JPS6023133B2 - Manufacturing method of semi-rigid/hard resin foam - Google Patents

Manufacturing method of semi-rigid/hard resin foam

Info

Publication number
JPS6023133B2
JPS6023133B2 JP8096279A JP8096279A JPS6023133B2 JP S6023133 B2 JPS6023133 B2 JP S6023133B2 JP 8096279 A JP8096279 A JP 8096279A JP 8096279 A JP8096279 A JP 8096279A JP S6023133 B2 JPS6023133 B2 JP S6023133B2
Authority
JP
Japan
Prior art keywords
mdi
resin foam
rigid
semi
urethane prepolymer
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP8096279A
Other languages
Japanese (ja)
Other versions
JPS565837A (en
Inventor
信公 高橋
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.)
Wako Chemical Co Ltd
Original Assignee
Wako Chemical Co Ltd
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 Wako Chemical Co Ltd filed Critical Wako Chemical Co Ltd
Priority to JP8096279A priority Critical patent/JPS6023133B2/en
Publication of JPS565837A publication Critical patent/JPS565837A/en
Publication of JPS6023133B2 publication Critical patent/JPS6023133B2/en
Expired legal-status Critical Current

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Description

【発明の詳細な説明】 (発明の目的) 本発明は末端NCO基%の極めて低いウレタンプレポリ
マーに4・4′ージフエニールメタンジイソシァネート
(以下MDIと略称する)の添加量を現場で加減するの
みで含浸フオームの物性を自由に加減できる半硬質・硬
質樹脂フオームの製造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION (Objective of the Invention) The present invention aims at reducing the amount of 4,4'-diphenylmethane diisocyanate (hereinafter abbreviated as MDI) to a urethane prepolymer having an extremely low percentage of terminal NCO groups. This invention relates to a method for manufacturing semi-rigid/hard resin foams that allows the physical properties of impregnated foams to be freely adjusted by adjusting them on-site.

(従釆技術) 従来のウレタンプレポリマーはトリレンジィソシアネー
ト(以下TDIと略称する)とポリオールとを反応させ
て作り、これをベースとし所望物性に応じてこのプレポ
リマ−の末端NCO基%をあらかじめ重合段階で最終製
品の所望の物性に応ずることにしていた。
(Subject technology) Conventional urethane prepolymers are made by reacting tolylene diisocyanate (hereinafter abbreviated as TDI) and polyol, and based on this, the percentage of terminal NCO groups of this prepolymer is adjusted according to the desired physical properties. The desired physical properties of the final product were determined in advance at the polymerization stage.

即ちNCO基%を大にすれば硬度及び衝撃吸収性は大と
なり、NCO基%を小にすればこれらは小となりクッシ
ョン性や伸びが大となっていた。然るにこのブレポリマ
ーの末端NCO基%を変化することは通常、製造工程を
更にさかのぼり、原料製造の基礎化学工場でないとでき
なかった。
That is, if the NCO group % is increased, the hardness and impact absorption properties are increased, and if the NCO group % is decreased, these are decreased and the cushioning properties and elongation are increased. However, changing the percentage of terminal NCO groups in this brepolymer is usually only possible by going further back in the manufacturing process and at the basic chemical plant that produces the raw materials.

かつ基礎化学工場は大量生産のため、末端のユーザーの
好みに応じて各種のNCO基%を有するものを製造する
ような親切さは一切なかった。そのためユーザーは所望
の硬度を有する樹脂含浸フオームを製造すること自体が
非常に困難で通常一定の硬度のものより作られなかった
。無理に硬度を変えるとしてもフオームの含浸量を苦心
して加減したり、不要な溶剤を使用したりして不経剤か
つ非能率的な作業をしていた。更にNCO基含有量が増
加するに連れ当然遊離のTDIが増加し、環境衛生基準
ではTDIが1%を超える薬剤は特定化学物質の指定品
目とされ、環境衛生上の特別な取扱を受けることになる
。従って或る程度以上のTDI基を用いると何かと支障
きたすことがあった。(発明の構成)本発明は上記の欠
点をなくすためのものであってNCO基%の極く低いよ
うにTDIの量を減じてポリオールとを反応させ、1種
類のみに限定してウレタンプレポリマーを基礎化学工場
で予じめ作って置く。
Moreover, since basic chemical factories are mass-produced, there is no flexibility in manufacturing products with various NCO group percentages according to the preferences of end users. Therefore, it is very difficult for users to manufacture a resin-impregnated foam having a desired hardness, and it is usually not possible to manufacture a resin-impregnated foam having a certain hardness. Even if the hardness was to be changed by force, the amount of impregnation in the foam had to be adjusted carefully, and unnecessary solvents were used, resulting in a tedious and inefficient process. Furthermore, as the NCO group content increases, free TDI naturally increases, and according to environmental hygiene standards, drugs with TDI exceeding 1% are designated as specified chemical substances and are subject to special handling in terms of environmental hygiene. Become. Therefore, the use of TDI groups above a certain level may cause some problems. (Structure of the Invention) The present invention is intended to eliminate the above-mentioned drawbacks, and is made by reducing the amount of TDI and reacting it with a polyol so that the percentage of NCO groups is extremely low, and by using only one type of urethane prepolymer. is made in advance at a basic chemical factory.

その後成形加工等の使用現場に於て、4・4−ジフエニ
ールメタンジイソシアネート(以下MDIと略称する)
を反応硬化後所要の物性に達成するように所望量を混合
し、軟質樹脂フオームに含浸させて熱プレス型中で圧縮
反応硬化させるものである。MDIは比較的最近の使用
されるようになった薬剤でウレタンフオームの製造に際
して特にコールドキュァを要求される場合や、製靴とか
ウレタンフオームの帯尺と布等とのラミネーチング用と
かの接着剤として使用されているに過ぎぬものである。
After that, at the site of use such as molding processing, 4,4-diphenylmethane diisocyanate (hereinafter abbreviated as MDI)
After reaction and curing, the desired amount is mixed to achieve the desired physical properties, impregnated into a soft resin foam, and then compressed and cured in a hot press mold. MDI is a chemical that has come into use relatively recently, and is used especially when cold curing is required when manufacturing urethane foam, or as an adhesive for shoe making or laminating urethane foam strips with cloth, etc. It is just something that has been done.

NCO基の極度に少ないウレタンプレポIJマーは通常
品であって自在に入手できる。
Urethane prepo IJmer with extremely few NCO groups is a common product and is freely available.

これにMD【を所望の硬度が出るように鷹梓混合すれば
よい。NCO基の極めて少ないウレタンプレポリマーは
MDIと楽に混和する。さらにMDIはTDIに比べ反
応性に富むため本混合液を使用した場合はTDIのみに
よるプレボリューを使用した場合に比して生産性の向上
につながることにもなる。なお、MDIとポリオールと
だけでのウレタンプレポリマーを作ろうとしても両者が
反応して僅かにウレタン結合を起しただけでも即座に反
応して非常に粘度が高くなって使いものにならなくなる
ので、実際には全く作られていない。
To this, MD may be mixed to obtain the desired hardness. Urethane prepolymers with very few NCO groups are easily miscible with MDI. Furthermore, since MDI has higher reactivity than TDI, when this mixed liquid is used, productivity is improved compared to when a pre-volume using only TDI is used. In addition, even if you try to make a urethane prepolymer using only MDI and polyol, even if the two react and even a slight urethane bond occurs, the reaction will instantly become extremely viscous, making it unusable. It is not made at all.

本願ではTDIとポリオールとを反応させた通常のウレ
タンプレポリマーにMDIを混合してもそんなことには
ならない。本願を使用した実施例を述べると、熱プレス
による成形品であって硬化後の所望物性に応じた分量比
で前述のウレタンプレポリマーにMDIを混合した液を
作り、メチレンクロライドを溶剤とした含浸液を作り、
これを軟質ウレタンフオーム板に含浸させ、ローラー等
で過剰の含浸液を絞り、僅かに加溢して溶剤のメチレン
ク。ラィドを揮発させ、ウレタンフオームの各気泡の内
壁にウレタンプレポリフオームを薄く一様に付着させる
。次に熱プレスの型中に収容してスチーム加熱しつつ圧
縮をすれば反応は即座に起り成形は完了する。従来通常
の発泡方法で成形品を作る時は10分以上の時間が掛っ
たが、本発明によれば2分程度で済むもので、生産速度
が極めて早い。然も非常に薄い部分や細部でも容易に成
形できる。更に表面を装飾用の表皮で飾りたいときはプ
レスの際に表面に表皮を被せてプレスで押し付ければ接
着剤無いこ一体成形ができ上る。(発明の作用) 本願の半硬質樹脂フオーム用含浸剤のウレタンプレポリ
マ−に対するMDIの混和量の比率による硬度の変化は
第1表に示す通りである。
In this application, such a problem does not occur even if MDI is mixed with a normal urethane prepolymer made by reacting TDI with a polyol. To describe an example using the present application, a molded article made by hot pressing is prepared by mixing MDI in the aforementioned urethane prepolymer in a proportion depending on the desired physical properties after curing, and impregnation using methylene chloride as a solvent. make a liquid,
A soft urethane foam plate is impregnated with this, and the excess impregnating liquid is squeezed out using a roller, etc., and the methylene chloride is removed by overflowing slightly. The urethane prepolyfoam is thinly and uniformly adhered to the inner wall of each cell of the urethane foam by volatilizing the Ride. Next, it is placed in a hot press mold and compressed while heating with steam, and the reaction occurs immediately and the molding is completed. Conventionally, it took more than 10 minutes to make a molded product using a normal foaming method, but according to the present invention, it only takes about 2 minutes, making the production speed extremely fast. However, even very thin parts and details can be easily molded. Furthermore, if you want to decorate the surface with a decorative skin, cover the surface with the skin during pressing and press it down to create an integral molding without using adhesive. (Function of the Invention) Table 1 shows the change in hardness depending on the ratio of the amount of MDI to the urethane prepolymer of the impregnating agent for semi-rigid resin foam of the present application.

横鍬に於て左端はMDIIOO%であり、右端はウレタ
ンプレポリマー100%あって中央は1:1即ち等量混
合を示す。堅軸はASKER−F Typeによる硬度
の目盛を示す。図によりMDIが多量に混和される程硬
度が大になることを示している。第2図は同じ〈含浸剤
のウレタンプレポリマーとMDIとの構成量の比率の相
違による含浸フオームの引張り強度変化を示し、横軸は
第1図と同じく左端は、MDIIOO%、右端はウレタ
ンプレポリマー100%で、堅軸は引張り強度をk9′
地の単位で示している。
On the horizontal hoe, the left end is MDIIOO%, the right end is 100% urethane prepolymer, and the center shows 1:1, ie, equal mixing. The hard axis shows the scale of hardness according to ASKER-F Type. The figure shows that the greater the amount of MDI mixed, the greater the hardness. Figure 2 shows the change in the tensile strength of the impregnated foam due to the difference in the ratio of the constituent amounts of the urethane prepolymer and MDI as the impregnating agent, and the horizontal axis is the same as in Figure 1. Made of 100% polymer, the hard shaft has a tensile strength of k9'
It is shown in units of land.

第3図は同じ〈含浸剤のウレタンプレポリマーとMDI
との構成量の比率の相違による含浸フオームの横軸は前
と同じく左端がMDIIOO%、布端がウレタンプレポ
リマー100%で堅軸な伸度を%で現わしている。
Figure 3 is the same (urethane prepolymer and MDI impregnating agent)
As for the horizontal axis of the impregnated foam due to the difference in the ratio of the constituent amounts, as before, the left end is MDIIOO%, the fabric end is 100% urethane prepolymer, and the hard axis represents the elongation in %.

図によれば曲線は殆んど直線に近く斜線を画き左上約2
0%より右上95%迄伸びている。この図によりMDI
の混和が増加するにつれ脆くなることを示して居る。第
4図は同じく含浸剤を構成するウレタンプレポリマーと
MDIとの構成量の比率相違による含浸フオームの反発
弾性変化を示したものである。
According to the diagram, the curve is almost straight with a diagonal line and about 2
It has grown from 0% to 95% in the upper right corner. This figure shows that MDI
It shows that as the amount of admixture increases, the brittleness increases. FIG. 4 also shows the impact resilience change of the impregnated foam due to the difference in the ratio of the urethane prepolymer and MDI constituting the impregnating agent.

同じく横軸左端はMDIIOO%、右端はウレタンプレ
ポリマー100%で中央は1:1を示し、堅藤は反発弾
性を%で示している。この曲線は左端が低く次第に上昇
勾配が急となりMDIが減少する程反発弾性が大になる
ことを示している。即ち概括すればMDIの量が多くな
る程硬く脆くなる傾向を有し、ウレタンポリマーが多く
なる程柔軟でフワフワする傾向を有している。引張強度
は硬度と伸度が丁度にマッチする1:1の比率の部分に
生じている。このように要求される物性に合う製品を現
場で容易に薬液の混合を変えることにより製造できる利
点を持つものである。(発明の効果)本発明はNCO基
%の極く低いようにTDIの量を減じTDIとポリオ−
ルとの反応させてウレタンプレポリマーを作って置き、
使用現場の随所で所望の物性に応じてMDIを其の都度
加減して混合し、樹脂フオームに含浸させて成形するの
で、その樹脂フオーム成形品の硬度等の物性を自在に変
化させる事ができる。
Similarly, the left end of the horizontal axis shows MDIIOO%, the right end shows 100% urethane prepolymer, the center shows 1:1, and Kanto shows impact resilience in %. This curve shows that the left end is low and the upward slope gradually becomes steeper, and as the MDI decreases, the rebound resilience increases. That is, generally speaking, the larger the amount of MDI, the harder and more brittle the material becomes, and the larger the amount of urethane polymer, the more flexible and fluffy the material becomes. The tensile strength occurs in the area where hardness and elongation exactly match in a 1:1 ratio. This has the advantage that products meeting the required physical properties can be manufactured on-site by easily changing the mixture of chemicals. (Effects of the Invention) The present invention reduces the amount of TDI so that the percentage of NCO groups is extremely low.
A urethane prepolymer is made by reacting with
Since MDI is mixed and impregnated into a resin foam at various locations where it is used, adjusting the amount depending on the desired physical properties, it is possible to freely change the physical properties such as hardness of the resin foam molded product. .

従ってウレタンプレポリマーは各種類を必要とせず1種
類のみ準備しておくのみで各種の物性の樹脂フオーム成
形品を得ることができる。さらに、反応基であるNCO
をTDIからMDIに起因させているものであるから、
生産性の向上、環境条件の改良も箸るしい。
Therefore, resin foam molded articles with various physical properties can be obtained by preparing only one type of urethane prepolymer without requiring each type. Furthermore, the reactive group NCO
is caused by MDI from TDI,
Improving productivity and improving environmental conditions are also significant.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図はウレタンプレポリマーとMDI混合液の構成相
違による含浸フオームの硬度変化図、第2図は同じく強
度変化図、第3図は同じく伸度変化図、第4図は同じく
反発弾性図である。 第1図 第2図 第3図 第4図
Figure 1 is a diagram of changes in hardness of the impregnated foam due to differences in composition of the urethane prepolymer and MDI mixture, Figure 2 is a diagram of changes in strength, Figure 3 is a diagram of changes in elongation, and Figure 4 is a diagram of impact resilience. be. Figure 1 Figure 2 Figure 3 Figure 4

Claims (1)

【特許請求の範囲】[Claims] 1 予じめNCO基%を極く低く抑えるようにトリジイ
ソシアネートの量を減じ、ポリオールを反応させて製造
したウレタンプレポリマーに成形直前4・4′−ジフエ
ニールメタンジイソシアネートを適宜に混合比率を変え
て混和し、軟質樹脂フオームに含浸させ、型中で加熱し
て所望物性を有する半硬質・硬質樹脂フオームの製造方
法。
1. Reduce the amount of tridiisocyanate in advance to keep the NCO group % extremely low, and mix 4,4'-diphenylmethane diisocyanate at an appropriate mixing ratio with the urethane prepolymer produced by reacting with polyol immediately before molding. A method for producing a semi-rigid/hard resin foam having desired physical properties by mixing and impregnating it into a soft resin foam and heating it in a mold.
JP8096279A 1979-06-27 1979-06-27 Manufacturing method of semi-rigid/hard resin foam Expired JPS6023133B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8096279A JPS6023133B2 (en) 1979-06-27 1979-06-27 Manufacturing method of semi-rigid/hard resin foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8096279A JPS6023133B2 (en) 1979-06-27 1979-06-27 Manufacturing method of semi-rigid/hard resin foam

Publications (2)

Publication Number Publication Date
JPS565837A JPS565837A (en) 1981-01-21
JPS6023133B2 true JPS6023133B2 (en) 1985-06-06

Family

ID=13733131

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8096279A Expired JPS6023133B2 (en) 1979-06-27 1979-06-27 Manufacturing method of semi-rigid/hard resin foam

Country Status (1)

Country Link
JP (1) JPS6023133B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5899531A (en) * 1981-12-09 1983-06-13 Ikeda Bussan Co Ltd Method for locally strengthening elasticity of damper material for cars

Also Published As

Publication number Publication date
JPS565837A (en) 1981-01-21

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