JP2000218647A - Device for supplying forming agent to resin foam molding machine and manufacture of resin foam - Google Patents
Device for supplying forming agent to resin foam molding machine and manufacture of resin foamInfo
- Publication number
- JP2000218647A JP2000218647A JP11026095A JP2609599A JP2000218647A JP 2000218647 A JP2000218647 A JP 2000218647A JP 11026095 A JP11026095 A JP 11026095A JP 2609599 A JP2609599 A JP 2609599A JP 2000218647 A JP2000218647 A JP 2000218647A
- Authority
- JP
- Japan
- Prior art keywords
- foaming agent
- resin foam
- molding machine
- supply pipe
- foam molding
- 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.)
- Granted
Links
- 239000011347 resin Substances 0.000 title claims abstract description 65
- 229920005989 resin Polymers 0.000 title claims abstract description 65
- 238000010097 foam moulding Methods 0.000 title claims abstract description 55
- 239000006260 foam Substances 0.000 title claims description 5
- 238000004519 manufacturing process Methods 0.000 title claims description 3
- 239000004088 foaming agent Substances 0.000 claims abstract description 119
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000007789 gas Substances 0.000 claims abstract description 30
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 18
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 18
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910001873 dinitrogen Inorganic materials 0.000 claims abstract description 15
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 9
- 239000004604 Blowing Agent Substances 0.000 claims description 23
- 238000001816 cooling Methods 0.000 claims description 10
- 238000005187 foaming Methods 0.000 claims description 8
- 238000010438 heat treatment Methods 0.000 claims description 3
- 238000000465 moulding Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 abstract description 7
- 239000000470 constituent Substances 0.000 abstract 1
- 230000001627 detrimental effect Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 10
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 5
- 238000010792 warming Methods 0.000 description 5
- 239000011810 insulating material Substances 0.000 description 4
- 239000012071 phase Substances 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- 230000008016 vaporization Effects 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000004880 explosion Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- JOYRKODLDBILNP-UHFFFAOYSA-N Ethyl urethane Chemical compound CCOC(N)=O JOYRKODLDBILNP-UHFFFAOYSA-N 0.000 description 1
- 239000011324 bead Substances 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 239000006261 foam material Substances 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
Landscapes
- Molding Of Porous Articles (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は樹脂発泡成形機への
液化炭酸ガスや液化窒素ガス等の発泡剤の供給装置およ
び樹脂発泡体の製造方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for supplying a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas to a resin foam molding machine and a method for producing a resin foam.
【0002】[0002]
【従来の技術】従来、樹脂発泡成形機で使用されている
発泡剤は、樹脂発泡成形機への定量安定供給性にすぐ
れ、樹脂への溶解度も高い炭化水素系ガス(ブタンガ
ス、ペンタンガス、イソブタンガス、ヘプタン、エタ
ン、プロパン、ペンタン等)や代替えフロンガスを用い
ている。2. Description of the Related Art Conventionally, a foaming agent used in a resin foam molding machine is excellent in quantitative and stable supply to a resin foam molding machine and has a high solubility in a resin, such as a hydrocarbon-based gas (butane gas, pentane gas, isobutane gas). Gas, heptane, ethane, propane, pentane, etc.) and alternative Freon gas.
【0003】[0003]
【発明が解決しようとする課題】従来の炭化水素系ガス
や代替フロンガスを発泡剤として用いた場合、ガス爆発
の危険性が大であるという欠点を有しており、かつオゾ
ン層の破壊の問題や地球温暖化等の問題が発生し、使用
し続けることが社会的に問題になっている。このため、
不燃性でオゾン層への影響がなく地球温暖化への影響も
少ない炭酸ガスや窒素ガスを発泡剤として使用すること
が考えられているが、炭酸ガスや窒素ガスは各種発泡成
形性に乏しく、さらに安定状態で供給することすらでき
ないという欠点があった。When a conventional hydrocarbon gas or alternative chlorofluorocarbon gas is used as a foaming agent, there is a disadvantage that the risk of gas explosion is great, and there is a problem of destruction of the ozone layer. And problems such as global warming have occurred, and it has become a social problem to continue using it. For this reason,
It is considered that carbon dioxide or nitrogen gas is used as a blowing agent because it is nonflammable and has no effect on the ozone layer and has little effect on global warming. Further, there is a drawback that it cannot be supplied even in a stable state.
【0004】本発明は以上のような従来の欠点に鑑み、
液化炭酸ガスや液化窒素ガスの不燃性でオゾン層を破壊
することもない地球温暖化への影響も少ない発泡剤を、
定量・安定状態で樹脂発泡成形機へ供給することができ
る樹脂発泡成形機への発泡剤の供給装置を提供すること
を目的としている。The present invention has been made in view of the above-mentioned conventional drawbacks,
A blowing agent that is non-flammable of liquefied carbon dioxide and liquefied nitrogen gas and does not destroy the ozone layer and has little impact on global warming,
It is an object of the present invention to provide an apparatus for supplying a foaming agent to a resin foam molding machine that can supply the foaming agent to the resin foam molding machine in a fixed and stable state.
【0005】本発明の前記ならびにそのほかの目的と新
規な特徴は次の説明を添付図面と照らし合わせて読む
と、より完全に明らかになるであろう。ただし、図面は
もっぱら解説のためのものであって、本発明の技術的範
囲を限定するものではない。The above and other objects and novel features of the present invention will become more completely apparent when the following description is read in conjunction with the accompanying drawings. However, the drawings are for explanation only, and do not limit the technical scope of the present invention.
【0006】[0006]
【課題を解決するための手段】上記目的を達成するため
に、本発明は液化炭酸ガスや液化窒素ガス等の発泡剤が
充填された発泡剤充填タンクと、この発泡剤充填タンク
の発泡剤を樹脂発泡成形機へ供給する発泡剤供給パイプ
と、この発泡剤供給パイプの前記樹脂発泡成形機寄りの
部位に介装されたポンプとからなる樹脂発泡成形機への
発泡剤の供給装置において、前記ポンプの上流部の前記
発泡剤供給パイプを通過する発泡剤を冷却する冷却器と
で樹脂発泡成形機への発泡剤の供給装置を構成してい
る。In order to achieve the above object, the present invention relates to a foaming agent filled tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, and a foaming agent in the foaming agent filled tank. In a foaming agent supply pipe for supplying to a resin foam molding machine, and a foaming agent supply device for a resin foam molding machine comprising a pump interposed at a portion of the foaming agent supply pipe near the resin foam molding machine, A cooling agent for cooling the foaming agent passing through the foaming agent supply pipe upstream of the pump constitutes a device for supplying the foaming agent to the resin foam molding machine.
【0007】[0007]
【発明の実施の形態】以下、図面に示す実施の形態によ
り、本発明を詳細に説明する。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail with reference to the embodiments shown in the drawings.
【0008】図1および図2に示す本発明の第1の実施
の形態において、1は液化炭酸ガスの発泡剤2が充填さ
れた発泡剤充填タンクで、この発泡剤充填タンク1は上
部には流量調節弁3が介装された発泡剤2を充填するた
めの充填用パイプ4が取付けられている。In the first embodiment of the present invention shown in FIGS. 1 and 2, reference numeral 1 denotes a foaming agent filling tank filled with a foaming agent 2 of liquefied carbon dioxide gas. A filling pipe 4 for filling the foaming agent 2 with a flow control valve 3 interposed is attached.
【0009】5は前記発泡剤充填タンク1内の発泡剤2
を該発泡剤充填タンク1の下部より樹脂発泡成形機6へ
供給する発泡剤供給パイプで、この発泡剤供給パイプ5
で発泡剤2が供給される樹脂発泡成形機6は一般に使用
されている成型機、押出ガス発泡における押出機、ビー
ズ発泡の圧力容器、ウレタン発泡における混合器等であ
る。5 is a foaming agent 2 in the foaming agent filling tank 1
Is supplied from the lower part of the foaming agent filling tank 1 to the resin foam molding machine 6 by using a foaming agent supply pipe 5.
The resin foam molding machine 6 to which the foaming agent 2 is supplied is a generally used molding machine, an extruder for extruded gas foaming, a pressure vessel for bead foaming, a mixer for urethane foaming, and the like.
【0010】7は前記発泡剤供給パイプ5の前記樹脂発
泡成形機6寄りの部位に介装された該樹脂発泡成形機6
へ所定の圧力で発泡剤2を供給するためのポンプであ
る。Reference numeral 7 denotes a resin foam molding machine 6 interposed at a portion of the foaming agent supply pipe 5 near the resin foam molding machine 6.
Is a pump for supplying the foaming agent 2 at a predetermined pressure.
【0011】8は前記ポンプ7の上流部の前記発泡剤供
給パイプ5を通過する発泡剤2を定量安定供給するため
に冷却する冷却器で、この冷却器8は冷凍機9からの冷
媒を循環させて冷却するものが使用されている。A cooler 8 cools the blowing agent 2 passing through the blowing agent supply pipe 5 upstream of the pump 7 so as to supply the blowing agent 2 quantitatively and stably. The cooler 8 circulates a refrigerant from a refrigerator 9. What is cooled by being used is used.
【0012】上記構成の樹脂発泡成形機への発泡剤の供
給装置10は発泡剤供給パイプ5を通過する発泡剤2を
ポンプ7の上流部の冷却器8で冷却して気化するのを防
止してポンプ7で樹脂発泡成形機6へ供給される。この
ため、ポンプ7から樹脂発泡成形機6までの発泡剤供給
パイプ5およびポンプ7での発泡剤2の気化が効率よく
阻止され、樹脂発泡成形機6に発泡剤2を定量安定状態
で供給することができる。なお、前記発泡剤供給パイプ
5、前記ポンプ7および前記冷却器8は断熱材で覆い断
熱処理するとより効率的である。The apparatus 10 for supplying a blowing agent to the resin foam molding machine having the above-described structure is configured to cool the blowing agent 2 passing through the blowing agent supply pipe 5 by the cooler 8 upstream of the pump 7 so as to prevent vaporization. And supplied to the resin foam molding machine 6 by the pump 7. For this reason, the foaming agent supply pipe 5 from the pump 7 to the resin foam molding machine 6 and the vaporization of the foaming agent 2 in the pump 7 are efficiently prevented, and the foaming agent 2 is supplied to the resin foam molding machine 6 in a quantitatively stable state. be able to. It is more efficient to cover the foaming agent supply pipe 5, the pump 7, and the cooler 8 with a heat insulating material and perform heat insulation treatment.
【0013】[0013]
【発明の異なる実施の形態】次に、図3ないし図16に
示す本発明の異なる実施の形態につき説明する。なお、
これらの本発明の異なる実施の形態の説明に当って、前
記本発明の第1の実施の形態と同一構成部分には同一符
号を付して重複する説明を省略する。Next, different embodiments of the present invention shown in FIGS. 3 to 16 will be described. In addition,
In the description of the different embodiments of the present invention, the same components as those of the first embodiment of the present invention are denoted by the same reference numerals, and duplicate description will be omitted.
【0014】図3および図4に示す本発明の第2の実施
の形態において、前記本発明の第1の実施の形態と主に
異なる点は、ポンプヘッド7aも冷却することができる
冷却器8Aを用いるとともに、発泡剤が常温以下の低温
の場合、発泡剤供給パイプ5を断熱材11で覆って断熱
処理した点で、このように構成した樹脂発泡成形機への
発泡剤の供給装置10Aにしても、前記本発明の第1の
実施の形態と同様な作用効果が得られるとともに、より
発泡材を定量安定供給することができる。The second embodiment of the present invention shown in FIGS. 3 and 4 mainly differs from the first embodiment of the present invention in that a cooler 8A which can also cool the pump head 7a is provided. When the blowing agent is at a low temperature below room temperature, the blowing agent supply pipe 5 is covered with a heat insulating material 11 and heat-insulated, so that the foaming agent supply device 10A to the resin foam molding machine thus configured is used. Even with this, the same operation and effect as those of the first embodiment of the present invention can be obtained, and the foam material can be more stably supplied in a quantitative manner.
【0015】図5および図6に示す本発明の第3の実施
の形態において、前記本発明の第1の実施の形態と主に
異なる点は、ポンプ7の下流の発泡剤供給パイプ5と発
泡剤充填タンク1とを連通する調節弁12または調整
弁、バイパス弁を介装した戻し通路13を設けるととも
に、該戻し通路13に冷却器14を設けて発泡剤充填タ
ンク1への熱負荷を防止できるようにした点で、このよ
うに構成した樹脂発泡成形機への発泡剤の供給装置10
Bにすることにより断続運転、待機運転、圧力確保の運
転形態に対応することができ、結果として発泡剤を安定
して供給することができる。なお、本発明の実施の形態
においても、発泡剤供給パイプ5、ポンプ7、冷却器
8、冷凍機9、調節弁12、戻し通路13および冷却器
14は断熱材で覆い断熱処理するとより効率的である。The third embodiment of the present invention shown in FIGS. 5 and 6 is mainly different from the first embodiment of the present invention in that the blowing agent supply pipe 5 downstream of the pump 7 A return valve 13 having a control valve 12 or a control valve and a bypass valve communicating with the agent filling tank 1 is provided, and a cooler 14 is provided in the return passage 13 to prevent a heat load on the foaming agent filling tank 1. In view of the point that the apparatus can be supplied, the apparatus 10 for supplying the foaming agent to the resin foam molding machine thus configured
By setting B, it is possible to cope with an operation mode of an intermittent operation, a standby operation, and a pressure securing, and as a result, a blowing agent can be stably supplied. Also in the embodiment of the present invention, it is more efficient to cover the foaming agent supply pipe 5, the pump 7, the cooler 8, the refrigerator 9, the control valve 12, the return passage 13, and the cooler 14 with a heat insulating material and perform a heat insulating treatment. It is.
【0016】図7および図8に示す本発明の第4の実施
の形態において、前記本発明の第3の実施の形態と主に
異なる点は、戻し通路13Aを発泡剤充填タンク1と冷
却器8との間の発泡剤供給パイプ5に連通させた点で、
このように構成した樹脂発泡成形機への発泡材の供給装
置10Cにしても、前記本発明の第3の実施の形態と同
様な作用効果が得られる。The fourth embodiment of the present invention shown in FIGS. 7 and 8 is mainly different from the third embodiment of the present invention in that the return passage 13A is provided with the blowing agent filled tank 1 and the cooler. 8 and the foaming agent supply pipe 5 between
The same operation and effect as those of the third embodiment of the present invention can be obtained also in the foaming material supply apparatus 10C to the resin foam molding machine configured as described above.
【0017】図9および図10に示す本発明の第5の実
施の形態において、前記本発明の第2の実施の形態と主
に異なる点は、ポンプ7の下流の発泡剤供給パイプ5の
樹脂発泡成形機6寄りの部位に液相あるいはガス相また
は超臨界相のいずれかの単一相となるように冷却または
加熱する熱交換器15を設けた点で、このように構成し
た樹脂発泡成形機への発泡剤の供給装置10Dにするこ
とにより、より確実に発泡剤2を樹脂発泡成形機6へ定
量安定供給することができる。The fifth embodiment of the present invention shown in FIGS. 9 and 10 is different from the second embodiment of the present invention mainly in that a resin for a foaming agent supply pipe 5 downstream of a pump 7 is provided. Resin foam molding configured in this manner is provided with a heat exchanger 15 for cooling or heating to a single phase of a liquid phase, a gas phase, or a supercritical phase at a portion near the foam molding machine 6. By using the blowing agent supply device 10D to the machine, the blowing agent 2 can be more reliably and stably supplied to the resin foam molding machine 6.
【0018】図11および図12に示す本発明の第6の
実施の形態において、前記本発明の第2の実施の形態と
主に異なる点は、冷却器8の上流部の発泡剤供給パイプ
5に流量計16、この流量計16の上流部に冷凍機18
を用いた冷却器17を設けた点で、このように流量計1
6の上流部に冷凍機18を設けて発泡剤を冷却する樹脂
発泡成形機への発泡剤の供給装置10Eにすることによ
り、より流量計16の精度を向上させることができ、よ
り発泡剤の定量供給性を可能とすることができる。な
お、冷却器8、17の冷凍機9、18を別々に設けたも
のについて図示したが、本発明はこれに限らず1個の冷
凍機9で冷却器8、17を冷却してもよい。The sixth embodiment of the present invention shown in FIGS. 11 and 12 is mainly different from the second embodiment of the present invention in that a blowing agent supply pipe 5 upstream of a cooler 8 is provided. Flow meter 16, and a refrigerator 18 upstream of the flow meter 16.
Thus, the flowmeter 1 is provided in that a cooler 17 using
By providing a refrigerator 18 at the upstream of the foaming agent supply device 10E to the resin foam molding machine that cools the foaming agent by providing the refrigerator 18, the accuracy of the flow meter 16 can be further improved, and the Quantitative supply can be made possible. Although the refrigerators 9 and 18 of the coolers 8 and 17 are shown separately, the present invention is not limited to this, and the refrigerators 8 and 17 may be cooled by one refrigerator 9.
【0019】図13および図14に示す本発明の第7の
実施の形態において、前記本発明の第1の実施の形態と
主に異なる点は、発泡剤供給パイプ5Aで発泡剤充填タ
ンク19の気化発泡剤2Aを樹脂発泡成形機6へ供給で
きるようにするとともに、発泡剤供給パイプ5Aに少な
くとも1個以上、本発明の実施の形態では2個の減圧弁
20、21と、この2個の減圧弁20、21の下流部位
に該減圧弁20、21の減圧率により気化発泡剤2Aを
加熱するヒーター22、23を設けた点で、このように
構成した樹脂発泡成形機への発泡剤の供給装置10Fに
することにより、減圧率による温度低下を防止して、安
定供給し、さらに気化発泡剤2Aの温度制御をすること
により、例えば、ビーズ発泡成形において、本発泡剤の
供給装置10Fを用いた場合、より均一で安定した製品
を得ることができる。The seventh embodiment of the present invention shown in FIGS. 13 and 14 is mainly different from the first embodiment of the present invention in that a foaming agent supply pipe 5A and a foaming agent filling tank 19 are used. In addition to allowing the vaporized foaming agent 2A to be supplied to the resin foam molding machine 6, at least one or more pressure reducing valves 20, 21 in the embodiment of the present invention, and the two pressure reducing valves 20, 21 in the foaming agent supply pipe 5A, In the point that heaters 22 and 23 for heating the vaporized foaming agent 2A by the pressure reduction rate of the pressure reducing valves 20 and 21 are provided downstream of the pressure reducing valves 20 and 21, the blowing agent is supplied to the resin foam molding machine configured as described above. By providing the supply device 10F, it is possible to prevent the temperature from being reduced by the decompression rate, to stably supply the temperature, and to further control the temperature of the vaporized foaming agent 2A. If you were, it is possible to obtain a more uniform and stable product.
【0020】図15および図16に示す本発明の第8の
実施の形態において、前記本発明の第7の実施の形態と
主に異なる点は、発泡剤供給パイプ5Aに減圧弁20、
ヒーター22、流量調節弁24および発泡剤供給パイプ
5Aに周囲温度による影響を阻止するためのヒーター2
5とを設けた点で、このように構成した樹脂発泡成形機
への発泡剤の供給装置10Gにしても、前記本発明の第
7の実施の形態と同様な作用効果が得られるとともに、
流量精度の向上を図ることができる。The eighth embodiment of the present invention shown in FIGS. 15 and 16 is mainly different from the seventh embodiment of the present invention in that a pressure reducing valve 20 is connected to a blowing agent supply pipe 5A.
Heater 2 for preventing the influence of ambient temperature on heater 22, flow control valve 24 and blowing agent supply pipe 5A
In the point that 5 is provided, the foaming agent supply device 10G to the resin foam molding machine configured as described above can provide the same operation and effect as the seventh embodiment of the present invention, and
The flow rate accuracy can be improved.
【0021】なお、前記本発明の各実施の形態では発泡
剤として液化炭酸ガス、気化炭酸ガスを用いるものにつ
いて説明したが、本発明はこれに限らず、液化窒素ガス
等の不燃性でオゾン層を破壊することがなく、地球温暖
化への影響の少ないガスを用いてもよい。また、前記本
発明の各実施の形態で用いた発泡剤充填タンク1にボン
ベを用いても同様な作用効果が得られる。In each of the above embodiments of the present invention, the case where liquefied carbon dioxide gas or vaporized carbon dioxide gas is used as the foaming agent has been described. However, the present invention is not limited to this. It is possible to use a gas that does not destroy the gas and has little effect on global warming. Further, similar effects can be obtained by using a cylinder for the foaming agent filling tank 1 used in each of the embodiments of the present invention.
【0022】[0022]
【発明の効果】以上の説明から明らかなように、本発明
にあっては次に列挙する効果が得られる。As is clear from the above description, the following effects can be obtained in the present invention.
【0023】(1)液化炭酸ガスや液化窒素ガス等の発
泡剤が充填された発泡剤充填タンクと、この発泡剤充填
タンクの発泡剤を樹脂発泡成形機へ供給する発泡剤供給
パイプと、この発泡剤供給パイプの前記樹脂発泡成形機
寄りの部位に介装されたポンプとからなる樹脂発泡成形
機への発泡剤の供給装置において、前記ポンプの上流部
の前記発泡剤供給パイプを通過する発泡剤を冷却する冷
却器を設けたので、液化炭酸ガスや液化窒素ガス等の不
燃性でオゾン層を破壊することがない発泡剤の安定供給
を阻害する気化を効率よく阻止して、樹脂発泡成形機へ
安定供給することができる。したがって、樹脂発泡成形
機へ液化炭酸ガスや液化窒素ガス等の発泡剤を定量安定
供給することができることにより、結果として安定した
均一な発泡体を得ることができる。(1) A foaming agent filling tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, a foaming agent supply pipe for supplying the foaming agent in the foaming agent filling tank to a resin foam molding machine, In a device for supplying a foaming agent to a resin foam molding machine comprising a pump interposed at a portion of the foaming agent supply pipe close to the resin foam molding machine, foaming passing through the foaming agent supply pipe upstream of the pump is provided. A resin cooler is provided to cool the agent, which effectively prevents vaporization that hinders the stable supply of a blowing agent that does not destroy the ozone layer due to incombustibility such as liquefied carbon dioxide gas or liquefied nitrogen gas. The machine can be supplied stably. Therefore, since a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas can be quantitatively and stably supplied to the resin foam molding machine, a stable and uniform foam can be obtained as a result.
【0024】(2)前記(1)によって、発泡剤として
液化炭酸ガスや液化窒素ガス等の不燃性でオゾン層を破
壊しないものを使用しているので、爆発事故等の心配が
なく、気軽に安全に作業を行なうことができる。(2) According to (1), since a non-flammable foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas which does not destroy the ozone layer is used, there is no fear of an explosion accident, etc. You can work safely.
【0025】(3)前記(1)によって、不燃性でオゾ
ン層を破壊することがなく、地球温暖化への環境に与え
る影響の少ないガスを用いて樹脂発泡成形を行なうこと
ができる。(3) According to the above (1), resin foam molding can be performed using a gas that is nonflammable and does not destroy the ozone layer and has little effect on the environment against global warming.
【0026】(4)請求項2〜6も前記(1)〜(3)
と同様な効果が得られる。(4) Claims 2 to 6 also apply to (1) to (3).
The same effect can be obtained.
【図1】本発明の第1の実施の形態の概略側面図。FIG. 1 is a schematic side view of a first embodiment of the present invention.
【図2】本発明の第1の実施の形態の概略平面図。FIG. 2 is a schematic plan view of the first embodiment of the present invention.
【図3】本発明の第2の実施の形態の概略側面図。FIG. 3 is a schematic side view of a second embodiment of the present invention.
【図4】本発明の第2の実施の形態の概略平面図。FIG. 4 is a schematic plan view of a second embodiment of the present invention.
【図5】本発明の第3の実施の形態の概略側面図。FIG. 5 is a schematic side view of a third embodiment of the present invention.
【図6】本発明の第3の実施の形態の概略平面図。FIG. 6 is a schematic plan view of a third embodiment of the present invention.
【図7】本発明の第4の実施の形態の概略側面図。FIG. 7 is a schematic side view of a fourth embodiment of the present invention.
【図8】本発明の第4の実施の形態の概略平面図。FIG. 8 is a schematic plan view of a fourth embodiment of the present invention.
【図9】本発明の第5の実施の形態の概略側面図。FIG. 9 is a schematic side view of a fifth embodiment of the present invention.
【図10】本発明の第5の実施の形態の概略平面図。FIG. 10 is a schematic plan view of a fifth embodiment of the present invention.
【図11】本発明の第6の実施の形態の概略側面図。FIG. 11 is a schematic side view of a sixth embodiment of the present invention.
【図12】本発明の第6の実施の形態の概略平面図。FIG. 12 is a schematic plan view of a sixth embodiment of the present invention.
【図13】本発明の第7の実施の形態の概略側面図。FIG. 13 is a schematic side view of a seventh embodiment of the present invention.
【図14】本発明の第7の実施の形態の概略平面図。FIG. 14 is a schematic plan view of a seventh embodiment of the present invention.
【図15】本発明の第8の実施の形態の概略側面図。FIG. 15 is a schematic side view of an eighth embodiment of the present invention.
【図16】本発明の第8の実施の形態の概略平面図。FIG. 16 is a schematic plan view of an eighth embodiment of the present invention.
1:発泡剤充填タンク、 2:発泡剤、3:流量調節
弁、 4:充填用パイプ、5、5A:発泡剤供給
パイプ、6:樹脂発泡成形機、 7:ポンプ、8、8
A:冷却器、 9:冷凍機、10、10A〜10
G:樹脂発泡成形機への発泡剤の供給装置、11:断熱
材、 12:調節弁、13、13A:戻し通
路、14:冷却器、15:熱交換器、 16:流
量計、17:冷却器、 18:冷凍機、19:
発泡剤充填タンク、20:減圧弁、21:減圧弁、
22:ヒーター、23:ヒーター、 2
4:流量調整弁、25:ヒーター。1: foaming agent filling tank, 2: foaming agent, 3: flow rate control valve, 4: filling pipe, 5, 5A: foaming agent supply pipe, 6: resin foam molding machine, 7: pump, 8, 8
A: cooler, 9: refrigerator, 10, 10A-10
G: apparatus for supplying a foaming agent to a resin foam molding machine, 11: heat insulating material, 12: control valve, 13, 13A: return passage, 14: cooler, 15: heat exchanger, 16: flow meter, 17: cooling Vessel, 18: refrigerator, 19:
Foaming agent filling tank, 20: pressure reducing valve, 21: pressure reducing valve,
22: heater, 23: heater, 2
4: Flow control valve, 25: heater.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 藤平 隆太郎 神奈川県川崎市川崎区千鳥町3番2号昭和 電工株式会社総合研究所川崎研究所内 (72)発明者 須藤 清 東京都千代田区三崎町3丁目3番23号昭和 炭酸株式会社内 (72)発明者 澤田 昇 東京都千代田区三崎町3丁目3番23号昭和 炭酸株式会社内 Fターム(参考) 4F212 AG20 AK13 UA13 UF06 UF23 UL07 UN15 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Ryutaro Fujihira 3-2 Chidori-cho, Kawasaki-ku, Kawasaki-shi, Kanagawa Prefecture Showa Denko KK Kawasaki Research Institute (72) Inventor Kiyoshi Sudo 3 Misaki-cho, Chiyoda-ku, Tokyo No. 3-23 Showa Carbonate Co., Ltd. (72) Inventor Noboru Sawada 3-3-23 Misakicho, Chiyoda-ku, Tokyo F-term in Showa Carbonate Co., Ltd. 4F212 AG20 AK13 UA13 UF06 UF23 UF23 UL07 UN15
Claims (6)
が充填された発泡剤充填タンクと、この発泡剤充填タン
クの発泡剤を樹脂発泡成形機へ供給する発泡剤供給パイ
プと、この発泡剤供給パイプの前記樹脂発泡成形機寄り
の部位に介装されたポンプとからなる樹脂発泡成形機へ
の発泡剤の供給装置において、前記ポンプの上流部の前
記発泡剤供給パイプを通過する発泡剤を冷却する冷却器
を設けたことを特徴とする樹脂発泡剤成形機への発泡剤
の供給装置。1. A foaming agent filling tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, a foaming agent supply pipe for supplying the foaming agent in the foaming agent filling tank to a resin foam molding machine, And a pump interposed at a portion of the agent supply pipe close to the resin foam molding machine, wherein the foaming agent passes through the foaming agent supply pipe upstream of the pump. A supply device for a foaming agent to a resin foaming agent molding machine, comprising a cooler for cooling the foaming agent.
が充填された発泡剤充填タンクと、この発泡剤充填タン
クの発泡剤を樹脂発泡成形機へ供給する発泡剤供給パイ
プと、この発泡剤供給パイプの前記樹脂発泡成形機寄り
の部位に介装されたポンプとからなる樹脂発泡成形機へ
の発泡剤の供給装置において、前記ポンプの上流部の前
記発泡剤供給パイプを通過する発泡剤の冷却および前記
ポンプヘッドを冷却する冷却器を設けたことを特徴とす
る樹脂発泡剤成形機への発泡材の供給装置。2. A foaming agent filling tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, a foaming agent supply pipe for supplying the foaming agent in the foaming agent filling tank to a resin foam molding machine, And a pump interposed at a portion of the agent supply pipe close to the resin foam molding machine, wherein the foaming agent passes through the foaming agent supply pipe upstream of the pump. A device for supplying a foaming material to a resin foaming agent molding machine, comprising a cooler for cooling the pump and cooling the pump head.
が充填された発泡剤充填タンクと、この発泡剤充填タン
クの発泡剤を樹脂発泡成形機へ供給する発泡剤供給パイ
プと、この発泡剤供給パイプの前記樹脂発泡成形機寄り
の部位に介装されたポンプとからなる樹脂発泡成形機へ
の発泡剤の供給装置において、前記ポンプの上流部の前
記発泡剤供給パイプを通過する発泡剤を冷却する冷却器
を設けるとともに、前記ポンプの下流部の前記発泡剤供
給パイプと前記発泡剤充填タンクあるいは前記冷却器の
上流部の発泡剤供給パイプとを連通させる調節弁が備え
られた戻し通路とを設けたことを特徴とする樹脂発泡成
形機への発泡剤の供給装置。3. A foaming agent filling tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, a foaming agent supply pipe for supplying the foaming agent in the foaming agent filling tank to a resin foam molding machine. And a pump interposed at a portion of the agent supply pipe close to the resin foam molding machine, wherein the foaming agent passes through the foaming agent supply pipe upstream of the pump. And a return passage provided with a control valve for communicating the blowing agent supply pipe downstream of the pump with the blowing agent filling tank or the blowing agent supply pipe upstream of the cooler. And a foaming agent supply device for a resin foam molding machine.
が充填された発泡剤充填タンクと、この発泡剤充填タン
クの発泡剤を樹脂発泡成形機へ供給する発泡剤供給パイ
プと、この発泡剤供給パイプの前記樹脂発泡成形機寄り
の部位に介装されたポンプとからなる樹脂発泡成形機へ
の発泡剤の供給装置において、前記ポンプの上流部の発
泡剤供給パイプを通過する発泡剤を冷却する冷却器を設
けるとともに、前記ポンプの下流部の前記発泡剤供給パ
イプの前記樹脂発泡成形機寄りの部位に該樹脂発泡成形
機へ発泡剤を単一相で供給できるように冷却あるいは加
熱する熱交換器を設けたことを特徴とする樹脂発泡成形
機への発泡剤の供給装置。4. A foaming agent filling tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, a foaming agent supply pipe for supplying the foaming agent in the foaming agent filling tank to a resin foam molding machine, In a supply device for a foaming agent to a resin foam molding machine comprising a pump interposed at a portion of the agent supply pipe near the resin foam molding machine, a foaming agent passing through a foaming agent supply pipe upstream of the pump is supplied. A cooling device for cooling is provided, and cooling or heating is performed at a portion of the foaming agent supply pipe downstream of the pump near the resin foaming machine so that the foaming agent can be supplied to the resin foaming machine in a single phase. An apparatus for supplying a foaming agent to a resin foam molding machine, comprising a heat exchanger.
が充填された発泡剤充填タンクと、この発泡剤充填タン
クの発泡剤を樹脂発泡成形機へ供給する発泡剤供給パイ
プと、この発泡剤供給パイプの前記樹脂発泡成形機寄り
の部位に介装されたポンプとからなる樹脂発泡成形機へ
の発泡剤の供給装置において、前記ポンプの上流部の前
記発泡剤供給パイプに流量計を設けるとともに、該流量
計の上流部の前記発泡剤供給パイプを通過する発泡剤を
冷却する上流部冷却器を設けたことを特徴とする樹脂発
泡成形機への発泡剤の供給装置。5. A foaming agent filling tank filled with a foaming agent such as liquefied carbon dioxide gas or liquefied nitrogen gas, a foaming agent supply pipe for supplying the foaming agent in the foaming agent filling tank to a resin foam molding machine; In a device for supplying a foaming agent to a resin foam molding machine comprising a pump interposed at a portion of the agent supply pipe near the resin foam molding machine, a flow meter is provided in the foaming agent supply pipe upstream of the pump. An apparatus for supplying a foaming agent to a resin foam molding machine, further comprising an upstream cooler for cooling the foaming agent passing through the foaming agent supply pipe upstream of the flow meter.
発泡剤の供給装置を用いて樹脂発泡体を製造することを
特徴とする樹脂発泡体の製造方法。6. A method for producing a resin foam, comprising using the apparatus for supplying a foaming agent to a resin foam molding machine according to claim 1 to produce a resin foam.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP02609599A JP4309502B2 (en) | 1999-02-03 | 1999-02-03 | Equipment for supplying foaming agent to resin foam molding machine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP02609599A JP4309502B2 (en) | 1999-02-03 | 1999-02-03 | Equipment for supplying foaming agent to resin foam molding machine |
Publications (2)
Publication Number | Publication Date |
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JP2000218647A true JP2000218647A (en) | 2000-08-08 |
JP4309502B2 JP4309502B2 (en) | 2009-08-05 |
Family
ID=12184049
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JP02609599A Expired - Lifetime JP4309502B2 (en) | 1999-02-03 | 1999-02-03 | Equipment for supplying foaming agent to resin foam molding machine |
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Cited By (6)
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JP2002013699A (en) * | 2000-06-29 | 2002-01-18 | Nippon Sanso Corp | Equipment and method for feeding liquefied gas |
JP2002168397A (en) * | 2000-11-30 | 2002-06-14 | Ishikawajima Plant Construction Co Ltd | Pressure delivery method and apparatus for low temperature liquid |
WO2010041427A1 (en) * | 2008-10-07 | 2010-04-15 | 株式会社プラステコ | Carbon dioxide supply system |
CN102133785A (en) * | 2010-12-07 | 2011-07-27 | 北京化工大学 | Carbon dioxide continuous and stable injection method and device |
CN102926989A (en) * | 2012-10-09 | 2013-02-13 | 中船澄西船舶修造有限公司 | Temperature control device of natural gas additive pump |
JP2021070202A (en) * | 2019-10-30 | 2021-05-06 | 旭有機材株式会社 | External foaming agent supply device |
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CN102060941B (en) | 2010-11-26 | 2012-12-26 | 漆又毛 | 6-deoxy alpha-amino acid derivative cyclodextrin, preparation and application thereof |
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1999
- 1999-02-03 JP JP02609599A patent/JP4309502B2/en not_active Expired - Lifetime
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002013699A (en) * | 2000-06-29 | 2002-01-18 | Nippon Sanso Corp | Equipment and method for feeding liquefied gas |
JP4493806B2 (en) * | 2000-06-29 | 2010-06-30 | 大陽日酸株式会社 | Liquid gas delivery equipment |
JP2002168397A (en) * | 2000-11-30 | 2002-06-14 | Ishikawajima Plant Construction Co Ltd | Pressure delivery method and apparatus for low temperature liquid |
WO2010041427A1 (en) * | 2008-10-07 | 2010-04-15 | 株式会社プラステコ | Carbon dioxide supply system |
CN102089565A (en) * | 2008-10-07 | 2011-06-08 | 株式会社普拉斯泰科 | Carbon dioxide supply system |
US8985139B2 (en) | 2008-10-07 | 2015-03-24 | Plasteco Corporation | Carbon dioxide supply system |
CN102133785A (en) * | 2010-12-07 | 2011-07-27 | 北京化工大学 | Carbon dioxide continuous and stable injection method and device |
CN102926989A (en) * | 2012-10-09 | 2013-02-13 | 中船澄西船舶修造有限公司 | Temperature control device of natural gas additive pump |
CN102926989B (en) * | 2012-10-09 | 2015-11-18 | 中船澄西船舶修造有限公司 | Natural gas additive pump temperature control apparatus |
JP2021070202A (en) * | 2019-10-30 | 2021-05-06 | 旭有機材株式会社 | External foaming agent supply device |
JP7433837B2 (en) | 2019-10-30 | 2024-02-20 | 旭有機材株式会社 | External blowing agent supply device |
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