JPS58108234A - Foamed sheet - Google Patents

Foamed sheet

Info

Publication number
JPS58108234A
JPS58108234A JP20734281A JP20734281A JPS58108234A JP S58108234 A JPS58108234 A JP S58108234A JP 20734281 A JP20734281 A JP 20734281A JP 20734281 A JP20734281 A JP 20734281A JP S58108234 A JPS58108234 A JP S58108234A
Authority
JP
Japan
Prior art keywords
ethylene
copolymer
olefin
alpha
radical polymerization
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.)
Pending
Application number
JP20734281A
Other languages
Japanese (ja)
Inventor
Yutaka Kanekawa
金川 豊
Yasukazu Yamashita
山下 康和
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
HAISHIITO KOGYO KK
Original Assignee
HAISHIITO KOGYO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by HAISHIITO KOGYO KK filed Critical HAISHIITO KOGYO KK
Priority to JP20734281A priority Critical patent/JPS58108234A/en
Publication of JPS58108234A publication Critical patent/JPS58108234A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)

Abstract

PURPOSE:To manufacture a foamed sheet having improved physical properties such as elongation, light transmittance, strength, heat insulation, etc., by compounding an ethylene polymer prepared by high-pressure radical polymerization with a specific ethylene-alpha-olefin copolymer, and subjecting the mixture to extrusion foaming. CONSTITUTION:About 80-50(wt)% homopolymer or copolymer of ethylene prepared by the high-pressure radical polymerization is compounded with about 20-50%, preferably about 25-40% copolymer of ethylene and a 3-8C alpha-olefin having a density of 0.91-0.95g/cm<3>, and foamed by extruding in the presence of a foaming agent. The ethylene-alpha-olefin copolymer is preferably the one containing about 0.2-8mol% alpha-olefin (propylene, butene-1, etc.) and having a melt index of about 0.5-30g/10-min.

Description

【発明の詳細な説明】 本発明は、発泡シートに関する。更に詳しくは、非架橋
のエチレン系重合体発泡シー)K関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a foam sheet. More specifically, it relates to non-crosslinked ethylene polymer foam sheet) K.

従来から、為圧ラジカル重合法によって得られたエチレ
ンの単独重合体または共1合体の発泡シートが、農業用
の保温資材などとして使用されているが、その発泡シー
トの物性的な改善がなお望まれている0本発明者らは、
高圧ラジカル重合法によって得られたエチレン重合体に
密度が091〜α96g/♂のエチレン−α−オレフィ
ン共重合体をブレンドし、これを発泡押出しすることK
より、伸びおよび光線透過率などの物性が一段と改善さ
れた非架橋の発泡シートる得ることができた。
Foamed sheets of ethylene homopolymers or comonomers obtained by pressure radical polymerization have been used as heat-insulating materials for agriculture, but improvements in the physical properties of these foamed sheets are still desired. The inventors have
K
As a result, it was possible to obtain a non-crosslinked foamed sheet with further improved physical properties such as elongation and light transmittance.

従って、本発明は非架橋の発泡シートに係り、この発泡
シートは、高圧ラジカル重合法によって得られたエチレ
ンの単独重合体または共重合体約80.50重量%およ
び密度α91〜α96g々3のエチレンと炭素数3〜8
のα−オレフィンとの共重合体約20〜50重量%よシ
なるエチレン系重合体を発泡剤の存在下で発泡押出しし
て得られる。
Accordingly, the present invention relates to a non-crosslinked foamed sheet, which is made of about 80.50% by weight of an ethylene homopolymer or copolymer obtained by a high-pressure radical polymerization method and an ethylene having a density α91 to α96g and carbon number 3-8
It is obtained by foaming and extruding an ethylene polymer comprising about 20 to 50% by weight of a copolymer with α-olefin in the presence of a blowing agent.

高圧ラジカル重合法忙よって得られるエチレンの単独重
合体または共重合体は、酸素または各種の有機過酸化物
、アゾ化合物、アセトキシム、アミン酸化合物などを重
合開始剤として、一般に反応圧力約1000〜3000
気圧の高圧下で行われるラジカル重合によって得られる
。ポリエチレンと同様に用いられるエチレン共重合体と
しては、エチレンと酢酸ビニル、ギ酸ビニル、グリコー
ル酸ビニル、プロピオン酸ビニル、安息%酸ビニルなど
のビニルエステル類、アクリル酸、メタクリル酸、エタ
クリル酸あるいはこれらの塩、アルキルエステルなどの
アクリル系単量体との共重合体などが含まれる。
Homopolymers or copolymers of ethylene obtained by high-pressure radical polymerization are generally produced at a reaction pressure of about 1,000 to 3,000 using oxygen, various organic peroxides, azo compounds, acetoximes, aminic acid compounds, etc. as polymerization initiators.
Obtained by radical polymerization carried out under high atmospheric pressure. Ethylene copolymers used in the same way as polyethylene include ethylene and vinyl esters such as vinyl acetate, vinyl formate, vinyl glycolate, vinyl propionate, vinyl benzoate, acrylic acid, methacrylic acid, ethacrylic acid, or these. Includes salts, copolymers with acrylic monomers such as alkyl esters, etc.

エチレンと炭素数3〜8のα−オレフィンとの共重合体
(密度α9ユ〜α9577/cm )は、エチレントプ
ロピレン、ブテン−11ペンテン−1、ヘキセン−1、
オクテン−1,3−メチルブテン−1、Q3−ジメチル
ブテン−1などとの共重合体であり、これらの共重合体
は、酸化クロム、酸化モリブデン、三塩化チタンまたは
四塩化チタン−アルキルアルミニウム、四塩化チタンな
どのチタン化合物−塩化マグネシウムなどのマグネシウ
ム化合物−(塩化)アルキルアルミニウムなどによって
代表される各種触媒を用い、約1〜100 kg/lの
低〜中圧下の気相重合、スラリー1合、溶液東金などに
よって製造される。そして、これらの共重合体は、約0
2〜8モル%のα−オレフィン含有漱および約α6〜3
0 g/l 0分のメルトインデックスを有することが
好ましい。
Copolymers of ethylene and α-olefins having 3 to 8 carbon atoms (densities α9 to α9577/cm ) include ethylenetopropylene, butene-11 pentene-1, hexene-1,
It is a copolymer with octene-1,3-methylbutene-1, Q3-dimethylbutene-1, etc., and these copolymers are copolymers with chromium oxide, molybdenum oxide, titanium trichloride or titanium tetrachloride-alkyl aluminum, tetrachloride, etc. Using various catalysts such as titanium compounds such as titanium chloride, magnesium compounds such as magnesium chloride, and alkylaluminum (chloride), gas phase polymerization is carried out under low to medium pressure of about 1 to 100 kg/l, slurry 1, Manufactured by Solution Togane and others. And these copolymers have approximately 0
2-8 mol% α-olefin containing racket and about α6-3
Preferably it has a melt index of 0 g/l 0 min.

高圧ラジカル重合法エチレン単独重合体iたは共重合体
とエチレン−α−オレフィン共1合体とは、それぞれ約
80〜501量%および約20〜50重量%の割合で混
合して用いられる。エチレン−α−オレフィン共重合体
の混合割合が約20重量%以下では、得られる発泡シー
トに物性改善の効果が得られない。逆に、約501量%
以上の割合で混合して用いると、この共重合体が直鎖状
の構造を有し、しか本分子量分布の範囲が狭いため、高
剪断速度下での溶融粘度が高く、このため発泡押出に際
して押出機、パンパリーミキツーなどのモーター負荷が
大きくなり、押出性が悪くなる。更に、この共重合体は
、高圧ラジカル重合法エチレン重合体と比較して溶融張
力が低い九め、それの混合割合を高めると発泡体が破泡
を起し易く、セルサイズが大きくなるなどの問題も発生
する。これら押出性、発泡性およびシートの物性などの
点を総合的に勘案すると、共重合体の混合割合としては
約25〜401E量%の範囲内が最も好ましい。
The high-pressure radical polymerized ethylene homopolymer i or copolymer and the ethylene-α-olefin copolymer are used in a mixture of about 80 to 501% by weight and about 20 to 50% by weight, respectively. If the mixing ratio of the ethylene-α-olefin copolymer is less than about 20% by weight, the resulting foamed sheet will not have the effect of improving the physical properties. On the contrary, about 501% by volume
When mixed at the above ratio, this copolymer has a linear structure and a narrow range of molecular weight distribution, resulting in a high melt viscosity at high shear rates, which makes it difficult to perform foam extrusion. The load on the motors of the extruder, bread parry mixer, etc. increases, and extrusion performance deteriorates. Furthermore, this copolymer has a lower melt tension than high-pressure radically polymerized ethylene polymer, and when its mixing ratio is increased, the foam tends to break and the cell size increases. Problems also arise. Considering these extrudability, foamability, physical properties of the sheet, etc., the most preferable mixing ratio of the copolymer is within the range of about 25 to 401E%.

発泡剤としては、加熱によって樹脂を発泡させるのに必
要なガスを発生せしめる分解型の化学発泡剤、例えば炭
酸ナトリウム、炭酸水素ナトリウム、硝酸アンモニウム
などの無機発砲剤またはジアゾアミノベンゼン、アゾジ
カルボンアミド、ジニトロソペンタメチレンテトラミン
、p+1”−オキシビスベンゼン、スルホニルヒドラジ
ド、アゾビスイソブチロニトリル、p−)ルエンスルホ
ニルヒドラジドなどの有機発泡剤が、一般にエチレン体
の自機化合物、例えばプロパン、ブタン、石油エーテル
、モノクロルトリフルオロメタン、ジクロルジフルオロ
メタン、モノクロルジフルオロメタン、ジクロルテトラ
フルオロエタン、トリクロルエチレンなどを含浸もしく
は押出機内に直接ガスを注入せしめて発泡剤としてもよ
く、更にはこれら両名の発泡剤を併用することもできる
As blowing agents, decomposition type chemical blowing agents that generate the gas necessary to foam the resin by heating, such as inorganic blowing agents such as sodium carbonate, sodium bicarbonate, and ammonium nitrate, or diazoaminobenzene, azodicarbonamide, dicarbonate, etc. Organic blowing agents such as nitrosopentamethylenetetramine, p+1''-oxybisbenzene, sulfonyl hydrazide, azobisisobutyronitrile, p-)luenesulfonyl hydrazide are generally ethylene-based organic compounds such as propane, butane, petroleum ether, etc. , monochlorotrifluoromethane, dichlorodifluoromethane, monochlorodifluoromethane, dichlorotetrafluoroethane, trichloroethylene, etc. may be used as a blowing agent by impregnating or directly injecting gas into the extruder. They can also be used together.

発泡シートの成形は、高圧ラジカル重合法エチレン11
1合体、エチレン−α−オレフィン共共合合体発泡剤お
よび必要に応じて発1’I!l助剤、着色剤などの4!
r槽配合剤を、押出機、ミキシングロールなと?用いて
、発泡剤が分解しない程度の温度で均一に混合した後、
発泡剤の分解温良以上の温度(約150〜250℃)で
押出機から発泡押出しすることKよって付われる。
The foam sheet is formed using high-pressure radical polymerization of ethylene 11.
1 combination, ethylene-α-olefin copolymer blowing agent and optionally blowing 1'I! l Auxiliary agents, coloring agents, etc. 4!
Is it an extruder or a mixing roll for R-tank compounding agent? After uniformly mixing at a temperature that does not decompose the blowing agent using
This is done by extruding the foam from an extruder at a temperature above the decomposition temperature of the foaming agent (approximately 150 to 250°C).

得られた発泡シートを農業用の&温資材などに使用する
場合には、厚さが約015〜2.0龍、発泡倍率が約1
3〜40倍程度であることが望ましい。この発泡シート
Vi特に伸びおよび光線透過率の点ですぐれており、引
帰弥尾は殆んど変らなくとも伸びかよいため、この発泡
シートを引張っても破れ難く、それはあたかも引張強度
が大きいためと思わせる程であシ、このため兼業用の保
温資材として使用し、それを張る場合の作業性にすぐれ
ており、また光線透過率が良好なことも植物の生長促進
を図るこの種の用途にとってきわd)て好ましい結果を
もたらす。
When using the obtained foam sheet for agricultural and thermal materials, etc., the thickness should be about 0.15 to 2.0 mm and the foaming ratio should be about 1.
It is desirable that it is about 3 to 40 times larger. This foam sheet Vi is particularly excellent in terms of elongation and light transmittance, and Hikiyao has good elongation even if it does not change much, so even if you pull this foam sheet, it is difficult to tear, which is probably due to its high tensile strength. For this reason, it is used as a heat-retaining material for dual purposes, and has excellent workability when it is stretched, and its good light transmittance makes it suitable for this type of use to promote plant growth. d) yields favorable results.

従って、本発明に係る発泡シートは、従来の光透過率お
よび物性強度の点でもすぐれている低コストの農業用の
保温資材として有効に用いられる。
Therefore, the foam sheet according to the present invention can be effectively used as a low-cost agricultural heat-retaining material that is superior in terms of light transmittance and physical strength compared to conventional sheets.

これらの点に関して更に詳細に述べると、従来の高圧ラ
ジカル重合法によって得られたエチレンの単独側合体ま
たは共重合体の発泡シートは、農業用の保温資材として
適当な約40〜60%の光線透過率を得ようとすると、
次のいずれかの方法をとることになるが、 (1)発泡倍率を約2倍以上と高くすればよいが、反面
これにより物性の低下が著しく、かかる用途に使用する
ことができない (2)発泡シートの厚さおよび坪量を上げることによっ
て、適度な保温性、光線透過率、物性強度などを得るこ
とができるが、経済的にみて好ましくない (3)発泡倍率を約しフ以下に低くして、酸化チタンな
どの顔料を添加してもよいが、これにより物性強度は保
たれるものの、発泡倍率が低いため保温性に劣るように
なる など、いずれの方法にも満足されない点づ;みらflる
To explain these points in more detail, foamed sheets of ethylene monomer or copolymer obtained by conventional high-pressure radical polymerization have a light transmittance of about 40 to 60%, which is suitable for use as agricultural heat-insulating materials. When trying to get the rate,
One of the following methods will be used: (1) It is possible to increase the expansion ratio to approximately 2 times or more, but on the other hand, this will significantly reduce the physical properties, making it impossible to use it for such purposes (2) By increasing the thickness and basis weight of the foam sheet, it is possible to obtain appropriate heat retention, light transmittance, physical strength, etc., but this is not desirable from an economic standpoint. Then, a pigment such as titanium oxide may be added, but although this maintains the physical strength, the foaming ratio is low, resulting in poor heat retention, and both methods are unsatisfactory. See you in the future.

しかるに1エチレン−α−オレフィン共重合体をブレン
ドして得られた本発明の発泡シートは、坪量が1259
/a2程度と軽量で、かつ発泡倍率力;約21倍と高く
、保温性の点でもすぐれている。
However, the foamed sheet of the present invention obtained by blending the 1-ethylene-α-olefin copolymer has a basis weight of 1259
It is lightweight at about /a2, has a high foaming ratio of about 21 times, and has excellent heat retention.

しかも、顔料などの添加剤を使用しなくとも適度な光線
透過率が得られ、更に物性siもす<” ttている々
ど、従来の発泡シートにみられ九…1艶点力(すべて改
善されておシ、従って経済性に富んだ饅業用の保温資材
として有効に使用すること25五できる。
What's more, a suitable light transmittance can be obtained without the use of additives such as pigments, and the physical properties are improved by 9.1 points (all improved) compared to conventional foam sheets. Therefore, it can be effectively used as an economical heat-insulating material for the rice cake industry.

次に、実施例について本発明の詳細な説明する。Next, the present invention will be described in detail with reference to examples.

実施例 表1に示される配合処方に従って、高圧ラジカル亀合法
によって得られたエチレン−酢酸ビニル共1合体く三井
ポリケミカル製品B −332−1、”酢酸ビニル含量
631量%、メルトインデックスa Og/l O分)
およびエチレン−α−オレフィン共共合合体三井石油化
学製品つルトゼツクスー2020L;密度α920に鉋
−メルトインデックス2.2 II/l 0分)よりな
るエチレン共重合体に1発泡剤としてのアゾジカルボン
ア、ミド、炭酸水素ナトリウムおよび発泡助剤を加え、
リボンプレンダーを用いてドライプレノドした。
EXAMPLE According to the formulation shown in Table 1, an ethylene-vinyl acetate co-monomer obtained by high-pressure radical oxidation method was produced.Mitsui Polychemical Product B-332-1, vinyl acetate content 631% by weight, melt index a Og/ l O minutes)
and an ethylene copolymer consisting of ethylene-α-olefin copolymer Mitsui Petrochemical Products Tsuruto Zexu 2020L; density α920 and plane-melt index 2.2 II/l 0 min), 1 azodicarbonate as a blowing agent, Add midi, sodium bicarbonate and blowing aid;
Dry pre-greased using a ribbon blender.

形成された混合物を、280I11径のオフセットダイ
(スリット幅α5冨l)を備えた115襲径の押出機(
Ll/D −22)のホッパーに供給し、最高温度を1
90℃に調節した加工条件下で発泡成形全行ない、厚さ
α28W1密度α4577/♂、坪量1251)7mの
発泡シートを成形した。
The formed mixture was passed through a 115 diameter extruder (with a 280I 11 diameter offset die (slit width α5).
Ll/D -22) is supplied to the hopper with a maximum temperature of 1
All foam molding was carried out under processing conditions adjusted to 90° C. to form a foam sheet having a thickness α28W1 density α4577/♂ and a basis weight 1251) 7 m.

表  1 得られた6発泡シートについて、JIS K −76’
767に規定される方法により、引張強度、伸びおよび
引裂強度の測定を行なった。表2の結果に示さ7Lル如
く、エチレン−α−オレフィン共謝金体ta合すること
により、発泡シートの物性強度および光線透過率が改善
されることが判る。
Table 1 Regarding the obtained 6 foam sheets, JIS K-76'
Tensile strength, elongation and tear strength were measured by the method specified in 767. As shown in the results in Table 2, it can be seen that the physical strength and light transmittance of the foamed sheet are improved by combining the ethylene-α-olefin co-metallic material.

表  2Table 2

Claims (1)

【特許請求の範囲】[Claims] Li41+圧ラジ力ル重合法によって得られたエチレン
の単独重合体ま九は共重合体約80〜60重量%および
密度α91〜α96#6IPのエチレンと炭素数3〜8
のα−オレフィンとの共重合体約20〜60重量%よシ
なるエチレン系重合体を発泡剤の存在下て発泡押出しし
て得られ九非架橋の発泡シート。
The homopolymer of ethylene obtained by Li41 + pressure radial polymerization method is a copolymer of about 80 to 60% by weight and ethylene with a density of α91 to α96 #6 IP and a carbon number of 3 to 8
A non-crosslinked foam sheet obtained by foaming and extruding an ethylene polymer comprising about 20 to 60% by weight of a copolymer with α-olefin in the presence of a blowing agent.
JP20734281A 1981-12-22 1981-12-22 Foamed sheet Pending JPS58108234A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20734281A JPS58108234A (en) 1981-12-22 1981-12-22 Foamed sheet

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20734281A JPS58108234A (en) 1981-12-22 1981-12-22 Foamed sheet

Publications (1)

Publication Number Publication Date
JPS58108234A true JPS58108234A (en) 1983-06-28

Family

ID=16538148

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20734281A Pending JPS58108234A (en) 1981-12-22 1981-12-22 Foamed sheet

Country Status (1)

Country Link
JP (1) JPS58108234A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60222222A (en) * 1984-04-20 1985-11-06 Japan Styrene Paper Co Ltd Preparation of polyethylene extrusion foaming body
JP2011102379A (en) * 2009-10-13 2011-05-26 Sumitomo Chemical Co Ltd Foamed sheet

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60222222A (en) * 1984-04-20 1985-11-06 Japan Styrene Paper Co Ltd Preparation of polyethylene extrusion foaming body
JPH0443934B2 (en) * 1984-04-20 1992-07-20 Jsp Corp
JP2011102379A (en) * 2009-10-13 2011-05-26 Sumitomo Chemical Co Ltd Foamed sheet

Similar Documents

Publication Publication Date Title
US4649001A (en) Process for producing polyethylene extruded foams
US4020025A (en) Extrudable foamable composition comprising an olefin polymer, a styrene polymer and a hydrogenated styrene butadiene block copolymer
JP7057752B2 (en) Polypropylene resin pre-foamed particles and method for producing the pre-foamed particles
JP4011962B2 (en) Method for producing polypropylene resin extruded foam sheet, produced extruded foam sheet, and molded article comprising the foamed sheet
WO2020004429A1 (en) Modified polypropylene resin and method for producing same, and extruded foam particles that use said modified polypropylene resin and method for their production
JPS63213531A (en) Composition for noncrosslinked foam
KR20020042474A (en) Foamed polyolefin resin sheet
JP3195674B2 (en) Method for producing non-crosslinked ethylene polymer expanded particles
KR20020013784A (en) Modified polypropylene, process for preparing modified polypropylene, modified polypropylene composition and foamed product
US5316840A (en) Wallpaper
JPS6245256B2 (en)
JP2019137847A (en) Propylene-based polymer composition and foamed molded product thereof
EP0107371A2 (en) Low density closed-cell foamed articles from ethylene copolymer/vinyl or vinylidene halide blends
JPS61146510A (en) Manufacture of crosslinked polyolefin foam
JPS58108234A (en) Foamed sheet
JP3808843B2 (en) Method for producing modified polypropylene resin composition and foam of the resin composition
US6262138B1 (en) Extrusion-foamed board of resin blend comprising modified polypropylene resin and polystyrene resin
US3696059A (en) Process for preparing olefin polymer foams
US20080128937A1 (en) Foamed rotomolded polyethylene
JP2003089735A (en) Polypropylene resin composition and container
JP2003026870A (en) Polyethylene resin composition, polyethylene resin composition for foaming and foamed product
JPH08231747A (en) Foam sheet of polypropylene resin composition
JPH0226653B2 (en)
JPS58141215A (en) Expansion of ethylene or propylene polymer
JPH09227707A (en) Production of polypropylene resin foam