JPS6128495B2 - - Google Patents
Info
- Publication number
- JPS6128495B2 JPS6128495B2 JP51119101A JP11910176A JPS6128495B2 JP S6128495 B2 JPS6128495 B2 JP S6128495B2 JP 51119101 A JP51119101 A JP 51119101A JP 11910176 A JP11910176 A JP 11910176A JP S6128495 B2 JPS6128495 B2 JP S6128495B2
- Authority
- JP
- Japan
- Prior art keywords
- foam
- conveyor
- foaming
- stock solution
- conveyor belt
- 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
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/34—Auxiliary operations
- B29C44/36—Feeding the material to be shaped
- B29C44/46—Feeding the material to be shaped into an open space or onto moving surfaces, i.e. to make articles of indefinite length
- B29C44/467—Foam spreading or levelling devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C44/00—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
- B29C44/20—Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of indefinite length
- B29C44/28—Expanding the moulding material on continuous moving surfaces without restricting the upwards growth of the foam
Landscapes
- Casting Or Compression Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
この発明は、合成樹脂気泡体の製造に際し、溝
形の離型紙を用いない方法に関し、さらに得られ
た気泡体をスライス、その他の何んら後加工を要
することなく、そのまま最終使用成品とすること
が出来る気泡体の製法に係るものである。[Detailed Description of the Invention] The present invention relates to a method for producing a synthetic resin foam without using a channel-shaped release paper, and without slicing the obtained foam or performing any other post-processing. This invention relates to a method for producing a foam that can be used as a final product as it is.
従来、ポリウレタンフオームなどの気泡体を製
造するには、一定速度で走行するコンベアー上
に、合成樹脂、ワツクスなどを内面に塗布したク
ラフト紙、合成樹脂薄板を溝形に折に曲げた連続
容器を載置し、これを一定速度で走行させ、この
溝形容器内に合成樹脂発泡原液をノズルから吐出
し、これを加熱することによつて該溝形容器内で
発泡させ連続的に製造している。こうして出来た
大きなスラブは、その後、成形に用いた底部・側
部の離型紙を剥離除去し、これをその後1〜2メ
ートルの長さに切断したのち約24時間程度保管す
ることによつて完全にキユアーさせ、次にこれを
表皮、その他不良部分を切除してから所定厚さに
スライスしてマツトレス、その他のクツシヨン体
に供されている。 Conventionally, to manufacture polyurethane foam and other foams, a continuous container made of kraft paper coated with synthetic resin, wax, etc. on the inside, or thin synthetic resin sheets bent into a groove shape is placed on a conveyor that moves at a constant speed. The synthetic resin foaming stock solution is discharged from the nozzle into the groove-shaped container, and is heated to foam in the groove-shaped container, thereby producing continuous production. There is. The large slab thus created is then peeled off and removed from the release paper on the bottom and sides used for molding, cut into lengths of 1 to 2 meters, and stored for about 24 hours to complete the process. The skin is then cured, the epidermis and other defective parts are removed, and the slices are sliced to a predetermined thickness to be used as pine tresses and other cushions.
しかしながら、このような従来方式による気泡
体の製法にはこれまで幾多の問題点が指摘されて
来た。すなわち、従来は多量の離型紙を用いる
外、一たん大きなスラブを造り、これをスライス
その他の切断加工を行なうところから、後加工に
経費がかかるとともに大量の不良材が排出するこ
と、またスライス以前のスラブのサイズが、例え
ば
巾2000mm×高さ900mm×長さ2000mm
という大きなところから、発泡反応後のキユアー
に当つて、150〜170℃という内部発熱を併い、し
かもこれが数時間も継続し火災その他の危険が生
じていた外、かかる高温の内部発熱に帰因して、
例えばポリウレタンフオームでは黄変が著るしく
発生し、特に得られたものの商品価値を極度に低
下せしめていた。こうしたことを回避するため
に、これまでもスライスなどの後加工の不要にし
た最終厚み寸法の気泡体を一挙に得ようと種々の
研究されては来たが、発泡完了の気泡体から溝形
に構成した離型紙を剥除する際に、気泡体の表面
に著るしい肌荒れを生じてしまうこと、気泡体の
製造に際して必然的に生ずる上面表皮が著るしく
硬質となつて、内部の柔軟な性状とは全く異質の
感触を呈すること、気泡体の断面形状が肩下りの
状態となつて断面方形のものが得られないことな
ど種々の問題点があり、未だ実現に至らず、結局
のところ、従来どおり溝形離型紙を用いて連続的
な大きなスラブを造り、これを大切りにカツトし
てから完全キユアーを行ない、しかるのちこれを
スライスして最終製品としている。この発明は従
来のこうした欠点を一挙に解決し、溝形離型紙を
一切用いることなく、しかも発泡原液を吐出して
発泡反応を完了して得られた気泡体がそのまま最
終需要製品とすることが出来る合成樹脂気泡体の
製造方法を得ようとしたものであつて、溝形離型
紙を用いることなく、離型性部材よりなる底部コ
ンベアベルトと、この上面両側に上記コンベアベ
ルトとは別体でかつこれと同期して移動する側帯
とで囲繞されず凹形コンベアを形成し、この一端
へクリーム状発泡初期原液を連続的に注入し、底
部コンベアベルトと側帯との合わせ目から発泡初
期原液の漏液を防止しつつ発泡反応を行なわせる
とともに、発泡ガスが気泡体の表面から出終つて
気泡の生成反応が終了した点から架橋反応が終了
する点にわたつて気泡体の上表面を押圧コンベア
ーで軽圧縮して最終製品厚み寸法の気泡体とする
ことを特徴とする。以下にこの発明の詳細を図示
した一実施例にもとづいて説明する。図において
1はコンベアーであつて、これにはテフロンシー
ト・ステンレス板その他の離型性部材のエンドレ
スベルトを張設しておく。このコンベアー1の上
面両側端には補強板21,22が直立してあり、
その各々の内側に底部コンベアとは別体で、かつ
離型剤を塗布した紙などからなる側帯31,32
が図示しないワインダーロールから上記コンベア
ーの速度と同期して供給され、その結果ここに溝
形離型紙を用いることなく、底部コンベアと側帯
とで形成された凹形コンベアが形成されるように
する。なお、この側帯は直立したエンドレスベル
トコンベアーで構成するようにしてもよい。4は
発泡原液の供給ノズルであつて、これにより例え
ばポリオール・トリレンジイソシアネートアミン
触媒などの混合液がミキシングヘツドで撹拌した
のち連続的に供給されるが、ここでの吐出発泡原
液を高粘度のクリーム状の発泡初期原液としてお
く。すなわち、吐出原液を上記の如く高粘度のク
リーム状の発泡初期原液とすることによつて、発
泡装置としての溝形容器を一枚の離型紙をコ字型
に折曲げてなる溝形容器としなくとも、単にコン
ベアー1の上面両側に側帯31,32を載置した
のみでその合てせ目からの液もれが防止されるこ
とが実験の結果確認されたものである。吐出発泡
原液をクリーム状の発泡初期原液とするために
は、例えば触媒量を増加するか、ノズル長を伸ば
すことにより容易に調整することが出来る。な
お、発泡原液は、得られた気泡体がそのまま最終
製品厚み寸法となるようにするため、これに応じ
た所定量の吐出量に予め調節しておかなければな
らない。5は発泡ガスが気泡体の表面から出終つ
て気泡の生成反応が終了した点から架橋反応が終
了する点にわたつて気泡体の上表面を軽圧縮する
押圧コンベアーであつて、離型性を考慮してテフ
ロン・ステンレス板その他の離型性部材を用い
る。この押圧コンベアー5は気泡体の発泡ガスが
気泡体の表面から出終つて気泡の生成反応が終了
した点から気泡体を軽圧縮することが必要で、そ
れ以前より気泡体の上表面を押圧することになる
と、発泡反応そのものを抑圧し、気泡の破れ、そ
の他の気泡荒れを生じるおそれがある。また、気
泡体の押圧も軽圧縮に止め、必要以上に押圧する
と均一な気泡体の成生が期待出来ない、更に、押
圧コンベアーはコンベアー1と製品厚み寸法の厚
み寸法に応じて離間するとともに、その長さも、
架橋反応が終了する点まで気泡体の上表面を軽圧
縮する必要から、得られる気泡体の厚さによつて
キユアーする時間が不安となり均一には定め得な
いが、一例としてマツトレスの製法をとると、長
さ約10メートルで十分である。なお、押圧コンベ
アー5は溝形コンベアーの底部を構成するコンベ
アー1と同期して同一方向に移動させることは勿
論である。また、押圧コンベアー5、および凹型
部と構成するコンベアー1には転写ロールを用い
離型剤をその表面に塗布しておけば、得られた気
泡体との離型は常に円滑に行なわれるのみらず、
気泡体の表面性状を一層向上させることができ
る。 However, a number of problems have been pointed out in the conventional methods for producing foams. In other words, in the past, in addition to using a large amount of release paper, a large slab was created and then subjected to slicing and other cutting processes, which resulted in high post-processing costs and the production of a large amount of defective material. Because the size of the slab is large, for example, 2000mm wide x 900mm high x 2000mm long, internal heat generation of 150 to 170°C occurs during curing after the foaming reaction, and this continues for several hours, causing a fire. Due to such high internal heat generation, in addition to other dangers,
For example, in the case of polyurethane foam, significant yellowing occurs, which extremely reduces the commercial value of the product obtained. In order to avoid this, various researches have been carried out to obtain foams with the final thickness without the need for post-processing such as slicing. When removing the release paper constructed in There are various problems such as the feel is completely different from normal properties, and the cross-sectional shape of the foam is sloping, making it impossible to obtain a square cross-section. However, as in the past, grooved release paper is used to create a continuous large slab, which is then cut into large pieces, cured completely, and then sliced to produce the final product. This invention solves all of these conventional drawbacks at once, and without using any grooved release paper, the foam obtained by discharging the foaming stock solution and completing the foaming reaction can be used as a final product as it is. This is an attempt to obtain a method for producing a synthetic resin foam that can be produced without using a channel-shaped release paper. A concave conveyor is formed without being surrounded by a side belt that moves in synchronization with the belt, and the creamy foaming initial stock solution is continuously injected into one end of the conveyor, and the foaming initial stock solution is poured from the joint between the bottom conveyor belt and the side belt. In addition to allowing the foaming reaction to occur while preventing liquid leakage, the upper surface of the foam is pressed by a conveyor from the point where the foaming gas finishes exiting from the surface of the foam and the bubble generation reaction ends to the point where the crosslinking reaction ends. It is characterized in that it is lightly compressed to form a foam with the thickness of the final product. The details of this invention will be explained below based on an illustrated embodiment. In the figure, reference numeral 1 denotes a conveyor, on which an endless belt of Teflon sheets, stainless steel plates, and other releasable members is stretched. Reinforcement plates 2 1 and 2 2 are upright on both ends of the upper surface of this conveyor 1.
Inside each of them, side bands 3 1 , 3 2 are separate from the bottom conveyor and made of paper or the like coated with a release agent.
is supplied from a winder roll (not shown) in synchronization with the speed of the conveyor, so that a concave conveyor consisting of a bottom conveyor and side bands is formed without using a grooved release paper. Incidentally, this side band may be constituted by an upright endless belt conveyor. Reference numeral 4 denotes a foaming stock solution supply nozzle, through which a mixed solution of, for example, a polyol/tolylene diisocyanate amine catalyst is stirred in a mixing head and then continuously supplied. Leave as a creamy foaming initial stock solution. That is, by using the high viscosity, cream-like foaming initial stock solution as the discharged stock solution as described above, the channel-shaped container as the foaming device can be made into a channel-shaped container made by folding a piece of release paper into a U-shape. At least as a result of experiments, it has been confirmed that simply placing the side bands 3 1 and 3 2 on both sides of the upper surface of the conveyor 1 can prevent liquid leakage from the joints. In order to make the discharged foaming stock solution into a cream-like foaming initial stock solution, it can be easily adjusted by, for example, increasing the amount of catalyst or extending the nozzle length. In addition, in order for the obtained foam to have the same thickness as the final product, the discharge amount of the foaming stock solution must be adjusted in advance to a predetermined amount corresponding to the thickness of the final product. 5 is a pressure conveyor that lightly compresses the upper surface of the foam from the point where the foaming gas finishes exiting from the surface of the foam and the bubble generation reaction ends to the point where the crosslinking reaction ends; With this in mind, use Teflon, stainless steel plates, and other releasable materials. This pressing conveyor 5 is required to lightly compress the foam from the point where the foaming gas of the foam has finished coming out from the surface of the foam and the bubble generation reaction has ended, and presses the upper surface of the foam from before that point. In this case, the foaming reaction itself may be suppressed, leading to bubble bursting and other bubble roughness. In addition, the pressure on the foam should be limited to light compression, and if the pressure is applied more than necessary, uniform foam formation cannot be expected.Furthermore, the pressure conveyor is spaced apart from the conveyor 1 according to the thickness of the product. Its length is also
Since it is necessary to lightly compress the upper surface of the foam until the crosslinking reaction is completed, the curing time may vary depending on the thickness of the resulting foam and cannot be set uniformly; however, as an example, we will use the method of manufacturing Mattress. A length of approximately 10 meters is sufficient. It goes without saying that the pressing conveyor 5 is moved in the same direction in synchronization with the conveyor 1 that forms the bottom of the channel conveyor. Furthermore, if a transfer roll is used for the pressure conveyor 5 and the conveyor 1 that constitutes the concave part, and a release agent is applied to the surface, the mold release from the obtained foam will always be performed smoothly. figure,
The surface properties of the foam can be further improved.
以上この発明によれば、従来の気泡体の製造時
の如く液状の発泡原液を用いることなく、高粘度
の発泡初期原液の使用によつて大量の溝形離型紙
を使用しなくて済むようにしたので、コストの低
下、使用ずみ離型紙の処理といつた問題が改善さ
れることはもちろん、得られる気泡体から離型紙
を剥離する際に気泡体の肌荒れを起すといつたこ
れまでの欠点が全て解決されることになつた。さ
らにこの発明によれば、吐出された発泡原液が最
終製品厚み寸法を離間させて配置した離型性コン
ベアーの間で軽圧縮されつつ発泡反応を行つて気
泡体を造るものであるから、ここに得られた気泡
体は断面方形を有することは勿論、その表面性状
は柔軟性に富み、従来のスラブより切出した切削
処女面と対比しても、これと同等もしくはそれ以
上の性状になる。もちろん、発泡反応と連続して
キユーまで完了してしまうので、その後内部発熱
や、これに帰因する火災の危険などは全くなく、
従つてポリウレタフオームの場合なども黄変が大
巾に回避することが出来る。スライス加工はもち
ろんなく、得られる気泡体はそのまま即座に使用
出来、製造原価を大巾に低下せしめることが出来
る。 As described above, according to the present invention, it is possible to eliminate the need to use a large amount of grooved release paper by using a high viscosity foaming initial stock solution instead of using a liquid foaming stock solution as in the conventional production of foams. This not only reduces costs and improves problems such as the treatment of used release paper, but also eliminates the drawbacks of the past, such as roughening of the surface of the foam when peeling the release paper from the resulting foam. were all resolved. Furthermore, according to the present invention, the discharged foaming stock solution is lightly compressed between the releasable conveyors arranged at a distance from each other in terms of the thickness of the final product, and a foaming reaction is carried out to produce the foam. The resulting foam naturally has a rectangular cross section, and its surface properties are highly flexible, and even when compared with the virgin cutting surface cut from a conventional slab, the properties are equal to or better than this. Of course, since the foaming reaction and the queue are completed in succession, there is no internal heat generation or any risk of fire resulting from this.
Therefore, even in the case of polyureta foam, yellowing can be largely avoided. Of course, there is no slicing process, and the resulting foam can be used immediately as it is, making it possible to significantly reduce manufacturing costs.
実施例
図に示す装置を用いて下記配合処方でポリウレ
タフオームを連続的に製造した。ただし、コンベ
アの巾200mm、コンベア上の両側帯間の巾1500
mm、コンベアスピード8m/分、ノズル長1m、底
部コンベアと押圧コンベアの間隔100mm、底部コ
ンベアと側帯とは別体で、その間に微小間隙を残
し、底部コンベア、押圧コンベア共にテフロンコ
ーテイングの上にシリコン系離型剤を塗布したも
のを用いた。Example Using the apparatus shown in the figure, polyureta foam was continuously manufactured using the following formulation. However, the width of the conveyor is 200mm, and the width between both sides of the conveyor is 1500mm.
mm, conveyor speed 8m/min, nozzle length 1m, interval between bottom conveyor and pressure conveyor 100mm, bottom conveyor and side belt are separate, leaving a small gap between them, and both bottom conveyor and pressure conveyor are coated with silicone on top of Teflon coating. A material coated with a mold release agent was used.
配合処方
CP―3000(グリセリンベース3官能分子量
3000
ポリエーテルポリオール 100重量部
水 4.0
トリエチレンジアミン 0.2
シリコンオイル 1.5
スズ触媒(ジブチルジラウレート) 0.25
フレオン11 5.0
トリレンジイソシアネート(T―80) 53.0
これによつて得られたものは、ノズルから吐出
した発泡初期原液が、底部コンベアと側帯との間
隙から漏水した痕跡がなく、コーナーのきれいな
方形断面の気泡体が得られた。Compounding formula CP-3000 (glycerin base trifunctional molecular weight
3000 Polyether polyol 100 parts by weight Water 4.0 Triethylenediamine 0.2 Silicone oil 1.5 Tin catalyst (dibutyl dilaurate) 0.25 Freon 11 5.0 Tolylene diisocyanate (T-80) 53.0 The resulting product is the initial stage of foaming discharged from the nozzle. There was no trace of the stock solution leaking from the gap between the bottom conveyor and the side band, and a foam with a square cross section with clean corners was obtained.
図はこの発明方法を示す一実施例の装置の斜視
図。
1……コンベア、31,32……側帯、4……
ノズル、5……押圧コンベア。
The figure is a perspective view of an apparatus according to an embodiment of the method of this invention. 1...Conveyor, 3 1 , 3 2 ...Side band, 4...
Nozzle, 5...press conveyor.
Claims (1)
なる底部コンベアベルトと、この上面両側に上記
コンベアベルトとは別体でかつこれと同期して移
動する側帯とで囲繞される凹形コンベアを形成
し、この一端へクリーム状発泡初期原液を連続的
に注入し、底部コンベアベルトと側帯と合わせ目
から発泡初期原液の漏液を防止しつつ発泡反応を
行なわせるとともに、発泡ガスが気泡体の表面か
ら出終つて気泡の生成反応が終了した点から架橋
反応が終了する点にわたつて気泡体の上表面を押
圧コンベアで軽圧縮して最終製品厚み寸法の気泡
体とすることを特徴とする合成樹脂気泡体の製造
方法。1 A concave conveyor surrounded by a bottom conveyor belt made of a releasable member without using a grooved release paper, and side bands on both sides of the upper surface that are separate from the conveyor belt and move in synchronization with the conveyor belt. A cream-like foaming initial stock solution is continuously injected into one end of the foaming reactor while preventing leakage of the foaming initial stock solution from the bottom conveyor belt, side band, and seam, and a foaming reaction is carried out. The upper surface of the foam is lightly compressed using a pressure conveyor from the point where the bubble generation reaction ends after exiting the surface to the point where the crosslinking reaction ends to form a foam having the thickness of the final product. Method for producing synthetic resin foam.
Priority Applications (6)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11910176A JPS5345371A (en) | 1976-10-04 | 1976-10-04 | Manufacture of synthetic resin foam |
| GB4080677A GB1593302A (en) | 1976-10-04 | 1977-09-30 | Method for continuous production of slabs of polyurethane foam |
| FR7729717A FR2366117A1 (en) | 1976-10-04 | 1977-10-03 | PROCESS FOR CONTINUOUSLY PRODUCING PLATES OF POROUS MATERIAL |
| DE19772744492 DE2744492A1 (en) | 1976-10-04 | 1977-10-04 | PROCESS FOR THE CONTINUOUS PRODUCTION OF FOAM BLOCKS OR -PLATES |
| BE181435A BE859349A (en) | 1976-10-04 | 1977-10-04 | PROCESS FOR THE CONTINUOUS PRODUCTION OF PLATES OR SLABS OF POROUS MATERIAL |
| US06/213,046 US4348164A (en) | 1976-10-04 | 1980-12-04 | Apparatus for continuous production of a slab of polyurethane foam |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11910176A JPS5345371A (en) | 1976-10-04 | 1976-10-04 | Manufacture of synthetic resin foam |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5345371A JPS5345371A (en) | 1978-04-24 |
| JPS6128495B2 true JPS6128495B2 (en) | 1986-06-30 |
Family
ID=14752922
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11910176A Granted JPS5345371A (en) | 1976-10-04 | 1976-10-04 | Manufacture of synthetic resin foam |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPS5345371A (en) |
| BE (1) | BE859349A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN121468852B (en) * | 2026-01-07 | 2026-04-03 | 福建省晋江市三盈鞋材有限公司 | A foaming equipment for sponge production |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3354503A (en) * | 1964-04-02 | 1967-11-28 | Gen Tire & Rubber Co | Urethane foaming apparatus |
| US3553300A (en) * | 1968-07-10 | 1971-01-05 | Tenneco Chem | Process for controlling the upper surface contour of foamable polyurethane during expansion in an open top mold |
-
1976
- 1976-10-04 JP JP11910176A patent/JPS5345371A/en active Granted
-
1977
- 1977-10-04 BE BE181435A patent/BE859349A/en not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| BE859349A (en) | 1978-02-01 |
| JPS5345371A (en) | 1978-04-24 |
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