JP2006281720A - Supplying device and method for polyurethane foaming stock liquid component - Google Patents

Supplying device and method for polyurethane foaming stock liquid component Download PDF

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JP2006281720A
JP2006281720A JP2005108265A JP2005108265A JP2006281720A JP 2006281720 A JP2006281720 A JP 2006281720A JP 2005108265 A JP2005108265 A JP 2005108265A JP 2005108265 A JP2005108265 A JP 2005108265A JP 2006281720 A JP2006281720 A JP 2006281720A
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stock solution
polyurethane foam
component
fed
heat exchanger
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Yoshio Nagura
由雄 名倉
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Toyo Tire Corp
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Toyo Tire and Rubber Co Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide the supplying device and method for a polyurethane foaming stock liquid, which realizes a proper temperature adjustment of a stock liquid feeding into a mixing head device even when the supplement of a large amount of the stock liquid at one time is necessary. <P>SOLUTION: This supplying device of the polyurethane foaming stock liquid component is equipped with a heat exchanger 3 for bringing a polyurethane foaming stock liquid component into a predetermined temperature range and a stock liquid tank 4 for storing the polyurehane foaming stock liquid component fed from this heat exchanger and equipped with a temperature adjusting function so as to be able to feed the polyurethane foaming stock liquid component from the stock liquid tank 4 to a mixing head 6 and, at the same time, to circulatingly feed the component from the mixing head 6 to the stock liquid tank 4 under the condition, in the middle of the feeding of the polyurethane foaming stock liquid component from the mixing head 6 to stock liquid tank 4, the component is fed to the heat exchanger 3. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明はポリウレタン発泡原液成分供給装置と供給方法に関し、詳しくは、ポリウレタン発泡原液成分を所定温度範囲にする熱交換器と、この熱交換器から送給されたポリウレタン発泡原液成分を貯留すると共に温度調節機能を備える原液タンクと、を備えていて、前記ポリウレタン発泡原液成分を、前記原液タンクからミキシングヘッドへ送給可能になっていると共に、前記ミキシングヘッドから前記原液タンクへ送給させ循環させるようになっているポリウレタン発泡原液成分供給装置と供給方法に関する。   The present invention relates to a polyurethane foam stock solution component supplying apparatus and a supply method, and more specifically, a heat exchanger that brings a polyurethane foam stock solution component into a predetermined temperature range, and a polyurethane foam stock solution component fed from the heat exchanger and storing a temperature. An undiluted solution tank having an adjustment function, and the polyurethane foam undiluted solution component can be fed from the undiluted solution tank to the mixing head, and is fed from the mixing head to the undiluted solution tank for circulation. The present invention relates to a polyurethane foam stock solution component supplying apparatus and a supplying method.

ポリウレタン発泡体を断熱材として有するパネル等の構成物を製造する場合、その原液成分である、液状ポリオール成分と液状ポリイソシアネート成分とを高圧あるいは低圧ミキシングヘッド装置の混合部に送給し、ここで混合・撹拌して反応させ、この混合反応液を所定の型枠内あるいは面材上に吐出して行う2液混合方式が一般的である。   When manufacturing a component such as a panel having a polyurethane foam as a heat insulating material, the liquid polyol component and the liquid polyisocyanate component, which are the raw liquid components, are fed to the mixing section of the high-pressure or low-pressure mixing head device. A two-liquid mixing method is generally used in which the reaction is performed by mixing and stirring, and this mixed reaction liquid is discharged into a predetermined mold or on a face material.

このポリウレタン発泡原液成分(以下、単に「原液」ということがある)を、ミキシングヘッド装置の混合部に供給する際、予め原液タンク内に貯留し、原液温度を所定範囲内にしてミキシングヘッド装置から吐出できるよう、温度調節を行っている。そして、ミキシングヘッド装置から吐出すべく、原液タンクから原液をミキシングヘッド装置へ送給すると、別に配置されている原液ドラム缶から、新たに原液タンク内に原液が補充される。この場合、一度に大量の原液を補充すると、原液温度を所定範囲内に温度調節することが難くなるため、原液タンク内の原液が少量減るごとに、減少した分だけ補充するようにしている(例えば、特許文献1。[0003][0004]の記載)。
特開平7−308932号公報
When this polyurethane foam stock solution component (hereinafter sometimes referred to simply as “stock solution”) is supplied to the mixing section of the mixing head device, it is stored in the stock solution tank in advance, and the stock solution temperature is kept within a predetermined range from the mixing head device. The temperature is adjusted so that it can be discharged. When the stock solution is fed from the stock solution tank to the mixing head device to be discharged from the mixing head device, the stock solution is newly replenished into the stock solution tank from a separately placed stock drum can. In this case, if a large amount of stock solution is replenished at a time, it is difficult to adjust the stock solution temperature within a predetermined range. Therefore, every time the stock solution in the stock solution tank is reduced, the reduced amount is replenished ( For example, Patent Document 1. [0003] [0004] description).
JP 7-308932 A

しかしながら、実際に硬質ポリウレタンフォームパネルなどを製造する場合に、少量づつ原液を補充しながらミキシングヘッド装置から原液を吐出することができないことがあり、そのような場合には一度に大量の原液を補充する必要のあるが、その場合には当然のことながら、適正な温度調節ができなくなる。   However, when manufacturing rigid polyurethane foam panels, etc., it may not be possible to discharge the stock solution from the mixing head device while replenishing the stock solution in small amounts. In such cases, replenish a large amount of stock solution at once. In this case, of course, proper temperature control cannot be performed.

もっとも、原液タンクには撹拌機が備えられているが、補充用の原液の温度が低く、原液タンク内の原液との温度差が大きいような場合には、補充用原液の比重が大きいため素早く原液タンクの底部に移動し、ミキシングヘッドに向けて送給される際には、低温の原液が送られてミキシングヘッドから吐出されるので、製品に発泡不良をもたらすおそれがある。   However, the stock solution tank is equipped with a stirrer. However, when the temperature of the stock solution for replenishment is low and the temperature difference from the stock solution in the stock solution tank is large, the specific gravity of the stock solution for replenishment is large, so it is quick. When moving to the bottom of the stock solution tank and being fed toward the mixing head, the low temperature stock solution is sent and discharged from the mixing head, which may result in poor foaming of the product.

そこで、本発明の目的は、上記従来技術の有する問題点に鑑みて、一度に大量の原液を補充する必要のある場合であっても、ミキシングヘッド装置に送給する原液に対して適正な温度調節ができるポリウレタン発泡原液成分供給装置と供給方法を提供することにある。   Therefore, in view of the above-described problems of the prior art, the object of the present invention is to provide a temperature suitable for the stock solution to be fed to the mixing head device even when it is necessary to replenish a large amount of stock solution at a time. An object of the present invention is to provide an apparatus and a method for supplying a polyurethane foam stock solution component that can be adjusted.

上記課題は、請求項記載の発明により達成される。すなわち、本発明に係る
ポリウレタン発泡原液成分供給装置の特徴構成は、ポリウレタン発泡原液成分を所定温度範囲にする熱交換器と、この熱交換器から送給されたポリウレタン発泡原液成分を貯留すると共に温度調節機能を備える原液タンクと、を備えていて、前記ポリウレタン発泡原液成分を、前記原液タンクからミキシングヘッドへ送給可能になっていると共に、前記ミキシングヘッドから前記原液タンクへ送給させ循環させるようになっていて、前記ポリウレタン発泡原液成分を前記ミキシングヘッドから前記原液タンクへ送給する途中に、前記熱交換器に送給させることにある。
The above object can be achieved by the invention described in the claims. That is, the characteristic configuration of the polyurethane foam undiluted liquid component supply device according to the present invention includes a heat exchanger that brings the polyurethane foam undiluted liquid component to a predetermined temperature range, and stores the polyurethane foam undiluted liquid component supplied from the heat exchanger and a temperature. An undiluted solution tank having an adjustment function, and the polyurethane foam undiluted solution component can be fed from the undiluted solution tank to the mixing head, and is fed from the mixing head to the undiluted solution tank for circulation. And the polyurethane foam concentrate solution component is fed to the heat exchanger while it is being fed from the mixing head to the concentrate tank.

この構成によれば、ミキシングヘッドからポリウレタン発泡原液成分が吐出され、一度に大量のポリウレタン発泡原液成分を補充する必要のある場合であっても、補充されるポリウレタン発泡原液成分とミキシングヘッドから戻される所定温度範囲にあるポリウレタン発泡原液成分とが、共に熱交換器に送給されるため、両者の混合による適温への平準化が進行し、熱交換器での温度調節が行い易くなって、ミキシングヘッド装置に送給するポリウレタン発泡原液成分に対して容易に適正な温度調節ができることになる。補充される大量のポリウレタン発泡原液成分を、殊更大容量の熱交換器を用いて処理する必要もなく、既存の設備を用いるだけで、容易にポリウレタン発泡原液成分の温度調節ができる。   According to this configuration, the polyurethane foam concentrate solution component is discharged from the mixing head, and even if it is necessary to replenish a large amount of polyurethane foam concentrate solution at once, it is returned from the replenished polyurethane foam concentrate component and the mixing head. Since both the polyurethane foam concentrate solution components in the specified temperature range are fed to the heat exchanger, leveling to an appropriate temperature is progressed by mixing them together, making it easier to adjust the temperature in the heat exchanger and mixing. It is possible to easily adjust the temperature appropriately for the polyurethane foam stock solution component fed to the head device. There is no need to process a large amount of the polyurethane foam stock solution component to be replenished by using a heat exchanger having a particularly large capacity, and the temperature of the polyurethane foam stock solution component can be easily adjusted only by using existing equipment.

その結果、一度に大量の原液を補充する必要のある場合であっても、ミキシングヘッド装置に送給する原液に対して適正な温度調節ができるポリウレタン発泡原液成分供給装置を提供することができた。   As a result, even when it is necessary to replenish a large amount of stock solution at once, it was possible to provide a polyurethane foam stock solution component supply device capable of adjusting the temperature appropriately for the stock solution fed to the mixing head device. .

前記ミキシングヘッドから前記熱交換器に送給させるポリウレタン発泡原液成分と、補充用に送給されるポリウレタン発泡原液成分と、を合流させて混合させる流体混合手段が前記熱交換器の上流側に設けられていることが好ましい。   A fluid mixing means is provided on the upstream side of the heat exchanger for mixing and mixing the polyurethane foam stock solution component fed from the mixing head to the heat exchanger and the polyurethane foam stock solution component fed for replenishment. It is preferable that

この構成によれば、補充用に送給されるポリウレタン発泡原液成分とミキシングヘッドから戻されるポリウレタン発泡原液成分との混合が、一層確実に均質化される。   According to this configuration, the mixing of the polyurethane foam stock solution component fed for replenishment and the polyurethane foam stock solution component returned from the mixing head is more reliably homogenized.

又、本発明に係るポリウレタン発泡原液成分供給方法の特徴構成は、ポリウレタン発泡原液成分を熱交換器により所定温度範囲にし、所定温度範囲にされたポリウレタン発泡原液成分を、温度調節機能を備える原液タンクに送給して貯留し、この原液タンクからミキシングヘッドへ前記ポリウレタン発泡原液成分を送給する共に、前記ミキシングヘッドから前記原液タンクへ送給して循環させるようにしている方法において、前記ポリウレタン発泡原液成分を前記ミキシングヘッドから前記原液タンクへ送給する途中で、前記熱交換器に送給することにある。   The polyurethane foam concentrate solution component supplying method according to the present invention is characterized in that the polyurethane foam concentrate solution component is brought to a predetermined temperature range by a heat exchanger, and the polyurethane foam concentrate solution component having a temperature range is adjusted to a predetermined temperature range. In the method in which the polyurethane foam stock solution component is fed from the stock solution tank to the mixing head, and the polyurethane foam stock solution component is fed from the mixing head to the stock solution tank for circulation. In the course of feeding the stock solution component from the mixing head to the stock solution tank, the solution is fed to the heat exchanger.

この構成によれば、一度に大量の原液を補充する必要のある場合であっても、ミキシングヘッド装置に送給する原液に対して適正な温度調節ができるポリウレタン発泡原液成分供給方法を提供できる。   According to this configuration, even when it is necessary to replenish a large amount of stock solution at a time, it is possible to provide a polyurethane foam stock solution component supplying method capable of adjusting temperature appropriately for the stock solution fed to the mixing head device.

前記ミキシングヘッドから前記熱交換器にポリウレタン発泡原液成分を循環・送給すると共に、この循環・送給されたポリウレタン発泡原液成分と、前記熱交換器に補充用に送給されるポリウレタン発泡原液成分とを合流させ、前記熱交換器の上流側で流体混合手段を用いて混合することが好ましい。   The polyurethane foam concentrate solution component is circulated and fed from the mixing head to the heat exchanger, and the polyurethane foam concentrate solution component circulated and fed, and the polyurethane foam concentrate component fed to the heat exchanger for replenishment And are mixed using a fluid mixing means on the upstream side of the heat exchanger.

この構成によれば、ミキシングヘッド装置に送給する原液に対して、一層適正な温度調節ができるポリウレタン発泡原液成分供給方法を提供できる。   According to this configuration, it is possible to provide a polyurethane foam stock solution component supplying method capable of adjusting the temperature more appropriately for the stock solution fed to the mixing head device.

本発明の実施形態を、図面を参照して詳細に説明する。図1は、本実施形態に係るポリウレタン発泡原液成分供給装置(以下、原液供給装置ということがある)の概略全体構成を示す。   Embodiments of the present invention will be described in detail with reference to the drawings. FIG. 1 shows a schematic overall configuration of a polyurethane foam stock solution component supply device (hereinafter sometimes referred to as a stock solution supply device) according to the present embodiment.

この原液供給装置は、別に用意されている原液貯留用ドラム缶1から供給ポンプ2等によって熱交換器3に原液を送給すると共に、この熱交換器3により適正な温度範囲に調節された原液を、温度調節機能を備えた原液タンク4に送給し、ここで十分に撹拌した後、原液を原液タンク3からメタリングポンプ5等を介してミキシングヘッド6へと送るようになっている。ミキシングヘッド6へと送られた原液は、常時、ミキシングヘッド6から原液タンク4へと戻され循環され、温度変動を少なくするようにされているが、本実施形態の場合、後述するように、ミキシングヘッド6から直接原液タンク4へ原液を戻さず、熱交換器3に戻すようにして、原液の温度変動を一層少なくするようにしている。そして、吐出時には、ミキシングヘッド6内のピストンヘッド(図示略)が作動して、ミキシングヘッド6先端のノズル6aから原液(後述する2液混合体)を吐出する。原液がミキシングヘッド6から吐出された後は、原液貯留用ドラム缶1から熱交換器3を介して原液タンク4に必要量が補充される。   This stock solution supply device feeds the stock solution from a separately prepared stock solution storage drum 1 to the heat exchanger 3 by a supply pump 2 and the like, and also feeds the stock solution adjusted to an appropriate temperature range by the heat exchanger 3. Then, it is fed to a stock solution tank 4 having a temperature control function, and after sufficiently stirring, the stock solution is sent from the stock solution tank 3 to the mixing head 6 via the metering pump 5 and the like. The stock solution sent to the mixing head 6 is always returned and circulated from the mixing head 6 to the stock solution tank 4 to reduce temperature fluctuations. In this embodiment, as will be described later, The stock solution is not returned directly from the mixing head 6 to the stock solution tank 4 but is returned to the heat exchanger 3 so that the temperature fluctuation of the stock solution is further reduced. At the time of discharge, a piston head (not shown) in the mixing head 6 is operated to discharge a stock solution (a two-liquid mixture described later) from the nozzle 6a at the tip of the mixing head 6. After the stock solution is discharged from the mixing head 6, the stock solution tank 4 is replenished with the necessary amount from the stock solution storage drum 1 through the heat exchanger 3.

熱交換器3は、原液貯留用ドラム缶1から送られる原液が冬季はかなり低く、夏季は高いため、これらを所定温度範囲内に収めるべく温度調節を行う。熱交換の方式は、特に限定されるものではない。   Since the stock solution sent from the stock solution storage drum can 1 is considerably low in winter and high in summer, the heat exchanger 3 adjusts the temperature to keep them within a predetermined temperature range. The heat exchange method is not particularly limited.

原液タンク3は、その外周を温度調節用のジャケット4aで被覆されていて、図示はしないが、外部から所定温度範囲内の水その他の液体がジャケット4a内を通流するようになっていると共に、原液タンク3内の原液を十分撹拌するための撹拌機4bを有する構成となっている。なお、図番Mは撹拌機4bの撹拌羽根を回転させる電動機である。   The outer periphery of the stock solution tank 3 is covered with a temperature adjusting jacket 4a. Although not shown, water and other liquids within a predetermined temperature range flow from the outside through the jacket 4a. And it has the structure which has the stirrer 4b for fully stirring the stock solution in the stock solution tank 3. FIG. In addition, the figure number M is an electric motor which rotates the stirring blade of the stirrer 4b.

ミキシングヘッド6は、図示はしないが、別の1組の原液供給装置と接続されており、ミキシングヘッド6の混合部において2液が混合・撹拌されて、これが先端ノズル6aから型枠内あるいは面材上に吐出される。ミキシングヘッド6から吐出される混合された原液は、その原液組成により、通常20〜30℃の範囲における所定温度に保持される。例えば、発泡剤にフロン(HFC等)を使用する場合は約20〜25℃程度、フロンを使用しない場合は約25〜30℃程度とされる。この温度範囲を外れると、粘度が変動して吐出し難くなると共に、2液を混合した後の反応速度にも制御し難い影響を与えるため、温度管理は重要な要素となる。   Although not shown, the mixing head 6 is connected to another set of undiluted solution supply devices, and the two liquids are mixed and stirred in the mixing section of the mixing head 6, and this is mixed in the formwork or surface from the tip nozzle 6 a. It is discharged onto the material. The mixed stock solution discharged from the mixing head 6 is normally kept at a predetermined temperature in the range of 20 to 30 ° C. depending on the composition of the stock solution. For example, when using chlorofluorocarbon (HFC or the like) as the foaming agent, the temperature is about 20 to 25 ° C., and when using no chlorofluorocarbon, the temperature is about 25 to 30 ° C. Outside this temperature range, the viscosity will fluctuate and it will be difficult to discharge, and the reaction rate after mixing the two liquids will also be difficult to control, so temperature management will be an important factor.

本実施形態の場合、原液は原液タンク4に戻されず、熱交換器3に戻されて、ここで温度調節され、その後原液タンク4に戻されるようになっている。このようになっていることから、原液タンク4に補充される原液の量が多い場合であっても、原液タンク4で貯留される原液の温度範囲を所定温度±2℃の範囲内に維持可能となる。つまり、補充のためにドラム缶1から送られてくる原液と、ミキシングヘッド6から戻される原液とが合流されて共に熱交換器3にて温度調節される。   In this embodiment, the stock solution is not returned to the stock solution tank 4 but is returned to the heat exchanger 3 where the temperature is adjusted and then returned to the stock solution tank 4. As a result, the temperature range of the stock solution stored in the stock solution tank 4 can be maintained within a predetermined temperature ± 2 ° C. even when the amount of the stock solution replenished in the stock solution tank 4 is large. It becomes. That is, the undiluted solution sent from the drum 1 for replenishment and the undiluted solution returned from the mixing head 6 are merged and the temperature is adjusted by the heat exchanger 3 together.

この場合、合流された原液が熱交換器3に導入される手前(上流)側で、例えばスタティックミキサーのような流体混合手段7により、十分に混合されることが好ましい。このようにすると、かなりの量の補充原液が混合されて熱交換器3に導入されたとしても、所定範囲の温度域に調節される時間を顕著に短くできて都合がよい。流体混合手段7としてスタティックミキサーを使用した場合、比較的短い時間で高い混合比率が得られ、均一度が高くなり好ましい。なお、図番8は逆止弁である。   In this case, it is preferable that the combined stock solution is sufficiently mixed by the fluid mixing means 7 such as a static mixer on the side (upstream) before being introduced into the heat exchanger 3. In this way, even if a considerable amount of the replenishment stock solution is mixed and introduced into the heat exchanger 3, the time for adjusting the temperature range to a predetermined range can be remarkably shortened, which is convenient. When a static mixer is used as the fluid mixing means 7, a high mixing ratio can be obtained in a relatively short time, and the degree of uniformity becomes high. In addition, the number 8 is a check valve.

本実施形態に使用されるポリウレタンフォーム原液は、特に限定されるものではなく、一般に使用される活性水素含有化合物、発泡剤、触媒等を含有する成分(ポリオール成分)と、ポリイソシアネート化合物を主成分とする成分(イソシアネート成分)を使用できる。   The polyurethane foam stock solution used in the present embodiment is not particularly limited, and a component (polyol component) containing a generally used active hydrogen-containing compound, a foaming agent, a catalyst, and the like, and a polyisocyanate compound are the main components. (Isocyanate component) can be used.

〔別実施の形態〕
(1)ポリウレタン発泡原液を吐出するミキシングヘッドは、高圧タイプでもよいし、低圧タイプのものでもよく、特に限定されるものではない。
[Another embodiment]
(1) The mixing head for discharging the polyurethane foam stock solution may be a high pressure type or a low pressure type, and is not particularly limited.

本発明の一実施形態に係るポリウレタン発泡原液成分供給装置を説明する概略全体構成図1 is a schematic overall configuration diagram illustrating a polyurethane foam stock solution component supply device according to an embodiment of the present invention.

符号の説明Explanation of symbols

3 熱交換器
4 原液タンク
6 ミキシングヘッド
7 流体混合手段
3 Heat exchanger 4 Stock solution tank 6 Mixing head 7 Fluid mixing means

Claims (4)

ポリウレタン発泡原液成分を所定温度範囲にする熱交換器と、この熱交換器から送給されたポリウレタン発泡原液成分を貯留すると共に温度調節機能を備える原液タンクと、を備えていて、前記ポリウレタン発泡原液成分を、前記原液タンクからミキシングヘッドへ送給可能になっていると共に、前記ミキシングヘッドから前記原液タンクへ送給させ循環させるようになっているポリウレタン発泡原液成分供給装置において、前記ポリウレタン発泡原液成分を前記ミキシングヘッドから前記原液タンクへ送給する途中に、前記熱交換器に送給させることを特徴とするポリウレタン発泡原液成分供給装置。 A heat exchanger for bringing the polyurethane foam stock solution component into a predetermined temperature range; and a stock solution tank for storing the polyurethane foam stock solution component fed from the heat exchanger and having a temperature adjusting function, the polyurethane foam stock solution In the polyurethane foam stock solution component supply device, the component can be fed from the stock solution tank to the mixing head, and is fed from the mixing head to the stock solution tank for circulation. Is supplied to the heat exchanger in the course of being fed from the mixing head to the stock solution tank. 前記ミキシングヘッドから前記熱交換器に送給させるポリウレタン発泡原液成分と、補充用に送給されるポリウレタン発泡原液成分と、を合流させて混合させる流体混合手段が前記熱交換器の上流側に設けられている請求項1記載のポリウレタン発泡原液成分供給装置。 A fluid mixing means is provided on the upstream side of the heat exchanger for mixing and mixing the polyurethane foam stock solution component fed from the mixing head to the heat exchanger and the polyurethane foam stock solution component fed for replenishment. The polyurethane foam undiluted solution component supply apparatus according to claim 1. ポリウレタン発泡原液成分を熱交換器により所定温度範囲にし、所定温度範囲にされたポリウレタン発泡原液成分を、温度調節機能を備える原液タンクに送給して貯留し、この原液タンクからミキシングヘッドへ前記ポリウレタン発泡原液成分を送給する共に、前記ミキシングヘッドから前記原液タンクへ送給して循環させるようにしているポリウレタン発泡原液成分供給方法において、前記ポリウレタン発泡原液成分を前記ミキシングヘッドから前記原液タンクへ送給する途中で、前記熱交換器に送給することを特徴とするポリウレタン発泡原液成分供給方法。 The polyurethane foam stock solution component is brought to a predetermined temperature range by a heat exchanger, and the polyurethane foam stock solution component that has been brought to the predetermined temperature range is supplied to and stored in a stock solution tank having a temperature control function, and the polyurethane is transferred from the stock solution tank to the mixing head In the polyurethane foam stock solution component supplying method, wherein the foaming stock solution component is fed from the mixing head to the stock solution tank and circulated, the polyurethane foam stock solution component is sent from the mixing head to the stock solution tank. A method of supplying a polyurethane foam concentrate solution component, wherein the component is fed to the heat exchanger during feeding. 前記ミキシングヘッドから前記熱交換器にポリウレタン発泡原液成分を循環・送給すると共に、この循環・送給されたポリウレタン発泡原液成分と、前記熱交換器に補充用に送給されるポリウレタン発泡原液成分とを合流させ、前記熱交換器の上流側で流体混合手段を用いて混合する請求項3記載のポリウレタン発泡原液成分供給方法。 The polyurethane foam concentrate solution component is circulated and fed from the mixing head to the heat exchanger, and the polyurethane foam concentrate solution component circulated and fed, and the polyurethane foam concentrate component fed to the heat exchanger for replenishment The method of supplying a polyurethane foam stock solution component according to claim 3, wherein the components are mixed together and mixed using a fluid mixing means upstream of the heat exchanger.
JP2005108265A 2005-04-05 2005-04-05 Supplying device and method for polyurethane foaming stock liquid component Withdrawn JP2006281720A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009113453A (en) * 2007-11-09 2009-05-28 Toyo Tire & Rubber Co Ltd Polyurethane foaming crude liquid component supplying device
CN115723287A (en) * 2022-12-16 2023-03-03 河北科技大学 Production equipment for controlling polyurethane foaming based on temperature

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009113453A (en) * 2007-11-09 2009-05-28 Toyo Tire & Rubber Co Ltd Polyurethane foaming crude liquid component supplying device
CN115723287A (en) * 2022-12-16 2023-03-03 河北科技大学 Production equipment for controlling polyurethane foaming based on temperature

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