JPH0441704A - Method for removing organic material by fluid layer furnace - Google Patents
Method for removing organic material by fluid layer furnaceInfo
- Publication number
- JPH0441704A JPH0441704A JP2149143A JP14914390A JPH0441704A JP H0441704 A JPH0441704 A JP H0441704A JP 2149143 A JP2149143 A JP 2149143A JP 14914390 A JP14914390 A JP 14914390A JP H0441704 A JPH0441704 A JP H0441704A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- attached
- pores
- fluidized bed
- spinneret
- 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
Landscapes
- Fluidized-Bed Combustion And Resonant Combustion (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
- Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)
- Cleaning In General (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、流動層炉による有機物除去方法に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a method for removing organic matter using a fluidized bed furnace.
更に詳しくは、使用済みの紡糸口金等のような、貫通さ
れた細孔に有機高分子材が付着されている被処理物を流
動層炉で加熱して熱分解除去する方法に関するものであ
る。More specifically, the present invention relates to a method for thermally decomposing and removing a processed material, such as a used spinneret, in which an organic polymer material is attached to the pores thereof, by heating it in a fluidized bed furnace.
[従来の技術]
ゴム、塗料、油、プラスチック等の有機高分子材が付着
している被処理物を流動層炉で加熱して熱分解除去する
ことは従来公知、例えば、特開昭63−282305号
公報においては、貫通された細孔に有機高分子材が付着
されている被処理物(具体的には、使用済みの紡糸口金
やフィルタ等)を、流動層炉で加熱して熱分解除去する
ことが開示されている。[Prior Art] It has been known in the art to thermally decompose a workpiece to which organic polymer materials such as rubber, paint, oil, plastic, etc. are attached by heating it in a fluidized bed furnace. In Japanese Patent No. 282305, a material to be treated (specifically, a used spinneret, a filter, etc.) having an organic polymer material attached to the penetrated pores is heated in a fluidized bed furnace to undergo thermal decomposition. Disclosed is removal.
[発明が解決しようとする課題]
しかし、かかる従来方法は、流動層に対して被処理物を
直接、浸漬したり、あるいは、例えば、特開昭63−1
35707号公報において開示されているように、r床
の流動媒体(アルミナ等)が通過し得る網目のバスゲッ
トに収容した姿で浸漬する関係上、処理中において被処
理物の細孔にアルミナ等の流動媒体が流入し、この孔を
閉塞、すなわち、詰りか発生し、その為、エアーガスの
流入が阻止又は妨げられてここに付着されている有機高
分子材を良好に熱分解除去することが困難であった。[Problems to be Solved by the Invention] However, in such conventional methods, the object to be treated is directly immersed in a fluidized bed, or, for example,
As disclosed in Japanese Patent No. 35707, since the material to be treated is immersed in a mesh bathget through which the fluidized medium (alumina, etc.) of the r-bed can pass, alumina, etc. is deposited into the pores of the material during treatment. The flowing medium flows into the hole, clogging or clogging the hole, which prevents or impedes the inflow of air gas, making it impossible to thermally decompose and remove the organic polymer material attached thereto. It was difficult.
なお、このような問題は、アルミナ等の流動媒体の直径
が一般に0.05w〜0,3圓であるから、被処理物の
貫通孔の直径が0.3tm以上といった比較的大きな孔
である場合においては発生しないが、直径が0.21以
下の細孔である場合においては発生し、従って、紡糸口
金や口金フィルタ等のような細孔を有する被処理物につ
いては、流動層炉による処理が妨げられていた。In addition, since the diameter of a fluid medium such as alumina is generally 0.05W to 0.3 mm, this problem occurs when the through hole of the object to be treated has a relatively large diameter such as 0.3 tm or more. Although it does not occur in the case of pores with a diameter of 0.21 or less, it does occur in the case of pores with a diameter of 0.21 or less. Therefore, processing objects with pores such as spinnerets and spinneret filters cannot be treated in a fluidized bed furnace. It was blocked.
本発明は、このようなことに着目し、これを解決すべく
各方面から鋭意検討の結果、被処理物の細孔が開口され
ている少なくとも一方の端面を、流動媒体の通過を阻止
してエアーガスだけを通過させ得るフィルタで遮蔽し、
かつこのフィルタを下側に位置されるように被処理物を
流動層中に浸漬して処理すればよいことを見出したので
ある。The present invention has focused on such a problem, and as a result of intensive studies from various aspects in order to solve this problem, the present invention has been developed by blocking the passage of a fluid medium through at least one end face of the object to be treated where the pores are opened. Shielded with a filter that allows only air gas to pass through,
They also discovered that the treatment can be carried out by immersing the object in a fluidized bed with this filter positioned below.
[課題を解決するための手段]
すなわち、本発明に係る流動層炉による有機物除去方法
は、貫通された細孔に有機高分子材が付着されている被
処理物を、加熱された流動層中に浸漬して前記有機高分
子材を熱分解除去する流動層炉による有機物除去方法に
おいて、流動媒体の通過を阻止してエアーガスだけを通
過させ得るフィルタを、前記細孔が開口されている少な
くとも一方の端面を遮蔽するように前記被処理物に装着
すると共にこれを、前記フィルタが下側に位置されるよ
うに前記流動層中に浸漬して処理することを特徴とする
ものである。[Means for Solving the Problems] In other words, the method for removing organic matter using a fluidized bed furnace according to the present invention is to place a workpiece having an organic polymer material attached to the pierced pores in a heated fluidized bed. In a method for removing organic substances using a fluidized bed furnace in which the organic polymer material is thermally decomposed and removed by immersion in the fluid, at least one of the filters having the pores opened is provided with a filter capable of blocking passage of the fluid medium and allowing only air gas to pass through. The filter is attached to the object to be processed so as to cover the end face of the object, and the object is immersed in the fluidized bed so as to be processed so that the filter is positioned below.
本発明において、有機高分子材とは、ゴム、塗料、油、
プラスチックなどの有機物を総称すると共に流動媒体と
は、r床に所定量に充填されるアルミナ等の耐火性粒子
を総称し、この流動媒体は、ガス分散板を通過してr床
に均一に供給されるエアーガス(加圧エアー)によって
流動化されて所謂、流動層を形成する。In the present invention, organic polymer materials include rubber, paint, oil,
Fluidized medium is a general term for organic substances such as plastics, and is a general term for refractory particles such as alumina that are filled in a predetermined amount into the r-bed, and this fluidized medium passes through a gas distribution plate and is uniformly supplied to the r-bed. It is fluidized by air gas (pressurized air) to form a so-called fluidized bed.
なお、流動層炉は、従来一般に知られている各種型式の
炉を用いることがでるきが、これの加熱は、ヒータによ
る電熱加熱、バーナによるガス加熱等のいずれであって
もよく、その温度は400℃〜600℃に制御される。Incidentally, the fluidized bed furnace can use various types of furnaces that are generally known in the past, but the heating may be done by electric heating with a heater, gas heating with a burner, etc., and the temperature is controlled at 400°C to 600°C.
これ以外の高温度で処理すると、最も一般的なアルミナ
を使用する場合に、これが被処理物に付着し易くなり、
かつ被処理物が金属の場合、これの損傷の危険性が大き
くなる。反対に、これ以外の低温度で処理すると、有機
高分子材の充分な熱分解が困難となる。目安温度である
が、例えば、ポリ塩化ビニルの場合は400°C〜50
0℃に、また、ポリプロピレンの場合は425℃〜50
0℃、更に、シリコン樹脂の場合は520°C〜560
℃に夫々加熱すればよい。When processing at a higher temperature than this, when using the most common alumina, this tends to adhere to the object to be processed.
In addition, when the object to be processed is metal, there is a greater risk of damage to the object. On the other hand, if the treatment is performed at a lower temperature than this, sufficient thermal decomposition of the organic polymer material becomes difficult. The approximate temperature is, for example, 400°C to 50°C for polyvinyl chloride.
0°C, or 425°C to 50°C for polypropylene
0℃, and in the case of silicone resin, 520℃~560℃
They can be heated to ℃.
また、被処理物は、貫通された細孔に有機高分子材が付
着されているものを対象とするが、処理温度に耐え得る
ものであれば、金属製、セラミ・ンク製以外のものであ
ってもよく、かつその形態も特定のものに限定されない
0貫通された細孔に有機高分子材が付着されている被処
理物の代表例として、使用済みの紡糸口金バック、これ
の構成部品である紡糸口金や口金フィルタ等が挙げられ
る。In addition, the object to be treated is one that has an organic polymer material attached to the pores that have been penetrated, but materials other than metal, ceramic, and ink can be used as long as they can withstand the processing temperature. A used spinneret bag and its constituent parts are representative examples of objects to be treated in which an organic polymer material is attached to the pores that are formed through the pores. Examples include spinnerets and spinneret filters.
更に、フィルタは、流動媒体の通過を阻止してエアーガ
スだけを通過させ得る限り、耐熱性のいかなるフィルタ
であってもよく、セラミック、ステンレス製などの板状
、フェルト状あるいは不織布状等の各種のフィルタを使
用することができ、かつその際、例えば、金網とセラミ
ックシートとの組み合せ体等のように複数材で構成して
らよい。Furthermore, the filter may be any heat-resistant filter as long as it can block the passage of the fluid medium and allow only air gas to pass through, and may be of various types, such as plate-shaped filters made of ceramic or stainless steel, felt-shaped filters, or non-woven fabric filters. Filters can be used and may be constructed of multiple materials, such as a combination of wire mesh and ceramic sheets.
なお、被処理物に対するフィルタの装着については、例
えば、第1図において示されている比較的薄い板状体の
紡糸口金1に対しては、フィルタ2を、細孔3が開口さ
れている対向端面夫々に当接させて各面を遮蔽するよう
に装着すればよく、その際、細孔3が開口されている対
向端面の一方の端面だけを遮蔽するように装着してもよ
いが、両方を遮蔽するように装着する方が好ましい。同
図において示されている態様においては、ボルト・ナツ
ト4を介してサンドイッチ構造に紡糸口金1に対して両
フィルタ2を装着している。しかし、これに限定されず
、他の態様、例えば、細孔3が開口されている紡糸口金
1の端面に、ボルト等を介して着脱し得るように直接、
固定する等、適宜!lE!機に装着することができる。Regarding attachment of the filter to the object to be processed, for example, for the relatively thin plate spinneret 1 shown in FIG. It may be attached so as to be in contact with each of the end faces and to shield each face.In that case, it may be attached so as to shield only one end face of the opposite end face where the pore 3 is opened, but both It is preferable to wear it so as to shield it. In the embodiment shown in the figure, both filters 2 are attached to the spinneret 1 in a sandwich structure via bolts and nuts 4. However, the present invention is not limited thereto, and other embodiments may be used, for example, directly on the end face of the spinneret 1 in which the pores 3 are opened so as to be attachable and detachable via bolts or the like.
Fix it as appropriate! lE! It can be installed on the machine.
また、第2図において示されている紡糸口金バック5に
対しては、紡糸口金1の細孔3が開口されている一方の
端面を、バック出口6を介在させて遮蔽するようにバッ
ク下端にフィルタ2を装着すればよい、その際、フィル
タ2を支持している治具7を、ボルト・ナツト4で雌ユ
ニオン8に固定したり、あるいは雌ユニオン8に螺着し
たりする等、各種手段で固定して装着することができる
。In addition, for the spinneret bag 5 shown in FIG. The filter 2 can be attached by various means such as fixing the jig 7 supporting the filter 2 to the female union 8 with bolts and nuts 4 or screwing it into the female union 8. It can be fixed and installed.
なお、第2図中、9は雄ユニオン、10はサンド、11
は口金フィルタ、12は多孔板、13はバック入口を夫
々示している。In addition, in Figure 2, 9 is a male union, 10 is a sand, and 11 is a male union.
12 represents a cap filter, 12 represents a perforated plate, and 13 represents a back inlet.
次に、このようにしてマスキングし得た被処理物、すな
わち、流動媒体の通過を阻止してエアーガスだけを通過
させ得るフィルタ2を装着した被処理物を、流動層中に
浸漬して処理するが、その際、例えば、紡糸口金パック
5の場合においては、フィルタ2を下側に位置させるよ
うに浸漬して処理する。また、細孔3が開口されている
紡糸口金11Fのような対向端面の一方だけを遮蔽する
ようにフィルタ2を装着した被処理物の場合においても
同様に浸漬して処理する。なお、いずれの場合において
も、被処理物は、流動層中に完全に没されるように浸漬
されるが、その際、直接浸漬だけでなく、流動媒体が通
過し得る網目状のパスゲットに収容して浸漬してもよい
。Next, the object to be treated that has been masked in this way, that is, the object to be treated is equipped with a filter 2 that can block passage of the fluid medium and allow only air gas to pass through, and is immersed in the fluidized bed for treatment. However, in this case, for example, in the case of the spinneret pack 5, the treatment is performed by immersing the spinneret pack 5 so that the filter 2 is positioned on the lower side. Further, in the case of a treated object such as a spinneret 11F in which pores 3 are opened and a filter 2 is attached so as to cover only one of the opposing end surfaces, the object is immersed and treated in the same manner. In either case, the object to be treated is immersed so that it is completely immersed in the fluidized bed, but at that time, it is not only immersed directly, but also immersed in a mesh-like pass get through which the fluid medium can pass. It may be stored and immersed.
而して、浸漬された紡糸口金バック5等の被処理物は流
動層によって加熱され、細孔3等に付着しているポリマ
ーが熱分解されて除去される。すなわち、紡糸口金パッ
ク5の場合においては、枦床の加熱されている流動媒体
及びエアーガスのうち、流動媒体はフィルタ2により通
過が阻止されエアーガスだけが通過し、バック出口6を
経て紡糸口金1の細孔3に流入し、更に、多孔板12、
口金フィルタ11、サンド10を経てバック入口13か
ら排出される。The immersed object to be processed, such as the spinneret bag 5, is heated by the fluidized bed, and the polymer adhering to the pores 3, etc. is thermally decomposed and removed. That is, in the case of the spinneret pack 5, out of the heated fluidizing medium and air gas in the spinneret bed, the fluidizing medium is blocked by the filter 2, and only the air gas passes through, and is released into the spinneret 1 through the back outlet 6. Flowing into the pores 3, the perforated plate 12,
It passes through the mouth filter 11 and the sand 10 and is discharged from the bag inlet 13.
その為、この加熱ガス単#流によって各構成部品に付着
されているポリマーが加熱されて分解除去される。なお
、除去に際し、紡糸口金1の細孔3が付着ポリマーで閉
塞されていると、最初にここの熱分解除去が行われ、貫
通されると、上段に配されている多孔板12の細孔へ流
入し、以下次々と熱分解除去することができる。Therefore, the polymer attached to each component is heated and decomposed and removed by this single flow of heated gas. In addition, during removal, if the pores 3 of the spinneret 1 are blocked by the attached polymer, thermal decomposition removal is performed first, and when the pores are penetrated, the pores of the perforated plate 12 arranged in the upper stage are removed. can be thermally decomposed and removed one after another.
このように、本発明においては、エアーカスだけを、し
かも、このガスを強制的に細孔3に流入させ得るように
しているのであり、これによって付着ポリマー等を迅速
、かつ良好に熱分解除去(空気酸化の効果が顕V)する
ことができる。なお、強制的に流入させ得るのは、流動
層は流動媒体を使用している関係上、層深さ方向の上下
位置で圧力差が生ずる為である。In this way, in the present invention, only the air waste, and moreover, this gas can be forced to flow into the pores 3, thereby quickly and effectively removing the adhering polymer, etc. by thermal decomposition ( The effect of air oxidation can be clearly seen. Note that the reason why the fluid can be forced to flow in is because a fluidized bed uses a fluidized medium, and a pressure difference occurs between the upper and lower positions in the bed depth direction.
[実施例1〕
第1図において示されているように、使用済みの紡糸口
金1に対し、ボルト・ナツト4を介して、直径が0.1
5amの細孔3(ポリエチレンテレフタレートが付着さ
れている)群が開口されている対向端画人々に当接させ
て各面を遮蔽するように2枚のフィルタ2を装着した。[Example 1] As shown in FIG. 1, a thread with a diameter of 0.1
Two filters 2 were attached so as to abut each side of the opposite ends, in which groups of pores 3 (to which polyethylene terephthalate was attached) of 5 am were opened, so as to shield each side.
なお、フィルタ2は、金網とセラミックシートとの組み
合せ体で構成したものを使用した。Note that the filter 2 used was a combination of a wire mesh and a ceramic sheet.
次に、これを網目状のバスケット中に、フィルタ2を水
平方向に位置させるようにセットし、予め520℃に加
熱した電熱加熱式流動層炉(流動媒体はアルミナを使用
し、と床にエアーガスを供給しなンに完全に没するよう
に浸漬し4時間処理した。その後、炉から取り出して冷
却させた後、検査したところ、全ての細孔3に付着物の
残留(除去不良)が見当らなかった。Next, this was set in a mesh basket so that the filter 2 was positioned horizontally, and an electrically heated fluidized bed furnace preheated to 520°C (alumina was used as the fluidized medium, and air gas was applied to the bed). It was then treated for 4 hours by being completely immersed in water without being supplied with water.After that, it was taken out from the furnace and cooled, and then inspected. There wasn't.
[比較例1]
2枚のフィルタ2を装着しないこと以外の条件は実施例
1と同一条件で処理したところ、細孔3群の約10%に
、アルミナの’t−1)(t#:去不良ンが発生してい
た。[Comparative Example 1] When processing was carried out under the same conditions as in Example 1 except that two filters 2 were not attached, about 10% of the 3 groups of pores were covered with alumina 't-1) (t#: There was an outbreak of malnutrition.
[実施例2]
第2図において示されているように、使用済みの紡糸口
金パック5の雌ユニオン8の下端に、直径が0.15+
mの細孔3(ナイロン6が付着されている)が開口され
ている紡糸口金1の一方の端面を、バック出口6を介在
させて遮蔽するように、治具7及びボルト・ナツト4を
介してフィルタ2を装着した。なお、フィルタ2はセラ
ミツフートで構成されたものを使用した。[Example 2] As shown in FIG. 2, a diameter of 0.15 +
A jig 7 and a bolt/nut 4 are used so as to cover one end surface of the spinneret 1 with the pores 3 (to which nylon 6 is attached) of 1. and installed filter 2. Note that the filter 2 used was one made of ceramic foot.
次に、これを網目状のバスゲット中に、フィルタ2を下
側に位置させるようにセットし、予め450℃に加熱し
た電熱加熱式流動層炉(流動媒体はアルミナを使用し、
r床にエアーガスを供給した)に完全に没するように浸
漬し4時間処理した。その後、炉から取り出して冷却さ
せた後、検査したところ、全ての細孔3に付着物の残留
(除去不良)が見当らなかった。なお、多孔板12、口
金フィルタ11も同様であった。Next, this was set in a mesh bathget with the filter 2 positioned at the bottom, and an electrically heated fluidized bed furnace preheated to 450°C (alumina was used as the fluidized medium).
(air gas was supplied to the bed) so as to be completely submerged and treated for 4 hours. Thereafter, when it was inspected after being taken out from the furnace and cooled, no deposits (defects in removal) were found in any of the pores 3. Note that the porous plate 12 and the cap filter 11 were also the same.
[比較例2コ
フィルタ2を装着しないで10時間処理したこと以外の
条件は実施例2と同一条件で処理したところ、細孔3群
の約75%にアルミナの詰り(除去不良)が発生してい
た。[Comparative Example 2] When the treatment was carried out under the same conditions as in Example 2 except that the treatment was carried out for 10 hours without attaching co-filter 2, approximately 75% of the 3 groups of pores were clogged with alumina (defective removal). Ta.
[発明の効果]
上述の如く、本発明によると、流動層炉による有機物除
去方法に間し、使用済みの紡糸口金パックや紡糸口金等
のような細孔を有する被処理物から付着有機高分子材を
除去する適した方法が得られる。[Effects of the Invention] As described above, according to the present invention, during a method for removing organic matter using a fluidized bed furnace, organic polymers attached from a workpiece having pores such as a used spinneret pack or spinneret can be removed. A suitable method of removing the material is obtained.
第1図は紡糸口金1に対するフィルタ2の装着態様を示
す正面図、第2図は紡糸口金パック5に対するフィルタ
2の装着態様を示す縦断面図である。
1・・・紡糸口金、2・・・フィルタ、3・・・細孔、
5・・・紡糸口金パック(被処理物)FIG. 1 is a front view showing how the filter 2 is attached to the spinneret 1, and FIG. 2 is a longitudinal sectional view showing how the filter 2 is attached to the spinneret pack 5. 1... Spinneret, 2... Filter, 3... Pore,
5... Spinneret pack (material to be processed)
Claims (1)
処理物を、加熱された流動層中に浸漬して前記有機高分
子材を熱分解除去する流動層炉による有機物除去方法に
おいて、流動媒体の通過を阻止してエアーガスだけを通
過させ得るフィルタを、前記細孔が開口されている少な
くとも一方の端面を遮蔽するように前記被処理物に装着
すると共にこれを、前記フィルタが下側に位置されるよ
うに前記流動層中に浸漬して処理することを特徴とする
流動層炉による有機物除去方法。1. In a method for removing organic matter using a fluidized bed furnace, the workpiece having an organic polymer material attached to the pierced pores is immersed in a heated fluidized bed to thermally decompose and remove the organic polymer material. A filter capable of blocking the passage of a fluid medium and allowing only air gas to pass through is attached to the object to be treated so as to cover at least one end face in which the pores are opened, and the filter is attached to A method for removing organic matter using a fluidized bed furnace, characterized in that the treatment is carried out by immersing it in the fluidized bed so as to be located on the side.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14914390A JPH06104924B2 (en) | 1990-06-06 | 1990-06-06 | Organic matter removal method by fluidized bed furnace |
| KR1019910008046A KR930005090B1 (en) | 1990-06-06 | 1991-05-17 | Method for removing organic substance by means of fluidized bed furnace |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP14914390A JPH06104924B2 (en) | 1990-06-06 | 1990-06-06 | Organic matter removal method by fluidized bed furnace |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0441704A true JPH0441704A (en) | 1992-02-12 |
| JPH06104924B2 JPH06104924B2 (en) | 1994-12-21 |
Family
ID=15468706
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP14914390A Expired - Lifetime JPH06104924B2 (en) | 1990-06-06 | 1990-06-06 | Organic matter removal method by fluidized bed furnace |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH06104924B2 (en) |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8984893B2 (en) | 2013-04-10 | 2015-03-24 | General Electric Company | System and method for augmenting gas turbine power output |
-
1990
- 1990-06-06 JP JP14914390A patent/JPH06104924B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH06104924B2 (en) | 1994-12-21 |
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