JPS63222811A - Batch-type manufacture of polyurethane foam - Google Patents

Batch-type manufacture of polyurethane foam

Info

Publication number
JPS63222811A
JPS63222811A JP62057416A JP5741687A JPS63222811A JP S63222811 A JPS63222811 A JP S63222811A JP 62057416 A JP62057416 A JP 62057416A JP 5741687 A JP5741687 A JP 5741687A JP S63222811 A JPS63222811 A JP S63222811A
Authority
JP
Japan
Prior art keywords
foaming
tank
stock solution
polyurethane foam
mixing
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
JP62057416A
Other languages
Japanese (ja)
Inventor
Sadao Kumasaka
貞男 熊坂
Satomi Tada
多田 郷見
Kazuo Hashimoto
橋本 一雄
Osamu Fujii
修 藤井
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 JP62057416A priority Critical patent/JPS63222811A/en
Priority to CA000541369A priority patent/CA1290895C/en
Priority to US07/070,774 priority patent/US4988271A/en
Priority to AU75357/87A priority patent/AU608520B2/en
Priority to KR1019870007469A priority patent/KR910000312B1/en
Priority to EG40887A priority patent/EG18673A/en
Priority to AT87110096T priority patent/ATE81065T1/en
Priority to EP87110096A priority patent/EP0273099B1/en
Priority to DE8787110096T priority patent/DE3782019T2/en
Priority to CN87104799A priority patent/CN1020560C/en
Publication of JPS63222811A publication Critical patent/JPS63222811A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain a polyurethane slab with flat top surface by providing the process in which the foaming stock solution of polyurethane is agitated and mixed, the process in which said foaming stock solution is poured into a foaming tank and the process in which the polyurethane foam slab with flat top surface is produced by the centrifugal force due to the rotation of the foaming tank. CONSTITUTION:An isocyanate component of a prescribed amount is charged in a mixing and agitating tank 25 from a raw material feeding pipe 32. Simultaneously, other raw materials such as polyol component and catalyst are charged in the agitating tank 25 from a pipe 34, and said materials are uniformly mixed by rotating an agitating wing 26. Then, the foaming stock solution prepared in the mixing and agitating tank 25 is poured into the foaming tank 11 through a discharging pipe 28 by opening an electromagnetic valve 29. Next, the foaming tank itself is rotated by way of a shaft 15 and a bar 13 by a motor 14, whereby the surface of the foaming stock solution rises even in the vicinity in contact with the foaming tank 1 almost same as the central part, and the polyurethane slab with flat top surface is obtained.

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する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for producing polyurethane foam.

[従来の技術] 従来、ウレタンフオームスラブは大型ブロック状に発泡
成形されたウレタンフオームで、これを所望の厚さにス
ライスし、あるいは所望の形状に切断加工することによ
り車両用内装材や車両用クッション材として広く使用さ
れている。
[Prior Art] Conventionally, urethane foam slabs are urethane foam that is foam-molded into large blocks, which are then sliced to a desired thickness or cut into a desired shape to be used as interior materials for vehicles or for vehicles. Widely used as cushioning material.

ところで、ポリウレタンフォームの製造方法として、第
5図に示す如く、大型の容器(発泡槽)1にポリウレタ
ン発泡原液を注入し、これを発泡ライズさせ、キュアさ
せることによりポリウレタンフォームスラブ2を製造す
る方法が知られている。この場合、発泡槽1の内面を図
示しない離型紙で覆って発泡操作を行なうのが普通であ
る。かかるパッチ式製造方法によれば、比較的狭い場所
でも実施できるという特徴を有する。また、この方法で
は、発泡槽1の形状を変化させることで任意形状のスラ
ブを製造できるという長所がある。
By the way, as a method for producing polyurethane foam, as shown in FIG. 5, a polyurethane foam slab 2 is produced by injecting a polyurethane foam stock solution into a large container (foaming tank) 1, foaming it, and curing it. It has been known. In this case, the foaming operation is usually performed with the inner surface of the foaming tank 1 covered with release paper (not shown). This patch type manufacturing method has the feature that it can be carried out even in a relatively narrow space. Furthermore, this method has the advantage that by changing the shape of the foaming tank 1, slabs of arbitrary shapes can be manufactured.

[発明が解決しようとする問題点] しかしながら、従来のバッチ式製造方法によれば、以下
に述べる問題点を有する。
[Problems to be Solved by the Invention] However, the conventional batch-type manufacturing method has the following problems.

即ち、発泡槽1にポリウレタン発泡原液を攪拌して注入
すると、発泡反応が進行し、除徐に液面が上昇(ライズ
)する。その際、発泡反応が進行するに伴ってライズす
る原液の粘度も上昇するから、発泡槽1に接触している
付近では発泡槽内面との摩擦抵抗により発泡が阻害され
てしまう。このため、発泡完了後のポリウレタンフォー
ムスラブ2は、第6図及び第7図に示すように、スラブ
の中央で高く周縁部で低い形状となり、平坦な頂面が得
られない。
That is, when the polyurethane foaming stock solution is stirred and poured into the foaming tank 1, the foaming reaction proceeds and the liquid level gradually rises. At this time, as the foaming reaction progresses, the viscosity of the rising stock solution also increases, so foaming is inhibited near the area where it contacts the foaming tank 1 due to frictional resistance with the inner surface of the foaming tank. For this reason, the polyurethane foam slab 2 after foaming has a shape that is high at the center and low at the periphery, as shown in FIGS. 6 and 7, and a flat top surface cannot be obtained.

その結果、第6図に二点鎖線で示したように、得られた
スラブ2の凸状頂部を所定の寸法になるまで切除しなけ
ればならず、廃棄部分を生じたり工程が増大する等の問
題があった。
As a result, as shown by the two-dot chain line in FIG. 6, the convex top of the obtained slab 2 must be cut off to a predetermined size, resulting in waste parts and an increase in the number of steps. There was a problem.

本発明は上記事情に鑑みてなされたもので、ポリウレタ
ンフォームスラブを製造する際、頂面が平坦なスラブを
得ることができるウレタンフオームの製造方法を提供す
ることを目的とする。
The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a method for manufacturing urethane foam that can produce a slab with a flat top surface when manufacturing a polyurethane foam slab.

[問題点を解決するための手段] 本発明は、ポリウレタン発泡原液を撹拌混合する工程と
、この発泡原液を発泡槽内に注入する工程と、発泡槽を
回転させ遠心力により上面が平坦なポリウレタンフォー
ムスラブを製造する工程とを具備することを要旨とする
[Means for Solving the Problems] The present invention consists of a step of stirring and mixing a polyurethane foaming stock solution, a step of injecting this foaming stock solution into a foaming tank, and a step of rotating the foaming tank and applying centrifugal force to form a polyurethane foam with a flat top surface. The gist is to include a process of manufacturing a foam slab.

[作用] 本発明によれば、適宜に混合、攪拌したポリウレタンフ
ォーム発泡原液を発泡槽に注入した後、発泡槽自体を適
宜な速度で回転させながら発泡させることにより、頂面
が平坦なポリウレタンフォームスラブを得ることができ
る。従って、従来のように凸状頂部を所定の形状になる
まで切ったりすることなく、ムダなスラブが生じないと
ともに切断工程を省略できる。
[Function] According to the present invention, polyurethane foam having a flat top surface is produced by pouring a polyurethane foam foaming stock solution mixed and stirred appropriately into a foaming tank, and then foaming while rotating the foaming tank itself at an appropriate speed. You can get slabs. Therefore, unlike the conventional method, the convex top portion is not cut into a predetermined shape, and unnecessary slabs are not generated and the cutting process can be omitted.

本発明において、発泡槽の回転速度は、発泡のライズに
より異なるが約20〜120回転/分とする。ここで、
回転数が20回回転弁より遅いと、十分な遠心力が得ら
れずポリウレタンフォームスラブを十分に平坦化できな
い。逆に、回転数が120回転/分を越えると、遠心力
が強すぎ発泡反応を阻害してワレなどを生じ易い。
In the present invention, the rotational speed of the foaming tank is approximately 20 to 120 revolutions per minute, although it varies depending on the rise of foaming. here,
If the rotation speed is slower than the 20 rotation valve, sufficient centrifugal force cannot be obtained and the polyurethane foam slab cannot be sufficiently flattened. On the other hand, if the rotational speed exceeds 120 rpm, the centrifugal force will be too strong, inhibiting the foaming reaction and easily causing cracks.

本発明において、ポリウレタンフォーム発泡原液は、ポ
リエーテルポリオール、ポリエステルポリオールなどの
ポリオールと、トリレンジイソシアネートなどの有機イ
ソシアネート、アミン触媒、錫触媒、発泡剤(水)、整
泡剤(シリコーン油)、その他顔料、充填剤等が要求さ
れる特性に応じて適宜に組合われて使用される。
In the present invention, the polyurethane foam foaming stock solution includes polyols such as polyether polyols and polyester polyols, organic isocyanates such as tolylene diisocyanate, amine catalysts, tin catalysts, blowing agents (water), foam stabilizers (silicone oil), and others. Pigments, fillers, etc. are used in appropriate combinations depending on the required properties.

[実施例] 以下、本発明の一実施例を第1図〜第4図を参照して説
明する。ここで、第1図は本発明に係るポリウレタンフ
ォームの製造装置、第2図は同装置に係る発泡槽の平面
図、第3図は同iitに係るシャフトの説明図、第4図
は前記発泡層の背面図である。
[Example] Hereinafter, an example of the present invention will be described with reference to FIGS. 1 to 4. Here, FIG. 1 is a polyurethane foam manufacturing apparatus according to the present invention, FIG. 2 is a plan view of a foaming tank according to the same apparatus, FIG. 3 is an explanatory diagram of a shaft according to the same IIT, and FIG. FIG. 3 is a rear view of the layer.

図中の11は、上部に開口部11aを有した円筒形状の
発泡槽である。前記開口部11aには、シャフト受孔1
2を有したバー13が設けられている。このバー13に
はモータ14に連結したシャフト15(第3図図示)の
先端部15aが係合するようになっており、前記モータ
14の回転によりシャフト15.バー13を介して発泡
槽自身が回転するようになっている。また、前記発泡槽
11の側壁には、発泡原液導入口11aが開口されてお
り、該導入口11aには開閉自在な扉16が設けられて
いる。更に、前記発泡槽11は、下部にキャスタ17を
取付けた支持台18上にローラ19を介して載置されて
いる。
11 in the figure is a cylindrical foaming tank having an opening 11a at the top. A shaft receiving hole 1 is provided in the opening 11a.
A bar 13 with 2 is provided. A tip end 15a of a shaft 15 (shown in FIG. 3) connected to a motor 14 engages with this bar 13, and as the motor 14 rotates, the shaft 15. The foaming tank itself is rotated via the bar 13. Further, a foaming stock solution introduction port 11a is opened in the side wall of the foaming tank 11, and a door 16 that can be opened and closed is provided in the introduction port 11a. Furthermore, the foaming tank 11 is placed on a support stand 18 with casters 17 attached to its lower part via rollers 19.

前記発泡槽11の近傍には、レール20が付設されてい
る。このレール20上には脚部に車輪21を設けた台車
22が載置され、押出しシリンダ23の伸縮により発泡
槽11に対して接近したり後退できるようになっている
。前記台車22には、回動軸24が水平に張設され、前
記回動軸24には円筒形の混合攪拌槽25が枢軸固定さ
れている。前記回動軸24は、図示しないモータ及び変
則ギアにより回動駆動されるようになっており、これに
より混合混合攪拌槽25は図中矢印で示す方向に回動傾
斜されるようになっている。混合撹拌槽25の内部には
その軸方向に攪拌羽根26が設けられ、この攪拌羽根2
6は混合撹拌槽25の下に付設されたモータ27により
回転駆動されるようになっている。また、前記混合攪拌
槽25の側面下端部には、発泡液吐出管28が斜下方に
向けて延設されている。この発泡原液吐出管28と前記
混合攪拌槽25とは、両者の境界部分に設けられた電磁
弁29を介して連通されている。
A rail 20 is attached near the foaming tank 11. A trolley 22 having wheels 21 on its legs is placed on the rail 20, and can approach or retreat from the foaming tank 11 by expanding and contracting the extrusion cylinder 23. A rotating shaft 24 is stretched horizontally on the cart 22, and a cylindrical mixing and stirring tank 25 is pivotally fixed to the rotating shaft 24. The rotation shaft 24 is rotatably driven by a motor and an irregular gear (not shown), so that the mixing agitation tank 25 is rotated and tilted in the direction indicated by the arrow in the figure. . A stirring blade 26 is provided inside the mixing stirring tank 25 in the axial direction, and this stirring blade 2
6 is adapted to be rotationally driven by a motor 27 attached below the mixing and stirring tank 25. Further, at the lower end of the side surface of the mixing and stirring tank 25, a foaming liquid discharge pipe 28 is provided extending obliquely downward. This foaming stock solution discharge pipe 28 and the mixing agitation tank 25 are communicated with each other via a solenoid valve 29 provided at the boundary between the two.

更に、混合攪拌槽25の上部には有機イソシアネート成
分の計量タンク30が配置され、該計量タンク30は配
管31を介して有機イソシアネート供給源に連結されて
いる。前記計量タンク30の下端には原料供給管32が
設けられ、該原料供給管32と計量タンク30の間には
i!磁弁33が設けられている。また、原料供給管32
には例えばポリオールや触媒等、イソシアネート成分以
外のポリウレタンフォーム原料供給配管34が連結され
ている。
Furthermore, a measuring tank 30 for the organic isocyanate component is arranged above the mixing and stirring tank 25, and the measuring tank 30 is connected to an organic isocyanate supply source via a pipe 31. A raw material supply pipe 32 is provided at the lower end of the measuring tank 30, and between the raw material supply pipe 32 and the measuring tank 30 there is an i! A magnetic valve 33 is provided. In addition, the raw material supply pipe 32
A pipe 34 for supplying polyurethane foam raw materials other than isocyanate components, such as polyols and catalysts, is connected to.

前記有機イソシアネート成分の計量タンク30にはポリ
ウレタンフォーム原料の洗浄溶剤供給管35が付設され
、この供給管35は洗浄溶剤タンク36に連結されてい
る。また、洗浄溶剤廃液受け37が設置され、この廃液
受け37はポンプ38を介して前記洗浄溶剤タンク36
に連結されている。
A cleaning solvent supply pipe 35 for polyurethane foam raw material is attached to the organic isocyanate component measuring tank 30, and this supply pipe 35 is connected to a cleaning solvent tank 36. Further, a cleaning solvent waste liquid receiver 37 is installed, and this waste liquid receiver 37 is connected to the cleaning solvent tank 3 through a pump 38.
is connected to.

次に、上記構造の製造装置の作用について説明する。Next, the operation of the manufacturing apparatus having the above structure will be explained.

まず、押出しシリンダ23を伸縮させ、混合攪拌槽25
を発泡槽11から後退させた状態でポリウレタンフォー
ム発泡原液の調整を行なう。即ち、配管31から計量タ
ンク30内に有機イソシアネート成分を供給して計量し
た後、電磁弁33を開くことにより、この所定量のイソ
シアネート成分を原料供給管32から混合攪拌槽25内
に投入する。同時に、配管34からポリオール成分及び
触媒等の他の原料を混合撹拌槽25内に投入する。
First, the extrusion cylinder 23 is expanded and contracted, and the mixing stirring tank 25 is
The polyurethane foam foaming stock solution is adjusted in a state where the polyurethane foam is retreated from the foaming tank 11. That is, after the organic isocyanate component is supplied into the metering tank 30 from the pipe 31 and measured, by opening the electromagnetic valve 33, a predetermined amount of the isocyanate component is introduced into the mixing tank 25 from the raw material supply pipe 32. At the same time, other raw materials such as a polyol component and a catalyst are introduced into the mixing tank 25 from the pipe 34 .

つづいて、攪拌羽根26を回転させ、均一に混合する。Next, the stirring blade 26 is rotated to mix uniformly.

次いで、押出しシリンダ23を伸張駆動させることによ
り混合攪拌槽25を図示の位置まで前進させ、発泡原液
吐出t!!!28の先端を発泡原液導入口11aから発
泡槽11内に挿入する。その際、扉16は発泡原液吐出
管28で押されて容易に開くようになっている。つづい
て、電磁弁29を開くことにより混合攪拌槽25内で調
整された発泡原液を吐出管28を通して発泡槽11内に
注入する。その際、必要に応じて回動軸24を回転させ
、混合攪拌槽25を前傾させることにより発泡原液の流
出を促進する。
Next, by driving the extrusion cylinder 23 to extend, the mixing and stirring tank 25 is advanced to the illustrated position, and the foaming stock solution is discharged t! ! ! 28 is inserted into the foaming tank 11 through the foaming stock solution inlet 11a. At this time, the door 16 is pushed by the foaming stock solution discharge pipe 28 so that it can be easily opened. Subsequently, by opening the electromagnetic valve 29, the foaming stock solution adjusted in the mixing stirring tank 25 is injected into the foaming tank 11 through the discharge pipe 28. At that time, the rotating shaft 24 is rotated as necessary to tilt the mixing and stirring tank 25 forward to promote outflow of the foaming stock solution.

この後、押出しシリンダ23を収縮駆動させることによ
り混合攪拌槽25を後退させ、1116を閉じる。次に
、モータ14によりシャフト15゜バー13を介して発
泡槽自体を回転させる。ここで、発泡槽11の回転速度
は発泡のライズにより異なるが、約20〜120回転/
分とする。その結果、発泡槽11内の発泡原液に遠心力
が働いて、発泡槽11に接触している付近でも発a原液
面が中央部と略同様にライズし、頂面が平坦なポリウレ
タンフォームスラブが得られる。
Thereafter, the extrusion cylinder 23 is driven to contract, thereby retracting the mixing tank 25 and closing 1116. Next, the foaming tank itself is rotated by the motor 14 via the shaft 15° bar 13. Here, the rotational speed of the foaming tank 11 varies depending on the rise of foaming, but is approximately 20 to 120 rpm.
minutes. As a result, a centrifugal force acts on the foaming solution in the foaming tank 11, and the surface of the foaming solution rises in the vicinity where it is in contact with the foaming tank 11, almost in the same way as in the center, resulting in a polyurethane foam slab with a flat top surface. can get.

一方、上記のように発泡槽11の中でポリタンフオーム
スラブの発泡成形が行われている間に、発泡槽11から
後退した混合攪拌1!28及びイソシアネート成分計量
タンク30では、次のようにして内面に付着しているポ
リウレタン発泡原液の洗浄が行われる。即ち、ポンプ3
8が駆動し、洗浄溶剤タンク36内に洗浄溶剤が供給さ
れ、更に混合攪拌槽25に洗浄溶剤が満たされる。つづ
いて、攪拌羽根26を回すことにより、混合攪拌槽26
の内壁に付着している発泡原液を溶解した後、電磁弁2
9を開いて洗浄溶剤を排出する。洗浄溶剤を排出する際
、吐出管28の内壁に付着している発泡原液も溶解され
る。こうして排出された洗浄溶剤は廃液受け37に貯溜
された後、ポンプ38で洗浄溶剤タンク36に送られ再
利用される。
On the other hand, while the polytan foam slab is being foam-molded in the foaming tank 11 as described above, the mixing stirring 1!28 and the isocyanate component measuring tank 30, which have been retreated from the foaming tank 11, perform the following operations. The polyurethane foaming solution adhering to the inner surface is cleaned. That is, pump 3
8 is driven, the cleaning solvent is supplied into the cleaning solvent tank 36, and the mixing and stirring tank 25 is further filled with the cleaning solvent. Next, by rotating the stirring blade 26, the mixing stirring tank 26
After dissolving the foaming stock solution adhering to the inner wall of the solenoid valve 2,
9 to drain the cleaning solvent. When the cleaning solvent is discharged, the foaming stock solution adhering to the inner wall of the discharge pipe 28 is also dissolved. The cleaning solvent thus discharged is stored in the waste liquid receiver 37, and then sent to the cleaning solvent tank 36 by the pump 38 and reused.

洗浄が終了すると、記述したのと同様にして次の発泡原
料の調整が行われる。また、発泡槽11は図示しないタ
ーンテーブルを回転して引出され、代わりに別の発泡槽
が図示の位置に設置される。
When the cleaning is completed, the next foaming material is prepared in the same manner as described. Further, the foaming tank 11 is pulled out by rotating a turntable (not shown), and another foaming tank is installed in its place at the position shown.

こうして、上記と同様の操作を繰返すことにより連続し
てポリウレタンフォームスラブの製造を行なうことがで
きる。
In this way, polyurethane foam slabs can be continuously manufactured by repeating the same operations as above.

しかして、本発明によれば、ポリウレタンフォーム原液
を攪拌台してこれを発泡槽11内に注入した後、モータ
14により発泡槽自体を所定の速度で回転させるため、
その遠心力により頂面が平坦なポリウレタンフォームス
ラブ(第8図図示)を得ることができる。
According to the present invention, after the polyurethane foam stock solution is injected into the foaming tank 11 using a stirring table, the foaming tank itself is rotated at a predetermined speed by the motor 14.
Due to the centrifugal force, a polyurethane foam slab with a flat top surface (as shown in FIG. 8) can be obtained.

なお、上記実施例において、モータに連結されるシャフ
トと発泡槽のバーの形状は上述した構成に限定されるも
のではない。即ち、モータの回転力が発泡槽に伝われば
よいため、シャフトとバーが係合する様々な構造のもの
が考えられる。
In the above embodiments, the shapes of the shaft connected to the motor and the bar of the foaming tank are not limited to the configurations described above. That is, since it is sufficient that the rotational force of the motor is transmitted to the foaming tank, various structures in which the shaft and the bar engage are conceivable.

また、上記実施例で述べたポリウレタンフォームの製造
装置の構造も上述した構造のものに勿論限定されない。
Furthermore, the structure of the polyurethane foam manufacturing apparatus described in the above embodiments is of course not limited to the structure described above.

[発明の効果] 以上詳述した如く本発明によれば、従来と比べ頂部が平
坦なポリウレタンフォームスラブを得ることができ、も
って従来のように凸状頂部を所定の形状になるまで切っ
たりすることなく、スラブの歩留りの向上、切断工程の
省略が可能なポリウレタンフォームの製造方法を提供で
きる。
[Effects of the Invention] As described in detail above, according to the present invention, it is possible to obtain a polyurethane foam slab with a flat top compared to the conventional method, so that the convex top can be cut to a predetermined shape as in the conventional method. It is possible to provide a method for manufacturing polyurethane foam that can improve the yield of slabs and omit the cutting process without any problems.

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

第1図は本発明に係るポリウレタンフォームの製造装置
の説明図、第2図は同装置に係る発泡槽の平面図、第3
図は同装置に係るシャフトの説明図、第4図は前記発泡
層の背面図、第5図は従来のバッチ式製造方法の説明図
、第6図は従来方法に得られるポリウレタンフォームス
ラブの斜視図、第7図は第6図の正面図、第8図は本発
明法により得られるポリウレタンフォームスラブの正面
図である。 11・・・発泡槽、12・・・シャフト受孔、13・・
・バー、14.27・・・モータ、15・・・シャフト
、16・・・爵、18・・・支持台、20・・・レール
、21・・・車輪、22・・・台車、23・・・押出し
シリンダ、24・・・回動軸、25・・・混合攪拌槽、
26・・・攪拌羽根、28・・・発a原液吐出管、29
.33・・・電磁弁、30・・・計量タンク、31・・
・配管、32・・・原料供給管、34・・・原料供給配
管、35・・・洗浄溶剤供給管、36・・・洗浄溶剤タ
ンク、37・・・洗浄溶剤廃液受け、38・・・ポンプ
。 出願人代理人 弁理士 鈴江武彦 第7図 第8図
FIG. 1 is an explanatory diagram of a polyurethane foam manufacturing apparatus according to the present invention, FIG. 2 is a plan view of a foaming tank according to the same apparatus, and FIG.
FIG. 4 is a rear view of the foam layer, FIG. 5 is an explanatory diagram of the conventional batch manufacturing method, and FIG. 6 is a perspective view of a polyurethane foam slab obtained by the conventional method. 7 is a front view of FIG. 6, and FIG. 8 is a front view of a polyurethane foam slab obtained by the method of the present invention. 11... Foaming tank, 12... Shaft receiving hole, 13...
・Bar, 14.27...Motor, 15...Shaft, 16...Support, 20...Rail, 21...Wheel, 22...Dolly, 23... ... Extrusion cylinder, 24 ... Rotating shaft, 25 ... Mixing stirring tank,
26... Stirring blade, 28... A raw solution discharge pipe, 29
.. 33...Solenoid valve, 30...Measuring tank, 31...
- Piping, 32... Raw material supply pipe, 34... Raw material supply pipe, 35... Cleaning solvent supply pipe, 36... Cleaning solvent tank, 37... Cleaning solvent waste liquid receiver, 38... Pump . Applicant's agent Patent attorney Takehiko Suzue Figure 7 Figure 8

Claims (1)

【特許請求の範囲】[Claims] ポリウレタン発泡原液を撹拌混合する工程と、この発泡
原液を発泡槽内に注入する工程と、発泡槽を回転させ遠
心力により頂面が平坦なポリウレタンフォームスラブを
製造する工程とを具備することを特徴とするポリウレタ
ンフォームの製造方法。
It is characterized by comprising a step of stirring and mixing a polyurethane foaming stock solution, a step of injecting this foaming stock solution into a foaming tank, and a step of rotating the foaming tank and producing a polyurethane foam slab with a flat top surface by centrifugal force. A method for producing polyurethane foam.
JP62057416A 1986-12-15 1987-03-12 Batch-type manufacture of polyurethane foam Pending JPS63222811A (en)

Priority Applications (10)

Application Number Priority Date Filing Date Title
JP62057416A JPS63222811A (en) 1987-03-12 1987-03-12 Batch-type manufacture of polyurethane foam
CA000541369A CA1290895C (en) 1986-12-25 1987-07-06 Method and an apparatus for producing polyurethane foam
US07/070,774 US4988271A (en) 1986-12-25 1987-07-07 Apparatus for producing polyurethane foam
AU75357/87A AU608520B2 (en) 1986-12-25 1987-07-08 A method and an apparatus for producing polyurethane foam
KR1019870007469A KR910000312B1 (en) 1986-12-15 1987-07-11 Method and apparatus for producing polyurethane foam
EG40887A EG18673A (en) 1986-12-25 1987-07-12 A batch type foaming apparatus for producing urethane foam slab. T
AT87110096T ATE81065T1 (en) 1986-12-25 1987-07-13 METHOD AND DEVICE FOR PRODUCTION OF POLYURETHANE FOAM.
EP87110096A EP0273099B1 (en) 1986-12-25 1987-07-13 A method and an apparatus for producing polyurethane foam
DE8787110096T DE3782019T2 (en) 1986-12-25 1987-07-13 METHOD AND DEVICE FOR PRODUCING POLYURETHANE FOAM.
CN87104799A CN1020560C (en) 1986-12-25 1987-07-13 Method and apparatus for producing low density polyurethane foam

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62057416A JPS63222811A (en) 1987-03-12 1987-03-12 Batch-type manufacture of polyurethane foam

Publications (1)

Publication Number Publication Date
JPS63222811A true JPS63222811A (en) 1988-09-16

Family

ID=13055044

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62057416A Pending JPS63222811A (en) 1986-12-15 1987-03-12 Batch-type manufacture of polyurethane foam

Country Status (1)

Country Link
JP (1) JPS63222811A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112142939A (en) * 2020-10-21 2020-12-29 惠彩材料科技(苏州)有限公司 Mixed foaming method of polyurethane

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112142939A (en) * 2020-10-21 2020-12-29 惠彩材料科技(苏州)有限公司 Mixed foaming method of polyurethane
CN112142939B (en) * 2020-10-21 2022-06-10 惠彩材料科技(苏州)有限公司 Mixed foaming method of polyurethane

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