JPS62288623A - Production of urethane foam - Google Patents

Production of urethane foam

Info

Publication number
JPS62288623A
JPS62288623A JP61130987A JP13098786A JPS62288623A JP S62288623 A JPS62288623 A JP S62288623A JP 61130987 A JP61130987 A JP 61130987A JP 13098786 A JP13098786 A JP 13098786A JP S62288623 A JPS62288623 A JP S62288623A
Authority
JP
Japan
Prior art keywords
polyol
ethylene oxide
component
polyether polyol
100pts
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
JP61130987A
Other languages
Japanese (ja)
Inventor
Kotaro Honda
本多 孝太郎
Hiromichi Hotta
浩通 堀田
Kazuo Mizumura
水村 一夫
Katsuji Kuribayashi
克次 栗林
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.)
M D KASEI KK
Original Assignee
M D KASEI 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 M D KASEI KK filed Critical M D KASEI KK
Priority to JP61130987A priority Critical patent/JPS62288623A/en
Publication of JPS62288623A publication Critical patent/JPS62288623A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To obtain a flexible foam having a low density, low impact resilience and energy absorption effect and suitable for shock absorbing materials, by reacting a specific polyol component with an organic diisocyanate component under expanding conditions. CONSTITUTION:100pts.wt. polyol component consisting of a polyether polyol with 0-50% ethylene oxide and 100-1,000pts.wt. polyether polyol with >=60% ethylene oxide content is reacted with an organic diisocyanate component under expanding condition. In the reaction, a tin catalyst in an amount of 0.01-0.10pts. wt. based on 100pts.wt. polyol component and an amine catalyst in an amount of 0.5-2.0pts.wt. based on 100pts.wt. polyol component are used alone or blended. 1.0-5.0pts.wt. water and 0-20pts.wt. Freon-11 as a foaming agent are blended with the polyol side for use.

Description

【発明の詳細な説明】 3、発明の詳細な説明 〔産業上の利用分野〕 本発明は、ウレタン発泡体の製造法に関するものである
。ウレタン発泡体は低い弾性率を有することから自動車
内装用パッド類や衝撃緩衝材として有効である。
Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Industrial Application] The present invention relates to a method for producing urethane foam. Since urethane foam has a low elastic modulus, it is effective as pads for automobile interiors and shock-absorbing materials.

〔従来の技術〕[Conventional technology]

軟質ウレタン発泡体は、自動車や家具用分野に広く使用
されている。これらに使用されるウレタン発泡体として
、反発弾性率がjO%以上の通称コールドキュアーフオ
ームと呼ばれるものかアシ、エチレンオキサイド含有率
IO−λθ九のポリエーテルポリオールを主に用いてい
る。
Soft urethane foam is widely used in the automobile and furniture fields. As the urethane foam used in these products, a so-called cold cure foam having a rebound modulus of jO% or more and a polyether polyol having an ethylene oxide content of IO-λθ9 are mainly used.

また反発弾性率が3O−J−ONの通称ホット又はセミ
ホットフオームは、エチレンオキサイド含有率O〜/(
1)X程度のポリエーテルポリオールを主に用いている
Also, the so-called hot or semi-hot foam with a rebound modulus of 3O-J-ON has an ethylene oxide content of O~/(
1) A polyether polyol of about X is mainly used.

採用によシ、一層低い反発弾性率のウレタン発泡体を提
供することを目的とする。
The purpose of this invention is to provide a urethane foam having a lower impact modulus.

〔問題点を解決するための手段〕[Means for solving problems]

本発明の目的は、エチレンオキサイド含有率o−zox
のポリエーテルポリオール700重量部およびエチレン
オキサイド含有率603以上のポリエーテルポリオール
ioo〜1ooo**部からなるポリオール成分と有機
イソシアネート成分を発泡条件下において反応させるこ
とによ)達成される。
The object of the present invention is to reduce the ethylene oxide content o-zox
This is achieved by reacting a polyol component consisting of 700 parts by weight of a polyether polyol with an ethylene oxide content of 603 or more and an organic isocyanate component with an organic isocyanate component under foaming conditions.

以下、本発明の詳細な説明する。The present invention will be explained in detail below.

ルである。このようなポリエーテルポリオールハ、水、
エチレングリコール、フロピレンゲリコール、グリセリ
ン又はトリメチルプロパン等を開始剤として使用し、こ
れにエチレンオキサイド、プロピレンオキサイド等のア
ルキレンオキサイドを付加させて得ることができる。ま
た本発明においては、前記ポリエーテルポリオールに、
アクリロニトリル又はポリスチレンをグラフト重合させ
た所謂ポリマーポリオール[用し得る。本発明で用いら
れるエチレンオキサイド含有率o−to!Aおよび60
X以上のポリエーテルポリオールの分子fkh通常to
oo〜1ooooの範囲とされる。
It is le. Such a polyether polyol, water,
It can be obtained by using ethylene glycol, propylene gellicol, glycerin, trimethylpropane, or the like as an initiator, and adding an alkylene oxide such as ethylene oxide or propylene oxide thereto. Further, in the present invention, the polyether polyol includes:
A so-called polymer polyol obtained by graft polymerization of acrylonitrile or polystyrene can be used. Ethylene oxide content used in the present invention o-to! A and 60
Molecules of polyether polyols of X or more fkh usually to
The range is oo to 1oooo.

本発明においては、エチレンオキサイド含有率がQ =
 705Aのポリエーテルポリオールと603以上のポ
リエーテルポリオールとを所定割合で使用することが重
要である。使用割合はエチレンオキサイド含有go−z
oNのポリエーテルポリオール100重量部に対して、
エチレンオキサイド含有藁tO%以上のポリエーテルポ
リオール10θ〜1000重量部である。
In the present invention, the ethylene oxide content is Q =
It is important to use a 705A polyether polyol and a 603 or higher polyether polyol in a predetermined ratio. The usage ratio is ethylene oxide containing go-z
For 100 parts by weight of oN polyether polyol,
Ethylene oxide-containing straw tO% or more polyether polyol is 10θ to 1000 parts by weight.

本発明に使用する有機ジイソシアネート成分としては、
ジフェニルメタンジイソシアネート。
The organic diisocyanate component used in the present invention includes:
Diphenylmethane diisocyanate.

夕 粗ジフェニルメfンジイソシアネート、トリレンジイソ
シアネートまたはそれらの変性物等が挙げられ、またそ
れらの混合物を使用することもできる。
Examples include crude diphenyl diisocyanate, tolylene diisocyanate, and modified products thereof, and mixtures thereof may also be used.

本発明は、上述したポリオール成分及び有機ジイソシア
ネート成分を原料として使用して低反発弾性率を有する
、軟質ポリウレタン発泡体本発明に使用する触媒は、ポ
リウレタン発泡体t−4111造する際、一般に使用さ
れるもので良く、例えば有機スズ化合物触媒、アミン系
触媒がある。有機スズ化合物触媒としては、スタナスオ
クトエート、スタナスオレエート、ジブチルスズジラウ
レート、ジブチルスズーーーエチルヘキソエート等があ
る。アミン触媒として例えば、トリエチレンジアミン、
N−メチルモリホリン。
The present invention is a flexible polyurethane foam having a low impact modulus using the above-mentioned polyol component and organic diisocyanate component as raw materials.The catalyst used in the present invention is generally used when producing polyurethane foam T-4111. For example, organic tin compound catalysts and amine catalysts may be used. Examples of the organic tin compound catalyst include stannath octoate, stannath oleate, dibutyltin dilaurate, dibutyltin-ethylhexoate, and the like. Examples of amine catalysts include triethylenediamine,
N-methylmorpholine.

テトラメチルへキサメチレンジアミン、ジメチルエタノ
ールアミン等を挙げることができるが特に限定されるも
のではない。使用量としては、ポリオール成分100重
量部に対してポリオール側にスズ触媒0.0 / −0
,l 0JII量部、アミン触媒0.2〜ム0重量部を
単独であるいは混合して使用する。
Examples include tetramethylhexamethylenediamine, dimethylethanolamine, etc., but are not particularly limited. The amount used is 0.0/-0 tin catalyst on the polyol side per 100 parts by weight of the polyol component.
, l0JII parts and 0.2 to 0 parts by weight of an amine catalyst are used alone or in combination.

本発明においては、発泡剤として、水及び必要によ〕低
沸点ハロゲンfヒ炭化水Tt’aとえは塩化メチレン、
フレオン−//等を混合して使用することによル望まれ
るフオーム@度を荀るととができる。使用量としては、
ポリオール成分1ooxfIk部に対してポリオール側
に水へ〇〜2.0 rIi量部、yv:tン−//  
o−aoM量WIst使用する。
In the present invention, as blowing agents, water and, if necessary, low-boiling point halogens, carbonated water Tt'a, methylene chloride, etc.
By using a mixture of freon and the like, a desired form can be obtained. As for the amount used,
0 to 2.0 rIi parts of water to the polyol side per 1 ooxfIk part of the polyol component, yv: ton-//
o-aoM quantity WIst is used.

〔実施例〕〔Example〕

実施例/〜3、比較例1−2 第1表に示した配合組成の原料(単位はいずれも′M量
部を示す)を液温度−1℃(インシアネート・ポリオー
ル)、混合時間j秒、モールド温度4Ij”C±j’c
(モールドサイズ4!ooxpooxioo■)脱型時
間3分の条件にてノ%ンドミックスで発泡させ第1表に
示した結果を得た。比較例を合せて表に示す。
Examples/~3, Comparative Example 1-2 Raw materials having the composition shown in Table 1 (all units indicate 'M parts) were mixed at a liquid temperature of -1°C (incyanate polyol) and a mixing time of j seconds. , mold temperature 4Ij"C±j'c
(Mold size 4! ooxpooxioo■) The foaming was performed using a non-permanent mix under the condition that the demolding time was 3 minutes, and the results shown in Table 1 were obtained. Comparative examples are also shown in the table.

*■ポリエーテルポリオール、開始剤グリセリン、go
、po付加、EO含有藁♂OX%分子i3≠00.、J
官能 *■ポリi−ポリオール、開始剤グリセリン。
*■Polyether polyol, initiator glycerin, go
, po addition, EO-containing straw♂OX% molecule i3≠00. , J.
Functionality *■Poly i-polyol, initiator glycerin.

KO,PO付加、KO含有率λO’Aのポリエーテルポ
リオールを7クリロニトリルグラフト重合、アクリロニ
トリル含有9/7X。
KO, PO addition, 7 acrylonitrile graft polymerization of polyether polyol with KO content λO'A, acrylonitrile containing 9/7X.

10含有率/J、jX、分子fJ 000*■ポリエー
テルポリオール、開始剤グリセリン。
10 content/J, jX, molecule fJ 000*■Polyether polyol, initiator glycerin.

go、po付加、!!!O含有率含有率7丹314粗ジ
フエニルメタンジイソシアネート、NOO含有藁J O
.O X 〈発明の効果〉 本発明によれば、柔軟で且つ低密度、低反発弾性のエネ
ルギー吸収効果に優れたウレタン発泡体を提供すること
ができ、自動車内装パッド類や、その他衝撃緩衝材とし
ての用途分野に大きく寄与するものである。
go, po addition,! ! ! O content content 7 Tan 314 crude diphenylmethane diisocyanate, NOO containing straw J O
.. O This will greatly contribute to the field of application.

Claims (1)

【特許請求の範囲】[Claims] (1)エチレンオキサイド含有率0〜50%のポリエー
テルポリオール100重量部およびエチレンオキサイド
含有率60%以上のポリエーテルポリオール100〜1
000重量部からなるポリオール成分と有機ジイソシア
ネート成分を発泡条件下で反応させることを特徴とする
軟質ウレタン発泡体の製造法。
(1) 100 parts by weight of polyether polyol with an ethylene oxide content of 0 to 50% and 100 to 1 part of a polyether polyol with an ethylene oxide content of 60% or more
A method for producing a flexible urethane foam, which comprises reacting a polyol component and an organic diisocyanate component of 000 parts by weight under foaming conditions.
JP61130987A 1986-06-05 1986-06-05 Production of urethane foam Pending JPS62288623A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61130987A JPS62288623A (en) 1986-06-05 1986-06-05 Production of urethane foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61130987A JPS62288623A (en) 1986-06-05 1986-06-05 Production of urethane foam

Publications (1)

Publication Number Publication Date
JPS62288623A true JPS62288623A (en) 1987-12-15

Family

ID=15047268

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61130987A Pending JPS62288623A (en) 1986-06-05 1986-06-05 Production of urethane foam

Country Status (1)

Country Link
JP (1) JPS62288623A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0913414A1 (en) * 1997-10-28 1999-05-06 Tokai Rubber Industries, Ltd. Soft polyurethane foam, method of producing the same and vehicle interior member using the same
CN113461904A (en) * 2021-08-10 2021-10-01 中山成长鞋材有限公司 Soft, high-elasticity, water-absorbing and non-swelling polyether foam and preparation method thereof
CN113583205A (en) * 2021-06-29 2021-11-02 佳化化学科技发展(上海)有限公司 Slow-resilience sponge and preparation method and application thereof

Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5298096A (en) * 1975-12-22 1977-08-17 M & T Chemicals Inc Process for producing polyurethane foam with high resilience
JPS54148893A (en) * 1978-05-15 1979-11-21 Bridgestone Corp Production of flexible polyether polyurethane foam
JPS5558216A (en) * 1978-10-24 1980-04-30 Mitui Toatsu Chem Inc Production of polyurethane foam
JPS5589326A (en) * 1978-12-27 1980-07-05 Toyoda Gosei Co Ltd Production of urethan foam for shock absorption
JPS5620017A (en) * 1979-07-30 1981-02-25 Achilles Corp Production or low-smoking rigid foam
JPS5653126A (en) * 1979-10-08 1981-05-12 Dai Ichi Kogyo Seiyaku Co Ltd Preparation of semirigid urethane foam
JPS5667330A (en) * 1979-11-07 1981-06-06 Mitui Toatsu Chem Inc Production of soft polyurethane foam
JPS56116716A (en) * 1980-02-19 1981-09-12 Asahi Glass Co Ltd Preparation of polyurethane foam for energy absorption
JPS56127627A (en) * 1976-07-06 1981-10-06 Union Carbide Corp High ethylene oxide quantity polyol and mixture containing it
JPS57131217A (en) * 1981-02-06 1982-08-14 Achilles Corp Production of low-smoking urethane-modified isocyanurate foam
JPS57135856A (en) * 1981-02-17 1982-08-21 Asahi Glass Co Ltd Polyether polyol composition
JPS57198722A (en) * 1981-06-02 1982-12-06 Mitui Toatsu Chem Inc Production of spray-type flexible polyurethane foam of high elasticity
JPS5925810A (en) * 1982-06-22 1984-02-09 Sumitomo Bayer Urethane Kk Preparation of flexible polyurethane foam
JPS60181115A (en) * 1984-02-28 1985-09-14 Sanyo Chem Ind Ltd Production of polyurethane
JPS60186519A (en) * 1980-06-30 1985-09-24 ユニオン・カ−バイド・コ−ポレ−シヨン Manufacture of urethane foam
JPS60206819A (en) * 1984-03-30 1985-10-18 Sanyo Chem Ind Ltd Production of polyurethane molding
JPS612723A (en) * 1984-06-14 1986-01-08 Sanyo Chem Ind Ltd Manufacture of foam
JPS6136315A (en) * 1984-07-30 1986-02-21 Nisshinbo Ind Inc Vibration-damping material
JPS61171720A (en) * 1985-01-24 1986-08-02 Sanyo Chem Ind Ltd Production of polyurethane

Patent Citations (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5298096A (en) * 1975-12-22 1977-08-17 M & T Chemicals Inc Process for producing polyurethane foam with high resilience
JPS56127627A (en) * 1976-07-06 1981-10-06 Union Carbide Corp High ethylene oxide quantity polyol and mixture containing it
JPS54148893A (en) * 1978-05-15 1979-11-21 Bridgestone Corp Production of flexible polyether polyurethane foam
JPS5558216A (en) * 1978-10-24 1980-04-30 Mitui Toatsu Chem Inc Production of polyurethane foam
JPS5589326A (en) * 1978-12-27 1980-07-05 Toyoda Gosei Co Ltd Production of urethan foam for shock absorption
JPS5620017A (en) * 1979-07-30 1981-02-25 Achilles Corp Production or low-smoking rigid foam
JPS5653126A (en) * 1979-10-08 1981-05-12 Dai Ichi Kogyo Seiyaku Co Ltd Preparation of semirigid urethane foam
JPS5667330A (en) * 1979-11-07 1981-06-06 Mitui Toatsu Chem Inc Production of soft polyurethane foam
JPS56116716A (en) * 1980-02-19 1981-09-12 Asahi Glass Co Ltd Preparation of polyurethane foam for energy absorption
JPS60186519A (en) * 1980-06-30 1985-09-24 ユニオン・カ−バイド・コ−ポレ−シヨン Manufacture of urethane foam
JPS57131217A (en) * 1981-02-06 1982-08-14 Achilles Corp Production of low-smoking urethane-modified isocyanurate foam
JPS57135856A (en) * 1981-02-17 1982-08-21 Asahi Glass Co Ltd Polyether polyol composition
JPS57198722A (en) * 1981-06-02 1982-12-06 Mitui Toatsu Chem Inc Production of spray-type flexible polyurethane foam of high elasticity
JPS5925810A (en) * 1982-06-22 1984-02-09 Sumitomo Bayer Urethane Kk Preparation of flexible polyurethane foam
JPS60181115A (en) * 1984-02-28 1985-09-14 Sanyo Chem Ind Ltd Production of polyurethane
JPS60206819A (en) * 1984-03-30 1985-10-18 Sanyo Chem Ind Ltd Production of polyurethane molding
JPS612723A (en) * 1984-06-14 1986-01-08 Sanyo Chem Ind Ltd Manufacture of foam
JPS6136315A (en) * 1984-07-30 1986-02-21 Nisshinbo Ind Inc Vibration-damping material
JPS61171720A (en) * 1985-01-24 1986-08-02 Sanyo Chem Ind Ltd Production of polyurethane

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0913414A1 (en) * 1997-10-28 1999-05-06 Tokai Rubber Industries, Ltd. Soft polyurethane foam, method of producing the same and vehicle interior member using the same
US6136879A (en) * 1997-10-28 2000-10-24 Tokai Rubber Industries, Ltd. Soft polyurethane foam, method of producing the same and vehicle interior member using the same
CN113583205A (en) * 2021-06-29 2021-11-02 佳化化学科技发展(上海)有限公司 Slow-resilience sponge and preparation method and application thereof
CN113461904A (en) * 2021-08-10 2021-10-01 中山成长鞋材有限公司 Soft, high-elasticity, water-absorbing and non-swelling polyether foam and preparation method thereof

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