JPS5823406B2 - Nanshitsu Urethane Foam No Seizouhouhou - Google Patents
Nanshitsu Urethane Foam No SeizouhouhouInfo
- Publication number
- JPS5823406B2 JPS5823406B2 JP50149487A JP14948775A JPS5823406B2 JP S5823406 B2 JPS5823406 B2 JP S5823406B2 JP 50149487 A JP50149487 A JP 50149487A JP 14948775 A JP14948775 A JP 14948775A JP S5823406 B2 JPS5823406 B2 JP S5823406B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- foam
- parts
- urethane foam
- value
- 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
Links
Description
【発明の詳細な説明】
本発明は独立気泡からなる軟質ポリウレタンフォームを
製造する方法の改良に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in the method of manufacturing closed-cell flexible polyurethane foam.
一般に軟質ポリウレタンフォームは連通気泡構。Generally, flexible polyurethane foam has an open cell structure.
造からなっているものである。It is made up of structures.
従ってこのような軟質ポリウレタンフォームは断熱性、
断音性に劣るものであり、室内を保温又は防音性にする
ための内装材としては適用し難いものであった。Therefore, such flexible polyurethane foam has insulation properties,
It has poor sound insulation properties and is difficult to be used as an interior material for making a room heat-insulating or sound-proof.
かかる見地から従来独立気泡からなる軟質ポリウレタン
フォームを得んとする方法が試みられている。From this point of view, conventional methods have been attempted to obtain flexible polyurethane foams consisting of closed cells.
即ち軟質ポリオールに触媒、発泡剤及び有機インシアネ
ートを添加反応して軟質ポリウレタンフォームを製造す
るものであるが、その場合触媒として使用する錫系触媒
とアミン系触媒の内特に発泡に有効作用を及ぼす錫系触
媒の添加量に細心の注意をはらっているものであり、そ
の量を調整することが極めて重要なことである。That is, flexible polyurethane foam is produced by adding and reacting a catalyst, a blowing agent, and an organic incyanate to a flexible polyol. In this case, among the tin-based catalyst and amine-based catalyst used as a catalyst, particularly effective foaming is performed. Careful attention is paid to the amount of tin-based catalyst added, and it is extremely important to adjust the amount.
而して錫系触媒の添加量は通常の軟質ポリオール100
重量部に対し0.05〜0.5重量部程度を使用するも
のであるが、該触媒は前記の如く微妙な作用を及ぼし、
その調整は極めて困難であり、添加量の如何によっては
軟質ポリウレタンフォームは著しく収縮し、これに伴い
異型のものとなる。Therefore, the amount of tin-based catalyst added is 100% of the normal soft polyol.
The catalyst is used in an amount of about 0.05 to 0.5 parts by weight, but as mentioned above, the catalyst has a delicate effect,
Adjustment is extremely difficult, and depending on the amount added, the flexible polyurethane foam will shrink significantly, resulting in irregular shapes.
従って常時一定の成型品を得ることが出来ないものであ
った。Therefore, it was not possible to always obtain a constant molded product.
父上記方法による場合には、反応熱が比較的高く(通常
150〜170℃)なるため、このままの状態におかれ
ると発泡体の内部にスコーチ(ヤケ)をおこし易く、良
質な軟質ポリウレタンフォームを得ることが出来難いも
のであった。In the case of using the above method, the reaction heat is relatively high (usually 150 to 170°C), so if left in this state, it is easy to cause scorch (scorch) inside the foam, making it difficult to use high-quality flexible polyurethane foam. It was difficult to obtain.
本発明はかかる欠点を改善するために鋭意研究を行った
結果独立気泡からなる軟質ポリウレタンフォームを容易
にかつ安定して製造する方法を見出したものである。The present invention has been made as a result of extensive research aimed at improving these drawbacks, and has resulted in the discovery of a method for easily and stably producing flexible polyurethane foam consisting of closed cells.
即ち本発明は官能基数3個以上にして且つOH価70以
上を有するポリヒドロキシ化合物と有機インシアネート
とを混合し、これを反応せしめて末端にOH基を有する
ウレタンプレポリマー20〜70重量部とポリエーテル
ポリオール80〜30重量部とを混合し、更に有機イソ
シアネート、錫系及びアミン系触媒、整泡剤その他必要
に応じて難燃剤、増量剤等を配合し、これを混合反応せ
しめることを特徴とするものである。That is, in the present invention, a polyhydroxy compound having three or more functional groups and an OH value of 70 or more is mixed with an organic incyanate, and the mixture is reacted with 20 to 70 parts by weight of a urethane prepolymer having an OH group at the end. It is characterized by mixing 80 to 30 parts by weight of polyether polyol, further adding organic isocyanates, tin-based and amine-based catalysts, foam stabilizers, and other flame retardants and extenders as necessary, and allowing the mixture to react. That is.
本発明においてポリヒドロキシ化合物において官能基数
3個以上及びOH価70以上と限定した理由は官能基数
2個以下のもの及びOH価70未満のものを使用する場
合には連通気泡のものが多く独立気泡のものが少いフオ
ームを得るためである。In the present invention, the reason why polyhydroxy compounds are limited to 3 or more functional groups and OH value 70 or more is that when using polyhydroxy compounds with 2 or less functional groups and OH value less than 70, they are often open-celled. This is to obtain a form with less .
従ってOH価は望ましくは70〜250の範囲のものが
好ましい。Therefore, the OH value is preferably in the range of 70 to 250.
而して官能基数3個以上にしてOK価70以上を有する
ポリヒドロキシ化合物としては、グリセリン、トリメチ
ロールプロパン(3官能)、ペンタエリスリトール、α
−メチルグリコシド(4官能)、その他エチレンジアミ
ン、ンルビトール、シュークローズなどに酸化エチレン
、酸化プロピレン等を附加重合せしめてOH価を70以
上としたものである。Examples of polyhydroxy compounds having three or more functional groups and an OK value of 70 or more include glycerin, trimethylolpropane (trifunctional), pentaerythritol, α
- Methyl glycoside (tetrafunctional), ethylenediamine, nrubitol, sucrose, etc. are added and polymerized with ethylene oxide, propylene oxide, etc. to have an OH value of 70 or more.
又、ウレタンプレポリマーはポリヒドロキシ化合物(O
H価70〜250)とトリレンジイソシアネート、ジフ
ェニルメタンジイソシアネート等の有機イソシアネート
とを常法によって得るものである。In addition, the urethane prepolymer is a polyhydroxy compound (O
H value 70 to 250) and organic isocyanates such as tolylene diisocyanate and diphenylmethane diisocyanate are obtained by a conventional method.
この場合ポリヒドロキシ化合物のOH基とイソシアネー
トのNCOが反応した結果、末端がOHとなるようにイ
ンシアネートの量を調整することが必要である。In this case, it is necessary to adjust the amount of incyanate so that the OH group of the polyhydroxy compound reacts with the NCO of the isocyanate, resulting in an OH terminal.
本発明において軟質のポリオールを得るには、例えばエ
チレングリコール、ジエチレングリコール、プロピレン
グリコール、(2官能)グリセリン(3官能)等に酸化
エチレン、酸化プロピレン等を附加重合せしめてOH価
を略70未満のものを使用するものである。In the present invention, in order to obtain a soft polyol, for example, ethylene glycol, diethylene glycol, propylene glycol, (bifunctional) glycerin (trifunctional), etc. are added and polymerized with ethylene oxide, propylene oxide, etc. to obtain a polyol having an OH value of approximately less than 70. is used.
又本発明方法においてウレタンプレポIJ −f −2
0〜70重量部と軟質ポリオール80〜30重量部の比
率にて配合する理由は、この範囲外にて混合反応せしめ
た場合には、十分な独立気泡の軟質ポリウレタンフォー
ムを得ることが出来ないためである。Further, in the method of the present invention, urethane prepo IJ-f-2
The reason for blending at a ratio of 0 to 70 parts by weight and 80 to 30 parts by weight of the flexible polyol is that if the mixing reaction is carried out outside this range, it will not be possible to obtain a sufficient closed-cell flexible polyurethane foam. It is.
なお、本発明方法において整泡剤としてはシリコンなど
であり、その他難燃剤、増量剤等適宜配合してもよい。In the method of the present invention, the foam stabilizer is silicone, etc., and other flame retardants, fillers, etc. may be added as appropriate.
次に本発明の実施例について説明する。Next, examples of the present invention will be described.
実施例 1
分子量約1000.3官能、OH価165のポリエーテ
ルポリオール100重量部に対しトリエンジイソシアネ
ート10重量部を添加混合し90℃にて3時間攪拌反応
させ残留OH#100のプレポリマーを得た。Example 1 10 parts by weight of triene diisocyanate was added and mixed to 100 parts by weight of a polyether polyol having a functional molecular weight of about 1000.3 and an OH value of 165, and the mixture was stirred and reacted at 90°C for 3 hours to obtain a prepolymer with residual OH #100. .
本プレポリマーを使用し下記配合処方にて軟質ウレタン
フオームを得た。A soft urethane foam was obtained using this prepolymer according to the following formulation.
得られたフオームは全体均一な独立気泡を有する良好な
ものであった。The obtained foam was good and had uniform closed cells throughout.
実施例 2
実施例1で得たプレポリマーを使用し下記配合処方にて
軟質ウレタンフオームを得た。Example 2 Using the prepolymer obtained in Example 1, a soft urethane foam was obtained according to the following formulation.
得られたフオームは全体均一な独立気泡を有する良好な
ものであった。The obtained foam was good and had uniform closed cells throughout.
比較例 1 下記配合処方にて軟質ウレタンフオームを得た。Comparative example 1 A soft urethane foam was obtained using the following formulation.
得られたフオームは下部は多少独立気泡を有しているが
中部、上部は連続気泡であった。The obtained foam had some closed cells in the lower part, but open cells in the middle and upper part.
なお本発明方法(実施例1)により得たウレタンフオー
ムの成型品と比較例により得たウレタンフオーム成型品
について第1図に示す如く上中下の各位置における通気
量を測定した結果は第2図に示す通りである。The results of measuring the air flow at each position in the upper, middle, and lower positions of the urethane foam molded product obtained by the method of the present invention (Example 1) and the urethane foam molded product obtained by the comparative example as shown in FIG. As shown in the figure.
以上詳述した如く本発明方法によればウレタンプレポリ
マーと軟質ポリオールとを混合することにより、収縮に
伴う変形が全くなく、全体均一な独立気泡を有する軟質
ポリウレタンフォームを得ることができる。As detailed above, according to the method of the present invention, by mixing a urethane prepolymer and a flexible polyol, it is possible to obtain a flexible polyurethane foam that is completely free from deformation due to shrinkage and has uniform closed cells throughout.
又反応工程における内部発熱が極めて低いため内部スコ
ーチ等をおこすおそれがなく、品質の優れたものを得る
等顕著な効果を有する。Furthermore, since the internal heat generation during the reaction process is extremely low, there is no risk of internal scorch, etc., and it has remarkable effects such as obtaining products of excellent quality.
第1図はウレタンフオームの通気量を測定するための試
料の斜視図、第2図は試料の上、中、下における位置と
通気量との関係を示すものである。FIG. 1 is a perspective view of a sample for measuring the airflow rate of urethane foam, and FIG. 2 shows the relationship between the upper, middle, and lower positions of the sample and the airflow rate.
Claims (1)
するヒドロキシル化合物と有機イソシアネートとを混合
し、これを反応せしめた末端にOH基:を有するウレタ
ンプレポリマー20〜70重量部と軟質ポリオール80
〜30重量部とを混合し、更に有機インシアネート、錫
系及びアミン系触媒、整泡剤その他必要に応じて難燃剤
、増量剤等を配合し、これを混合反応せしめることを特
徴とする。 軟質ウレタンフオームの製造方法。[Scope of Claims] 1 Urethane prepolymer having OH group at the end, which is obtained by mixing a hydroxyl compound having 3 or more functional groups and having an OH value of 7.0 or more with an organic isocyanate and reacting the mixture. 70 parts by weight and 80 parts by weight of soft polyol
-30 parts by weight, and further blended with an organic incyanate, a tin-based and amine-based catalyst, a foam stabilizer, a flame retardant, an extender, etc. as necessary, and then mixed and reacted. Method for manufacturing soft urethane foam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50149487A JPS5823406B2 (en) | 1975-12-17 | 1975-12-17 | Nanshitsu Urethane Foam No Seizouhouhou |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP50149487A JPS5823406B2 (en) | 1975-12-17 | 1975-12-17 | Nanshitsu Urethane Foam No Seizouhouhou |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5273997A JPS5273997A (en) | 1977-06-21 |
JPS5823406B2 true JPS5823406B2 (en) | 1983-05-14 |
Family
ID=15476217
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP50149487A Expired JPS5823406B2 (en) | 1975-12-17 | 1975-12-17 | Nanshitsu Urethane Foam No Seizouhouhou |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5823406B2 (en) |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS57133599A (en) * | 1981-02-12 | 1982-08-18 | Mitsubishi Electric Corp | Semiconductor memory device |
US8445556B2 (en) | 2006-12-29 | 2013-05-21 | Rubberlite, Inc. | Cellular elastomer compositions |
-
1975
- 1975-12-17 JP JP50149487A patent/JPS5823406B2/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
JPS5273997A (en) | 1977-06-21 |
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