JP2001246215A - Method and apparatus for treating fine particles of fatty acid in exhaust gas - Google Patents

Method and apparatus for treating fine particles of fatty acid in exhaust gas

Info

Publication number
JP2001246215A
JP2001246215A JP2000060815A JP2000060815A JP2001246215A JP 2001246215 A JP2001246215 A JP 2001246215A JP 2000060815 A JP2000060815 A JP 2000060815A JP 2000060815 A JP2000060815 A JP 2000060815A JP 2001246215 A JP2001246215 A JP 2001246215A
Authority
JP
Japan
Prior art keywords
fatty acid
exhaust gas
fine particles
filter
melting point
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
Application number
JP2000060815A
Other languages
Japanese (ja)
Other versions
JP3321569B2 (en
Inventor
Tomoji Utagawa
朋二 雅楽川
Naonobu Motozawa
尚信 元澤
Hiroyuki Toge
博之 峠
Muneyuki Yamaguchi
宗志 山口
Kinichi Odajima
金一 小田島
Hisashi Yanaka
久志 谷中
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.)
Mitsubishi Paper Mills Ltd
Toyo Seisakusho KK
Original Assignee
Mitsubishi Paper Mills Ltd
Toyo Seisakusho KK
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 Mitsubishi Paper Mills Ltd, Toyo Seisakusho KK filed Critical Mitsubishi Paper Mills Ltd
Priority to JP2000060815A priority Critical patent/JP3321569B2/en
Publication of JP2001246215A publication Critical patent/JP2001246215A/en
Application granted granted Critical
Publication of JP3321569B2 publication Critical patent/JP3321569B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To efficiently collect fine particles of fatty acid in exhaust gas containing scattered fatty acid generated at a time of the extrusion molding/ processing of a resin by an easy technique to safely remove them without causing the generation of a fire after collection. SOLUTION: Exhaust gas containing scattered fatty acid is heated to a temperature higher than the melting point of the fatty acid with a heater 4 to form fine particles of liquefied fatty acid and steam whose temperature is higher than the melting point of the fatty acid is sprayed on these fine particles to make moisture adhere to the surfaces of the fine particles and a large number pf the fine particles are permitted to adhere to each other by the adhesion force of moisture to grow to form fatty acid mist of large particles, and the exhaust gas containing this fatty acid mist is passed through a filter 6 to cause the fatty acid mist to adhere on the filter to remove the same.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は樹脂の押出成形・加
工時に発生するガス中の脂肪酸微粒子の除去方法及びそ
の装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for removing fatty acid fine particles in a gas generated during extrusion molding and processing of a resin.

【0002】[0002]

【従来の技術】合成樹脂の押出成形・加工時には、加熱
により劣化した樹脂成分を含むミストとともに、成形加
工性を向上させるために樹脂に配合されている添加剤
(脂肪酸等)が揮発または飛散することにより、当該押
出成形機の周辺に粉塵を含むガスが発生して、作業環境
を悪化させることになる。
2. Description of the Related Art During extrusion molding and processing of a synthetic resin, additives (fatty acids and the like) incorporated in the resin to improve the moldability are volatilized or scattered together with a mist containing a resin component degraded by heating. As a result, gas containing dust is generated around the extruder, which deteriorates the working environment.

【0003】そこで、従来は発生したガスをその周辺空
気とともに、フードよりファンにて強制吸引して大気中
に放出しているが、脂肪酸微粒子は60℃未満になると
凝固するので、当該押出成形機周辺空気との混合、排出
ダクト経路中の放熱等により排ガス温度が60℃未満に
下げられ、その結果、白煙となって煙突から吹き出さ
れ、環境・衛生上問題とされている。
Therefore, conventionally, the generated gas is forcibly sucked by a fan from a hood together with the surrounding air and discharged into the atmosphere. However, the fatty acid fine particles solidify below 60 ° C. The exhaust gas temperature is reduced to less than 60 ° C. by mixing with ambient air, heat radiation in the discharge duct path, etc., and as a result, white smoke is blown out of the chimney, which is an environmental and sanitary problem.

【0004】[0004]

【発明が解決しようとする課題】この問題を解決すべ
く、従来は、脂肪酸微粒子を含む排ガスを水洗浄装置
(スクラバー)に通過させるか、あるいは電気集塵機に
通すかして脂肪酸微粒子を除去して大気中に放出してい
る。
In order to solve this problem, conventionally, an exhaust gas containing fatty acid fine particles is removed by passing the exhaust gas containing a fatty acid fine particle through a water washing device (scrubber) or an electric dust collector. Released into the atmosphere.

【0005】しかし、水洗浄装置(スクラバー)を使用
する場合は除去率が10%前後と除去効率が非常に低
く、また、電気集塵機を使用する場合は捕集効率はよい
が、反面において脂肪酸を含む粉塵が電気集塵機に堆積
し、火災発生の原因となるなどの問題点があった。
However, when a water scrubber (scrubber) is used, the removal efficiency is very low at around 10%, and when an electrostatic precipitator is used, the collection efficiency is good, but on the other hand, fatty acids are not removed. There is a problem that the dust contained in the dust collector accumulates and causes a fire.

【0006】[0006]

【本発明の目的】本発明は排ガス中の脂肪酸微粒子を容
易な手法でしかも効率よく捕集でき、かつ捕集後は火災
発生の原因となることもなくて安全な排ガス中の脂肪酸
微粒子の除去方法及びその装置に関する。
An object of the present invention is to remove fatty acid fine particles from exhaust gas by a simple method and efficiently, and to remove fatty acid fine particles from exhaust gas safely without causing a fire after the collection. A method and an apparatus therefor.

【0007】[0007]

【本発明の手段】本発明の排ガス中の脂肪酸微粒子の処
理方法は、樹脂の押出成形・加工時に発生する飛散脂肪
酸を含む排ガスを、脂肪酸の融点よりも高い温度で加熱
して液状化脂肪酸の微粒子とせしめ、この微粒子に、脂
肪酸の融点よりも高い温度の水蒸気を吹き付けることに
より微粒子の表面に水分を付着させ、その水分の付着力
で多数の微粒子どうしを結合、成長させて大きい粒子の
脂肪酸ミストとなし、この脂肪酸ミストを含む排ガスを
濾過器へ通すことにより脂肪酸ミストを濾過器に付着せ
しめて除去することを特徴とする。
The method of the present invention for treating fatty acid fine particles in exhaust gas comprises heating the exhaust gas containing scattered fatty acids generated during extrusion molding and processing of the resin at a temperature higher than the melting point of the fatty acid. Water is attached to the surface of the fine particles by spraying water vapor at a temperature higher than the melting point of the fatty acid onto the fine particles, and a large number of the fine particles are combined and grown by the adhesive force of the water to produce a fatty acid of a large particle. The method is characterized in that the exhaust gas containing the fatty acid mist is passed through a filter to remove the fatty acid mist by adhering to the filter.

【0008】また、本発明に係る排ガス中の脂肪酸微粒
子の処理装置は、樹脂の押出成形・加工時に発生する飛
散脂肪酸を含む排ガスの排気ダクトに接続する脂肪酸除
去装置内に排ガスの流れ方向に順次ヒータ、蒸気噴霧
器、濾過器を設け、排気ダクトからの排ガスを、脂肪酸
の融点よりも高い温度で前記ヒータによって加熱して脂
肪酸を液状の微粒子ならしめ、次ぎに排ガスに、脂肪酸
の融点よりも高い温度の蒸気を前記蒸気噴霧器から吹き
付けて脂肪酸の表面に水分を付着させ、その水分の付着
力によって複数の微粒子どうしを結合させて大きい粒子
の脂肪酸ミストに成長させ、次いで排ガスを前記濾過器
に通すことにより脂肪酸ミストを濾過器に付着せしめ
て、脂肪酸が除去された排ガスとして排気できる構造の
ものとしてある。
Further, the apparatus for treating fatty acid fine particles in exhaust gas according to the present invention is arranged in a fatty acid removing apparatus connected to an exhaust duct for exhaust gas containing scattered fatty acids generated during extrusion molding and processing of a resin in the direction of flow of the exhaust gas. A heater, a steam atomizer, and a filter are provided, and the exhaust gas from the exhaust duct is heated by the heater at a temperature higher than the melting point of the fatty acid to convert the fatty acid into liquid fine particles. Next, the exhaust gas is higher than the melting point of the fatty acid. A steam at a temperature is sprayed from the steam atomizer to attach moisture to the surface of the fatty acid, the plurality of fine particles are combined by the adhesive force of the moisture to grow into a fatty acid mist of large particles, and then the exhaust gas is passed through the filter. In this way, the fatty acid mist is attached to the filter so that the exhaust gas can be exhausted as the exhaust gas from which the fatty acid has been removed.

【0009】さらに本発明の装置は、濾過器によって捕
捉されずして流下する液状脂肪酸を排出するドレンパイ
プを装置の底部に設けてある。
Further, in the apparatus of the present invention, a drain pipe for discharging the liquid fatty acid which is not captured by the filter and flows down is provided at the bottom of the apparatus.

【0010】また、本発明の装置においては、濾過器に
付着した脂肪酸を洗浄するために、脂肪酸の融点よりも
高い温度の温水を濾過器が水没される液面になるように
供給する手段と、温水によって溶かされて温水の上層に
溜まる脂肪酸液を装置外に排出する手段とを備える。
Further, in the apparatus of the present invention, means for supplying hot water having a temperature higher than the melting point of the fatty acid so as to reach a liquid level at which the filter is submerged, in order to wash the fatty acid attached to the filter. Means for discharging the fatty acid liquid dissolved in the warm water and accumulated in the upper layer of the warm water to the outside of the apparatus.

【0011】さらに本発明の装置においては、排気ダク
トに複数基の脂肪酸除去装置を並設し、そのうちの或る
脂肪酸除去装置が脂肪酸ミストの除去運転をしていると
きは、残りの脂肪酸除去装置が濾過器に付着している脂
肪酸の洗浄運転されるよう逐次脂肪酸の除去運転と洗浄
運転が切り換えられるようにしてある。
Further, in the apparatus of the present invention, a plurality of fatty acid removing devices are arranged in parallel in the exhaust duct, and when one of the fatty acid removing devices is performing a fatty acid mist removing operation, the remaining fatty acid removing device is provided. The operation is sequentially switched between the fatty acid removal operation and the washing operation so that the fatty acid adhering to the filter is washed.

【0012】[0012]

【実施例】本発明の一実施例を図1〜3に基づいて説明
する。樹脂の押出成形・加工時に発生する飛散脂肪酸を
含む排ガスGは図1の排気ダクト1によって脂肪酸除去
装置2に導かれる。同装置2は、排ガスの流路本体3内
に排ガスの流れ方向で順次ヒータ4、蒸気噴霧器5、デ
ミスタ等の金属製の濾過器6を備えている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of the present invention will be described with reference to FIGS. Exhaust gas G containing scattered fatty acids generated during extrusion molding and processing of the resin is guided to the fatty acid removing device 2 by the exhaust duct 1 of FIG. The device 2 includes a heater 4, a steam atomizer 5, and a metal filter 6 such as a demister in the exhaust gas flow path main body 3 in the flow direction of the exhaust gas.

【0013】排気ダクト1からの排ガスは、脂肪酸の融
点よりも高い温度の例えば60℃以上にヒータ4によっ
て加熱され、脂肪酸は液状の微粒子となる。なお、脂肪
酸にはステアリン酸、パルミチン酸、ミリスチン酸等が
あり、ステアリン酸の融点は70.1℃、パルミチン酸
の融点は63℃、ミリスチン酸の融点は53.8℃であ
るが、不純物を含むことにより融点がいずれも60℃未
満に降下し、例えば不純物を含むステアリン酸の融点は
58℃である。
Exhaust gas from the exhaust duct 1 is heated by the heater 4 to a temperature higher than the melting point of the fatty acid, for example, 60 ° C. or higher, so that the fatty acid becomes liquid fine particles. In addition, fatty acids include stearic acid, palmitic acid, and myristic acid. The melting points of stearic acid are 70.1 ° C, the melting point of palmitic acid is 63 ° C, and the melting point of myristic acid is 53.8 ° C. The melting point drops below 60 ° C. in each case due to the inclusion. For example, the melting point of stearic acid containing impurities is 58 ° C.

【0014】脂肪酸の微粒子には次ぎの蒸気噴霧器5か
ら60℃以上の温度の蒸気が吹き付けられて表面に水分
が付着し、水の付着力によって複数の微粒子どうしが結
合し、成長して大きい粒子のミストとなる。
The fatty acid fine particles are sprayed with steam at a temperature of 60 ° C. or more from the next steam sprayer 5 to adhere moisture to the surface, and a plurality of fine particles are combined by the adhesive force of the water and grow to form large particles. Mist.

【0015】排ガスは次ぎのデミスタ等の金属製濾過器
6を通る際に脂肪酸のミストが捕集されるが、脂肪酸の
ミストは成長した大きな粒子となっているので、濾過器
6による捕集が容易にしかも充分になされる。脂肪酸が
除去された排ガスは送風機7によって煙突等に送られ、
大気中に放散される。
When the exhaust gas passes through a metal filter 6 such as a demister, fatty acid mist is collected. Since the fatty acid mist is formed as large particles that have grown, the fatty acid mist is collected by the filter 6. It is easy and sufficient. The exhaust gas from which the fatty acids have been removed is sent to a chimney or the like by a blower 7,
Dissipated into the atmosphere.

【0016】濾過器6によって捕集された脂肪酸のミス
トは次第に温度が低下して60℃未満になることによっ
て凝固し、濾過器に固着するが、濾過器によって捕捉さ
れなかった脂肪酸のミストは装置のドレンパイプ8から
脂肪酸の然るべき処理部へ排出される。
The fatty acid mist collected by the filter 6 gradually solidifies by lowering the temperature to below 60 ° C. and solidifies on the filter, but the fatty acid mist not captured by the filter is removed by the apparatus. From the drain pipe 8 to the appropriate processing section for fatty acids.

【0017】排ガス中の脂肪酸ミストの除去を所要時間
行った後は濾過器に付着している脂肪酸を除去する必要
がある。そのためには図2のように装置内へ濾過器6が
浸漬される液面になるように温水13を供給し、この温
水には脂肪酸の融点よりも高い温度のものを使用する。
After the fatty acid mist in the exhaust gas has been removed for a required time, it is necessary to remove the fatty acid adhering to the filter. For this purpose, as shown in FIG. 2, hot water 13 is supplied so as to have a liquid level in which the filter 6 is immersed in the apparatus, and hot water having a temperature higher than the melting point of the fatty acid is used.

【0018】かくすることにより、濾過器6に付着して
いた固型脂肪酸は温水によって溶かされ、溶けた脂肪酸
14は温水13よりも比重が小であるので、温水の上層
に溜まる。上層に溜まった脂肪酸14を装置の側部に設
けたオーバーフロー管9の開閉弁V1 を開くことにより
脂肪酸の然るべき廃棄処理部へ排出する。
As a result, the solid fatty acid adhering to the filter 6 is dissolved by the warm water, and the dissolved fatty acid 14 has a specific gravity smaller than that of the warm water 13 and thus accumulates in the upper layer of the warm water. It is discharged to appropriate disposal unit of the fatty acids by opening the opening and closing valve V 1 of the overflow pipe 9 provided with a fatty acid 14 collected in the upper layer on the side of the device.

【0019】温水供給手段は種々あるが、その一例を示
すと、前記ドレンパイプ8から行なう。その場合は、温
水供給管10をドレンパイプ8に開閉弁V2 を介して接
続し、ドレンパイプ8にも開閉弁V3 、V4 を設ける。
There are various types of hot water supply means. One example is hot water supply means from the drain pipe 8. In that case, connected via an on-off valve V 2 hot water supply pipe 10 to the drain pipe 8, to the drain pipe 8 is provided an opening and closing valve V 3, V 4.

【0020】かくすることにより、脂肪酸ミストの除去
運転時には温水供給パイプの開閉弁V2 は閉じるととも
にオーバーフロー管の開閉弁V1 も閉じ、ドレンパイプ
の開閉弁V3 、 V4 は開いておく。
[0020] By thus, upon removal operation of the fatty acid mist is also closed off valve V 1 of the overflow pipe is closed off valve V 2 of the hot water supply pipe on-off valve V 3, V 4 of the drain pipe is left open.

【0021】濾過器の洗浄運転時には、ドレンパイプの
開閉弁V3 は開、V4 は閉とし、温水供給パイプの開閉
弁V2 を開いて装置内へ濾過器が没するまで温水を供給
し、また、オーバーフロー管の開閉弁V1 は開とする。
During the washing operation of the filter, the open / close valve V 3 of the drain pipe is opened and V 4 is closed, and the open / close valve V 2 of the hot water supply pipe is opened to supply hot water until the filter sinks into the apparatus. in addition, the on-off valve V 1 of the overflow pipe is opened.

【0022】排気ダクト1からは24時間連続して排ガ
スが送られるので、脂肪酸除去装置は運転を中止できな
い。これに対応するために、本発明では排気ダクト1に
接続した給気ヘッダ11aに脂肪酸除去装置2をそれぞ
れ開閉手段たるダンパ手段V5 を介して複数基並列に接
続し、また、脂肪酸除去装置2の排気口は排気ヘッダ1
1bに接続し、同ヘッダは1本の排気管12で送風機7
に接続する。
Since the exhaust gas is sent from the exhaust duct 1 continuously for 24 hours, the operation of the fatty acid removing device cannot be stopped. To cope with this, in the present invention through the damper means V 5 serving respectively opening and closing means to supply header 11a fatty removal device 2 connected to the exhaust duct 1 connected to the plurality based on parallel, also fatty acid removal device 2 Exhaust port is exhaust header 1
1b, and the header is connected to the blower 7 by one exhaust pipe 12.
Connect to

【0023】かくすることにより、或る脂肪酸除去装置
の開閉ダンパだけは閉とし、残りの脂肪酸除去装置の開
閉ダンパは開として、開ダンパの脂肪酸除去装置で脂肪
酸ミストの除去運転をする反面、閉ダンパの脂肪酸除去
装置では濾過器の洗浄運転をし、以下脂肪酸除去装置の
脂肪酸ミスト除去運転と濾過器の洗浄運転を逐次切り換
えることにより、連続して脂肪酸ミストの除去運転を行
なえる。
By doing so, only the opening / closing damper of a certain fatty acid removing device is closed, and the opening / closing dampers of the remaining fatty acid removing device are opened, and while the fatty acid mist removing operation is performed by the fatty acid removing device of the open damper, the opening / closing damper is closed. In the fatty acid removing device of the damper, the cleaning operation of the filter is performed, and the fatty acid mist removing operation of the fatty acid removing device and the cleaning operation of the filter are sequentially switched, whereby the fatty acid mist removing operation can be continuously performed.

【0024】この際、脂肪酸除去装置は2台ではなく、
3台以上であることが望ましい。2台であると各脂肪酸
除去装置は排気ダクトからの排ガスの最大風量に対応で
きるものでなければならず、各脂肪酸除去装置は大型、
能力の大なるものが要求されるが、脂肪酸除去装置が例
えば6台であれば、1台が洗浄運転を行っている間に残
りの5台が除去運転を行うので、各装置の能力は排ガス
の最大風量の1/5のものですみ、各装置の小型化、小
能力化を期せる利点がある。
At this time, the number of fatty acid removing devices is not two,
It is desirable to have three or more. If there are two units, each fatty acid removing device must be able to handle the maximum air volume of exhaust gas from the exhaust duct, and each fatty acid removing device is large,
Although a large capacity is required, if the number of fatty acid removing devices is, for example, 6, the remaining 5 units perform the removing operation while one unit performs the cleaning operation. Only 1/5 of the maximum air volume of the device, and there is an advantage that the size and capacity of each device can be reduced.

【0025】さらに、流路本体3は図のようにU字管状
のベンド管となし、一方のガス吸入管側には荒目の濾過
器を、他方の排出管側には密目の濾過器を配することに
より脂肪酸ミストの除去をより充分にできる。
Further, the flow path main body 3 is formed as a U-shaped bend pipe as shown in the figure, and a coarse filter is provided on one gas suction pipe side and a dense filter is provided on the other discharge pipe side. The fatty acid mist can be more sufficiently removed by disposing

【0026】[0026]

【発明の作用、効果】本発明によれば、樹脂の押出成形
・加工時に発生する脂肪酸微粒子を含む排ガスから、ヒ
ータ、蒸気噴霧器、濾過器で脂肪酸を容易かつ充分に除
去できて、従来の水洗浄装置を使用する場合よりも脂肪
酸の除去効率が格段に高く、しかも電気集塵機を使用す
る場合のような火災発生のおそれもまずなく、また、構
造が比較的シンプルで、製造コストの低い装置を提供で
きる。
According to the present invention, fatty acids can be easily and sufficiently removed from exhaust gas containing fatty acid fine particles generated during resin extrusion molding and processing by a heater, a steam atomizer, and a filter. Fatty acid removal efficiency is much higher than when a washing device is used.Furthermore, there is almost no risk of fire occurring when using an electrostatic precipitator, and a device with a relatively simple structure and low manufacturing cost is required. Can be provided.

【0027】さらに、本発明によれば化学薬品は一切使
用する必要がないので、作業環境を害することなく、安
全に脂肪酸を除去できる。
Further, according to the present invention, it is not necessary to use any chemicals, so that fatty acids can be safely removed without damaging the working environment.

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

【図1】本発明に係る装置の実施例による脂肪酸ミスト
の除去運転状態を示す縦断正面図。
FIG. 1 is a longitudinal sectional front view showing an operation state of removing fatty acid mist by an embodiment of the apparatus according to the present invention.

【図2】本発明に係る装置の実施例による濾過器の洗浄
運転状態を示す縦断正面図。
FIG. 2 is a longitudinal sectional front view showing a cleaning operation state of a filter according to an embodiment of the apparatus according to the present invention.

【図3】脂肪酸除去装置を複数台並列に設けた本発明の
実施例を示す斜視図。
FIG. 3 is a perspective view showing an embodiment of the present invention in which a plurality of fatty acid removing devices are provided in parallel.

【符号の説明】[Explanation of symbols]

1 排気ダクト 2 脂肪酸除去装置 3 流路本体 4 ヒータ 5 蒸気噴霧器 6 濾過器 7 送風機 8 ドレンパイプ 9 オーバーフロー管 10 温水供給管 11a 給気ヘッダ 11b 排気ヘッダ 12 排気管 13 温水 14 溶けた脂肪酸 DESCRIPTION OF SYMBOLS 1 Exhaust duct 2 Fatty acid remover 3 Flow path main body 4 Heater 5 Steam sprayer 6 Filter 7 Blower 8 Drain pipe 9 Overflow pipe 10 Hot water supply pipe 11a Air supply header 11b Exhaust header 12 Exhaust pipe 13 Hot water 14 Melted fatty acid

───────────────────────────────────────────────────── フロントページの続き (72)発明者 元澤 尚信 東京都千代田区丸の内3丁目4番2号 三 菱製紙株式会社内 (72)発明者 峠 博之 東京都品川区東品川四丁目11番34号 株式 会社東洋製作所内 (72)発明者 山口 宗志 東京都品川区東品川四丁目11番34号 株式 会社東洋製作所内 (72)発明者 小田島 金一 東京都品川区東品川四丁目11番34号 株式 会社東洋製作所内 (72)発明者 谷中 久志 東京都品川区東品川四丁目11番34号 株式 会社東洋製作所内 Fターム(参考) 4D032 AC07 AC39 BA03 BA06 BB05 CA01 CA10 DA10 4D058 JA12 JB03 JB24 KC04 LA01 MA12 MA51 QA01 QA03 QA05 QA11 RA02 RA15 SA15 UA01 UA25  ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Naobu Motozawa 3-4-2, Marunouchi, Chiyoda-ku, Tokyo Mitsubishi Paper Mills Co., Ltd. (72) Hiroyuki Toge 4--11-34, Higashishinagawa, Shinagawa-ku, Tokyo No. Inside the Toyo Seisakusho Co., Ltd. (72) Inventor Muneshi Yamaguchi 4--11-34 Higashi-Shinagawa, Shinagawa-ku, Tokyo Inside the Toyo Seisakusho Co., Ltd. (72) Kinichi Odashima 4-1-134, Higashi-Shinagawa, Shinagawa-ku, Tokyo No. Inside the Toyo Seisakusho Co., Ltd. (72) Inventor Hisashi Yanaka 4-11-34, Higashishinagawa, Shinagawa-ku, Tokyo F-term inside the Toyo Seisakusho 4D032 AC07 AC39 BA03 BA06 BB05 CA01 CA10 DA10 4D058 JA12 JB03 JB24 KC04 LA01 MA12 MA51 QA01 QA03 QA05 QA11 RA02 RA15 SA15 UA01 UA25

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】樹脂の押出成形・加工時に発生する飛散脂
肪酸を含む排ガスを、脂肪酸の融点よりも高い温度で加
熱して液状化脂肪酸の微粒子とせしめ、この微粒子に、
脂肪酸の融点よりも高い温度の水蒸気を吹き付けること
により微粒子の表面に水分を付着させ、その水分の付着
力で多数の微粒子どうしを結合、成長させて大きい粒子
の脂肪酸ミストとなし、この脂肪酸ミストを含む排ガス
を濾過器へ通すことにより脂肪酸ミストを濾過器に付着
せしめて除去することを特徴とする排ガス中の脂肪酸微
粒子の処理方法。
1. Exhaust gas containing scattered fatty acids generated during extrusion molding and processing of a resin is heated at a temperature higher than the melting point of the fatty acids to form liquefied fatty acid fine particles.
By spraying water vapor at a temperature higher than the melting point of the fatty acid, water is attached to the surface of the fine particles, and a large number of fine particles are combined and grown by the adhesive force of the water to form a fatty acid mist of large particles. A method for treating fatty acid fine particles in exhaust gas, wherein the fatty acid mist is attached to the filter and removed by passing exhaust gas containing the gas through a filter.
【請求項2】樹脂の押出成形・加工時に発生する飛散脂
肪酸を含む排ガスの排気ダクトに接続する脂肪酸除去装
置内に排ガスの流れ方向に順次ヒータ、蒸気噴霧器、濾
過器を設け、排気ダクトからの排ガスを、脂肪酸の融点
よりも高い温度で前記ヒータによって加熱して脂肪酸を
液状の微粒子ならしめ、次ぎに排ガスに、脂肪酸の融点
よりも高い温度の蒸気を前記蒸気噴霧器から吹き付けて
脂肪酸の表面に水分を付着させ、その水分の付着力によ
って複数の微粒子どうしを結合させて大きい粒子の脂肪
酸ミストに成長させ、次いで排ガスを前記濾過器に通す
ことにより脂肪酸ミストを濾過器に付着せしめて、脂肪
酸が除去された排ガスとして排出する排ガス中の脂肪酸
微粒子の処理装置。
2. A heater, a steam atomizer, and a filter are sequentially provided in a flow direction of exhaust gas in a fatty acid removing device connected to an exhaust duct of exhaust gas containing scattered fatty acids generated during extrusion molding and processing of a resin. The exhaust gas is heated by the heater at a temperature higher than the melting point of the fatty acid to convert the fatty acid into liquid fine particles, and then a steam having a temperature higher than the melting point of the fatty acid is sprayed on the exhaust gas from the steam atomizer to the surface of the fatty acid. By adhering moisture, the plurality of fine particles are combined with each other by the adhesive force of the moisture to grow into a fatty acid mist of large particles, and then the exhaust gas is passed through the filter to attach the fatty acid mist to the filter, whereby the fatty acid is removed. Equipment for treating fatty acid fine particles in exhaust gas discharged as removed exhaust gas.
【請求項3】請求項2に記載の装置において、濾過器に
よって捕捉されずして流下する液状脂肪酸を排出するド
レンパイプを装置の底部に設けてなる排ガス中の脂肪酸
微粒子の処理装置。
3. An apparatus for treating fatty acid fine particles in exhaust gas according to claim 2, wherein a drain pipe for discharging the liquid fatty acid that is not captured by the filter and flows down is provided at the bottom of the apparatus.
【請求項4】請求項2に記載の装置において、濾過器に
付着した脂肪酸を洗浄するために、脂肪酸の融点よりも
高い温度の温水を濾過器が水没される液面になるように
供給する手段と、温水によって溶かされて温水の上層に
溜まる脂肪酸液を装置外に排出する手段とを備える排ガ
ス中の脂肪酸微粒子の処理装置。
4. The apparatus according to claim 2, wherein hot water having a temperature higher than the melting point of the fatty acid is supplied so as to reach a liquid level at which the filter is submerged, in order to wash fatty acids attached to the filter. An apparatus for discharging fatty acid liquid dissolved in hot water and remaining in an upper layer of the warm water outside the apparatus.
【請求項5】請求項2に記載の装置において、排気ダク
トに複数基の脂肪酸除去装置を並列に接続し、そのうち
の或る脂肪酸除去装置が脂肪酸ミストの除去運転をして
いるときは、残りの脂肪酸除去装置が濾過器に付着して
いる脂肪酸の洗浄運転されるよう逐次脂肪酸の除去運転
と洗浄運転が切り換えられるようにした排ガス中の脂肪
酸微粒子の処理装置。
5. The apparatus according to claim 2, wherein a plurality of fatty acid removing devices are connected in parallel to the exhaust duct, and when one of the fatty acid removing devices is performing a fatty acid mist removing operation, the remaining fatty acid removing device is connected to the exhaust duct. The apparatus for treating fatty acid fine particles in exhaust gas, wherein the fatty acid removing apparatus is sequentially switched between a fatty acid removing operation and a washing operation such that the fatty acid removing apparatus is operated to wash the fatty acid adhering to the filter.
JP2000060815A 2000-03-06 2000-03-06 Method and apparatus for treating fatty acid fine particles in exhaust gas Expired - Fee Related JP3321569B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000060815A JP3321569B2 (en) 2000-03-06 2000-03-06 Method and apparatus for treating fatty acid fine particles in exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000060815A JP3321569B2 (en) 2000-03-06 2000-03-06 Method and apparatus for treating fatty acid fine particles in exhaust gas

Publications (2)

Publication Number Publication Date
JP2001246215A true JP2001246215A (en) 2001-09-11
JP3321569B2 JP3321569B2 (en) 2002-09-03

Family

ID=18581064

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000060815A Expired - Fee Related JP3321569B2 (en) 2000-03-06 2000-03-06 Method and apparatus for treating fatty acid fine particles in exhaust gas

Country Status (1)

Country Link
JP (1) JP3321569B2 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100770390B1 (en) 2005-11-21 2007-10-26 가부시키가이샤 캬타라 Method of processing alkali-activation exhaust gas
JP5895071B1 (en) * 2015-01-29 2016-03-30 慶源 ▲黄▼ Air dust cleaner

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100770390B1 (en) 2005-11-21 2007-10-26 가부시키가이샤 캬타라 Method of processing alkali-activation exhaust gas
JP5895071B1 (en) * 2015-01-29 2016-03-30 慶源 ▲黄▼ Air dust cleaner

Also Published As

Publication number Publication date
JP3321569B2 (en) 2002-09-03

Similar Documents

Publication Publication Date Title
WO2011091650A1 (en) Laser marking dust-removal device and dust-removal method
CN107062326B (en) Fume exhaust fan
CN104150194A (en) Dust-suppression sweeping system for material conveyor belt
US5762663A (en) Wet dust collecting apparatus
JP6167326B2 (en) Paint mist processing equipment
CN106944933A (en) A kind of explosion-proof dust pelletizing system of intermetallic composite coating
JP3321569B2 (en) Method and apparatus for treating fatty acid fine particles in exhaust gas
JP2009019813A (en) Cleaning mechanism of indoor unit
JP2004089837A (en) Method and apparatus for treating exhaust gas from optical fiber production process
CN108568431A (en) Efficient low-resistance electrostatic precipitation filtration system
CN208825054U (en) A kind of treadmill controller cleaner
CN209997403U (en) electric automatization dust collector
CN104923055B (en) Tail gas treatment system and method of drying machine and drying dedusting system
JP3107375B2 (en) Oil mist collection device
JP2007247920A (en) Range hood
CN209434615U (en) One kind being convenient for clean power distribution cabinet
JP3411816B2 (en) Cleaning method for electric precipitator
KR100485929B1 (en) Dust and Offensive Odor Removal System Using in Combination with Rotating Screen and Cyclone Scrubber
JP5208253B2 (en) How to clean the heat exchanger
CN108043823A (en) A kind of intermetallic composite coating cleaning device
JP4745285B2 (en) Waste plastic treatment facility and method for reducing humidity of exhaust gas using the same
JP2009178271A (en) Electric vacuum cleaner and dust collecting method using the same
JP2009136816A (en) Dust collector
KR20160051015A (en) Dust Collector Apparatus
JP2559290B2 (en) Method and apparatus for cleaning and collecting inner surface of pipe

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees