JPH0834871A - Method for manufacturing plastic sheet whose thickness increases by heating - Google Patents
Method for manufacturing plastic sheet whose thickness increases by heatingInfo
- Publication number
- JPH0834871A JPH0834871A JP17250694A JP17250694A JPH0834871A JP H0834871 A JPH0834871 A JP H0834871A JP 17250694 A JP17250694 A JP 17250694A JP 17250694 A JP17250694 A JP 17250694A JP H0834871 A JPH0834871 A JP H0834871A
- Authority
- JP
- Japan
- Prior art keywords
- thickness
- thermoplastic resin
- heating
- temperature
- melting point
- 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
Links
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、加熱することにより面
方向の寸法が変化することなく、厚み方向のみを増加で
きるプラスチックシートの製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a plastic sheet which can be increased only in the thickness direction without changing the dimension in the surface direction by heating.
【0002】[0002]
【従来技術とその課題】上記の特性を有するプラスチッ
クシートの製造方法として、熱可塑性樹脂の形状記憶
効果を利用する方法や、化学発泡剤を分散させた樹脂
シートを用いる方法が考えられる。前者の形状記憶効
果による方法は、熱可塑性樹脂からなる発泡体基材を、
該樹脂の融点より若干低い程度の温度まで加熱した状態
で圧縮歪みを与え、圧縮状態のまま急冷することにより
圧縮歪みを凍結しておき、この状態でシート状物として
使用し、再加熱することにより圧縮凍結された歪みが弾
性回復し厚みの増加を得るというものである。2. Description of the Related Art As a method for producing a plastic sheet having the above characteristics, a method utilizing the shape memory effect of a thermoplastic resin and a method using a resin sheet in which a chemical foaming agent is dispersed can be considered. The former method based on the shape memory effect uses a foam base material made of a thermoplastic resin,
A compressive strain is applied in a state of being heated to a temperature slightly lower than the melting point of the resin, and the compressive strain is frozen by rapid cooling in a compressed state, and used as a sheet in this state, and reheated. The compression-frozen strain recovers elastically and an increase in thickness is obtained.
【0003】したがって、その回復挙動は、一般的に温
度上昇に伴って漸次回復していく傾向にあり、シート保
管中の温度条件によっては、使用前にある程度厚みが回
復してしまう恐れがある。また、高い回復率を得るため
には、基材樹脂の融点より若干低い温度まで再加熱する
必要があり、なおかつ、融点を超えてしまうと厚みの回
復は望めないため、厚みの回復時にはかなり厳密な温度
管理が必要となる。Therefore, the recovery behavior thereof generally tends to gradually recover as the temperature rises, and depending on the temperature conditions during sheet storage, the thickness may recover to some extent before use. Also, in order to obtain a high recovery rate, it is necessary to reheat to a temperature slightly lower than the melting point of the base resin, and once the melting point is exceeded, it is not possible to recover the thickness, so it is quite strict when recovering the thickness. Temperature control is required.
【0004】各部位の厚み回復率についても、その部分
毎の熱及び応力の履歴によって異なってくるため、均一
な回復厚みを得るには、加熱・冷却各段階での温度・圧
力の面方向での均一性を確保する必要が有る。また、基
材樹脂の融点近くまで加熱することにより、面方向に原
シートの熱履歴に由来した寸法変化を誘起することを避
けられない。The thickness recovery rate of each part also varies depending on the history of heat and stress of each part. Therefore, in order to obtain a uniform recovery thickness, the temperature and pressure planes at each heating / cooling step should be used. It is necessary to ensure the uniformity of In addition, it is inevitable to induce a dimensional change due to the heat history of the original sheet in the surface direction by heating the base resin close to the melting point.
【0005】これに対して後者の発泡剤を利用する方
法においては、厚みが変化を始める温度は、発泡剤の分
解開始温度と同一となり、しきい値的特性を持たせられ
るが、樹脂中に発泡剤を均一に分散させる必要があり、
分散が不均一なシートでは、発泡後の厚みが不均一とな
るという問題があり、また、一般的に150℃程度より
低い温度で発泡し、且つ常温で安定な化学発泡剤を得る
ことが難しいという問題がある。On the other hand, in the latter method using a foaming agent, the temperature at which the thickness begins to change is the same as the decomposition start temperature of the foaming agent, and threshold characteristics can be given. It is necessary to disperse the foaming agent evenly,
A sheet with non-uniform dispersion has a problem that the thickness after foaming becomes non-uniform, and it is generally difficult to obtain a chemical foaming agent that foams at a temperature lower than about 150 ° C. and is stable at room temperature. There is a problem.
【0006】[0006]
【課題を解決するための手段】本発明は上記問題点を解
消できる加熱により厚みが増加するプラスチックシート
の製造方法を提供することを目的とする。請求項1の発
明は熱可塑性樹脂からなる発泡体基材A中に、該樹脂の
溶融開始温度より低融点の熱可塑性樹脂成分Bを分散混
入させた後、熱可塑性樹脂成分Bの融点から発泡体基材
Aの溶融開始温度の加熱温度範囲で厚み方向に圧縮する
ことを特徴とするものである。SUMMARY OF THE INVENTION It is an object of the present invention to provide a method of manufacturing a plastic sheet whose thickness is increased by heating which can solve the above problems. According to the invention of claim 1, a thermoplastic resin component B having a melting point lower than the melting start temperature of the resin is dispersed and mixed in a foam base material A made of a thermoplastic resin, and then foaming is performed from the melting point of the thermoplastic resin component B. It is characterized in that it is compressed in the thickness direction within the heating temperature range of the melting start temperature of the body substrate A.
【0007】ここで発泡体基材Aで使用する熱可塑性樹
脂としては、比較的高融点を有する樹脂で、分散混入さ
せる熱可塑性樹脂成分Bの融点付近(厚み増加のための
加熱温度域)で圧縮に対する回復弾性もしくはゴム弾性
を得られるものであれば、特に制限なく使用でき、具体
的にはポリプロピレン、ナイロン6、ナイロン66等の
各種ポリアミド樹脂、熱可塑性ポリウレタンエラストマ
ー等の各種熱可塑性エラストマー等が好適に使用でき
る。また、電子線照射やシラノール縮合等の化学架橋に
よる架橋構造を付与したものも好適に使用できる。The thermoplastic resin used in the foam substrate A is a resin having a relatively high melting point, and is near the melting point of the thermoplastic resin component B to be dispersed and mixed (heating temperature range for increasing the thickness). Any material can be used without particular limitation as long as it can obtain recovery elasticity or rubber elasticity with respect to compression. Specifically, various polyamide resins such as polypropylene, nylon 6, nylon 66, and various thermoplastic elastomers such as thermoplastic polyurethane elastomer can be used. It can be preferably used. Further, those having a crosslinked structure formed by chemical crosslinking such as electron beam irradiation or silanol condensation can be preferably used.
【0008】発泡体基材Aの厚みとしては、使用目的等
により異なるが0.5〜20mm程度のものが好適に使
用できる。また熱可塑性樹脂成分Bとしては、上記発泡
体基材Aの溶融開始温度より、低温、好ましくは50℃
以上低い温度域の融点を有する熱可塑性樹脂を選択する
ことができる。特定の物品中に組み込んでから加熱し、
厚みを回復させる場合を考慮すると、熱可塑性樹脂成分
Bの融点は、50〜150℃程度の範囲にあることが好
ましい。熱可塑性樹脂成分Bとしては具体的にはポリエ
チレンオキサイド、ポリエチレン、エチレン・酢酸ビニ
ル共重合体、エチレン・エチルアクリレート共重合体、
塩化ビニル・酢酸ビニル共重合体等が好適に使用でき
る。The thickness of the foam substrate A varies depending on the purpose of use and the like, but a thickness of about 0.5 to 20 mm can be preferably used. The thermoplastic resin component B is lower than the melting start temperature of the foam base material A, preferably 50 ° C.
A thermoplastic resin having a melting point in the above low temperature range can be selected. After incorporating into a specific article, heat it,
Considering the case of recovering the thickness, the melting point of the thermoplastic resin component B is preferably in the range of about 50 to 150 ° C. Specific examples of the thermoplastic resin component B include polyethylene oxide, polyethylene, ethylene / vinyl acetate copolymer, ethylene / ethyl acrylate copolymer,
Vinyl chloride / vinyl acetate copolymer and the like can be preferably used.
【0009】ついで、上記熱可塑性樹脂成分Bを分散混
入させた発泡体基材Aを用い、熱可塑性樹脂成分Bの融
点から発泡体基材Aの溶融開始温度の加熱温度範囲で厚
み方向に圧縮する必要がある。圧縮方法としては通常の
熱プレス法や加熱ロール間で連続的に圧縮する方法等に
よればよい。圧縮比としては使用目的等により適宜決め
ることができるが、圧縮後の厚み/圧縮前の厚み=0.
1〜0.6程度とするのが好ましい。Then, the foam base material A in which the thermoplastic resin component B is dispersed and mixed is used and compressed in the thickness direction in the heating temperature range from the melting point of the thermoplastic resin component B to the melting start temperature of the foam base material A. There is a need to. As a compression method, an ordinary hot pressing method or a method of continuously compressing between heating rolls may be used. The compression ratio can be appropriately determined according to the purpose of use, etc., but the thickness after compression / thickness before compression = 0.
It is preferably about 1 to 0.6.
【0010】請求項2の発明は熱硬化性樹脂からなる発
泡体基材C中に、該樹脂の熱分解開始温度より低融点の
熱可塑性樹脂成分Dを分散混入させた後、熱可塑性樹脂
成分Dの融点から発泡体基材Cの溶融開始温度の加熱温
度範囲で厚み方向に圧縮することを特徴とするものであ
る。According to the second aspect of the present invention, a thermoplastic resin component D having a melting point lower than the thermal decomposition initiation temperature of the resin is dispersed and mixed in a foam base material C made of a thermosetting resin, and then the thermoplastic resin component is mixed. It is characterized by compressing in the thickness direction in the heating temperature range from the melting point of D to the melting start temperature of the foam substrate C.
【0011】ここで発泡体基材Cで使用する熱硬化性樹
脂としては、ポリウレタン樹脂、シリコーン樹脂、可撓
性エポキシ樹脂等が好適に使用でき、加硫ゴム等の架橋
型エラストマーも使用できる。発泡体基材Cの厚みは請
求項1の発泡体基材Aと同様に0.5〜20mm程度の
ものが好適に使用できる。Here, as the thermosetting resin used for the foam base material C, polyurethane resin, silicone resin, flexible epoxy resin and the like can be preferably used, and crosslinked elastomer such as vulcanized rubber can also be used. The thickness of the foam base material C is preferably about 0.5 to 20 mm as in the foam base material A of claim 1.
【0012】また熱可塑性樹脂成分Dとしては、上記発
泡体基材Cの熱分解開始温度より低温、好ましくは50
℃以上低い温度域の融点を有する熱可塑性樹脂を選択す
ることができる。特定の物品中に組み込んでから加熱
し、厚みを回復させる場合を考慮すると、熱可塑性樹脂
成分Dの融点は、50〜150℃程度の範囲にあること
が好ましい。熱可塑性樹脂成分Dとしては上述した熱可
塑性樹脂成分Bと同一でよい。The thermoplastic resin component D is lower than the thermal decomposition starting temperature of the foam substrate C, preferably 50.
It is possible to select a thermoplastic resin having a melting point in a temperature range lower than 0 ° C. Considering the case where the thermoplastic resin component D is incorporated into a specific article and then heated to recover the thickness, the melting point of the thermoplastic resin component D is preferably in the range of about 50 to 150 ° C. The thermoplastic resin component D may be the same as the above-mentioned thermoplastic resin component B.
【0013】ついで、上記熱可塑性樹脂成分Dを分散混
入させた発泡体基材Cを用い、熱可塑性樹脂成分Dの融
点から発泡体基材Cの溶融開始温度の加熱温度範囲で厚
み方向に圧縮する必要がある。圧縮方法としては上記請
求項1で述べた通常の熱プレス法や加熱ロール間で連続
的に圧縮する方法等によればよい。また圧縮比としても
同様に、圧縮後の厚み/圧縮前の厚み=0.1〜0.6
程度とするのが好ましい。Then, the foam base material C in which the thermoplastic resin component D is dispersed and mixed is used, and compressed in the thickness direction in the heating temperature range from the melting point of the thermoplastic resin component D to the melting start temperature of the foam base material C. There is a need to. The compression method may be the usual hot pressing method described in claim 1 or a method of continuously compressing between heating rolls. Similarly, as a compression ratio, thickness after compression / thickness before compression = 0.1 to 0.6
It is preferable to set the degree.
【0014】請求項3の発明は上記発泡体基材A、Cが
連続気泡発泡体であるとともに、熱可塑性樹脂成分B、
Dが溶剤に可溶な樹脂からなり、溶剤に溶解させた熱可
塑性樹脂成分B、Dを上記発泡体基材A、Cに含浸させ
て熱可塑性樹脂成分を分散混入させることを特徴とする
ものである。According to a third aspect of the present invention, the foam base materials A and C are open-cell foams, and a thermoplastic resin component B is used.
D is composed of a resin soluble in a solvent, and the thermoplastic resin components B and D dissolved in the solvent are impregnated into the foam base materials A and C to disperse and mix the thermoplastic resin component. Is.
【0015】本発明では発泡体基材A、Cと熱可塑性樹
脂成分B、Dとを予め配合したものをシート化して後、
発泡体とする場合は連続気泡体、独立気泡体のいずれで
も良いが、上記請求項3の連続気泡体からなる発泡体基
材A、Cを形成した後、熱可塑性樹脂成分B、Dを内部
へ侵入させ保持する方法が簡便で好ましい。この場合、
発泡体基材A、Cは熱可塑性樹脂成分B、Dの溶液に侵
されない材質とする必要がある。In the present invention, the foam base materials A and C and the thermoplastic resin components B and D are previously blended into a sheet,
The foam may be either an open cell or a closed cell, but after forming the foam base materials A and C made of the open cell of claim 3, the thermoplastic resin components B and D are internally added. The method of infiltrating into and holding it is simple and preferable. in this case,
The foam base materials A and C must be made of a material that is not attacked by the solution of the thermoplastic resin components B and D.
【0016】ここで、上記方法で得られた加熱により厚
みが増加するシートの片面または両面に、耐熱性が良好
で、加熱によって寸法変化の少ないフイルムを積層して
もよい。積層方法は、圧縮工程の前または後工程で、適
宜通常の方法で積層すればよい。Here, a film having good heat resistance and a small dimensional change due to heating may be laminated on one side or both sides of the sheet obtained by the above method, the thickness of which is increased by heating. As a laminating method, laminating may be appropriately performed by a usual method before or after the compression step.
【0017】[0017]
【作用】本発明のプラスチックシートにおいては、発泡
体基材A、C中に分散混入されている熱可塑性樹脂成分
B、Dが加熱状態で溶融した後、冷却されるとガラス状
態となり、加熱圧縮された発泡体基材A、Cを厚みを減
じた状態で保持できる。そこで該発泡体基材には、形状
記憶効果による場合と異なり、基材発泡体の内部的な歪
みの凍結よりはむしろ、単にガラス状態になった熱可塑
性樹脂成分により外部的に弾性回復を阻まれている状態
にある。In the plastic sheet of the present invention, the thermoplastic resin components B and D dispersed and mixed in the foam base materials A and C are melted in a heated state, and then, when cooled, become a glass state and are heated and compressed. The foam base materials A and C thus prepared can be held in a state in which the thickness is reduced. Therefore, unlike the case due to the shape memory effect, the foam base material externally prevents the elastic recovery by the thermoplastic resin component in the glass state rather than the internal strain of the base foam being frozen. It is in a rare state.
【0018】加熱圧縮された上記プラスチックシートの
厚みを増加させるにあたっては、該シートを再び熱可塑
性樹脂成分の融点以上に加熱してやればよく、この加熱
により熱可塑性樹脂成分は再び溶融状態となり、外部的
に固定されていた発泡体基材の弾性力が開放されて厚み
が回復する。In order to increase the thickness of the heat-compressed plastic sheet, the sheet may be heated again to a temperature equal to or higher than the melting point of the thermoplastic resin component, and this heating causes the thermoplastic resin component to be in a molten state again and externally. The elastic force of the foam base material fixed to is released and the thickness is recovered.
【0019】以下、本発明を実施例により説明する。The present invention will be described below with reference to examples.
【0020】[0020]
実施例1 発泡体基材シ−ト(A):低密度ポリエチレン独立気泡
発泡体 (ガラス転移温度:−20℃、溶融開始温度120℃)
熱可塑性樹脂成分(B):ポリエチレンオキサイド樹
脂 (融点 60℃) 上記(A)100重量部に対して、(B)成分10重量
部を各々ペレットで混合し押出機(シリンダ−径40m
m、L/D28)に供給すると共に、押出機シリンダ−
途中から、発泡剤としてブタン15部を添付し、口金幅
300mm、リップ厚み0.2mmの口金より押出成形
し、(B)成分が分散された独立気泡のポリエチレン発
泡体(発泡倍率約30倍、厚み4mm)を得た。Example 1 Foam base sheet (A): Low density polyethylene closed cell foam (glass transition temperature: -20 ° C, melting start temperature 120 ° C)
Thermoplastic Resin Component (B): Polyethylene Oxide Resin (Melting Point 60 ° C.) 10 parts by weight of the component (B) is mixed in pellets with respect to 100 parts by weight of the above (A), and an extruder (cylinder-diameter 40 m) is used.
m, L / D 28) and at the same time the extruder cylinder
From the middle, 15 parts of butane was attached as a foaming agent, and extrusion molding was performed from a die having a mouth width of 300 mm and a lip thickness of 0.2 mm to obtain a closed-cell polyethylene foam in which the component (B) was dispersed (expansion ratio about 30 times, A thickness of 4 mm) was obtained.
【0021】ついで、油圧プレスで70℃の温度下10
分間の予熱後、7.0kg/cm2で加圧し、加圧した
まま23℃まで徐冷し、厚み0.8mmのプラスチック
シ−トを得た。得られたシートを用い、一定温度に保持
した熱風循環式オーブン中に5分間載置し、加熱温度と
厚み変化の状況を測定、観察した。その結果を下記に示
した。ここで、厚み変化は圧縮後の厚み(0.8mm)
に対する加熱後の厚み増加分の比率である。Then, using a hydraulic press, at a temperature of 70 ° C., 10
After preheating for one minute, the pressure was 7.0 kg / cm @ 2 and the pressure was gradually cooled to 23 DEG C. to obtain a plastic sheet having a thickness of 0.8 mm. Using the obtained sheet, the sheet was placed in a hot air circulation type oven maintained at a constant temperature for 5 minutes, and the heating temperature and the situation of the thickness change were measured and observed. The results are shown below. Here, the change in thickness is the thickness after compression (0.8 mm)
Is the ratio of the increase in thickness after heating.
【0022】 加熱温度 45℃ 65℃ 85℃ 105℃ 125℃ −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 厚み変化 12.7% 214% 363% 371% 263% ・熱可塑性樹脂成分(B)の溶融開始温度を5℃越える
65℃から、圧縮後の厚みの3倍程度に増加しており、
さらに発泡体基材シ−ト(A)の溶融開始温度である1
20℃迄の範囲で高い厚みの増加を得ている。85℃か
ら105℃の範囲で、面方向の厚みの均一性は良好で、
また面方向の寸法変化も極く僅かであった。Heating temperature 45 ° C. 65 ° C. 85 ° C. 105 ° C. 125 ° C. −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− Change 12.7% 214% 363% 371% 263% ・ From 65 ° C, which exceeds the melting start temperature of the thermoplastic resin component (B) by 5 ° C, has increased to about 3 times the thickness after compression,
Furthermore, it is the melting start temperature of the foam base sheet (A).
A high thickness increase is obtained up to 20 ° C. In the range of 85 ° C to 105 ° C, the thickness uniformity in the surface direction is good,
Moreover, the dimensional change in the plane direction was also very small.
【0023】実施例2 発泡体基材シート(C):熱硬化性ポリウレタン樹脂連
続気泡体 (ガラス転移温度−20℃、熱分解開始温度180℃、
厚み0.6mm) 熱可塑性樹脂成分(D):塩化ビニル−酢酸ビニル共重
合樹脂 (溶融開始温度75℃) 上記(D)の酢酸エチル20%溶液を発泡体基材シート
(C)に含浸後、表面の付着液を除去し、50℃にて5
分間乾燥した。ついで、油圧プレスで85℃の温度下5
分間の予熱後、7.0Kg/cm2 で加圧し、加圧した
まま23℃まで徐冷し、厚み0.3mmのプラスチック
シートを得た。Example 2 Foam substrate sheet (C): Thermosetting polyurethane resin open-cell body (glass transition temperature -20 ° C, thermal decomposition starting temperature 180 ° C,
Thickness 0.6 mm) Thermoplastic resin component (D): vinyl chloride-vinyl acetate copolymer resin (melting start temperature 75 ° C.) After impregnating a 20% ethyl acetate solution of the above (D) into the foam substrate sheet (C) , Remove the adherent liquid on the surface, and
Dried for minutes. Then, with a hydraulic press, at a temperature of 85 ° C, 5
After preheating for 1 minute, the pressure was 7.0 kg / cm 2 , and the pressure was gradually reduced to 23 ° C. to obtain a 0.3 mm-thick plastic sheet.
【0024】得られたシ−トを用い、実施例1と同様の
評価を行った。 加熱温度 65℃ 85℃ 105℃ 125℃ 145℃ −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 厚み変化 5% 96% 100% 99% 98% ・熱可塑性樹脂成分(D)の溶融開始温度を10℃越え
る85℃から、圧縮後の厚み(0.3mm)の2倍程度
に増加しており、さらに加熱温度を上昇させても厚みの
増加に変化がないことが分かる。面方向の厚み増加の均
一性は良好であり、また面方向の寸法変化も見られなか
った。Using the sheet obtained, the same evaluation as in Example 1 was performed. Heating temperature 65 ° C. 85 ° C. 105 ° C. 125 ° C. 145 ° C. −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− Thickness change 5% 96% 100% 99% 98% ・ The melting start temperature of the thermoplastic resin component (D) has increased from 85 ° C, which is 10 ° C higher, to about twice the thickness after compression (0.3 mm), and the heating temperature It can be seen that there is no change in the increase in thickness even when is increased. The uniformity of thickness increase in the surface direction was good, and no dimensional change in the surface direction was observed.
【0025】比較例1 実施例2で使用した発泡体基材シート(C)のみを油圧
プレスで85℃の温度下5分間の予熱の後7.0Kg/
cm2 の圧力で加圧し、加圧したまま23℃まで冷却し
た、しかしながら、加圧を中止すると、元の厚みに戻
り、サンプルが得られなかった。Comparative Example 1 Only the foam substrate sheet (C) used in Example 2 was preheated at 85 ° C. for 5 minutes in a hydraulic press to 7.0 kg /.
It was pressurized with a pressure of cm 2 and cooled to 23 ° C. while being pressurized. However, when the application of pressure was stopped, the original thickness was restored and a sample could not be obtained.
【0026】比較例2 独立気泡発泡ポリエチレンシート(厚み1mm、融点1
05℃)を油圧プレスで85℃の温度下10分間の予熱
後7.0Kg/cm2 の圧力で加圧し、加圧したまま直
ちに23℃まで急冷し圧縮歪みを凍結させ、形状記憶効
果による厚み回復のサンプルとした。プレス後の厚みは
0.3mmであった。Comparative Example 2 Closed-cell expanded polyethylene sheet (thickness 1 mm, melting point 1
(05 ° C) with a hydraulic press at a temperature of 85 ° C for 10 minutes, and then pressurizing it at a pressure of 7.0 Kg / cm 2 and then immediately quenching it to 23 ° C to freeze the compressive strain while maintaining the thickness due to the shape memory effect. It was used as a recovery sample. The thickness after pressing was 0.3 mm.
【0027】得られたシートを用い、実施例1と同様の
評価を行なった。 加熱温度 65℃ 85℃ 105℃ 125℃ 145℃ −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 厚み変化 43% 88% 109% 35% 5% ・圧縮歪みを加えた温度(85℃)から20℃を越える
温度で高い厚み増加率を得られたが、面方向の収縮が著
しく、また、厚みの均一性も実施例1に比べて劣った。
更に125℃以上に加熱すると溶融軟化が始まり、厚み
増加は困難であった。The same evaluation as in Example 1 was performed using the obtained sheet. Heating temperature 65 ° C. 85 ° C. 105 ° C. 125 ° C. 145 ° C. −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− Thickness change 43 % 88% 109% 35% 5% ・ A high thickness increase rate was obtained from the temperature (85 ° C) to which compressive strain was applied to over 20 ° C, but the shrinkage in the plane direction was remarkable, and the thickness uniformity was also high. Was also inferior to Example 1.
Further heating to 125 ° C. or higher causes melting and softening, and it is difficult to increase the thickness.
【0028】比較例3 低密度ポリエチレン(融点105℃)100重量部に対
して発泡剤(DPT系)6重量部、発泡助剤(尿素系)
6重量部をロールで練りながら添加混合した後、油圧プ
レスで厚み0.3mmのシートとし、これに電子線照射
による架橋処理を行い(ゲル分25%)、発泡剤による
厚み増加シートのサンプルとした。Comparative Example 3 6 parts by weight of a foaming agent (DPT type) and 100 parts by weight of low density polyethylene (melting point 105 ° C.), a blowing aid (urea type).
After 6 parts by weight were added and mixed while kneading with a roll, a sheet with a thickness of 0.3 mm was formed by a hydraulic press, and this was subjected to a crosslinking treatment by electron beam irradiation (gel content 25%) to obtain a sample of a sheet for increasing thickness with a foaming agent. did.
【0029】得られたシートを用い、実施例1と同様の
評価を行なった。 加熱温度 65℃ 85℃ 105℃ 125℃ 145℃ −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− 厚み変化 0 0 3% 1% 194% ・145℃という高い温度で漸く発泡剤が分解を始め、
極めて大きな厚み増加を得たが、同時に面方向にも寸法
が拡大してしまった。厚みの均一性は悪く、ガス抜けの
発生により表面状態も良くなかった。The same evaluation as in Example 1 was performed using the obtained sheet. Heating temperature 65 ° C. 85 ° C. 105 ° C. 125 ° C. 145 ° C. −−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−−− Thickness change 0 0 3% 1% 194% · At a high temperature of 145 ° C, the blowing agent begins to decompose,
Although a very large increase in thickness was obtained, at the same time the dimensions also expanded in the plane direction. The thickness uniformity was poor, and the surface condition was not good due to the occurrence of gas escape.
【0030】[0030]
【発明の効果】上述したように本発明によれば、加熱す
ることにより面方向の寸法が変化することなく、厚み方
向のみを増加できるプラスチックシートが容易に得られ
るという利点がある。As described above, according to the present invention, it is possible to easily obtain a plastic sheet which can be increased only in the thickness direction without changing the dimension in the plane direction by heating.
Claims (3)
中に、該樹脂の溶融開始温度より低融点の熱可塑性樹脂
成分(B)を分散混入させた後、熱可塑性樹脂成分
(B)の融点から発泡体基材(A)の溶融開始温度の加
熱温度範囲で厚み方向に圧縮することを特徴とする加熱
により厚みが増加するプラスチックシートの製造方法。1. A foam base material (A) made of a thermoplastic resin.
A thermoplastic resin component (B) having a melting point lower than the melting start temperature of the resin is dispersed and mixed therein, and then the melting start temperature of the foam base material (A) is heated from the melting point of the thermoplastic resin component (B). A method for producing a plastic sheet, the thickness of which is increased by heating, which comprises compressing in the thickness direction in a temperature range.
中に、該樹脂の熱分解開始温度より低融点の熱可塑性樹
脂成分(D)を分散混入させた後、熱可塑性樹脂成分
(D)の融点から発泡体基材(C)の分解開始温度の加
熱温度範囲で厚み方向に圧縮することを特徴とする加熱
により厚みが増加するプラスチックシートの製造方法。2. A foam base material (C) made of a thermosetting resin.
After the thermoplastic resin component (D) having a melting point lower than the thermal decomposition start temperature of the resin is mixed therein, the decomposition starting temperature of the foam base material (C) is changed from the melting point of the thermoplastic resin component (D). A method for producing a plastic sheet, the thickness of which increases by heating, which comprises compressing in a thickness direction within a heating temperature range.
泡体であるとともに、熱可塑性樹脂成分(B)、(D)
が溶剤に可溶な樹脂からなり、溶剤に溶解させた熱可塑
性樹脂成分(B)、(D)を上記発泡体基材(A)、
(C)に含浸させて熱可塑性樹脂成分を分散混入させる
ことを特徴とする請求項1又は請求項2記載の加熱によ
り厚みが増加するプラスチックシートの製造方法。3. The foam base materials (A) and (C) are open-cell foams, and the thermoplastic resin components (B) and (D).
Is a resin soluble in a solvent, and the thermoplastic resin components (B) and (D) dissolved in the solvent are added to the foam base material (A),
The method for producing a plastic sheet of which thickness is increased by heating according to claim 1 or 2, wherein (C) is impregnated and a thermoplastic resin component is dispersed and mixed therein.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17250694A JPH0834871A (en) | 1994-07-25 | 1994-07-25 | Method for manufacturing plastic sheet whose thickness increases by heating |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP17250694A JPH0834871A (en) | 1994-07-25 | 1994-07-25 | Method for manufacturing plastic sheet whose thickness increases by heating |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0834871A true JPH0834871A (en) | 1996-02-06 |
Family
ID=15943234
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP17250694A Pending JPH0834871A (en) | 1994-07-25 | 1994-07-25 | Method for manufacturing plastic sheet whose thickness increases by heating |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0834871A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1457305A1 (en) | 2003-03-14 | 2004-09-15 | Nichias Corporation | Thermally expandable material and method for producing the same |
| EP1746314A2 (en) | 2005-07-21 | 2007-01-24 | Nichias Corporation | Seal structure and process for producing same |
-
1994
- 1994-07-25 JP JP17250694A patent/JPH0834871A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1457305A1 (en) | 2003-03-14 | 2004-09-15 | Nichias Corporation | Thermally expandable material and method for producing the same |
| EP1746314A2 (en) | 2005-07-21 | 2007-01-24 | Nichias Corporation | Seal structure and process for producing same |
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