JPH07102623B2 - Volatile scatter remover - Google Patents
Volatile scatter removerInfo
- Publication number
- JPH07102623B2 JPH07102623B2 JP8684788A JP8684788A JPH07102623B2 JP H07102623 B2 JPH07102623 B2 JP H07102623B2 JP 8684788 A JP8684788 A JP 8684788A JP 8684788 A JP8684788 A JP 8684788A JP H07102623 B2 JPH07102623 B2 JP H07102623B2
- Authority
- JP
- Japan
- Prior art keywords
- hot air
- volatile
- high temperature
- heat exchanger
- temperature field
- 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 - Fee Related
Links
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Shaping By String And By Release Of Stress In Plastics And The Like (AREA)
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明はポリプロピレン、ポリエステル、ナイロン等の
プラスチックフィルム製造設備、特にその延伸装置に適
用されるオリゴマー、オイルミスト等の揮発性飛散物の
除去装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a facility for producing plastic films such as polypropylene, polyester, nylon, etc., and in particular, a device for removing volatile scattered substances such as oligomers and oil mist, which is applied to a stretching device thereof. It is about.
(従来の技術) 従来延伸フィルムの製造にあたって最も一般的な方法と
しては、温度制御された熱風を循環してフィルムの予
熱、延伸、熱固定及び冷却をする方法が採用されてい
る。しかしこの方法においては、稼動中において前記熱
風中に昇華物、オイルミスト等が飛散してこれらが製造
中のフィルムに付着すると云う欠点をもっていた。な
お、前記飛散物の例としては、ポリエステル延伸時のオ
リゴマー、ポリプロピレン延伸時の添加剤蒸発成分等が
ある。(Prior Art) Conventionally, the most general method for producing a stretched film is to circulate hot air whose temperature is controlled to preheat, stretch, heat set and cool the film. However, this method has a drawback in that sublimates, oil mist and the like scatter in the hot air during operation and adhere to the film being manufactured. Examples of the scattered substances include oligomers during polyester stretching and additive evaporation components during polypropylene stretching.
ところでこれらの飛散物を除去するため、従来は、例え
ば特開昭58−65731号公報に示す如く、熱風を更に昇温
させることなく、通常の運転温度で酸化触媒層に通して
ポリエステルのオリゴマーを燃焼除去する方法が開示さ
れている。この方法は、酸化触媒層に白金等の貴金属を
担持させて、200〜250℃の比較的低温で燃焼させること
を特徴としている。By the way, in order to remove these scattered matters, conventionally, as shown in, for example, JP-A-58-65731, polyester oligomers are passed through the oxidation catalyst layer at a normal operating temperature without further heating the hot air. A method of burning off is disclosed. This method is characterized in that a noble metal such as platinum is supported on the oxidation catalyst layer and burned at a relatively low temperature of 200 to 250 ° C.
(発明が解決しようとする課題) しかしながら前記従来方法をポリプロピレンフィルムの
延伸に応用しようとしても、熱風温度が通常160℃と低
いため十分な燃焼効果が得られない。また添加剤から発
生したオイルミストの触媒毒により急速に性能が劣化し
実用的ではなかった。(Problems to be Solved by the Invention) However, even if the above-mentioned conventional method is applied to the stretching of a polypropylene film, a sufficient combustion effect cannot be obtained because the hot air temperature is usually as low as 160 ° C. In addition, the performance was rapidly deteriorated by the catalyst poison of oil mist generated from the additive, which was not practical.
これに対し、例えば特開昇60−97829号公報には活性
炭、アルミナ、白土等の吸着剤によるオリゴマー、オイ
ルミストの除去方法が開示されており、特に活性炭ペレ
ットが有効であるとしている。しかし、活性炭等の一般
の吸着剤は吸着できる物質が限られる、所謂選択性があ
り、且つ吸着温度が上昇すると共に吸着能力が低下する
特性をもつ。例えばポリエステルフィルムの延伸温度は
230〜250℃であり、この温度は通常活性炭から吸着物質
を脱着させる温度であり、この温度でオリゴマーの吸着
操作を行なうことは極めて効率が悪く、大量の活性炭を
必要とする。またオイルミスト類は一般に吸着しにく
く、早期に破過する傾向がある。On the other hand, for example, Japanese Unexamined Patent Publication No. 60-97829 discloses a method for removing oligomers and oil mist with an adsorbent such as activated carbon, alumina, and clay, and it is said that activated carbon pellets are particularly effective. However, general adsorbents such as activated carbon have so-called selectivity, which limits the substances that can be adsorbed, and have the characteristic that the adsorption capacity decreases as the adsorption temperature rises. For example, the stretching temperature of polyester film is
The temperature is 230 to 250 ° C., which is a temperature at which the adsorbed substance is usually desorbed from the activated carbon, and the adsorption operation of the oligomer at this temperature is extremely inefficient and requires a large amount of activated carbon. In addition, oil mists are generally difficult to adsorb and tend to break through early.
更に破過に達した吸着剤は、脱着操作によって吸着物質
を離脱させる必要があるが、このためには吸着温度より
150〜200℃高い温度で脱着しなければならないため、一
般的には吸着剤メーカに再生処理を委託する形となる。For the adsorbent that has reached the breakthrough, it is necessary to desorb the adsorbent by the desorption operation.
Since it has to be desorbed at a high temperature of 150 to 200 ° C, the adsorbent manufacturer generally entrusts the regeneration process.
本発明は、前記従来の酸化触媒における熱風温度範囲の
制限や触媒毒の問題、吸着剤における吸着物質の選択
性、高温雰囲気中での吸着能力の低下、短寿命等の前記
従来の課題を一挙に解決し、各種のフィルム延伸におい
て提案して熱風中の揮発性飛散物を除去できるプラスチ
ックフィルム延伸装置の揮発性飛散物除去装置を得るこ
とを目的とするものである。The present invention provides a summary of the conventional problems such as the limitation of the hot air temperature range and the catalyst poison in the conventional oxidation catalyst, the selectivity of the adsorbent in the adsorbent, the reduction of the adsorption capacity in a high temperature atmosphere, and the short life. It is an object of the present invention to solve the above problems and to provide a volatile scattering material removing device for a plastic film stretching device, which is proposed in various film stretching processes and is capable of removing volatile scattering materials in hot air.
(課題を解決するための手段) このため本発明は、フィルムを加熱する熱風の循環経
路、セラミック多孔体で仕切られた閉込高温場、熱交換
器、及び前記閉込高温場に前記循環経路より循環熱風の
一部を前記熱交換器を介して導入し、再び同熱交換器を
介して同熱風循環経路に戻すよう熱風を循環させる入口
及び出口ダクトとよりなるもので、これを課題解決のた
めの手段とするものである。(Means for Solving the Problems) Therefore, the present invention provides a circulation path for hot air for heating a film, a closed high temperature field partitioned by a ceramic porous body, a heat exchanger, and the closed high temperature field for the circulation path. A part of the circulating hot air is introduced through the heat exchanger, and the inlet and outlet ducts circulate the hot air so as to return to the hot air circulation path through the heat exchanger again. Is a means for.
(作用) 熱風循環経路内を循環するフィルムを加熱する熱風の一
部を、セラミック多孔体で仕切られた閉込高温場に熱交
換器を介して導入し、再び同熱交換器を介して熱風を循
環経路に戻すもので、熱風中の揮発飛散物又は成分を前
記閉込高温場で完全燃焼させて除去できる。(Function) A part of the hot air that heats the film circulating in the hot air circulation path is introduced into the enclosed high temperature field partitioned by the ceramic porous body through the heat exchanger, and the hot air is again passed through the heat exchanger. Is returned to the circulation path, and the volatile scattered substances or components in the hot air can be completely burned and removed in the enclosed high temperature field.
(実施例) 以下本発明の実施例を図面に基づいて詳述すると、第1
図は本発明の主要技術の一つである閉込高温場100の原
理図を示す。(Embodiment) The embodiment of the present invention will be described in detail below with reference to the drawings.
The figure shows a principle diagram of a confined high temperature field 100 which is one of the main techniques of the present invention.
閉込高温場100の基本構成は、第1図(ロ)に示すセラ
ミック多孔体101,101′及び容器104で囲まれた空間内の
電気ヒータ102からなっている。この閉込高温場100にオ
リゴマー等の揮発性飛散物を含む空気103を導くことに
より、前記飛散物を効率良く燃焼分解できる。また第1
図(イ)のグラフは、セラミック多孔体101,101′で囲
まれた閉込高温場100及びその前後の温度プロフィルを
示したもので、Bセラミック多孔体101′の有無によっ
え高温閉込効果が異なることを示している。The basic configuration of the confined high temperature field 100 is composed of the ceramic porous bodies 101 and 101 'shown in FIG. 1B and the electric heater 102 in the space surrounded by the container 104. By introducing the air 103 containing a volatile scattered substance such as an oligomer to the enclosed high temperature field 100, the scattered substance can be efficiently burned and decomposed. Also the first
The graph of Fig. (A) shows the confined high temperature field 100 surrounded by the ceramic porous bodies 101 and 101 'and the temperature profile before and after it. The high temperature confinement effect depends on the presence or absence of the B ceramic porous body 101'. It shows that they are different.
次に第1図に示した原理に基づき、セラミック多孔体に
よる閉込高温場100に熱交換器105を組合せ、延伸フィル
ム製造装置に接続した例を第2図に示す。第2図におい
て200は延伸フィルム製造装置の熱風循環装置部、150は
閉込高温場100と熱交換器105からなる揮発性飛散物除去
装置である。Next, based on the principle shown in FIG. 1, an example in which a heat exchanger 105 is combined with a confined high temperature field 100 made of a ceramic porous body and connected to a stretched film manufacturing apparatus is shown in FIG. In FIG. 2, reference numeral 200 is a hot air circulating device part of the stretched film manufacturing apparatus, and 150 is a volatile scattered matter removing device including a closed high temperature field 100 and a heat exchanger 105.
延伸フィルム製造装置の熱風循環装置(揮発性飛散成分
除去装置150の1部)部200は、熱風203を循環するため
のファン201、同ファン201を駆動するためのモータ20
2、熱風203の通路となるダクト204、熱風203を噴流化し
てフィルム206に吹きつけるためのノズル箱205、フィル
ム206を左右に引張りながら送行させるためのクリップ
走行機構207、熱風203を加熱するためのヒータ208等か
らなっている。The hot air circulating device (a part of the volatile scattered component removing device 150) unit 200 of the stretched film manufacturing apparatus includes a fan 201 for circulating the hot air 203 and a motor 20 for driving the fan 201.
2, a duct 204 which is a passage of the hot air 203, a nozzle box 205 for jetting the hot air 203 to blow it onto the film 206, a clip traveling mechanism 207 for pulling the film 206 left and right, and a hot air 203 for heating the hot air 203 It is composed of a heater 208 and the like.
一方揮発性飛散物除去装置150は、循環熱風203の一部10
3を受入れるための入口ダクト106、熱交換器105、セラ
ミック多孔体101,101′、電気ヒータ102、容器104から
なる閉込高温場100の出口ダクト107で構成されている。On the other hand, the volatile scattered material removal device 150 is a part of the circulating hot air 203.
It is composed of an inlet duct 106 for receiving 3 and a heat exchanger 105, ceramic porous bodies 101 and 101 ', an electric heater 102, and an outlet duct 107 of a closed high temperature field 100 including a container 104.
以上の如く構成された実施例について作用を説明する
と、フィルム206から揮発飛散したオリゴマー等の揮発
性飛散物は、熱風103と共に入口ダクト106を通った後、
熱交換器105を経由し、セラミック多孔体101、電気ヒー
タ102、セラミック多孔体101′を通過して完全燃焼され
る。そしてこの燃焼による燃焼ガスは、再び熱交換器10
5に入り、燃焼前のオリゴマー等の含有空気103を予熱す
ると同時に、燃焼ガス自体は冷却されて出口ダクト107
経由で、前記熱風循環装置部200内部のヒータ208付近に
排出される。なお、本実施例では、閉込高温場100の熱
源として電気ヒータ102を用いたが、プロパン等の燃料
ガスを導入する方式としても、全く同様の効果が得られ
る。Explaining the operation of the example configured as described above, volatile scattered substances such as oligomers volatilized and scattered from the film 206, after passing through the inlet duct 106 with the hot air 103,
Through the heat exchanger 105, the ceramic porous body 101, the electric heater 102, and the ceramic porous body 101 'are completely burned. Then, the combustion gas generated by this combustion is returned to the heat exchanger 10
5, the pre-combustion air 103 containing oligomers and the like is preheated, and at the same time, the combustion gas itself is cooled and the outlet duct 107
It is discharged to the vicinity of the heater 208 inside the hot air circulation device section 200 via the above. In the present embodiment, the electric heater 102 is used as the heat source of the high temperature field 100 for confinement, but the same effect can be obtained by introducing the fuel gas such as propane.
(発明の効果) 以上詳細に説明した如く本発明によれば、熱風中の揮発
性飛散物が燃焼除去されるので、熱風循環経路の熱風中
の揮発性飛散物の濃度を著しく低減できると共に、従来
方法に比べ、循環熱風中の揮発性飛散物を安定して除去
することが可能となり、欠点の少ない高品質のフィルム
が極めて低コストで生産できる。(Effects of the Invention) According to the present invention as described in detail above, since the volatile scattered substances in the hot air are burned and removed, the concentration of the volatile scattered substances in the hot air in the hot air circulation path can be significantly reduced, and Compared with the conventional method, it is possible to stably remove the volatile scattered substances in the circulating hot air, and it is possible to produce a high quality film with few defects at an extremely low cost.
第1図(イ)は本発明の実施例における閉込高温場の原
理を説明する線図、第1図(ロ)は同閉込高温場の原理
を説明する構造図、第2図は同閉込高温場と熱交換器の
組合せからなる延伸フィルム製造装置の熱風循環装置部
を含む揮発性飛散物除去装置の断面図である。 図の主要部分の説明 100……閉込高温場、101,101′……セラミック多孔体 102……電気ヒータ、103……熱風の一部 105……熱交換器、106……入口ダクト 107……出口ダクト、 150……揮発性飛散物除去装置 200……熱風循環装置部、201……ファン 202……モータ、203……熱風 204……循環経路、205……ノズル箱 206……フィルム、208……ヒータFIG. 1 (a) is a diagram for explaining the principle of the confined high temperature field in the embodiment of the present invention, FIG. 1 (b) is a structural diagram for explaining the principle of the confined high temperature field, and FIG. 2 is the same. FIG. 3 is a cross-sectional view of a volatile scattered material removing device including a hot air circulation device part of a stretched film manufacturing apparatus including a combination of a confined high temperature field and a heat exchanger. Description of the main parts of the figure 100 ... Closed high temperature field, 101, 101 '... Porous ceramic body 102 ... Electric heater, 103 ... Part of hot air 105 ... Heat exchanger, 106 ... Inlet duct 107 ... Outlet Duct, 150 …… Volatile scattered matter removing device 200 …… Hot air circulation device part, 201 …… Fan 202 …… Motor, 203 …… Hot air 204 …… Circulation path, 205 …… Nozzle box 206 …… Film, 208… …heater
Claims (1)
ミック多孔体で仕切られた閉込高温場、熱交換器、及び
前記閉込高温場に前記循環経路より循環熱風の一部を前
記熱交換器を介して導入し、再び同熱交換器を介して同
熱風循環経路に戻すような熱風を循環させる入口及び出
口ダクトとよりなることを特徴とする揮発性飛散物除去
装置。1. A circulation path of hot air for heating a film, a closed high temperature field partitioned by a ceramic porous body, a heat exchanger, and a part of the circulating hot air from the circulation path to the closed high temperature field. A volatile scattered matter removing device comprising: an inlet and an outlet duct for circulating hot air introduced through a heat exchanger and returned to the same hot air circulation path through the same heat exchanger.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8684788A JPH07102623B2 (en) | 1988-04-08 | 1988-04-08 | Volatile scatter remover |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8684788A JPH07102623B2 (en) | 1988-04-08 | 1988-04-08 | Volatile scatter remover |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01258942A JPH01258942A (en) | 1989-10-16 |
JPH07102623B2 true JPH07102623B2 (en) | 1995-11-08 |
Family
ID=13898205
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8684788A Expired - Fee Related JPH07102623B2 (en) | 1988-04-08 | 1988-04-08 | Volatile scatter remover |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07102623B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006327650A (en) * | 2005-05-27 | 2006-12-07 | Yoshino Kogyosho Co Ltd | Synthetic resin cup shaped container |
-
1988
- 1988-04-08 JP JP8684788A patent/JPH07102623B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006327650A (en) * | 2005-05-27 | 2006-12-07 | Yoshino Kogyosho Co Ltd | Synthetic resin cup shaped container |
JP4725886B2 (en) * | 2005-05-27 | 2011-07-13 | 株式会社吉野工業所 | Synthetic resin cup-shaped container |
Also Published As
Publication number | Publication date |
---|---|
JPH01258942A (en) | 1989-10-16 |
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Legal Events
Date | Code | Title | Description |
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LAPS | Cancellation because of no payment of annual fees |