JPS62164709A - Production of polyurethane foam - Google Patents

Production of polyurethane foam

Info

Publication number
JPS62164709A
JPS62164709A JP61005589A JP558986A JPS62164709A JP S62164709 A JPS62164709 A JP S62164709A JP 61005589 A JP61005589 A JP 61005589A JP 558986 A JP558986 A JP 558986A JP S62164709 A JPS62164709 A JP S62164709A
Authority
JP
Japan
Prior art keywords
foaming
stock solution
polyurethane foam
pressure
urethane
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
JP61005589A
Other languages
Japanese (ja)
Inventor
Sadao Kumasaka
貞男 熊坂
Satomi Tada
多田 郷見
Koretoshi Katsuki
是利 香月
Ryoji Nagamine
長嶺 亮二
Masao Idei
正男 出井
Yosuke Sato
陽介 佐藤
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.)
Human Industry Corp
Original Assignee
Human Industry Corp
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 Human Industry Corp filed Critical Human Industry Corp
Priority to JP61005589A priority Critical patent/JPS62164709A/en
Publication of JPS62164709A publication Critical patent/JPS62164709A/en
Pending legal-status Critical Current

Links

Landscapes

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

Abstract

PURPOSE:To obtain a low-density polyurethane foam without causing scorching, by foaming a specified urethane foaming stock solution in an atmosphere of a reduced pressure. CONSTITUTION:A urethane foaming stock solution is obtained by mixing a polyol (e.g., polyether polyol) with an organic isocyanate (e.g., tolylene diisocyanate) and, optionally, an amine catalyst (e.g., triethylenediamine), a silicone oil, a tin catalyst (e.g., dibutyltin dilaurate), and a blowing agent (e.g., water). This solution is foamed. When it starts rising, the pressure is reduced so that the degree of vacuum may be at least 50mmHg, preferably, 100-500mmHg below atmospheric pressure, and the foaming is continued.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明はポリウレタンフォームの製造方法に関し、特に
低密度のポリウレタンフォームを得る方法に係る。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for producing polyurethane foam, and in particular to a method for obtaining low density polyurethane foam.

〔従来の技術〕[Conventional technology]

ポリウレタンフォームは広範囲の用途に使用されており
、その目的とする用途に応じて低密産品から高密度量に
亘る種々の製品が製造されている。
Polyurethane foams are used in a wide variety of applications and are manufactured in a variety of products ranging from low-density products to high-density quantities depending on their intended use.

ポリウレタンフォーム製造する際に製品の密度の調節す
る手段としては1発泡剤(主に水)や発泡助剤(トリク
ロロモノフルオロメタン、メチレンクロライド等の低沸
点溶剤)の添加量を増減する方法が従来行なわれている
。従って、密度のポリウレタンフォームを製造する場合
には1発泡倍率が高くなるように多くの水を使用して発
泡を行なっている。
When manufacturing polyurethane foam, the conventional method for adjusting the density of the product is to increase or decrease the amount of blowing agents (mainly water) and blowing aids (low-boiling solvents such as trichloromonofluoromethane and methylene chloride). It is being done. Therefore, when producing high-density polyurethane foam, a large amount of water is used to perform foaming so as to increase the foaming ratio.

〔発明が解決しようとする問題点〕[Problem that the invention seeks to solve]

ところで、ポリウレタンフォームの製造における発泡作
用は有機インシアネートと水との反応で生成する炭酸ガ
スによるものであるため、従来の製造方法では目的とす
る製品の密度に応じで原料の配合処方を変えなければな
らない、特に、低密度のウレタンフオームを製造するた
めには発泡剤である水の添加量を多くしなければならず
、このため次のような問題を生じていた。
By the way, the foaming effect in the production of polyurethane foam is due to carbon dioxide gas generated by the reaction between organic incyanate and water, so in conventional production methods, the formulation of raw materials must be changed depending on the density of the desired product. In particular, in order to produce a low-density urethane foam, it is necessary to add a large amount of water as a blowing agent, which causes the following problems.

第−は、多量の水とインシアネートとを反応させること
になるため、発泡体の内部温度が反応熱で著しく高くな
り、所謂スコーチ(焼けによる変色)を生じ易いことで
ある。従って、スコーチ防止剤を添加しなければならな
い。
The first problem is that since a large amount of water and incyanate are reacted, the internal temperature of the foam becomes significantly high due to the heat of reaction, which tends to cause so-called scorch (discoloration due to burning). Therefore, scorch inhibitors must be added.

更に、水の添加比率はポリオール100重量部に対して
6〜7重量部が上限であるが、このような低密度発泡体
では上記の問題が顕著に現れ、火災発生の危険もある。
Further, the upper limit of the addition ratio of water is 6 to 7 parts by weight per 100 parts by weight of polyol, but in such a low density foam, the above-mentioned problems are noticeable and there is a risk of fire.

第二は、有機イソシアネート、トリクロロモノフルオロ
メタン等の使用量が増大するためガスロスが高くなり、
歩留が低下することである。
Second, gas loss increases due to increased usage of organic isocyanates, trichloromonofluoromethane, etc.
This results in a decrease in yield.

上記車情に鑑み1本発明は同一配合処方の発泡原液から
密度の異なる種々のポリウレタンフォーム、特に低密度
量を製造することを目的とする。
In view of the above circumstances, it is an object of the present invention to produce polyurethane foams of various densities, particularly low-density products, from a foaming solution having the same formulation.

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

本発明では1発泡原液の処方を変える代りに、発泡させ
る雰囲気の圧力を変化させることで製品の密度をtia
mすることにした。
In the present invention, instead of changing the formulation of the foaming stock solution, the density of the product is changed by changing the pressure of the foaming atmosphere.
I decided to m.

即ち、本発明によるポリウレタンフォームの製造方法は
、ポリオール、有機インシアネート、アミン触媒、シリ
コーン油、錫触媒、発泡剤としての水、顔料、充填剤等
の物性改良剤、その他ウレタンフオームの製造に通常使
用される配合成分から選択した原料を混合してウレタン
発泡原液を調製し、該ウレタン発泡原液を発泡させてポ
リウレタンフォームを製造する方法において、減圧雰囲
気下で発泡させることを特徴とするものである。
That is, the method for producing polyurethane foam according to the present invention uses polyol, organic incyanate, amine catalyst, silicone oil, tin catalyst, water as a blowing agent, physical property improvers such as pigments and fillers, and other materials commonly used in the production of urethane foam. A method for producing polyurethane foam by mixing raw materials selected from the ingredients used to prepare a urethane foam stock solution and foaming the urethane foam stock solution, which is characterized by foaming under a reduced pressure atmosphere. .

本発明における発泡原液の各原料成分としては、従来使
用されているものをそのまま用いることができる8例え
ば、ポリオールとしてはポリエーテルポリオール、或い
はポリエステルポリオールを用いることができる。また
、有機イソシアネートとしてはトリレンジイソシアネー
ト、4.4′−ジフェニルメタンジイソシアネート、ポ
リメリックMDI、ナフタレンジイソシアネート等を用
いることができる。
As each raw material component of the foaming stock solution in the present invention, those conventionally used can be used as they are.8 For example, as the polyol, polyether polyol or polyester polyol can be used. Further, as the organic isocyanate, tolylene diisocyanate, 4,4'-diphenylmethane diisocyanate, polymeric MDI, naphthalene diisocyanate, etc. can be used.

本発明において所定の減圧雰囲気を得る形態としては、
例えば発泡容器自体を減圧室として構成し、ポンプで吸
引すればよい、また発泡容器を別途用意した減圧室内に
収容して発泡させるようにしてもよい、何れにしても、
バッチ式のプロセスの方が適用し易い、しかし、大規模
な減圧室を用いれば連続式のプロセスにも適用可能であ
る。
In the present invention, the form of obtaining a predetermined reduced pressure atmosphere is as follows:
For example, the foaming container itself may be configured as a decompression chamber and suction may be performed using a pump, or the foaming container may be housed in a separately prepared decompression chamber to cause foaming.
Batch-type processes are easier to apply, but continuous processes can also be applied if a large-scale vacuum chamber is used.

本発明における減圧雰囲気は、配合処方や目的とする製
品の密度等によって当然に変化する0通常は常圧からの
減圧量が略50濡taHg以上とするのが良く、最適に
は常圧からの減圧量が100〜500 mmHHの範囲
である。
The reduced pressure atmosphere in the present invention naturally varies depending on the formulation, the density of the target product, etc. Usually, the amount of reduced pressure from normal pressure is preferably approximately 50 wet taHg or more, and optimally the reduced pressure from normal pressure is approximately 50 taHg or more. The amount of pressure reduction is in the range of 100 to 500 mmHH.

本発明において減圧を行なう時点は、発泡原液を注入後
すぐでもよいが、発泡反応が開始して発泡原液のライズ
が開始してからの方が好ましい。
In the present invention, the pressure may be reduced immediately after the foaming stock solution is injected, but preferably after the foaming reaction has started and the foaming stock solution has started to rise.

〔作用〕[Effect]

本発明における発泡反応自体は、従来のポリウレタンフ
ォーム製造の際の発泡反応と全く同じで、有機インシア
ネートと水の反応で生成した炭酸ガスの作用で気泡が形
成される。
The foaming reaction itself in the present invention is exactly the same as the foaming reaction in conventional polyurethane foam production, and bubbles are formed by the action of carbon dioxide gas produced by the reaction of organic incyanate and water.

しかし、本発明では炭酸ガスによる発泡作用が減圧下で
行なわれるため、その作用が増強されることになる。即
ち、気泡の形成は発泡原液中で生成した炭酸ガスの逃散
力に依存し、この逃散力は雰囲気圧に対する生成した炭
酸ガス蒸気圧の相対的な大きさで決まる。従って、生成
した炭酸ガスの全量が同一でその分圧が同じであっても
、雰囲気圧力が低ければその逃散力は大きくなる。しか
も生成した炭酸ガスが気化し易いから、生成量が同じで
も発泡に有効に作用する比率が向上する。
However, in the present invention, since the foaming effect of carbon dioxide gas is performed under reduced pressure, the effect is enhanced. That is, the formation of bubbles depends on the escape power of the carbon dioxide gas generated in the foaming stock solution, and this escape force is determined by the relative magnitude of the vapor pressure of the generated carbon dioxide gas with respect to the atmospheric pressure. Therefore, even if the total amount of carbon dioxide gas produced is the same and its partial pressure is the same, the lower the atmospheric pressure, the greater its escaping force. Moreover, since the generated carbon dioxide gas is easily vaporized, the ratio of effective effect on foaming is improved even if the amount of generated carbon dioxide remains the same.

こうして同一処方の発泡原液も用いた場合にも、生成す
る炭酸ガスの気化効率を向上し、且つその発泡作用を増
強することによって発泡倍率を高め、低密度のポリウレ
タンフォームが得られる。
In this way, even when a foaming stock solution with the same formulation is used, the foaming ratio is increased by improving the vaporization efficiency of the generated carbon dioxide gas and reinforcing its foaming action, and a low-density polyurethane foam can be obtained.

〔実施例〕 ポリエーテルポリオール    100.00重量部(
分子量3000.3官能、 OH価56)トリエチレン
ジアミン      0.08  /1ノルマルエチル
モルホリン    Q、5  ttシリコーン油   
       1,4  /1ジブチルチンジラウレー
トQ、35  ttトリクロロモノフルオロメタン  
5.OttH204,0/1 トリレンジイソシアネー)     53.Ott上記
配合処方からなるポリウレタン発泡原液を調製し、下記
のようにしてバッチ方式でポリウレタンフォームを製造
した。
[Example] Polyether polyol 100.00 parts by weight (
Molecular weight 3000.3 functional, OH value 56) Triethylenediamine 0.08/1 normal ethylmorpholine Q, 5 tt silicone oil
1,4/1 dibutyltin dilaurate Q, 35 tt trichloromonofluoromethane
5. OttH204,0/1 tolylene diisocyanate) 53. Ott A polyurethane foam stock solution having the above-mentioned formulation was prepared, and polyurethane foam was produced in a batch manner as described below.

まず、添付の図面に示す減圧タンク11内に収容されて
いる発泡容器lO内に上記で調製した発泡原液を注入し
、減圧タンクの蓋を閉じて密封した0次いで、発泡原液
のライズが開始してからバルブ12を開き、減圧タンク
llを真空ポンプ13に連通させて減圧タンク内を所定
の量だけ減圧した。この減圧下で発泡を完了させた後、
送気管14を開いて減圧タンク内を常圧に戻し、発泡容
器10からポリウレタンフォームを取り出した。なお、
所定の減圧下に発泡が行なわれているか否かについては
2減圧タンク11に付設したゲージ15により常時監視
した。
First, the foaming stock solution prepared above is poured into the foaming container 10 housed in the vacuum tank 11 shown in the attached drawing, and the lid of the vacuum tank is closed and sealed.Next, the foaming stock solution starts to rise. Then, the valve 12 was opened, and the pressure reduction tank 11 was communicated with the vacuum pump 13 to reduce the pressure in the pressure reduction tank by a predetermined amount. After completing foaming under this reduced pressure,
The air pipe 14 was opened to return the inside of the vacuum tank to normal pressure, and the polyurethane foam was taken out from the foaming container 10. In addition,
Whether or not foaming was being carried out under a predetermined reduced pressure was constantly monitored using a gauge 15 attached to the two reduced pressure tanks 11.

タンク11内の減圧量を100 mmHg、200 r
arsHg。
Reduce the pressure inside the tank 11 to 100 mmHg and 200 r.
arsHg.

300 mmHg、 400 mmHg、500■■H
gとして上記の方法によりポリウレタンフォームを製造
し、夫々の場合に得られた製品の特性を調べた。また、
比較例として同一の発泡原液を常圧下、即ち減圧量0■
■Hgで同様に発泡させ、得られた製品の特性を調べた
。これらの結果を下記第1表に示す。
300mmHg, 400mmHg, 500■■H
Polyurethane foam was produced using the method described above, and the properties of the products obtained in each case were investigated. Also,
As a comparative example, the same foaming stock solution was used under normal pressure, that is, the amount of pressure reduction was 0
(2) Foaming was carried out in the same manner using Hg, and the properties of the obtained product were investigated. These results are shown in Table 1 below.

第    1    表 上記の結果に示すように、同じ配合処方の発泡原液を用
いて密度の異なる種々のポリウレタンフォームを得るこ
とができた。しかも、密度0.0098g/c+s”の
低密度量でもスコーチ現象は全く見られなかった。
As shown in the results in Table 1 above, it was possible to obtain various polyurethane foams with different densities using the same foaming stock solution. Furthermore, no scorch phenomenon was observed even at a low density of 0.0098 g/c+s''.

また、実施例量では表面のスキン層が比較例量よりもか
なり薄くなっていた。これは、減圧しているため雰囲気
中に存在する酸素分圧が低く。
Furthermore, the skin layer on the surface of the Example amount was considerably thinner than that of the Comparative Example amount. This is because the pressure is reduced, so the oxygen partial pressure present in the atmosphere is low.

従って発泡の過程で酸素との接触により生じる表面性状
の劣化が抑制されたものと推定される。
Therefore, it is presumed that the deterioration of surface properties caused by contact with oxygen during the foaming process was suppressed.

〔発明の効果〕〔Effect of the invention〕

以上詳述したように1本発明によれば同一配合処方の発
泡原液から密度の異なる種々のポリウレタンフォームを
製造することができ、特に従来のようなスコーチ現象を
生じることなく低密度のポリウレタンフォームを製造で
きる等、WJ著な効果が得られるものである・
As detailed above, according to the present invention, various polyurethane foams with different densities can be produced from a foaming stock solution having the same formulation, and in particular, low-density polyurethane foams can be produced without causing the scorch phenomenon as in the past. It is a product that can be manufactured and has remarkable effects from WJ.

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

添付の図面は、本発明の実施例で用いた発泡装置の説明
図である。 10・・・発泡容器、11・・・減圧タンク、12・・
・真空バルブ、13・・・真空ポンプ、14・・・送気
管、15・・・圧力ゲージ
The attached drawings are explanatory views of the foaming device used in the examples of the present invention. 10... Foaming container, 11... Decompression tank, 12...
・Vacuum valve, 13... Vacuum pump, 14... Air pipe, 15... Pressure gauge

Claims (1)

【特許請求の範囲】[Claims] ポリオール、有機イソシアネート、アミン触媒、シリコ
ーン油、錫触媒、発泡剤としての水、顔料、充填剤等の
物性改良剤、その他ウレタンフォームの製造に通常使用
される配合成分から選択した原料を混合してウレタン発
泡原液を調製し、該ウレタン発泡原液を発泡させてポリ
ウレタンフォームを製造する方法において、減圧雰囲気
下で発泡させることを特徴とするポリウレタンフォーム
の製造方法。
By mixing raw materials selected from polyols, organic isocyanates, amine catalysts, silicone oils, tin catalysts, water as blowing agents, physical property improvers such as pigments and fillers, and other compounding components commonly used in the production of urethane foam. A method for producing polyurethane foam by preparing a urethane foaming stock solution and foaming the urethane foaming stock solution, the method comprising foaming under a reduced pressure atmosphere.
JP61005589A 1986-01-14 1986-01-14 Production of polyurethane foam Pending JPS62164709A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61005589A JPS62164709A (en) 1986-01-14 1986-01-14 Production of polyurethane foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61005589A JPS62164709A (en) 1986-01-14 1986-01-14 Production of polyurethane foam

Publications (1)

Publication Number Publication Date
JPS62164709A true JPS62164709A (en) 1987-07-21

Family

ID=11615425

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61005589A Pending JPS62164709A (en) 1986-01-14 1986-01-14 Production of polyurethane foam

Country Status (1)

Country Link
JP (1) JPS62164709A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4408968A1 (en) * 1993-03-16 1994-09-22 Toyoda Gosei Kk Process and polyurethane material for the moulding of a semirigid structural foam
US5449698A (en) * 1991-09-26 1995-09-12 Toyoda Gosei Co., Ltd. Method and apparatus for producing integral skin polyurethane foam
US5464582A (en) * 1990-06-12 1995-11-07 Toyoda Gosei Co., Ltd. Method for molding polyurethane foam under subatmospheric pressures
US5476619A (en) * 1993-06-19 1995-12-19 Toyoda Gosei Co., Ltd. Process for molding an integral skin foam using an evacuated mold cavity
US5540576A (en) * 1992-12-22 1996-07-30 Toyoda Gosei Co., Ltd. Apparatus having a vacuum chamber for producing moldings
DE4447494C2 (en) * 1993-04-30 1998-05-28 Toyoda Gosei Kk Integral skin foam mouldings prodn.
JP2010260932A (en) * 2009-04-30 2010-11-18 Bridgestone Corp Polyurethane foam molding

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5464582A (en) * 1990-06-12 1995-11-07 Toyoda Gosei Co., Ltd. Method for molding polyurethane foam under subatmospheric pressures
US5589202A (en) * 1990-06-12 1996-12-31 Toyoda Gosei Co., Ltd. Apparatus for molding polyurethane foam
US5449698A (en) * 1991-09-26 1995-09-12 Toyoda Gosei Co., Ltd. Method and apparatus for producing integral skin polyurethane foam
US5540576A (en) * 1992-12-22 1996-07-30 Toyoda Gosei Co., Ltd. Apparatus having a vacuum chamber for producing moldings
DE4408968A1 (en) * 1993-03-16 1994-09-22 Toyoda Gosei Kk Process and polyurethane material for the moulding of a semirigid structural foam
US5633289A (en) * 1993-03-16 1997-05-27 Toyoda Gosei Co., Ltd. Process for molding an integral skin foam and a polyurethane material for molding the same
DE4408968C2 (en) * 1993-03-16 1998-07-09 Toyoda Gosei Kk Process for molding an integral foam
DE4447494C2 (en) * 1993-04-30 1998-05-28 Toyoda Gosei Kk Integral skin foam mouldings prodn.
US5476619A (en) * 1993-06-19 1995-12-19 Toyoda Gosei Co., Ltd. Process for molding an integral skin foam using an evacuated mold cavity
JP2010260932A (en) * 2009-04-30 2010-11-18 Bridgestone Corp Polyurethane foam molding

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