JPS604767B2 - Method and device for discharging liquid synthetic resin raw materials - Google Patents

Method and device for discharging liquid synthetic resin raw materials

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Publication number
JPS604767B2
JPS604767B2 JP52063069A JP6306977A JPS604767B2 JP S604767 B2 JPS604767 B2 JP S604767B2 JP 52063069 A JP52063069 A JP 52063069A JP 6306977 A JP6306977 A JP 6306977A JP S604767 B2 JPS604767 B2 JP S604767B2
Authority
JP
Japan
Prior art keywords
raw material
synthetic resin
resin raw
liquid synthetic
discharging
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
Application number
JP52063069A
Other languages
Japanese (ja)
Other versions
JPS53147761A (en
Inventor
実 斉藤
隆一 高橋
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP52063069A priority Critical patent/JPS604767B2/en
Publication of JPS53147761A publication Critical patent/JPS53147761A/en
Publication of JPS604767B2 publication Critical patent/JPS604767B2/en
Expired legal-status Critical Current

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  • Application Of Or Painting With Fluid Materials (AREA)
  • Coating Apparatus (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Moulding By Coating Moulds (AREA)

Description

【発明の詳細な説明】 本発明は液状の合成樹脂原料、例えば反応と同時に粘性
、体積が急速に変るポリウレタンフオーム原料を均一に
、かつ飛散な〈吐出する方法とその装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method and apparatus for discharging liquid synthetic resin raw materials, such as polyurethane foam raw materials whose viscosity and volume rapidly change upon reaction, uniformly and without scattering.

従来、例えばポリウレタンフオームをモールド的に充填
した複合パネル、発泡体を製造する場合、一般に吹付法
(スプレー法)、注入法が用いられていた。
Conventionally, when manufacturing composite panels or foams filled with polyurethane foam in a molded manner, spraying methods and injection methods have generally been used.

しかしながらスプレー法で例えば第1図に示す如き金属
板Aの凹部Bにフオーム原料をスプレーすると、■吹付
領域(第1図においてLで示す)が少くとも50〜10
0伽必要であること、■高圧でスプレーされるためポリ
ウレタンフオーム原料の反応途中の生成物が霧状で浮遊
するので安全衛生上非常に悪い。■スプレーパターンが
ノズルと吐出面の最短距離(中央部)に一番多く、そこ
から離れるに従って減少する分布所謂山状の積層となり
、均一スプレーが不可能である。■高圧でスプレーする
ため飛散量が多い。なお低圧力では混合不足で反応時間
物性に悪影響があるために高圧でスプレーしている。■
スプレー量が少し、フオーム、所謂薄肉例えば10〜5
瓜吻位のフオームを形成するようにスプレ−できない。
また注入法には■吐出が線状である。■注入量は大量で
ある。■飛散はない。■フオームは厚肉である。■広幅
(約20〜30伽)にフオーム原料を均一に吐出分布す
るにはトラバースするか吐出口を複数個配列することが
必要である等の点を考慮することがある。換言すれば薄
物のフオーム(約10〜20側、5仇舷以下)を形成す
るに不向きであること、広幅には吐出口をトラバースす
るか、複数個配列するが、均一分布の組織にな物こくい
こと。トラバースの際無駄なく領域内にフオーム原料を
吐出できないこと等があることである。本発明はこのよ
うな欠′点を除去するために高圧でスプレーされるフオ
ーム原料を一担減圧し、その減圧された圧力で原料自体
を圧送し、その出口において方向変換せしめてより一層
混合をよくすると共にフィルム状的な吐出になるように
したポIJウレタンフオーム等の合成樹脂発泡体原料の
吐出方法およびその装置を提供する。
However, when the foam raw material is sprayed into the recess B of the metal plate A as shown in FIG. 1 using the spray method, the spray area (indicated by L in FIG.
(1) Because it is sprayed under high pressure, products during the reaction of the polyurethane foam raw materials are suspended in the form of mist, which is very bad in terms of safety and health. (2) The spray pattern is most common at the shortest distance between the nozzle and the discharge surface (in the center) and decreases as the distance from there increases, resulting in a so-called mountain-like stacked layer, making it impossible to spray uniformly. ■Because it is sprayed under high pressure, there is a large amount of scattering. It should be noted that spraying is carried out at high pressure because low pressure causes insufficient mixing and adversely affects the reaction time and physical properties. ■
Small amount of spray, foam, so-called thin wall e.g. 10-5
It is not possible to spray to form a proboscis form.
Furthermore, in the injection method, (1) discharge is linear. ■The amount of injection is large. ■There is no scattering. ■The foam is thick. (2) In order to uniformly discharge and distribute the foam raw material over a wide width (approximately 20 to 30 degrees), consideration may be given to the necessity of traversing or arranging a plurality of discharge ports. In other words, it is unsuitable for forming thin forms (approximately 10 to 20 sides, 5 broadsides or less), and for wide widths, traversing or arranging multiple discharge ports is difficult, but it is difficult to form a uniformly distributed structure. It's hard. During traverse, the foam material may not be discharged into the area without waste. In order to eliminate these drawbacks, the present invention first reduces the pressure of the foam raw material that is sprayed at high pressure, uses the reduced pressure to pump the raw material itself, and changes its direction at the outlet to achieve further mixing. To provide a method and apparatus for discharging raw materials for synthetic resin foam such as polyurethane foam, which can be discharged in a film-like manner.

以下に図面を用いて本発明に係る液状の合成樹脂原料の
吐出方法とその装置の一実施例について詳細に説明する
DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of a method for discharging a liquid synthetic resin raw material and an apparatus therefor according to the present invention will be described below in detail with reference to the drawings.

第2図は上記装置を示す縦断面図であり、例えばポリウ
レタンフオーム原料を定速で移動する第1図に示す如き
金属板の凹部に吐出する場合を示す。1はスプレーガン
で例えばェアレスタィプであり、上記原料を高圧(約1
0〜100k9/地)で約9k9/minの割合でスプ
レーするものである。
FIG. 2 is a longitudinal cross-sectional view of the above-mentioned apparatus, showing, for example, a case in which polyurethane foam raw material is discharged into a concave portion of a moving metal plate as shown in FIG. 1 at a constant speed. 1 is a spray gun, for example of airless type, which sprays the above raw materials at high pressure (approximately 1
0 to 100k9/ground) and sprays at a rate of about 9k9/min.

2,3は原料循環系であり、循環系2はポリオール用、
循環系3はポリィソシアネ−ト用に用いる。
2 and 3 are raw material circulation systems, circulation system 2 is for polyol;
Circulation system 3 is used for polyisocyanate.

4は開閉弁、5は弁開閉用の駆動機構、6はノズルで約
2〜5側?位の口径d,に形成されている。
4 is an on-off valve, 5 is a drive mechanism for opening and closing the valve, and 6 is a nozzle on the 2-5 side? It is formed to have an aperture of about d.

なおこの口径d,はスプレー量、圧力によって例示と関
係なく大きく変化する。7は中空体でノズルの口径d,
より大きい口径もの中空部8に形成し、上端入口にノズ
ル装着構造、下端の出口9に傾斜した開□10を設ける
と共に入口と出口9を直線的に蓮適状態にしたものであ
る。
Note that this aperture diameter d varies greatly depending on the spray amount and pressure, regardless of the example. 7 is a hollow body with a nozzle diameter d,
It is formed in a hollow part 8 with a larger diameter, has a nozzle mounting structure at the upper end inlet, has an inclined opening 10 at the lower end outlet 9, and has the inlet and outlet 9 in a straight line.

さらに詳説すると、中空体7はノズルから高圧でスプレ
ーされた霧状または泡状、一部液状のスプレー物を混合
すると共にスプレー圧力を大幅に減圧し、かつスプレー
物で中空部8を充満してスプレー圧とその液圧によって
ノズル6から乱流でスプレーされた原料を層流化して吐
出せしめる長さ1を有する。これは出口9から等圧力的
に吐出するためである。また関口10はスプレー物の流
れ方向、所謂中空部8の鞠心10に対して層流の流れ方
向を変換するために角度8,を有して形成する。なお角
度8,は中空部口径d,と圧力との相対.的関係によっ
て例えば第3図に示す如き断面になる。この角度8,の
例としては約300、600がある。また開□10の中
空部8の軸心側女台端10aは混合原料を吐出する範囲
をコント。ールするためのものであり、例えば第4図a
に示す如くs=oから10aが中空部8の中心部から始
まるときは理論的に180oの範囲内に吐出可能になり
、これにより偏心、所謂sが大きくなるに従って吐出範
囲は第4図b,cに示す如く狭い範囲になる。もちろん
、実際には粘性、その他の抵抗によって狭い角度で吐出
される。11は衝突用板で鏡面に形成した衝突用平面1
1aを有し中空体7から層流化されて圧送されてくる原
料と衝突して圧力の再低減と方向変換用行わしめると共
にフィルム状で原料を吐出するものである。
More specifically, the hollow body 7 mixes the mist, foam, and partially liquid spray sprayed at high pressure from the nozzle, significantly reduces the spray pressure, and fills the hollow part 8 with the spray. It has a length 1 that allows the raw material sprayed in a turbulent flow from the nozzle 6 to be laminarized and discharged by the spray pressure and its liquid pressure. This is because the liquid is discharged from the outlet 9 under equal pressure. Further, the entrance 10 is formed at an angle 8 to change the flow direction of the laminar flow relative to the flow direction of the spray material, ie, the so-called maricenter 10 of the hollow portion 8 . Note that the angle 8 is relative to the hollow diameter d and the pressure. Depending on the relationship, the cross section will be as shown in FIG. 3, for example. An example of this angle 8 is approximately 300,600. Further, the female end 10a on the axis side of the hollow portion 8 of the opening □10 controls the range from which the mixed raw material is discharged. For example, Figure 4a
As shown in FIG. 4, when 10a starts from the center of the hollow part 8 from s=o, it is theoretically possible to discharge within a range of 180 degrees, and as the eccentricity, so-called s, increases, the discharge range increases as shown in FIG. The range is narrow as shown in c. Of course, in reality, it is ejected at a narrow angle due to viscosity and other resistance. 11 is a collision plate and is a collision plane 1 formed into a mirror surface.
1a, collides with the raw material pumped in laminar flow from the hollow body 7, reduces the pressure again, changes direction, and discharges the raw material in the form of a film.

この衝突用板の大きさは衝突の圧力によって変るほか、
吐出範囲にも関係がある。またフィルム状で吐出される
吐出面は少くとも原料の背面への回りを抑制するために
鋭角に形成する。もちろん、衝突用板が層硫化された圧
力によって振動あるいは変形しないものであれば薄板体
でもよい。12は装着臭で中空体7と衝突用板11を着
脱可能に装着するものである。
The size of this collision plate varies depending on the pressure of the collision, and
It is also related to the discharge range. Further, the discharge surface for discharging the material in the form of a film is formed at an acute angle in order to at least prevent the raw material from going around to the back side. Of course, a thin plate may be used as long as the collision plate does not vibrate or deform due to the pressure of layer sulfurization. Reference numeral 12 denotes a mounting part for removably mounting the hollow body 7 and the collision plate 11.

次に製造方法について説明する。Next, the manufacturing method will be explained.

まずスプレーガン1のノズル6を金属板Aのフオ−ム原
料吐出面Bに対して垂直状に配置する。このノズル端に
中空体7の入口を連結し、その下端に衝突用板I1を第
2図の如く直交するように装着する。また金属板Aは矢
印方向に30m/minの速度で連続して移動している
と仮定する。なお、例えばフオームの厚さ15側、吐出
量1.5k9/min、スプレー圧力30k9/地、d
,=2帆?、も=8肋ぐ、1=10伍舷、a,=600
、82=150、H=300、フィルム状で吐出される
原料が衝突板から離れるときの速度4.4の′SEC、
S=0.8側、=30仇ゅ A液、B液の液温20q0
とする。そこでいま弁6が上方に上昇すると、A液とB
液がノズル6から混合と同時に務状でスプレーされる。
スプレーされた混合物は中空体7の中空部8にスプレー
されると同時に大きい体積のため減少される。しかも反
応が開始されるため粘度が上昇するし、上方から混合物
が次々と供給される。それによって直ちに中空部は混合
物によって充満される。すると中空部のノズル機から幾
分下方の位置、すなわちスプレーノズルの圧力によって
乱流が層硫化せしめられて、かつスプレー圧力も付加さ
れて液圧でもつて衝突用板11に連続して衝突すると同
時に閉口10からフィルム状で吐出される。なお理論的
にフィルム状で吐出される理由は明らかでないが、閉口
10では層流になって一定圧力で鏡面上に吐出し、かつ
粘性と圧力の相対的なバランスも付加されて原料が霧状
にならずに薄膜、所謂フィルム状になって衝突用板の端
縁から水平方向に初速度Vo=4.4凧/SECで吐出
される。そして金属板A上に凹部Bに一点鎖線で示すよ
うに吐出される。これが金属板A上では第5図に示すパ
ターンになる。この円孤状の軌跡が金属板Aとの凹部B
に形成される。なお衝突用板1 1から吐出されて約I
Q地位の範囲は完全なフィルム状であり、吐出中の急速
な反応等のために粘度が増し、金属坂上では完全なフィ
ルム状の積層でなく、第5図の如く幾分空間を有して吐
出されたパターンになる。しかし、これはこの場合、非
常に好ましい結果となる。すなわち、ポリウレタンの場
合、クリームタイムで吐出し、粘性、自己接着性の増大
するゲルタィムで落下付着すると金属板との接着が良く
、後日に剥離等もないからである。もちろん、金属板の
移動速度を遅くすると完全に第5図のパターンで金属板
が移動すると、その上にアルミ箔13が積層される。こ
れをある間隔を有して対面させた上下の無端ベルト14
,15間に送出する。この間隔間で加溢、加圧されて一
定(15肌厚)の複合パネルを得る。このパネルを切断
し観察してみると、成分の混合が十分に行われているた
め発泡組織(気泡)が均一で、しかも均一に吐出されて
いるので密度が一様である。換言すれば小量の原料を所
定の厚さに効率よく発泡形成したことである。また金属
板の端緑には原料の飛散物が全くなく、作業環境におい
ても混合物の浮遊は全く見られなかったので、有効に原
料を使用していた。以上、説明したのは本発明に係る液
状の合成樹脂原料を吐出する方法の一例にすぎず、例え
ば第6図に示す如くノズル、中空体を吐出面に対し83
の角度で支持し、混合された原料を関口から短い距離で
吐出面に吐出すようにして吐出すること′もできる。
First, the nozzle 6 of the spray gun 1 is arranged perpendicularly to the foam material discharge surface B of the metal plate A. The inlet of the hollow body 7 is connected to this nozzle end, and the collision plate I1 is attached to the lower end thereof so as to be perpendicular to it as shown in FIG. Further, it is assumed that the metal plate A is continuously moving in the direction of the arrow at a speed of 30 m/min. For example, the foam thickness is 15, the discharge rate is 1.5k9/min, the spray pressure is 30k9/ground, d
, = 2 sails? , also = 8 ribs, 1 = 10 yards, a, = 600
, 82=150, H=300, 'SEC' of the velocity of 4.4 when the raw material discharged in film form leaves the collision plate,
S = 0.8 side, = 30㎇ Liquid temperature of A liquid and B liquid 20q0
shall be. Now, when valve 6 moves upward, liquid A and B
The liquid is sprayed from the nozzle 6 simultaneously with mixing.
The sprayed mixture is sprayed into the hollow part 8 of the hollow body 7 and at the same time is reduced due to its large volume. Moreover, since the reaction starts, the viscosity increases, and the mixture is successively fed from above. As a result, the hollow space is immediately filled with the mixture. Then, the turbulent flow is laminarized by the pressure of the spray nozzle at a position slightly below the nozzle machine in the hollow part, and the spray pressure is also applied, so that it continuously collides with the collision plate 11 with hydraulic pressure. It is discharged from the closing port 10 in the form of a film. The theoretical reason why the material is discharged in the form of a film is not clear, but at the closing port 10, it becomes a laminar flow and is discharged onto the mirror surface with a constant pressure, and the relative balance between viscosity and pressure is also added, so that the raw material becomes a mist. Instead, it becomes a thin film, a so-called film, and is discharged from the edge of the collision plate in the horizontal direction at an initial velocity Vo=4.4 kites/SEC. Then, it is discharged onto the metal plate A into the recess B as shown by the dashed line. This becomes the pattern shown in FIG. 5 on metal plate A. This arc-shaped locus is the concave B with the metal plate A.
is formed. It should be noted that approximately I
The range of the Q layer is completely film-like, and the viscosity increases due to rapid reactions during discharge, etc. On the metal slope, the layer is not completely film-like, but has some spaces as shown in Figure 5. It becomes a discharged pattern. However, this is a very favorable result in this case. That is, in the case of polyurethane, if it is discharged during the cream time and falls and adheres during the gel time, where viscosity and self-adhesiveness increase, it will adhere well to the metal plate and will not peel off later. Of course, if the moving speed of the metal plate is slowed down, the metal plate will move completely in the pattern shown in FIG. 5, and the aluminum foil 13 will be laminated thereon. Upper and lower endless belts 14 facing each other with a certain interval
, 15. It is flooded and pressurized during this interval to obtain a composite panel of constant (15 skin thickness). When this panel was cut and observed, it was found that the foam structure (bubbles) was uniform because the ingredients were sufficiently mixed, and the density was uniform because the foam was discharged uniformly. In other words, a small amount of raw material was efficiently foamed to a predetermined thickness. In addition, there were no scattered raw materials on the edge of the metal plate, and no floating of the mixture was observed in the working environment, so the raw materials were used effectively. What has been described above is only one example of the method for discharging the liquid synthetic resin raw material according to the present invention. For example, as shown in FIG.
It is also possible to discharge the mixed raw materials by discharging them onto the discharge surface over a short distance from the entrance.

さらに液状の合成樹脂原料としてはフェノールフオーム
、エポキシフオーム、ユリアフオーム、ポリイソシアヌ
レートフオーム等も同様に吐出できる。上述したように
本発明に係る吐出方法およびその装置によれば、化学反
応を急速に行なう合成樹脂原料を所定の広幅内に均一散
布状で吐出できる特徴がある。
Further, as liquid synthetic resin raw materials, phenol foam, epoxy foam, urea foam, polyisocyanurate foam, etc. can be similarly discharged. As described above, the discharging method and device according to the present invention have the feature that synthetic resin raw materials that rapidly undergo chemical reactions can be uniformly distributed within a predetermined wide width.

また吐出物がフィルム状であるため作業環境に混合物の
微粒子が浮遊せず、しかも所定範囲以外に飛散しないた
め作業能率、歩止り、安全衛生上大きな特徴がある。さ
らに上記の如き原料を少量でも均一に分散せしめられる
ので薄物フオームで、かつ広幅を形成できる。
In addition, since the discharged material is in the form of a film, fine particles of the mixture do not float in the working environment and are not scattered outside a predetermined range, which has great advantages in terms of work efficiency, yield, and safety and health. Furthermore, since the above-mentioned raw materials can be uniformly dispersed even in a small amount, a thin form and a wide width can be formed.

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

第1図は液状の合成樹脂原料を吐出されるべき、例えば
金属板の一例を示す斜視図、第2図は本発明に係る吐出
方法装置を説明するための縦断面図、第3図は本発明に
係る装置の一部である関口の断面を示す説明図、第4図
a,bおよびcは吐出状態の一例を示す説明図、第5図
は本発明により吐出されるパターンの一例を示す説明図
、第6図はその他の実施例を示す説明図である。 1……スプレーガン、6……ノズル、7……中空体、8
・・・・・・中空部、10・・・・・・関口、11・…
・・衝突用板。 オー風 オ2 図 オ3図 才4図 才5図 オ6■
FIG. 1 is a perspective view showing an example of, for example, a metal plate from which a liquid synthetic resin raw material is to be discharged, FIG. 2 is a longitudinal cross-sectional view for explaining the discharge method and apparatus according to the present invention, and FIG. An explanatory diagram showing a cross section of a sekiguchi which is a part of the device according to the invention, FIGS. 4 a, b and c are explanatory diagrams showing an example of a discharge state, and FIG. 5 shows an example of a pattern discharged according to the present invention. An explanatory diagram, FIG. 6, is an explanatory diagram showing another embodiment. 1... Spray gun, 6... Nozzle, 7... Hollow body, 8
...Hollow part, 10...Sekiguchi, 11...
...Collision plate. O wind O 2 Fig. O 3 Fig. 4 Fig. 5 Fig. O 6 ■

Claims (1)

【特許請求の範囲】 1 液状の合成樹脂原料を高圧で中空体内に混合しなが
ら噴射し、該中空体で噴射圧力を減圧すると共に混合、
圧送して層流とならしめ、該層流を平面状の鏡面に衝突
して混合液をフイルム状的に吐出したことを特徴とする
液状の合成樹脂原料を吐出する方法。 2 層流を鏡面に直交する如く衝突した特許請求の範囲
第1項記載の液状の合成樹脂原料を吐出する方法。 3 液状の合成樹脂原料がポリウレタンフオーム、ポリ
イソシアヌレートフオーム、フエノールフオーム、ユリ
アフオーム、エポキシフオーム等からなる特許請求の範
囲第1項、第2項記載の液状の合成樹脂原料を吐出する
方法。 4 液状の合成樹脂原料が高圧で中空体内に噴射される
ときに液状あるいは霧状、泡状で噴射される特許請求の
範囲第1項〜第3項記載の液状の合成樹脂原料を吐出す
る方法。 5 液状の合成樹脂原料を噴射するスプレーガンと、該
スプレーガンのノズル口径より少くとも大きい入口と原
料の流れ方向に対し傾斜した開口を形成した出口とを直
線状の中空部で連結した中空体と、該出口に上記中空部
の軸心と少くともある角度で対面する如く平面状の鏡面
を有する衝突用板を着脱自在に密着固着したことを特徴
とする液状の合成樹脂原料を吐出する装置。 6 開口の傾斜角が衝突用板に対し15〜90°である
特許請求の範囲第5項記載の液状の合成樹脂原料を吐出
する装置。 7 中空部の縦断面積と開口の縦断面積がほぼ等しい特
許請求の範囲第5項、第6項記載の液状の合成樹脂原料
を吐出する装置。 8 ノズルを噴射された液状の原料が吐出される面に対
し平行でない状態で支持し、該ノズルと中空体を直線状
に連結し、該中空体の下端に衝突用板を直交する如く固
着した特許請求の範囲第5項〜第7項記載の液状の合成
樹脂原料を吐出する装置。 9 開口の衝突用板と接触する面積を変化することによ
って吐出される原料の吐出範囲を制御する特許請求の範
囲第5項〜第8項記載の液状の合成樹脂原料を吐出する
装置。
[Claims] 1. Injecting a liquid synthetic resin raw material at high pressure while mixing it into a hollow body, reducing the injection pressure in the hollow body and mixing it,
A method for discharging a liquid synthetic resin raw material, characterized in that the laminar flow is made into a laminar flow by force-feeding, and the laminar flow collides with a planar mirror surface to discharge a mixed liquid in the form of a film. 2. A method for discharging a liquid synthetic resin raw material according to claim 1, in which a laminar flow collides perpendicularly with a mirror surface. 3. A method for discharging a liquid synthetic resin raw material according to claims 1 and 2, wherein the liquid synthetic resin raw material is composed of polyurethane foam, polyisocyanurate foam, phenol foam, urea foam, epoxy foam, etc. 4. A method for discharging a liquid synthetic resin raw material according to claims 1 to 3, in which the liquid synthetic resin raw material is injected into a hollow body under high pressure in the form of a liquid, mist, or foam. . 5. A hollow body in which a spray gun that injects a liquid synthetic resin raw material, an inlet that is at least larger than the nozzle diameter of the spray gun, and an outlet that has an opening inclined with respect to the flow direction of the raw material are connected by a linear hollow part. and a device for discharging liquid synthetic resin raw material, characterized in that a collision plate having a flat mirror surface is removably firmly fixed to the outlet so as to face the axis of the hollow portion at least at a certain angle. . 6. The apparatus for discharging liquid synthetic resin raw material according to claim 5, wherein the opening has an inclination angle of 15 to 90 degrees with respect to the collision plate. 7. An apparatus for discharging a liquid synthetic resin raw material according to claims 5 and 6, wherein the vertical cross-sectional area of the hollow portion and the vertical cross-sectional area of the opening are approximately equal. 8 The nozzle was supported in a state not parallel to the surface from which the injected liquid raw material was discharged, the nozzle and the hollow body were connected in a straight line, and the collision plate was fixed to the lower end of the hollow body so as to be perpendicular to the surface. An apparatus for discharging a liquid synthetic resin raw material according to claims 5 to 7. 9. An apparatus for discharging a liquid synthetic resin raw material according to claims 5 to 8, wherein the discharge range of the discharged raw material is controlled by changing the area of the opening in contact with the collision plate.
JP52063069A 1977-05-30 1977-05-30 Method and device for discharging liquid synthetic resin raw materials Expired JPS604767B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP52063069A JPS604767B2 (en) 1977-05-30 1977-05-30 Method and device for discharging liquid synthetic resin raw materials

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP52063069A JPS604767B2 (en) 1977-05-30 1977-05-30 Method and device for discharging liquid synthetic resin raw materials

Publications (2)

Publication Number Publication Date
JPS53147761A JPS53147761A (en) 1978-12-22
JPS604767B2 true JPS604767B2 (en) 1985-02-06

Family

ID=13218676

Family Applications (1)

Application Number Title Priority Date Filing Date
JP52063069A Expired JPS604767B2 (en) 1977-05-30 1977-05-30 Method and device for discharging liquid synthetic resin raw materials

Country Status (1)

Country Link
JP (1) JPS604767B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5648166Y2 (en) * 1978-11-30 1981-11-11
DE102005005151A1 (en) * 2005-02-04 2006-08-10 Hennecke Gmbh Process and apparatus for producing polyurethane block foam

Also Published As

Publication number Publication date
JPS53147761A (en) 1978-12-22

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