JPS6289738A - Ethylenic resin composition for open-cell foam - Google Patents
Ethylenic resin composition for open-cell foamInfo
- Publication number
- JPS6289738A JPS6289738A JP22774385A JP22774385A JPS6289738A JP S6289738 A JPS6289738 A JP S6289738A JP 22774385 A JP22774385 A JP 22774385A JP 22774385 A JP22774385 A JP 22774385A JP S6289738 A JPS6289738 A JP S6289738A
- Authority
- JP
- Japan
- Prior art keywords
- foam
- open
- silicone oil
- cell
- parts
- 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 abstract description 53
- 239000011342 resin composition Substances 0.000 title 1
- 239000000203 mixture Substances 0.000 claims abstract description 18
- 229920005989 resin Polymers 0.000 claims abstract description 15
- 239000011347 resin Substances 0.000 claims abstract description 15
- 229920002545 silicone oil Polymers 0.000 claims abstract description 13
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 4
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims abstract description 4
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 15
- 239000005977 Ethylene Substances 0.000 claims description 15
- 239000004604 Blowing Agent Substances 0.000 claims description 6
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 19
- 238000010521 absorption reaction Methods 0.000 abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 10
- 239000004088 foaming agent Substances 0.000 abstract description 5
- 230000035699 permeability Effects 0.000 abstract description 4
- 210000004027 cell Anatomy 0.000 description 23
- 238000010438 heat treatment Methods 0.000 description 12
- -1 polyethylene Polymers 0.000 description 12
- 238000005187 foaming Methods 0.000 description 9
- 239000004698 Polyethylene Substances 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
- 229910052782 aluminium Inorganic materials 0.000 description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 5
- 239000012752 auxiliary agent Substances 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 239000000843 powder Substances 0.000 description 4
- 239000000654 additive Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 229910010272 inorganic material Inorganic materials 0.000 description 3
- 239000011147 inorganic material Substances 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229920000435 poly(dimethylsiloxane) Polymers 0.000 description 3
- 229920000642 polymer Polymers 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
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000002411 adverse Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 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
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 239000004156 Azodicarbonamide Substances 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
- 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
- 230000000996 additive effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 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
- 230000009172 bursting Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 239000003431 cross linking reagent Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 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
- 239000012528 membrane Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000013518 molded foam Substances 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
- 230000000704 physical effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 1
- 229920006267 polyester film 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
- 239000002356 single layer Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000004381 surface treatment Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 239000000326 ultraviolet stabilizing agent Substances 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (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
油からなる、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 based on ethylene resin for producing open-cell foam in a single step. More specifically, the present invention relates to a composition for producing an open-cell foam in a single step, comprising an ethylene resin, a blowing agent, and a silicone oil.
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、未発・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p材として
使用される。The object of the present invention is to provide a composition for ethylene resin open-cell foam that has good air permeability, water absorption, and weather resistance. Because it is a cellular foam, it is more flexible than a closed cell foam, and has a superior texture and feel.The manufacturing method is characterized by:
An open-cell foam can be obtained by a one-stage heating method, and there is no need for a process of bursting the foam by applying pressure. This foam is used as a cushioning material, a heat insulating material, a sound absorbing material, or a p-material for cushions, pillows, mats, winter clothing, carpet linings, balls, toys, supporters, filters, etc.
現在エチレン系樹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、気泡径が大
きいものでキメが荒く、手触りが悪く、商品価値の低い
ものに限うレる。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, foams made of ethylene resin are used as insulation materials, packaging materials,
Although they are used in large quantities as cushioning materials, most of them are closed-cell foams and are not used for applications that require water absorption, breathability, etc. Although some open-cell foams with air permeability can be found, they are limited to those with large cell diameters, rough texture, poor texture, and low commercial 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
、工程が二段階となる上、得られた発泡体は厚さが薄く
なり、気泡は連続化されているが、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47−31695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、液体窒素等の高価な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 broken by pressure, but the process was two-step, the resulting foam was thinner, and the cells became open. However, the bubble membranes overlap and cannot be said to have good water absorption or air permeability. To improve this, Japanese Patent Publication No. 47-31695 proposes a method in which 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. Although this method has been proposed, in the case of polyethylene, it is necessary to cool it with an expensive refrigerant such as liquid nitrogen, and the equipment becomes 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ンンを相当多量に混合
し、一段加圧、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、−万態定形ポリプロピレンは
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
量材として少量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 pressurizing and 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 substance that uses the properties of clay, and it is difficult to obtain molded products by itself, and it has traditionally been added in small amounts as an extender to low-cost foams, as disclosed in this patent. Mixing in large quantities will adversely affect the mechanical properties and feel of the foam.
特公昭54−63172号の技術内容はポリオレフィン
樹脂100重量部に対し無機物粉末を30〜300重量
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 content of Japanese Patent Publication No. 54-63172 is to disperse and mix 30 to 300 parts by weight of inorganic powder with 100 parts by weight of polyolefin resin, foam it to form a closed-cell foam, and then deform it to break the foam. It is characterized by
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る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要なのである。Moreover, in this method, it is said that the communication of air bubbles is made even 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 requires mixing 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.
本願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、換言すれは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なく、吸水性、耐候性および感触
のすぐれたエ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、シリコーン油の少量添加によ
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。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。The inventors of the present application have conducted intensive studies to solve the many problems contained in these prior art technologies, and have found that (a) a single process as simple as possible, in other words, a separate process for breaking the bubbles; Developed a method for producing open-cell ethylene resin foam that has excellent water absorption, weather resistance, and texture without losing the characteristics of the ethylene resin itself due to large amounts of additives. It is characterized by the fact that by adding a small amount of silicone oil, the diameter of the bubbles before and after breaking can be made fine and highly uniform. 2) For this reason, it is possible to produce not only a batch method in a heating furnace but also an endless method, and e) the composition before foaming can be made into pellets,
The shape is not limited to powder, film, sheet, etc.
即ち本発明はエチレン系樹脂100重量部、発泡剤1〜
30重量部からなる発泡性組成物に一般式
%式%
(′ただし、Rは、アルキル基、フェニル基、および水
素から選ばれる基でありすべてのRが同−基であっても
、一部のRがべつの基であってもよく、nは1〜10,
000の整数である。)で表わされるシリコーン油(l
lL1〜5重量部を添加したことを特徴とする、均一で
微細な気泡を有するエチレン系樹脂連続気泡型発泡体用
組成物に関する。That is, in the present invention, 100 parts by weight of ethylene resin, 1 to 10 parts by weight of blowing agent,
% ('However, R is a group selected from an alkyl group, a phenyl group, and hydrogen, and even if all R's are the same group, some R may be another group, n is 1 to 10,
It is an integer of 000. ) silicone oil (l
The present invention relates to an ethylene resin open-cell foam composition having uniform and fine cells, characterized in that 1 to 5 parts by weight of 1L is added.
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々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、さらに言えば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
ーグー、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 furthermore, it is also possible to form them continuously on-line. 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, Ni-Goo, or other mixing method is used to obtain 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k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 use powdered ethylene resin and mix other additive components in powdered or liquid form to obtain a powdered composition, which is then heated to form an open-cell foam. can.
この発明によって得られた発泡体は微細で、かつ均一な
発泡材造を持っている。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微
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100〜2
00μ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 has a fine and uniform foam structure. Once this forms closed cells,
It is known that even with many conventional methods for breaking these bubbles, when the cells are closed, fine cells do not become uniform, fine, open cells at the stage of cell breaking. Only a foam containing air cells is obtained. For example, as shown in Example 1, the average bubble diameter is 100 to 2.
It has been impossible to obtain open-cell bodies consisting of microscopic cells of 00 μm size using conventional methods.
本発明の特徴の一つは耐候性のft′Lだ発泡体が得ら
れることにある。例えば、6ケ月Iv1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 it provides a weather resistant ft'L foam. For example, even if it is left outdoors for 6 months, it will not change color 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、練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1合体、エチレン−α・オレフィン系共重合体、その
他をいう。In the present invention, the ethylene resin is a polymer whose main component is ethylene, and includes high-pressure polyethylene, low-pressure low-density polyethylene, and kneaded low-density polyethylene (LLDPE).
), ethylene-vinyl ester copolymer, ethylene-
Refers to alkyl acrylate copolymers, ethylene-propylene copolymers, ethylene-α/olefin copolymers, and others.
本発明において使用される発泡剤は、発泡温度が90°
C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 or higher 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−)ルエンスルホニルヒドラジド(助剤入
) 、44 +−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-) luenesulfonyl hydrazide (with auxiliary agent), 44 +-oxybis(benzenesulfonyl hydrazide) (with auxiliary agent), n-hebutane, n-octane, n
-nonane, n-decane.
本発明に使用されるシリコーン油は、一般式RI 5i
O−(R,SiO)n−8iRm で表わされるもの
であり、ここにおいて、Rは、アルキル基、フェニル基
、および水素から選ばれた基であり、すべてのRが同−
基であっても、一部のRが別の基であってもよい。The silicone oil used in the present invention has the general formula RI 5i
O-(R,SiO)n-8iRm, where R is a group selected from an alkyl group, a phenyl group, and hydrogen, and all R are the same-
group, or some R's may be different groups.
上記において、nは1〜10,000であり、100〜
t000が好ましい。In the above, n is 1 to 10,000, and 100 to
t000 is preferred.
本発明の発泡性組成物の各成分の比率を以下に示す。The ratio of each component of the foamable composition 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量部必要である。The blowing agent is 1 to 3 parts by weight per 100 parts by weight of ethylene resin.
ON amount part is required.
1重量部未滴では、発泡の効果がほとんどなく3ON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
分解物の債が増えるだけで、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 3 parts by weight, the amount of decomposed products of the blowing agent that wastefully escapes into the atmosphere during foaming increases, resulting in poor efficiency.
シリコーン油の量は、Q、1〜Stt部必要である。0
.1重量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 oil required is Q, 1 to Stt parts. 0
.. If it is less than 1 part by weight, it will not have the effect of providing bubbles with a uniform fine structure, and if it is more than 5 parts by weight, oozing will be noticeable.
Adversely affects the physical properties of the foam.
本発明において組成物には必WKより、酸化安定剤、紫
外線安定剤、無機光てん剤、顔料、難燃剤、可塑剤、そ
の他の添加剤あるいは他のw脂、ゴム類などを配合する
ことができる。In the present invention, the composition must contain oxidation stabilizers, ultraviolet stabilizers, inorganic photonic agents, pigments, flame retardants, plasticizers, other additives, other waxes, rubbers, etc. can.
本発明において組成物を加熱する際の温度は、発泡に必
要な温度以上であり、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 higher than the temperature required for foaming, and specifically is 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Kより、
構造が固定化される。In the present invention, the foam is cooled after heating.
The structure is fixed.
冷却m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
アルミニウムな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、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 performed under normal pressure or under increased 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重シチの
エチレン−酢酸ビニル共重合体(日本ユニカーfi)1
00部に対し、助剤入すアゾジカーボンアミド「セルマ
イクCAP149J(発泡温度125℃; 三協化成製
)10部、NUC−シリコーンオイルL−45(日本ユ
ニカー製メチルシリコーン油; 10,0OOC8;
n=750)1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。このペレットを厚
さ1n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、1900Cの
オープン中で4分間加熱した後、取り出して放冷した。Example 1 Ethylene-vinyl acetate copolymer with a melt index of 20 and a vinyl acetate component of 28 polymers (Nippon Unicar fi) 1
00 parts, 10 parts of azodicarbonamide "Celmic CAP149J (foaming temperature 125°C; manufactured by Sankyo Kasei), which contains an auxiliary agent, NUC-silicone oil L-45 (methyl silicone oil manufactured by Nippon Unicar; 10.0OOC8;
n=750) was kneaded in a Banbury mixer at 80° C. for 5 minutes, and then pelletized. The pellets were compression-molded into a sheet with a thickness of 1 nm, placed on a polyester film, placed on an aluminum plate, heated in an open air at 1900 C for 4 minutes, then taken out and allowed to cool.
得られた発泡体は厚さ7 m 、その#魯とんどが気泡
径100〜200μρの気泡からなり、見掛は密度0.
1097cm、”の連続気泡型発泡体であった。最大吸
水量は0.739部cm”であった。The obtained foam has a thickness of 7 m, most of which consists of cells with a cell diameter of 100 to 200 μρ, and an apparent density of 0.
It was an open-cell foam with a diameter of 1097 cm.The maximum water absorption amount was 0.739 parts cm.
比較例1
実施例1と同様にして、シリコーン油を使用しないで得
た発泡体は、厚さ7 fm 、気泡径1〜3間Sの、荒
い気泡を有し、見掛は密度0.11 /i/crIL”
の連続気泡型発泡体であった。最大吸水量は0.66E
/cm”であツタ。Comparative Example 1 A foam obtained in the same manner as in Example 1 without using silicone oil had a thickness of 7 fm, rough cells with a cell diameter of 1 to 3 S, and an apparent density of 0.11. /i/crIL”
It was an open cell foam. Maximum water absorption is 0.66E
/cm” and ivy.
実施例2
メルトインデックス20、アクリル酸エチル成分20
N H%のエチレン−アクリル酸エチル共重合体(日本
ユニカー1f!りIoo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13
0℃; 三協化成製)5部、NUC−シリコーンオイル
L−45(日本ユニカー製メチルシリコーン油; t
ooocs; n=244)1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。この
ペレットを厚さ2龍のシートに圧縮成形した。このシー
トをアルミ板に乗せて、190℃のオープン中で5分間
加熱した後、取り出して放冷した。得られた発泡体は厚
さ6−5 m麓、気泡径100〜250μeの気泡から
なり、見掛は密度11221!/am”の連続気+!2
型発泡体であった。最大吸水量はα23y/α1であっ
た。Example 2 Melt index 20, ethyl acrylate component 20
NH% of ethylene-ethyl acrylate copolymer (Nippon Unicar 1F!Ioo part), Azocica-bonamide foaming agent [Celmic CAP124J (foaming temperature 13
0°C; Sankyo Kasei) 5 parts, NUC-silicone oil L-45 (Nippon Unicar methyl silicone oil; t
ooocs; n=244) was kneaded in a Banbury mixer at 80° C. for 5 minutes, and then pelletized. The pellets were compression molded into a sheet with a thickness of 2 mm. This sheet was placed on an aluminum plate and heated in an open air at 190°C for 5 minutes, then taken out and left to cool. The obtained foam is 6-5 m thick, consists of cells with a cell diameter of 100-250 μe, and has an apparent density of 11221! /am” continuous energy +!2
It was a molded foam. The maximum water absorption amount was α23y/α1.
実施例3
メルトインデックスα4、密i[L894のエチレン−
αオレフィン共重合体DFDA−1138(ユニオンカ
ーバイドfi)100部に対し、アゾシカ−ボンアミド
系発泡剤[セルヶイクCAP501]J(発泡温度15
0℃; 三協化成製)10音Is、NUC−シリコーン
オイルL−45(日本ユニカー製メチルシリコーン油;
1000C8; n=244)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。このペレットを厚さ2朋のシートに圧縮成形した
ものをアルミ板に乗せて、2oo℃のマツフル炉で5分
間加熱した後、取り出して放冷した。Example 3 Melt index α4, density i [L894 ethylene-
To 100 parts of α-olefin copolymer DFDA-1138 (Union Carbide fi), Azocica-bonamide foaming agent [Celgaik CAP501] J (foaming temperature 15
0°C; manufactured by Sankyo Kasei) 10 sound Is, NUC-silicone oil L-45 (methyl silicone oil manufactured by Nippon Unicar;
1000C8; n=244) was kneaded in a Banbury mixer at 125°C for 10 minutes, and then pelletized. The pellets were compression-molded into a sheet with a thickness of 2 mm, placed on an aluminum plate, heated in a Matsufuru furnace at 20° C. for 5 minutes, and then taken out and allowed to cool.
得られた発泡体は、アルミ板から芥易にはく離した。こ
の発泡体は厚さ8龍、気泡径100〜300μ饅の気泡
からなり、見掛は密度0.2597α1の連続気泡型発
泡体であった。最大吸水量はQ、3411/cm”であ
った。The obtained foam was easily peeled off from the aluminum plate. This foam had a thickness of 8 mm, consisted of cells with a cell diameter of 100 to 300 μm, and had an apparent open-cell foam with a density of 0.2597α1. The maximum water absorption amount was Q, 3411/cm''.
実施例4
実施例3と同様にして、DFDA−1138の代わりに
メルトインデックス25、密度α9145のポリエチレ
ンDNDJ −040sR(日本ユニカー類)を使用し
て、発泡体を得た。この発泡体は浮さ8m11.気泡径
150〜SOOμg、見掛は密度[L 26 g/l”
の連続気泡型発泡体であった。Example 4 A foam was obtained in the same manner as in Example 3, using polyethylene DNDJ-040sR (Nippon Unicar) having a melt index of 25 and a density of α9145 instead of DFDA-1138. This foam has a float of 8m11. Bubble diameter 150~SOOμg, apparent density [L 26 g/l”
It was an open cell foam.
最大吸水量は0.521/■1であった。The maximum water absorption amount was 0.521/■1.
代理人の氏名 倉 内 基 弘 l)゛・−冒L1
手続袖正書
昭和61年2月4日
補正をする名
事件との関係 特許i1願人名称
日本ユニカー株式会社Name of agent: Motohiro Kurauchi l)゛・-该L1 Relationship to the famous case for which the procedure sleeve is amended on February 4, 1986 Patent i1 Name of applicant Nippon Unicar Co., Ltd.
Claims (1)
らなる発泡性組成物に一般式 R_3SiO−(R_2SiO_n−SiR_3(ただ
し、Rは、アルキル基、フエニル基、および水素から選
ばれる基であり、すべてのRが同一基であつても、一部
のRがべつの基であつてもよく、nは1〜10,000
の整数である。)で表わされるシリコーン油0.1〜5
重量部を添加したことを特徴とする、均一で微細な気泡
を有するエチレン系樹脂連続気泡型発泡体用組成物。[Scope of Claims] A foamable composition comprising 100 parts by weight of an ethylene resin and 1 to 30 parts by weight of a blowing agent has the general formula R_3SiO-(R_2SiO_n-SiR_3 (where R is an alkyl group, a phenyl group, and hydrogen). It is a selected group, and all R's may be the same group or some R's may be different groups, and n is 1 to 10,000.
is an integer. ) silicone oil 0.1-5
1. An open-cell ethylene resin foam composition having uniform and fine cells, characterized in that the composition contains parts by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP22774385A JPS6289738A (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 |
---|---|---|---|
JP22774385A JPS6289738A (en) | 1985-10-15 | 1985-10-15 | Ethylenic resin composition for open-cell foam |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6289738A true JPS6289738A (en) | 1987-04-24 |
JPH055254B2 JPH055254B2 (en) | 1993-01-21 |
Family
ID=16865673
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP22774385A Granted JPS6289738A (en) | 1985-10-15 | 1985-10-15 | Ethylenic resin composition for open-cell foam |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6289738A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5236898A (en) * | 1975-09-16 | 1977-03-22 | Miyata Kogyo Kk | Liquid fire extinguishing agent |
JPS5867734A (en) * | 1981-10-20 | 1983-04-22 | Nippon Yunikaa Kk | Production of foamed product of crosslinked ethylenic resin with continuous foam structure |
JPS60109804A (en) * | 1983-10-03 | 1985-06-15 | ゼネラル・エレクトリツク・カンパニイ | Method of blending high-viscosity silicon |
-
1985
- 1985-10-15 JP JP22774385A patent/JPS6289738A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5236898A (en) * | 1975-09-16 | 1977-03-22 | Miyata Kogyo Kk | Liquid fire extinguishing agent |
JPS5867734A (en) * | 1981-10-20 | 1983-04-22 | Nippon Yunikaa Kk | Production of foamed product of crosslinked ethylenic resin with continuous foam structure |
JPS60109804A (en) * | 1983-10-03 | 1985-06-15 | ゼネラル・エレクトリツク・カンパニイ | Method of blending high-viscosity silicon |
Also Published As
Publication number | Publication date |
---|---|
JPH055254B2 (en) | 1993-01-21 |
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