう
な試験を10回繰り返し、平均値を求めた。評価結果を
表1及び表2に示す。
中空成形品寸法精度:中子を溶解除去した後の中子成形
品の内筒部分の内径をノギスで測定した。この場合、図
2の(イ)に示した様に、等間隔の点a1〜a10の10
箇所について内筒内径を16等分して測定を行い、偏差
の変動幅を求め、内径の平均値に対する100分率表示
で示した。Dissolving / removing time (20 ° C., standing): One molded product obtained by injection molding polypropylene around the core,
Immerse in a water tank containing 50 liters of water at 20 ° C,
The time until the core was completely dissolved was measured. Such a test was repeated 10 times and the average value was calculated. The evaluation results are shown in Tables 1 and 2. Hollow molded product dimensional accuracy: The inner diameter of the inner cylinder part of the core molded product after the core was dissolved and removed was measured with a caliper. 10 In this case, as shown in FIG. 2 (b), equally spaced points a 1 ~a 10
The inner diameter of the inner cylinder was divided into 16 equal parts for measurement, the fluctuation range of the deviation was determined, and the percentage of the mean value of the inner diameter was displayed.
【0034】実施例2オキシアルキレン基含有PVA(A)
重量平均重合度:350
ポリオキシエチレンモノアリルエーテル(化1でXが
H)(オキシエチレンの平均縮合度は25)単位の共重
合割合:2.4モル%
ポリマー全体に占めるオキシアルキレン単位の割合:3
5重量%
酢酸ビニル成分のケン化度:90モル%Example 2 Weight-average degree of polymerization of PVA (A) containing oxyalkylene group : 350 Copolymerization ratio of polyoxyethylene monoallyl ether (X in formula 1 is H) (average degree of condensation of oxyethylene is 25) units: 2.4 mol% Ratio of oxyalkylene units in the whole polymer: 3
5% by weight Saponification degree of vinyl acetate component: 90 mol%
【0035】無機系フィラー(B) ガラス繊維 平均繊維径(μ):10 アスペクト比 :300 Inorganic filler (B) Glass fiber Average fiber diameter (μ): 10 Aspect ratio: 300
【0036】上記の樹脂を表1に示す配合比率で実施例
1と同様に中子用樹脂組成物の中子としての適性を評価
する為、ペレット状の樹脂組成物を得、該成形用ペレッ
トを射出成形機に供給して射出成形し、熱変形温度、水
溶解時間及び曲げ弾性率の評価を行った。In order to evaluate the suitability of the resin composition as shown in Table 1 for the core of the resin composition for cores in the same manner as in Example 1, a pelletized resin composition was obtained, and the pellets for molding were obtained. Was supplied to an injection molding machine for injection molding, and the heat deformation temperature, the water dissolution time and the flexural modulus were evaluated.
【0037】又上記の無機系フィラー(B)を配合した
オキシアルキレン基含有PVAのペレットをブロー成形
機に供給して下記の条件でブロー成形し、図1の(ロ)
に示した曲管形状の中子を成形した。
成形機 :株式会社タハラ製のブロー成形機
TPF−403
スクリュー径 40mmφ、L/D=24
シリンダー温度 :C1/C2/C3/C4/D(H)=
180/190/210/210/200(℃)
スクリュー回転数 :30rpm
モーター付加 :24アンペア
押出量 :8.7kg/hr
パリソン下降時間 :24秒
成形品の重量と肉厚:重量320g 、肉厚2.5mm
成形サイクル :型締め 約17秒、エアブロー
約20秒、トータル 約55秒The pellets of oxyalkylene group-containing PVA blended with the above-mentioned inorganic filler (B) are fed to a blow molding machine and blow molded under the following conditions, and the result is shown in FIG.
The bent core-shaped core shown in Fig. 3 was molded. Molding machine: Co. Tahara manufactured by blow molding machine TPF-403 Screw diameter 40mmφ, L / D = 24 cylinder temperature: C 1 / C 2 / C 3 / C 4 / D (H) =
180/190/210/210/200 (° C) Screw rotation speed: 30 rpm Motor addition: 24 amp extrusion rate: 8.7 kg / hr parison descent time: 24 seconds Weight and wall thickness of molded product: weight 320 g, wall thickness 2 0.5 mm molding cycle: Mold clamping for about 17 seconds, air blow
About 20 seconds, total about 55 seconds
【0038】次に、上記で得た中子を金型内にセット
し、実施例1と同じ条件で中子の周囲にポリプロピレン
を射出成形した。射出成形後、金型から射出成形品を取
り出し、温度70℃の水中にて通水条件下に中子の溶解
を行い、以下の方法により溶解時間及び中空成形品の寸
法精度を求めた。又、中子作製後20℃、65%RHで
10日間放置した後の中子についても同様に射出成形を
行い、溶解時間及び中空成形品の寸法精度を求めた。Next, the core obtained above was set in a mold, and polypropylene was injection-molded around the core under the same conditions as in Example 1. After injection molding, the injection-molded product was taken out of the mold, the core was dissolved in water at a temperature of 70 ° C. under flowing conditions, and the dissolution time and the dimensional accuracy of the hollow-molded product were determined by the following methods. Further, injection molding was similarly performed on the core after leaving the core at 20 ° C. and 65% RH for 10 days, and the melting time and the dimensional accuracy of the hollow molded product were determined.
【0039】溶解除去時間(70℃、通水):中子の周
囲にポリフェニレンエーテルを射出成形して得た成形品
1個を、温度70℃の水50リットルの入った水槽中に
浸漬し、ポンプにより水槽の水を1分間当たり50リッ
トルの割合で循環させ、中子が完全に溶解するまでの時
間を測定した。このような試験を10回繰り返し、平均
値を求めた。Dissolution and removal time (70 ° C., water flow): One molded product obtained by injection molding polyphenylene ether around the core was immersed in a water tank containing 50 liters of water at a temperature of 70 ° C. The water in the water tank was circulated at a rate of 50 liters per minute by a pump, and the time until the core was completely dissolved was measured. Such a test was repeated 10 times and the average value was calculated.
【0040】中空成形品寸法精度:中子を溶解除去した
後の中子成形品の内筒部分の内径をノギスで測定した。
この場合、図2の(ロ)に示した様に、等間隔の点b1
〜b10の10箇所について内筒内径を16等分して測定
を行い、偏差の変動幅を求め、内径の平均値に対する1
00分率表示で示した。評価結果は表1及び表2に示し
た。実施例3〜17及び比較例1〜3についても実施例
1及び実施例2に準じて評価を行った。評価結果は表1
及び表2に示した。Dimensional accuracy of hollow molded product: The inner diameter of the inner cylinder part of the core molded product after the core was dissolved and removed was measured with a caliper.
In this case, as shown in FIG. 2 (b), equally spaced points b 1
Perform measurement of the inner cylinder inner diameter 16 equal portions for 10 locations ~b 10, obtains the variation width of the deviation, 1 to the average value of the inner diameter
It is shown by the percentage display. The evaluation results are shown in Tables 1 and 2. Evaluations were performed for Examples 3 to 17 and Comparative Examples 1 to 3 according to Example 1 and Example 2. Table 1 shows the evaluation results.
And shown in Table 2.
【0041】実施例3オキシアルキレン基含有PVA(A)
重量平均重合度:350
ポリオキシエチレンモノアリルエーテル(化1でXが
H)(オキシエチレンの平均縮合度は20)単位の共重
合割合:2.0モル%
ポリマー全体に占めるオキシアルキレン単位の割合:2
0重量%
酢酸ビニル成分のケン化度:95モル%Example 3 Weight average degree of polymerization of oxyalkylene group-containing PVA (A) : 350 Copolymerization ratio of polyoxyethylene monoallyl ether (X in formula 1 is H) (average degree of condensation of oxyethylene is 20) units: 2.0 mol% Ratio of oxyalkylene units in the entire polymer: 2
0% by weight Saponification degree of vinyl acetate component: 95 mol%
【0042】無機系フィラー(B) ガラス繊維 平均繊維径(μ):8 アスペクト比 :320 Inorganic filler (B) Glass fiber Average fiber diameter (μ): 8 Aspect ratio: 320
【0043】実施例4オキシアルキレン基含有PVA(A)
重量平均重合度:350
ポリオキシエチレンモノアリルエーテル(化1でXがC
H3)(オキシエチレンの平均縮合度は22)単位の共
重合割合:2.2モル%
ポリマー全体に占めるオキシアルキレン単位の割合:2
0重量%
酢酸ビニル成分のケン化度:90モル%Example 4 Oxyalkylene group-containing PVA (A) Weight average degree of polymerization: 350 Polyoxyethylene monoallyl ether (where X is C
H 3 ) (The average degree of condensation of oxyethylene is 22) Copolymerization ratio of units: 2.2 mol% Ratio of oxyalkylene units in the entire polymer: 2
0% by weight Saponification degree of vinyl acetate component: 90 mol%
【0044】無機系フィラー(B) ガラス繊維 平均繊維径(μ):12 アスペクト比 :300 Inorganic filler (B) Glass fiber Average fiber diameter (μ): 12 Aspect ratio: 300
【0045】実施例5オキシアルキレン基含有PVA(A)
重量平均重合度:500
ポリオキシエチレンモノアリルエーテル(化1でXがC
H3)(オキシエチレンの平均縮合度は25)単位の共
重合割合:2.4モル%
ポリマー全体に占めるオキシアルキレン単位の割合:3
5重量%
酢酸ビニル成分のケン化度:90モル%Example 5 PVA (A) containing oxyalkylene group Weight average degree of polymerization: 500 Polyoxyethylene monoallyl ether (where X is C
H 3 ) Copolymerization ratio of units (average degree of condensation of oxyethylene is 25): 2.4 mol% Ratio of oxyalkylene units in the whole polymer: 3
5% by weight Saponification degree of vinyl acetate component: 90 mol%
【0046】無機系フィラー(B) ガラス繊維 平均繊維径(μ):10 アスペクト比 :300 Inorganic filler (B) Glass fiber average fiber diameter (μ): 10 Aspect ratio: 300
【0047】実施例6オキシアルキレン基含有PVA(A)
重量平均重合度:420
ポリオキシエチレンビニルエーテル(化2でXがH)
(オキシエチレンの平均縮合度は22)単位の共重合割
合:2.1モル%
ポリマー全体に占めるオキシアルキレン単位の割合:2
2重量%
酢酸ビニル成分のケン化度:92モル%Example 6 Weight-average degree of polymerization of oxyalkylene group-containing PVA (A) : 420 Polyoxyethylene vinyl ether (X in formula 2 is H)
(The average degree of condensation of oxyethylene is 22) Copolymerization ratio of units: 2.1 mol% Ratio of oxyalkylene units in the whole polymer: 2
2% by weight Saponification degree of vinyl acetate component: 92 mol%
【0048】無機系フィラー(B) ガラス繊維 平均繊維径(μ):10 アスペクト比 :300 Inorganic filler (B) Glass fiber Average fiber diameter (μ): 10 Aspect ratio: 300
【0049】実施例7
無機系フィラー(B)が平均フィラー径8μ、アスペク
ト比80の雲母である以外は実施例1と同様に評価を行
った。
実施例8
無機系フィラー(B)が平均フィラー径10μ、アスペ
クト比25のタルクである以外は実施例1と同様に評価
を行った。
実施例9
無機系フィラー(B)が平均フィラー径1μ、アスペク
ト比30のウイスカー状炭酸カルシウムである以外は実
施例1と同様に評価を行った。Example 7 Evaluation was made in the same manner as in Example 1 except that the inorganic filler (B) was mica having an average filler diameter of 8 μ and an aspect ratio of 80. Example 8 Evaluation was performed in the same manner as in Example 1 except that the inorganic filler (B) was talc having an average filler diameter of 10 μ and an aspect ratio of 25. Example 9 Evaluation was performed in the same manner as in Example 1 except that the inorganic filler (B) was a whisker-like calcium carbonate having an average filler diameter of 1 μ and an aspect ratio of 30.
【0050】実施例10
ポリマー全体に占めるオキシアルキレン単位の割合が6
5重量%であるオキシアルキレン基含有PVA(A)を
用いた以外は実施例1と同様に評価を行った。
実施例11
ポリマー全体に占めるオキシアルキレン単位の割合が
1.7重量%であるオキシアルキレン基含有PVA
(A)を用いた以外は実施例1と同様に評価を行った。
実施例12
重量平均重合度1100であるオキシアルキレン基含有
PVA(A)を用いた以外は実施例1と同様に評価を行
った。Example 10 The ratio of oxyalkylene units in the entire polymer was 6
Evaluation was performed in the same manner as in Example 1 except that 5% by weight of oxyalkylene group-containing PVA (A) was used. Example 11 PVA containing oxyalkylene groups in which the proportion of oxyalkylene units in the entire polymer is 1.7% by weight.
Evaluation was performed in the same manner as in Example 1 except that (A) was used. Example 12 Evaluation was performed in the same manner as in Example 1 except that the oxyalkylene group-containing PVA (A) having a weight average polymerization degree of 1100 was used.
【0051】実施例13
重量平均重合度75であるオキシアルキレン基含有PV
A(A)を用いた以外は実施例1と同様に評価を行っ
た。
実施例14
ケン化度58モル%のオキシアルキレン基含有PVA
(A)を用いた以外は実施例1と同様に評価を行った。
実施例15
オキシエチレンの平均縮合度が2であるオキシアルキレ
ン基含有PVA(A)を用いた以外は実施例1と同様に
評価を行った。Example 13 Oxyalkylene group-containing PV having a weight average polymerization degree of 75
Evaluation was performed in the same manner as in Example 1 except that A (A) was used. Example 14 Oxyalkylene group-containing PVA having a saponification degree of 58 mol%
Evaluation was performed in the same manner as in Example 1 except that (A) was used. Example 15 Evaluations were made in the same manner as in Example 1 except that the oxyalkylene group-containing PVA (A) having an average degree of condensation of oxyethylene of 2 was used.
【0052】実施例16
オキシエチレンの平均縮合度が115であるオキシアル
キレン基含有PVA(A)を用いた以外は実施例1と同
様に評価を行った。Example 16 Evaluations were made in the same manner as in Example 1 except that the oxyalkylene group-containing PVA (A) having an average degree of condensation of oxyethylene of 115 was used.
【0053】比較例1
無機系フィラー(B)の配合量が0重量%である以外は
実施例1と同様に評価を行った。
比較例2
ガラス繊維の配合量が70重量%である以外は実施例1
と同様に評価を行った。
比較例3
グリセリンを15重量%含有した重量平均重合度35
0、酢酸ビニル成分のケン化度90モル%のポリビニル
アルコールを用いた以外は実施例1と同様に評価を行っ
た。比較例
4ガラス繊維のアスペクト比が14である以外は実施例1
と同様に評価を行った。 Comparative Example 1 Evaluation was carried out in the same manner as in Example 1 except that the blending amount of the inorganic filler (B) was 0% by weight. Comparative Example 2 Example 1 except that the glass fiber content was 70% by weight.
It evaluated similarly to. Comparative Example 3 Weight average polymerization degree of 35 containing 15% by weight of glycerin
The evaluation was performed in the same manner as in Example 1 except that polyvinyl alcohol having a vinyl acetate component saponification degree of 90 mol% was used. Comparative Example 4 Example 1 except that the aspect ratio of the glass fiber was 14.
It evaluated similarly to.
【0054】[0054]
【表1】 [Table 1]
【0055】[0055]
【表2】
(注)α:中子作製後放置することなく中空成形品の製
造に使用。
β:中子作製後20℃、65%RH下で10日間放置し
た後中空成形品の製造に使用。
イ:枝付き円筒形状、ロ:曲管形状。[Table 2] (Note) α: Used for manufacturing hollow molded products without leaving after core production. β: Used to manufacture hollow molded products after leaving the cores at 20 ° C. and 65% RH for 10 days after manufacturing. A: Cylindrical shape with branches, B: Curved tube shape.
【0056】オキシアルキレン基を含有したポリビニル
アルコール系樹脂(A)にアスペクト比が20以上であ
る無機系フィラー(B)を1〜60重量%配合すること
により、かかる樹脂組成物からなる中子の剛性が吸湿等
により経時的に低下することが無く、耐熱性、水溶解速
度及び水溶解除去性に優れ、且つ仕上がり精度が良好な
中空成形品を得ることが出来る中子用樹脂組成物及びそ
れを用いた中空成形品の製造法が得られ大変有用であ
る。The polyvinyl alcohol resin (A) containing an oxyalkylene group has an aspect ratio of 20 or more.
That by inorganic filler (B) blending 1 to 60% by weight, such rigidity of the core of the resin composition without be decreased over time due to moisture absorption or the like, heat resistance, water dissolution rate and water solubility It is very useful to obtain a resin composition for cores which can obtain a hollow molded product having excellent removability and good finishing accuracy, and a method for producing a hollow molded product using the same.
【0057】[0057]
【図1】中子の形状を示した正面図である。FIG. 1 is a front view showing the shape of a core.
【図2】中空成形品の寸法精度の測定部位を示した説明
図である。FIG. 2 is an explanatory view showing a measurement site for dimensional accuracy of a hollow molded product.
a1〜a10:測定点 b1〜b10:測定点a 1 to a 10 : measurement points b 1 to b 10 : measurement points
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI C08K 3/34 C08K 3/34 (58)調査した分野(Int.Cl.7,DB名) C08L 29/10 B29C 33/52 B29C 45/26 C08F 16/18 C08K 3/26 C08K 3/34 ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI C08K 3/34 C08K 3/34 (58) Fields investigated (Int.Cl. 7 , DB name) C08L 29/10 B29C 33/52 B29C 45/26 C08F 16/18 C08K 3/26 C08K 3/34
Claims (5)
ルアルコール系樹脂(A)にアスペクト比が20以上で
ある無機系フィラー(B)を1〜60重量%配合するこ
とを特徴とする中子用樹脂組成物。1. A polyvinyl alcohol-based resin (A) containing an oxyalkylene group having an aspect ratio of 20 or more.
A resin composition for a core, comprising 1 to 60% by weight of an inorganic filler (B).
ルアルコール系樹脂(A)のケン化度が60〜100モ
ル%、オキシアルキレン基の平均縮合度が3〜100、
オキシアルキレン基の含有量が1〜60重量%、重量平
均重合度が100〜2000であることを特徴とする請
求項1記載の中子用樹脂組成物。2. The polyvinyl alcohol-based resin (A) containing an oxyalkylene group has a saponification degree of 60 to 100 mol%, and an average degree of condensation of the oxyalkylene group is 3 to 100,
The resin composition for a core according to claim 1, wherein the content of the oxyalkylene group is 1 to 60% by weight and the weight average degree of polymerization is 100 to 2000.
平均フレーク径が1〜30μであることを特徴とする請
求項1又は2記載の中子用樹脂組成物。3. The resin composition for cores according to claim 1, wherein the inorganic filler (B) has an average fiber diameter or an average flake diameter of 1 to 30 μm .
ガラス繊維、ウイスカー状炭酸カルシウムの中から少な
くとも1種類選ばれることを特徴とする請求項3記載の
中子用樹脂組成物。4. The inorganic filler (B) is talc, mica,
The resin composition for cores according to claim 3, wherein at least one kind is selected from glass fiber and whisker-like calcium carbonate.
囲に成形材料を射出成形してから中子を水で溶解除去し
て中空成形品を製造するにあたり、前記中子として請求
項1乃至4のいずれかに記載の中子用樹脂組成物を用い
ることを特徴とする中空成形品の製造法。5. A hollow core is produced by inserting a water-soluble core into a mold, injection molding a molding material around the core, and dissolving and removing the core with water to produce a hollow molded article. A method for producing a hollow molded article, which comprises using the resin composition for a core according to any one of claims 1 to 4.
Priority Applications (1)
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---|---|---|---|
JP13357494A JP3527538B2 (en) | 1994-05-23 | 1994-05-23 | Core resin composition and method for producing hollow molded article using the same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13357494A JP3527538B2 (en) | 1994-05-23 | 1994-05-23 | Core resin composition and method for producing hollow molded article using the same |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH07316379A JPH07316379A (en) | 1995-12-05 |
JP3527538B2 true JP3527538B2 (en) | 2004-05-17 |
Family
ID=15107999
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JP13357494A Expired - Lifetime JP3527538B2 (en) | 1994-05-23 | 1994-05-23 | Core resin composition and method for producing hollow molded article using the same |
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Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH08142064A (en) * | 1994-11-14 | 1996-06-04 | Tsutsui Plast:Kk | Production of resin product having complicated inner surface shape |
JPH10324784A (en) * | 1997-03-27 | 1998-12-08 | Kuraray Co Ltd | Thermally melting polyvinyl alcoholic resin composition |
JP4071846B2 (en) * | 1997-06-03 | 2008-04-02 | 大成プラス株式会社 | Method for producing plastic molded body |
JP2001293742A (en) * | 2000-04-11 | 2001-10-23 | Daisee Kogyo Kk | Method for manufacturing injection-molded article |
EP1234647A1 (en) * | 2001-02-23 | 2002-08-28 | Vantico AG | Method of producing models by using a water soluble core |
ES1067176Y (en) * | 2008-02-12 | 2009-02-01 | Campin David Aranda | PROTECTIVE COVER FOR DRINK CANS |
TW201522022A (en) * | 2013-12-02 | 2015-06-16 | A Pro Tech Co Ltd | Molding method for carbon fiber material of bicycle |
DE102017102565A1 (en) * | 2017-02-09 | 2018-08-09 | CG Rail - Chinesisch-Deutsches Forschungs- und Entwicklungszentrum für Bahn- und Verkehrstechnik Dresden GmbH | A method for producing a hollow carrier made of a fiber composite material, a core formed as a hollow body and its use and the use of the hollow carrier made of fiber composite material |
CN109115644B (en) * | 2018-08-29 | 2020-12-22 | 重庆三磊玻纤股份有限公司 | Method for detecting acetone dissolution rate of glass fiber |
WO2020217695A1 (en) * | 2019-04-26 | 2020-10-29 | 積水化学工業株式会社 | Core resin |
EP3984715B1 (en) | 2020-10-13 | 2023-11-15 | Technische Universität München | Fiber-reinforced soluble core and method for its manufacture |
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1994
- 1994-05-23 JP JP13357494A patent/JP3527538B2/en not_active Expired - Lifetime
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