JPS6289739A - Ethylenic resin composition for open-cell foam - Google Patents
Ethylenic resin composition for open-cell foamInfo
- Publication number
- JPS6289739A JPS6289739A JP22774485A JP22774485A JPS6289739A JP S6289739 A JPS6289739 A JP S6289739A JP 22774485 A JP22774485 A JP 22774485A JP 22774485 A JP22774485 A JP 22774485A JP S6289739 A JPS6289739 A JP S6289739A
- Authority
- JP
- Japan
- Prior art keywords
- foam
- open
- parts
- cell
- weight
- 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
Links
- 239000006260 foam Substances 0.000 title claims description 72
- 239000011342 resin composition Substances 0.000 title 1
- 239000000203 mixture Substances 0.000 claims abstract description 22
- 229920001400 block copolymer Polymers 0.000 claims abstract description 15
- 229920001296 polysiloxane Polymers 0.000 claims abstract description 15
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 4
- 125000003710 aryl alkyl group Chemical group 0.000 claims abstract description 4
- 125000003118 aryl group Chemical group 0.000 claims abstract description 4
- 125000003917 carbamoyl group Chemical group [H]N([H])C(*)=O 0.000 claims abstract description 4
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 4
- 238000000465 moulding Methods 0.000 claims abstract description 4
- 125000005702 oxyalkylene group Chemical group 0.000 claims abstract description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 14
- 239000005977 Ethylene Substances 0.000 claims description 14
- 229920005989 resin Polymers 0.000 claims description 14
- 239000011347 resin Substances 0.000 claims description 14
- 239000000463 material Substances 0.000 claims description 6
- 239000004604 Blowing Agent Substances 0.000 claims description 5
- 229920005992 thermoplastic resin Polymers 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims 2
- 238000000034 method Methods 0.000 abstract description 17
- 238000010521 absorption reaction Methods 0.000 abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 12
- 239000004088 foaming agent Substances 0.000 abstract description 6
- 239000004215 Carbon black (E152) Substances 0.000 abstract 1
- 229930195733 hydrocarbon Natural products 0.000 abstract 1
- 210000004027 cell Anatomy 0.000 description 24
- 238000010438 heat treatment Methods 0.000 description 15
- -1 polyethylene Polymers 0.000 description 13
- 238000005187 foaming Methods 0.000 description 11
- 239000000843 powder Substances 0.000 description 7
- 239000004698 Polyethylene Substances 0.000 description 6
- 229910052782 aluminium Inorganic materials 0.000 description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 6
- 239000008188 pellet Substances 0.000 description 6
- 229920000573 polyethylene Polymers 0.000 description 6
- 239000004743 Polypropylene Substances 0.000 description 5
- 239000012752 auxiliary agent Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 229920006267 polyester film Polymers 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 239000000654 additive Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 238000007796 conventional method Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 229910010272 inorganic material Inorganic materials 0.000 description 3
- 239000011147 inorganic material Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- OZAIFHULBGXAKX-UHFFFAOYSA-N 2-(2-cyanopropan-2-yldiazenyl)-2-methylpropanenitrile Chemical compound N#CC(C)(C)N=NC(C)(C)C#N OZAIFHULBGXAKX-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229920001971 elastomer Polymers 0.000 description 2
- 239000010408 film Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000002156 mixing Methods 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000003381 stabilizer Substances 0.000 description 2
- NBOCQTNZUPTTEI-UHFFFAOYSA-N 4-[4-(hydrazinesulfonyl)phenoxy]benzenesulfonohydrazide Chemical compound C1=CC(S(=O)(=O)NN)=CC=C1OC1=CC=C(S(=O)(=O)NN)C=C1 NBOCQTNZUPTTEI-UHFFFAOYSA-N 0.000 description 1
- ICGLPKIVTVWCFT-UHFFFAOYSA-N 4-methylbenzenesulfonohydrazide Chemical compound CC1=CC=C(S(=O)(=O)NN)C=C1 ICGLPKIVTVWCFT-UHFFFAOYSA-N 0.000 description 1
- 239000004156 Azodicarbonamide Substances 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- 239000004606 Fillers/Extenders Substances 0.000 description 1
- 229920010126 Linear Low Density Polyethylene (LLDPE) Polymers 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 239000011358 absorbing material Substances 0.000 description 1
- 229920000800 acrylic rubber Polymers 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 1
- 235000019399 azodicarbonamide Nutrition 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 125000000118 dimethyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000005038 ethylene vinyl acetate Substances 0.000 description 1
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000009477 glass transition Effects 0.000 description 1
- 238000007731 hot pressing Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 239000012774 insulation material Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical compound CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000005022 packaging material Substances 0.000 description 1
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000002985 plastic film Substances 0.000 description 1
- 229920006255 plastic film Polymers 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 229920005672 polyolefin resin Polymers 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 229920002545 silicone oil Polymers 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 239000011800 void material Substances 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
本発明はエチレン系樹脂を主成分とする単一工程で連続
気泡型発泡体を製造するための組成物に関する。さらに
詳しくは、エチレン系樹脂、発泡剤およびシリコーンブ
ロックコポリマーからなる、単一工程で連続気泡型発泡
体を製造するための組成物に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a composition for producing an open-cell foam in a single step, the main component of which is an ethylene resin. More particularly, the present invention relates to a composition for producing open-cell foam in a single step, comprising an ethylene resin, a blowing agent, and a silicone block copolymer.
本発明の目的は、通気性、吸水性、耐候性があるエチレ
ン系樹脂連続気泡型発泡体用組成物を提供するものであ
り、本発明の組成物により製造される発泡体は連続気泡
型であるため独立気泡型より柔軟で、風合い、触感が秀
れた発泡体であり、その製造方法の特色としては、一段
加熱法によって連続気泡型発泡体が得られる事であり、
加圧によって破泡する工程を必要としない。この発泡体
の用途はクッション、枕、マット、防寒衣、カーペット
の裏打ち、ボール、玩具、サポータ−あるいはフィルタ
ー等に緩衝材、断熱材、吸音材、または戸材として使用
される。An object of the present invention is to provide a composition for an ethylene resin open-cell foam that has air permeability, water absorption, and weather resistance. Because of this, it is a foam that is more flexible and has a better texture and feel than closed-cell foams, and its production method is characterized by the fact that open-cell foams can be obtained using a one-step heating method.
There is no need for a process of breaking bubbles by applying pressure. This foam is used as a cushioning material, a heat insulating material, a sound absorbing material, or a door material for cushions, pillows, mats, winter clothing, carpet linings, balls, toys, supporters, filters, etc.
現在エチレン系!ig脂からなる発泡体は断熱材、梱包
材、クッション材などとして多量使用されているが、そ
れらは殆んど独立気泡系発泡体であり、吸水性、通気性
などを必要とする用途には使用されていない。通気性を
有する連続気泡型発泡体も一部には見られるが、気泡径
が太きいものでキメが荒く、手触りが惑く、曲品価値の
低いものに限られる。一方ゴムあるいはポリウレタン系
連続気泡系発泡体は、紫外線あるいはオゾンにより急激
に劣化する。Currently ethylene-based! Foams made from Ig resin are used in large quantities as insulation materials, packaging materials, cushioning materials, etc., but most of them are closed-cell foams, and are not suitable for applications that require water absorption, breathability, etc. not being used. Although some open-cell foams with air permeability can be found, they are limited to those with large cell diameters, rough texture, and confusing texture, and low product value. On the other hand, rubber or polyurethane open-cell foams are rapidly degraded by ultraviolet rays or ozone.
エチレン系樹脂からなる従来の連続気泡型発泡体は、一
旦独立気泡型発泡体を製造し、これを加熱膨張させて発
泡する方法が知られているが、この方法によって得た発
泡体は「へたり」を生じ、弾力がなく、均一な破泡が困
難で気泡径も粗大である。これを解決するため一旦独立
気泡を成形後、これを加圧破泡する方法が開発されたが
、工程が二股階となる上、得られた発泡体は厚さが薄く
なり、気泡は遵幌化されているが、気泡膜は重なりあっ
て吸水性、通気性とも良好とは言えない。こ′れを改善
するために特公昭47−51695号においては、独立
気泡型発泡体をまずガラス転移温度付近またはそれ以下
の温度に冷却し、しかるのちにこれを圧縮して気泡膜を
破壊する方法が提案されたが、この方法ではポリエチレ
ンの場合、液体窒素等の高価々冷媒で冷却する事が必要
となり、装置的にも高価なものとなる。Conventional open-cell foams made of ethylene resin are produced by first producing closed-cell foams and then heating and expanding them. It has no elasticity, it is difficult to break the bubbles uniformly, and the bubble diameter is large. In order to solve this problem, a method was developed in which closed cells were first molded and then compressed to break them, but the process involved two steps, the thickness of the resulting foam was thin, and the cells became compliant. However, the bubble membranes overlap and cannot be said to have good water absorption or air permeability. In order to improve this, in Japanese Patent Publication No. 47-51695, the closed-cell foam is first cooled to a temperature near or below the glass transition temperature, and then compressed to destroy the cell membrane. A method has been proposed, but in the case of polyethylene, this method requires cooling with an expensive refrigerant such as liquid nitrogen, and the equipment is also expensive.
一方、特公昭55−42100号では一段工程で連続気
泡型のポリエチレン発泡体を得る方法としてポリエチレ
ンに架橋剤と共に無定形ポリプロピレンを相当多量に混
合し、一段加工、加熱プレス法が提案された。しかしこ
の方法では無定形ポリプロピレンを30〜50重量%混
合する事が好ましいとされ、20重量%以下では連続気
泡率が低くなるとしている。無定形ポリプロピレンは結
晶性ポリプロピレン製造時副生ずるもので、従来より利
用価値がなく、廃棄されていたものであるから、これを
活用する事は意味があるが、−万態定形ボリプロビレン
は室温でも粘着性を用する粘土状物であって、単独では
成形品を得る事が困難であり、従来から低価格発泡体の
増量材として少廿添加されていたもので、この特許に開
示されているように多量混合すると、発泡体の機械的特
性や感触に悪影響を及ぼす。On the other hand, Japanese Patent Publication No. 55-42100 proposed a one-step hot pressing method in which a fairly large amount of amorphous polypropylene was mixed with polyethylene together with a crosslinking agent as a method for obtaining an open-cell polyethylene foam in a one-step process. However, in this method, it is said that it is preferable to mix 30 to 50% by weight of amorphous polypropylene, and if it is less than 20% by weight, the open cell ratio will be low. Amorphous polypropylene is a by-product during the production of crystalline polypropylene, and it has no use value and has been discarded, so it makes sense to utilize it, but - universally shaped polypropylene is sticky even at room temperature. It is a clay-like material that uses adhesive properties and is difficult to make into molded products by itself, and has traditionally been added in small amounts as an extender to low-cost foams, as disclosed in this patent. When mixed in large amounts, the mechanical properties and feel of the foam are adversely affected.
特公昭54−65172号の技術自答はポリオレフィン
樹脂100重量部に対し無機物粉末を30〜300重蛍
部分散混合させた上で発泡させて独立気泡型発泡体とし
、これに変形を与えて破泡させる事を特色としている。The technical answer in Japanese Patent Publication No. 54-65172 is to mix 100 parts by weight of polyolefin resin with 30 to 300 parts of inorganic powder and foam it to form a closed cell foam, which is then deformed and ruptured. It is characterized by foaming.
しかもこの方法においては無機物界面とポリマーとの接
着力を積極的に低下せしめろような表面処理を無機物粉
末に施す事によって気泡の連通化は一層効果的であると
している。すなわちこの発泡体は単に破泡のために多量
の無機物を混合する事が必皆なのである。Moreover, in this method, the communication of air bubbles is made more effective by subjecting the inorganic powder to a surface treatment that actively reduces the adhesive force between the inorganic material interface and the polymer. In other words, this foam must be mixed with a large amount of inorganic material simply to break the foam.
その無機物の存在によって発泡体の機械的性質や触感が
本来のポリエチレン発泡体と異ったものとなる事は容易
に想像できる。そしてさらに重要なことは、連続気泡型
の発泡体をポリオレフィンで製造する事が如何に困難で
あるかを示すものである。It is easy to imagine that the presence of the inorganic material causes the mechanical properties and tactile sensation of the foam to differ from those of the original polyethylene foam. More importantly, it shows how difficult it is to produce open-cell foams from polyolefins.
本顛発明者らはこれらの先願技術が包含している多くの
問題点を解決するべく鋭意検討の結果、イ)出来るだけ
簡単な単一工程で、換言すれば破泡のための別工程を用
いる事なく、口)多量の添加剤によってエチレン系樹脂
自体の特色を失う事もkく、吸水性、耐候性および感触
のすぐれた工チレン系樹脂連続気泡型発泡体の製造方法
を開発し得たものであり、シリコーンブロックコポリマ
ーの少門添加によって破泡前後の気泡径を微細でかつ均
一度の高いものとする事ができた事を特色としている。As a result of intensive studies in order to solve the many problems contained in these prior art technologies, the present inventors found that (a) a single process as simple as possible, in other words, a separate process for foam breaking; We have developed a method for producing open-cell ethylene resin foam that has excellent water absorption, weather resistance, and texture without using a large amount of additives and without losing the characteristics of the ethylene resin itself. It is characterized by the fact that by adding a small amount of silicone block copolymer, the cell diameter before and after the bubble breakage can be made fine and highly uniform.
二)このため加熱炉内でのバッチ式製造方法のみならず
、エンドレス方式の製造が可能であり、ホ)発泡前の組
成物はペレット、粉末、フィルム、シートなど形状には
限定されない。2) Therefore, not only a batch-type production method in a heating furnace but also an endless-type production method is possible, and e) the composition before foaming is not limited to shapes such as pellets, powder, films, and sheets.
即ち、本発明はエチレン系樹脂100iIri部、発泡
剤1〜30重偕部からなる発泡性組成物に一般式
(上式において、Rは一価の炭化水素基、Xは−(0)
p −(Cn H* n O) t −R’R1はH
、アルキル、アリール、
アラルキル又はカルバミル基
から選択した基、
Pは0メは1
Yは(CnHtnO) t−R’
mは0から300
nは2から10
3は1から30
qは1から300
tは1から100
又、ここにおいて(CnH,no)
はオキシアルキレン基
又はかかる基の混合物である。)
から選択されたシリコーンブロックコポリマーα1〜5
重量部を添加したことを特徴とする、加熱成形後基材と
の離形性が優れ、均一で微細な気泡を有する熱可塑性樹
脂連続気泡型発泡体用組成物に関する。That is, the present invention provides a foamable composition comprising 100 parts of an ethylene resin and 1 to 30 parts of a blowing agent of the general formula (in the above formula, R is a monovalent hydrocarbon group, and X is -(0)).
p -(Cn H* n O) t -R'R1 is H
, alkyl, aryl, aralkyl or carbamyl group, P is 0 me is 1 Y is (CnHtnO) t-R' m is 0 to 300 n is 2 to 10 3 is 1 to 30 q is 1 to 300 t is from 1 to 100, and (CnH, no) is an oxyalkylene group or a mixture of such groups. ) Silicone block copolymers α1-5 selected from
The present invention relates to a thermoplastic resin open-cell foam composition which has excellent mold releasability from a base material after heat molding and has uniform and fine cells, in which the present invention has added parts by weight.
これらの本願発明の特色を以下に具体的に説明する。発
泡用組成物の形態を問わないという事は単にペレット、
粉末、フィルム、シートから連続気泡型発泡体を得る事
ができる事であり、さらに舊えはそれらを連続化したオ
ンライン成形をも可能とする。例えば薄層発泡シートを
得るためには薄いフィルム状に成形後加熱炉を通過させ
る事によって製造できる、また厚手シートの場合にはペ
レットを単層に散布した状態で加熱炉を通過させる事に
よって製造する事も可能であり、塊状発泡体を一旦製造
し、これをスライスする従来法より生産性を高かめる事
ができる。勿論これらの組成物を得る段階で押出機やニ
ーダ−1その他の混合方法をとるにしてもその温度を発
泡剤が実質的に分解しない温度である事が必要である。These features of the present invention will be specifically explained below. The form of the foaming composition does not matter, simply pellets,
It is possible to obtain open-cell foams from powders, films, and sheets, and it also enables continuous online molding of them. For example, to obtain a thin foam sheet, it can be manufactured by forming it into a thin film and passing it through a heating furnace, and in the case of a thick sheet, it can be manufactured by passing pellets spread in a single layer through a heating furnace. It is also possible to do this, and the productivity can be increased compared to the conventional method of once producing a bulk foam and slicing it. Of course, even if an extruder, kneader 1, or other mixing method is used at the stage of obtaining these compositions, the temperature must be such that the blowing agent does not substantially decompose.
また粉末状のエチレン系樹脂を用いて、これに粉末状ま
たは液状の他の添加成分を混合することによって粉末状
組成物を得、これを加熱することによって連続気泡型発
泡体とする事もできる。It is also possible to obtain a powder composition by using powdered ethylene resin and mixing other additive components in powder or liquid form, and by heating this, it is possible to make an open-cell foam. .
この発明によって得られた発泡体は微細で、かつ均一な
発l!2m造を持っている。これは独立気泡を一旦形成
し、これを破泡させる多くの従来法でも独立気泡の時に
は做細な気泡が破泡の段階で均一微細な連続気泡になら
ない事が知られており、また一段式で加熱膨張させる発
泡法では多くの粗大気泡を含んだ発泡体が得られるに過
ぎない。例えば実施例1に示すような気泡径平均80〜
120μというような微細気泡からなる連続気泡体を従
来の方法によって得る事は不可能であった。The foam obtained by this invention is fine and uniform! I have a 2m structure. It is known that even with many conventional methods in which closed cells are formed once and then broken, the tiny cells do not turn into uniform, fine, open cells at the stage of cell breaking. The foaming method in which the foam is heated and expanded only yields a foam containing many coarse cells. For example, as shown in Example 1, the average bubble diameter is 80~
It has been impossible to obtain open-cell bodies consisting of microscopic cells of 120 microns by conventional methods.
本発明の特徴の一つは耐候性の優れた発泡体が得られる
ことにある。例えば、6ケ月問屋外に放置しても、変色
や劣化のないものが得られる。One of the features of the present invention is that a foam with excellent weather resistance can be obtained. For example, even if it is left outdoors for six months, it will not discolor or deteriorate.
本発明においてエチレン系樹脂とは、エチレンを主成分
とする重合体であり、高圧法ポリエチレン、低圧法低密
度ポリエチレン、線状低密度ポリエチレン(LLDPE
)、エチレン−ビニルエステル共重合体、エチレン−ア
クリル酸アルキル共重合体、エチレン−プロピレン系共
重合体、エチレン−α・オレフィン系共l°合体、その
−他をいう。In the present invention, the ethylene resin is a polymer whose main component is ethylene, including high-pressure polyethylene, low-pressure low-density polyethylene, and linear low-density polyethylene (LLDPE).
), ethylene-vinyl ester copolymer, ethylene-alkyl acrylate copolymer, ethylene-propylene copolymer, ethylene-α/olefin copolymer, and others.
本発明において使用される発泡剤は、発泡温度が90℃
以上のものが望ましい。促進剤あるいは助剤を併用して
分解温度を調節することもできる。The foaming agent used in the present invention has a foaming temperature of 90°C.
The above is desirable. The decomposition temperature can also be adjusted by using a promoter or an auxiliary agent.
例として次のものが挙げられる。Examples include:
アゾビスイソブチロニトリル、ジアゾカーボンアミド(
助剤入)、P−トルエンスルホニルヒドラジド(助剤入
)、4.4’−オキシビス(ベンゼンスルホニルヒドラ
ジド)(助剤入)、n−へブタン、n−オクタン、n−
ノナン、n−デカン。Azobisisobutyronitrile, diazocarbonamide (
(with auxiliary agent), P-toluenesulfonyl hydrazide (with auxiliary agent), 4,4'-oxybis(benzenesulfonylhydrazide) (with auxiliary agent), n-hebutane, n-octane, n-
Nonane, n-decane.
本発明において使用されるシリコーンブロックコポリマ
ーは、一般式
%式%
(上式において、Rは一価の炭化水素基、Xは−(0)
−(CnHlnO)t−R’R’はH,アルキル、アリ
ール、
アラルキル又はカルバミル基
から選択した基、
Pは0又は1
Yは(Cn H! n O) t−R’mは0から30
0
nは2から10
Sは1から30
qは1から300
tは1から100
又、ここにおいて(CnH,no)
はオキシアルキレン基
又はかかる基の混合物である。)
から選択されたシリコーンブロックコポリマーであり、
その分子量は500以上のものが望ましい。The silicone block copolymer used in the present invention has the general formula % (in the above formula, R is a monovalent hydrocarbon group, and X is -(0)
-(CnHlnO)t-R'R' is a group selected from H, alkyl, aryl, aralkyl, or carbamyl group, P is 0 or 1 Y is (Cn H! n O) t-R'm is 0 to 30
0 n is from 2 to 10 S is from 1 to 30 q is from 1 to 300 t is from 1 to 100 In this case, (CnH, no) is an oxyalkylene group or a mixture of such groups. ) is a silicone block copolymer selected from
Its molecular weight is preferably 500 or more.
500より小さいと、加工中に揮発してしまう事がある
。分子量が20.000以上のものは、室温で固体にな
る場合があるが本発明には使用可能である。なお、固体
で分散が気になる場合には、溶剤に俗解して使用する事
も可能である。If it is less than 500, it may volatilize during processing. Those with a molecular weight of 20,000 or more may become solid at room temperature, but can be used in the present invention. In addition, if it is a solid and dispersion is a concern, it is also possible to use it as a solvent.
シリコーンブロックコポリマーを使用することにより、
組成物を加熱して発泡させ、冷却させた場合、得られた
発泡体と、金属板やプラスチック膜などとの接着性が弱
く、組成物を金属板上で発泡させた場合、冷却後、容易
に発泡体を金属板から引剥すことができる。By using silicone block copolymer,
When the composition is foamed by heating and then cooled, the resulting foam has poor adhesion to metal plates, plastic films, etc.; The foam can then be peeled off the metal plate.
本発明の発泡性組成%rの各成分の比率を以下に示す。The ratio of each component in the foamable composition %r of the present invention is shown below.
発泡剤は、エチレン系樹脂100重量部に対して1〜3
ON遺部必要である。The blowing agent is 1 to 3 parts by weight per 100 parts by weight of ethylene resin.
ON remains are necessary.
1重升部未満では、発泡の効果がほとんどなく、30重
量部より多いと、発泡時に無駄に大気中に逃散する発泡
剤分解物の量が増えるだけで、効率が悪い。If the amount is less than 1 part by weight, there is almost no foaming effect, and if it is more than 30 parts by weight, the amount of foaming agent decomposition products wastefully escaping into the atmosphere during foaming increases, resulting in poor efficiency.
シリコーンブロックコポリマーの量は、α5〜5重を部
必要である。0.5重針部より少ないと均一微細な構造
の気泡を与える効果がなく、5重量部より多いとにじみ
出しが著しく、発泡体の物性に悪影響を与える。The amount of silicone block copolymer required is 5 to 5 parts α. If the amount is less than 0.5 parts by weight, there will be no effect of providing cells with a uniform fine structure, and if it is more than 5 parts by weight, oozing will be significant and the physical properties of the foam will be adversely affected.
本発明において組成物には必要により、酸化安定剤、紫
外脚安定剤、無機光てん剤、顔料、碓燃剤、可塑剤、そ
の他の添加剤あるいは他の樹脂、ゴム類などを配合する
ことができる。In the present invention, the composition may contain oxidation stabilizers, ultraviolet leg stabilizers, inorganic photonic agents, pigments, flame retardants, plasticizers, other additives, other resins, rubbers, etc., if necessary. .
本発明において組成物を加熱する際の温度は、発泡に必
要な温g以上であり、具体的には約120〜250℃の
間である。In the present invention, the temperature at which the composition is heated is at least the temperature g required for foaming, specifically between about 120 and 250°C.
本発明において加熱後、発泡体を冷却することにより、
構造が固定化される。In the present invention, by cooling the foam after heating,
The structure is fixed.
冷却温度は50℃以下が望ましい。The cooling temperature is desirably 50°C or less.
加熱の方法としては、電気などの加熱ガス、鉄あるいは
アルミニウム々どの加熱された金属との直接あるいは間
接の接触、赤外線、バーナ、電熱などによる外部加熱の
ほか、高周波加熱などの内部加熱も適用できる。Heating methods include heating gas such as electricity, direct or indirect contact with heated metals such as iron or aluminum, external heating using infrared rays, burners, electric heat, etc., as well as internal heating such as high frequency heating. .
さらに1目的により常圧下で加熱することも、加圧下で
加熱することもできる。以下に実施例を挙げる。Furthermore, depending on the purpose, heating can be carried out under normal pressure or under pressure. Examples are given below.
実施例1
メルトインデックス20、酢酸ビニル成分28重量%の
エチレン−酢酸ビニル共重合体(日本ユニカー製)10
0部に対し、助剤入りアゾシカ−ボンアミド「セルマイ
クCAP149J(発泡温度125℃; 三協化成製)
10部、(a)式で表わされるシリコーンブロックコポ
リマー(日本ユニカーg; 1sooC8)1mをパ
ンツ(リーミキサーで80℃で5分間混練した後、ペレ
ット化した。Example 1 Ethylene-vinyl acetate copolymer with a melt index of 20 and a vinyl acetate component of 28% by weight (manufactured by Nippon Unicar) 10
0 parts, Azocica-bonamide with auxiliary agent "Cellmic CAP149J (foaming temperature 125°C; manufactured by Sankyo Kasei)
10 parts and 1 m of a silicone block copolymer represented by the formula (a) (Nippon Unicar G; 1sooC8) were kneaded at 80° C. for 5 minutes using a pant (Lee mixer), and then pelletized.
(−)Si(0((CHs )* S’i0)m (C
t也O)特(cm几0)!IC4馬〕。(-)Si(0((CHs)*S'i0)m (C
tyaO)Special(cm几0)! IC4 horse].
(a)
このペレットを厚さ1鰭のシートに圧縮成形したものを
ポリエステルフィルム上に置き、これをアルミ板に乗せ
て、190℃のオープン中で4分間加熱した後、取り出
して放冷した。得られた発泡体は、ポリエステルフィル
ムから容易にはく離した。この発泡体は厚さ7s++a
、気泡径80〜120μeの、均一でボイドがなく、微
細な気泡を有し、見掛は密度[1,10g/cIL3の
連続気泡型発泡体であった。最大吸水量はα7597c
m”であった。(a) This pellet was compression-molded into a 1-fin-thick sheet, placed on a polyester film, placed on an aluminum plate, heated in an open air at 190°C for 4 minutes, and then taken out and allowed to cool. The resulting foam was easily peeled off from the polyester film. This foam has a thickness of 7s++a
It had uniform, void-free, and fine cells with a cell diameter of 80 to 120 μe, and the appearance was an open-cell foam with a density of 1.10 g/cIL3. Maximum water absorption is α7597c
It was "m".
実施例2
実施例1と同様にして、アルミ板に直接シートを置いて
加熱した。発泡体のアルミ板からのはく離は容易であっ
た。発泡体の物性は実施例1で得られたものと同様であ
った。Example 2 In the same manner as in Example 1, a sheet was placed directly on an aluminum plate and heated. The foam was easily peeled off from the aluminum plate. The physical properties of the foam were similar to those obtained in Example 1.
比較例1
実施例1と同様にして、シリコーンブロックコポリマー
を使用しないで得た発泡体は、ポリエステルフィルムに
接着してしまい、引きはがしたところ、発泡体が、凝集
破壊した。発泡体は厚さ71it、気泡径1〜3 Bg
の、荒い気泡を有し、見掛は密度I111 l/am”
の連続気泡型発泡体であった。Comparative Example 1 A foam obtained in the same manner as in Example 1 without using a silicone block copolymer adhered to a polyester film, and when it was peeled off, the foam suffered cohesive failure. Foam thickness: 71it, cell diameter: 1-3 Bg
It has rough air bubbles with an apparent density of I111 l/am”
It was an open cell foam.
最大吸水量は0.66− g/cm”であった。The maximum water absorption amount was 0.66-g/cm''.
比較例2
実施例1と同様にして、シリコーンブロックコポリマー
を使用する代わりにジメチルシリコーン油(10,00
0CS p日本ユニカー製)を使用して発泡体は、ポリ
エステルフィルムに接着してしまい、引きはがしたとこ
ろ、発泡体が凝集破壊した。この発泡体は厚さ71m、
気泡径100〜200μ廼で、発泡体の断面積scm”
当たり、1個平均のボイド(Q、5〜1 m B )が
見られた。見掛は密度(L 109/CrrL”、最大
吸水量173 fi/cm”の連続気泡型発泡体であっ
た。Comparative Example 2 Similar to Example 1, but instead of using silicone block copolymer, dimethyl silicone oil (10,000
0CSp (manufactured by Nippon Unicar), the foam adhered to the polyester film, and when it was peeled off, the foam suffered cohesive failure. This foam is 71m thick.
With a cell diameter of 100-200μ, the cross-sectional area of the foam is cm”
An average of one void (Q, 5 to 1 mB) was observed per sample. The appearance was an open-cell foam with a density (L 109/CrrL" and a maximum water absorption of 173 fi/cm").
実施例3
実施例1と同様にして、添加剤として、ケイ酸マグネシ
ウム系粉末ミクロンホワイトφs、 o o 。Example 3 In the same manner as in Example 1, magnesium silicate powder Micron White φs, o o was used as an additive.
S(林化成製)20部を更に、加えて得た発泡体は、ポ
リエステルフィルムから容易にはく離した。The foam obtained by further adding 20 parts of S (manufactured by Hayashi Kasei) was easily peeled off from the polyester film.
この発泡体は厚さ7龍、気泡径280〜230μCの、
均一でボイドががいものであった。見掛は密度α131
1部cm”、最大吸水量α2711部cm”の連続気泡
型発泡体であった。This foam has a thickness of 7 mm and a bubble diameter of 280 to 230 μC.
It was uniform and void-free. The apparent density is α131
It was an open cell foam with a maximum water absorption α of 2711 parts cm".
実施例4
実施例3と同様にして、ステンレススチール板上に直接
シートを置いて加熱した。発泡体のステンレススチール
板からのはく離は容易であった。Example 4 In the same manner as in Example 3, a sheet was placed directly on a stainless steel plate and heated. Peeling of the foam from the stainless steel plate was easy.
比較例3
比較例2と同様にして、ステンレススチール板上に直接
シートを置いて加熱して得た発泡体をステンレススチー
ル板から引きはがそうとしたところ、発泡体が、凝集破
壊した。Comparative Example 3 In the same manner as in Comparative Example 2, when a foam obtained by placing a sheet directly on a stainless steel plate and heating it was attempted to be peeled off from the stainless steel plate, the foam suffered cohesive failure.
実施例5
メルトインデックス20.アクリル酸エチル成分20重
量%のエチレン−アクリル酸エチル共重合体(日本ユニ
カー3Q)100部に対し、アゾシカ−ボンアミド系発
泡剤「セルマイクCAP124J(発泡温度130℃:
三協化成製)5部、(b)式で表わされるシリコーン
ブロックコポリマー(日本ユニカー族; 500C8)
t5部をバンバリーミキサ−で80℃で5分間混練した
後、ペレット化した。Example 5 Melt index 20. To 100 parts of ethylene-ethyl acrylate copolymer (Nippon Unicar 3Q) containing 20% by weight of ethyl acrylate component, azocica-bonamide foaming agent "Celmic CAP124J (foaming temperature 130°C:
(manufactured by Sankyo Kasei) 5 parts, silicone block copolymer represented by formula (b) (Japan Unicar family; 500C8)
After kneading 5 parts of t in a Banbury mixer at 80°C for 5 minutes, it was pelletized.
(CHs )S i (0((CHs )t S 1o
t4(Ct山0)tscaH*]s (b)このペ
レットを厚さI II+のシートに圧縮成形したものを
銅板に乗せて、190°Cのオープン中で5分間加熱し
た後、取り出して放冷した。得られた発泡体は、銅板か
ら容易にはく離した。この発泡体は厚さ3.5顛、気泡
径100〜150μ2の、均一でボイドがなく、微細な
気泡を有し、見掛は密度α21.!9/clIL3の連
続気泡型発泡体であった。(CHs ) S i (0((CHs )t S 1o
t4 (Ct mountain 0) tscaH*]s (b) This pellet was compression molded into a sheet with a thickness of I II+, placed on a copper plate, heated in an open air at 190°C for 5 minutes, and then taken out and left to cool. did. The resulting foam was easily peeled off from the copper plate. This foam has a thickness of 3.5 mm, a bubble diameter of 100 to 150 μ2, uniform, void-free, and fine bubbles, and an apparent density of α21. ! It was an open cell foam of 9/clIL3.
最大吸水量はα25 、!i’/cm”であった。Maximum water absorption is α25! i'/cm".
実施例6
メルトインデックス(L4、密度0.894のエチレン
−αオレフィン共重合体DFDA−1158(ユニオン
カーバイド製)100部に対し、アゾジカ−ボンアミド
系発泡剤[セルマイクCAP 500 J(発泡温度1
50℃: 三協化成製)10部、(e)式で表わされる
シリコーンブロックコポリマー(日本ユニカー類;
tooocs)1部をバンバリーミキサ−で125℃で
10分間混練した後、ペレット化した。Example 6 An azodicarbonamide foaming agent [Celmic CAP 500 J (foaming temperature 1
50°C: 10 parts (manufactured by Sankyo Kasei), silicone block copolymer represented by formula (e) (Nippon Unicar;
1 part of the mixture was kneaded in a Banbury mixer at 125° C. for 10 minutes, and then pelletized.
(CL )St(O((C山)msio)s(Ct山0
)1゜(C,ル0)1゜QL)m(c)
このペレットを厚さ2 MNのシートに圧縮成形したも
のをアルミ板に乗せて、200℃のマツフル炉で5分間
加熱した後、取り出して放冷した。得られた発泡体は、
アルミ板から容易にはく離した。(CL)St(O((C mountain)msio)s(Ct mountain 0
)1゜(C, LE0)1゜QL)m(c) This pellet was compression-molded into a sheet with a thickness of 2 MN, placed on an aluminum plate, and heated in a Matsufuru furnace at 200°C for 5 minutes. It was taken out and left to cool. The obtained foam is
It was easily peeled off from the aluminum plate.
この発泡体は厚さ8m、気泡径150〜200μのの、
均一でボイドがなく、見掛は密度0.2411/am”
の連続気泡型発泡体であった。最大吸水量は0.299
77cm”であった。This foam has a thickness of 8m and a cell diameter of 150-200μ.
Uniform and void-free, with an apparent density of 0.2411/am”
It was an open cell foam. Maximum water absorption is 0.299
It was 77 cm.
実施例7
呆施例6と同様にして、DFDA−1138の代りにメ
ルトインデックス25、密度0.9145のポリエチレ
ンDNDJ−0405R(日本ユニカー類)を使用して
、発泡体を得た。この発泡体は厚さ8真尻、気泡径20
0〜500μC1見掛は密度0.289/Cm”の連続
気泡型発泡体であった。最大吸水量は0.5697の3
であった。Example 7 A foam was obtained in the same manner as in Example 6, using polyethylene DNDJ-0405R (Nippon Unicar) having a melt index of 25 and a density of 0.9145 instead of DFDA-1138. This foam has a thickness of 8 mm and a cell diameter of 20 mm.
0~500μC1 It was an open-cell foam with an apparent density of 0.289/Cm. The maximum water absorption was 0.5697.
Met.
r″−−t
; 1
代理人の氏名 倉 内 基 弘 ′同
風 間 弘 志 、 1(、〜/
手続補正書
昭和61年2月4日
特許庁長官 宇 買 道 部 殿
事件の表示 昭和60年特 願第227744Fi発明
の名称 エチレン系樹脂連続気泡型発泡体用組成物補
正をする者
事件との関係 特許出願人名 称
日本ユニカー株式会社r″--t ; 1 Name of agent: Motohiro Kurauchi
Hiroshi Kazama, 1 (,~/ Procedural amendment dated February 4, 1985, Director General of the Patent Office, Ubuya Michibe Case, 1985 Patent Application No. 227744Fi, Name of the invention, For ethylene resin open-cell foams Relationship with the composition amendment case Patent applicant name Nippon Unicar Co., Ltd.
Claims (1)
らなる発泡性組成物に一般式 ▲数式、化学式、表等があります▼ 又は ▲数式、化学式、表等があります▼ (上式において、Rは一価の炭化水素基、 Xは−(O)_p−(CnH_2_nO)_t−R^1
R^1はH、アルキル、アリール、 アラルキル又はカルバミル基 から選択した基、 Pは0又は1 Yは(CnH_2nO)_t−R^1 mは0から300 nは2から10 sは1から30 qは1から300 tは1から100 又、ここにおいて(CnH_2nO)は オキシアルキレン基 又はかかる基の混合物である。) から選択されたシリコーンブロツクコポリマー0.1〜
5重量部を添加したことを特徴とする加熱成形後基材と
の離形性が優れ均一で微細な気泡を有する熱可塑性樹脂
連続気泡型発泡体用組成物。[Claims] A foamable composition consisting of 100 parts by weight of ethylene resin and 1 to 30 parts by weight of a blowing agent has a general formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ or ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (In the above formula, R is a monovalent hydrocarbon group, X is -(O)_p-(CnH_2_nO)_t-R^1
R^1 is a group selected from H, alkyl, aryl, aralkyl, or carbamyl group, P is 0 or 1 Y is (CnH_2nO)_t-R^1 m is 0 to 300 n is 2 to 10 s is 1 to 30 q is 1 to 300; t is 1 to 100; and (CnH_2nO) is an oxyalkylene group or a mixture of such groups. ) Silicone block copolymer selected from 0.1 to
5 parts by weight of a thermoplastic resin open-cell foam composition having excellent mold releasability from a base material after heat molding and having uniform and fine cells.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22774485A JPS6289739A (en) | 1985-10-15 | 1985-10-15 | Ethylenic resin composition for open-cell foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP22774485A JPS6289739A (en) | 1985-10-15 | 1985-10-15 | Ethylenic resin composition for open-cell foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6289739A true JPS6289739A (en) | 1987-04-24 |
| JPH055255B2 JPH055255B2 (en) | 1993-01-21 |
Family
ID=16865688
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP22774485A Granted JPS6289739A (en) | 1985-10-15 | 1985-10-15 | Ethylenic resin composition for open-cell foam |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6289739A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60124632A (en) * | 1983-12-09 | 1985-07-03 | Nippon Yunikaa Kk | Production of open-cellular crosslinked ethylene resin foam |
-
1985
- 1985-10-15 JP JP22774485A patent/JPS6289739A/en active Granted
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS60124632A (en) * | 1983-12-09 | 1985-07-03 | Nippon Yunikaa Kk | Production of open-cellular crosslinked ethylene resin foam |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH055255B2 (en) | 1993-01-21 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |