JPH0752004B2 - Organic matter removal method by fluidized bed furnace - Google Patents

Organic matter removal method by fluidized bed furnace

Info

Publication number
JPH0752004B2
JPH0752004B2 JP2153044A JP15304490A JPH0752004B2 JP H0752004 B2 JPH0752004 B2 JP H0752004B2 JP 2153044 A JP2153044 A JP 2153044A JP 15304490 A JP15304490 A JP 15304490A JP H0752004 B2 JPH0752004 B2 JP H0752004B2
Authority
JP
Japan
Prior art keywords
fluidized bed
container body
lid
container
pores
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 - Lifetime
Application number
JP2153044A
Other languages
Japanese (ja)
Other versions
JPH0445310A (en
Inventor
久郎 阿部
茂生 江藤
隆志 小國
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.)
Toray Engineering Co Ltd
Original Assignee
Toray Engineering Co Ltd
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 Toray Engineering Co Ltd filed Critical Toray Engineering Co Ltd
Priority to JP2153044A priority Critical patent/JPH0752004B2/en
Priority to KR1019910008046A priority patent/KR930005090B1/en
Publication of JPH0445310A publication Critical patent/JPH0445310A/en
Publication of JPH0752004B2 publication Critical patent/JPH0752004B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B7/00Cleaning by methods not provided for in a single other subclass or a single group in this subclass
    • B08B7/0064Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes
    • B08B7/0071Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes by heating
    • B08B7/0078Cleaning by methods not provided for in a single other subclass or a single group in this subclass by temperature changes by heating in a fluidized bed
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B08CLEANING
    • B08BCLEANING IN GENERAL; PREVENTION OF FOULING IN GENERAL
    • B08B2220/00Type of materials or objects being removed
    • B08B2220/04Polymers

Landscapes

  • Cleaning In General (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)
  • Spinning Methods And Devices For Manufacturing Artificial Fibers (AREA)

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。
TECHNICAL FIELD The present invention relates to a method for removing organic substances by 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 of thermally decomposing and removing an object to be treated, such as a used spinneret, which has an organic polymer material attached to its perforated pores, 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イル
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 is conventionally known to heat and remove by thermal decomposition an object to be treated to which an organic polymer material such as rubber, paint, oil and plastic adheres in a fluidized bed furnace. In Japanese Patent No. 282305, an object to be treated (specifically, a used spinneret, filter, etc.) having an organic polymer material attached to the penetrated pores is heated in a fluidized bed furnace to be thermally decomposed. It is disclosed to remove.

[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63−1357
07号公報において開示されているように、床のアルミ
ナ等の流動媒体が通過し得る網目のバスケットに収容し
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、詰りが発生し、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, according to such a conventional method, the object to be treated is directly immersed in the fluidized bed, or, for example, JP-A-63-1357.
As disclosed in JP 07, the fluid medium such as alumina in the bed is immersed in a mesh basket that allows the fluid medium such as alumina to pass therethrough. Flow in and block this hole, that is, clogging occurs, so that the inflow of air gas is blocked or hindered, and it is difficult to thermally decompose and remove the organic polymer material adhering thereto. It was

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0.05mm〜0.3mm〜であるから、被処理物の貫通
孔の直径が0.3mm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0.2mm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
イ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。
Incidentally, such a problem occurs in the case where the diameter of the fluidized medium such as alumina is generally 0.05 mm to 0.3 mm, and therefore the diameter of the through hole of the object to be treated is a relatively large hole such as 0.3 mm or more. Although not, it occurs in the case of pores having a diameter of 0.2 mm or less, therefore, for objects to be treated having pores such as spinneret and spinneret filter, the treatment in a fluidized bed furnace was hindered. .

そこで、例えば、特公昭42−18892号公報において開示
されているように、全周壁を、流動媒体の通過を阻止し
てガスだけを通過させ得る通気性壁で構成した容器を使
用し、これの中に被処理物を収容して流動層に浸漬して
処理すること等が試みられていたが、このようにして処
理しても、細孔へのガス流入が十分でなく、従って、流
動媒体による目詰りは防止し得ても、迅速な熱分解除去
が困難であった。
Therefore, for example, as disclosed in Japanese Examined Patent Publication (Kokoku) No. 42-18892, a container is used in which the entire peripheral wall is formed of an air permeable wall that prevents passage of a fluid medium and allows only gas to pass. It has been attempted to store the object to be treated therein and to immerse it in a fluidized bed for treatment, but even with such treatment, the gas flow into the pores is not sufficient, and therefore the fluidized medium is Although it is possible to prevent the clogging due to the heat treatment, it is difficult to quickly remove it by thermal decomposition.

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、非通気性材で構成され、か
つ蓋と容器本体底とに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イルタを装着した蓋付き容器
を用い、しかも、この容器の中に、細孔が蓋と容器本体
底とが対向される方向に配されるように被処理物を容器
本体底の内面に接触若しくは近接せしめて収容すると共
にこれを、容器本体底が下側に位置されるように流動層
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 pays attention to such a situation, and as a result of intensive studies from various directions to solve this, it is composed of a non-permeable material and prevents the passage of the fluid medium between the lid and the bottom of the main body of the container to prevent air gas. A container with a lid equipped with a filter that allows only the passage of the material to be processed is used, and the object to be treated is placed in the container so that the pores are arranged in the direction in which the lid and the container body bottom face each other. It has been found that they can be placed in contact with or close to the inner surface of the container, and can be treated by immersing the container in the fluidized bed so that the bottom of the container body is located on the lower side.

[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、被通気性材で構成され、かつ蓋と容器本体の底
とに流動媒体の通過を阻止してエアーガスだけを通過さ
せ得るフイルタを装着した蓋付き容器の中に、前記細孔
が前記蓋と前記容器本体の底とが対向される方向に配さ
れるように前記被処理物を前記容器本体の底内面の接触
若しくは近接せしめて収容すると共にこれを、前記容器
本体の底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] That is, in the method for removing an organic substance by a fluidized bed furnace according to the present invention, an object to be treated in which an organic polymer material is attached to perforated pores is heated in a fluidized bed. In an organic matter removal method by a fluidized bed furnace in which the organic polymer material is thermally decomposed and removed by immersion in an air-permeable material, which is made of an aerated material and prevents passage of a fluidized medium between the lid and the bottom of the container body, only air gas is used. In a container with a lid equipped with a filter capable of passing through, the object to be treated is placed on the bottom inner surface of the container body such that the pores are arranged in a direction in which the lid and the bottom of the container body are opposed to each other. Of the container body and the container body is housed in close proximity to the container body, and the container body is immersed in the fluidized bed so that the bottom of the container body is located on the lower side.

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、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, the organic polymer material means rubber, paint, oil,
The term “fluid medium” is a general term for organic substances such as plastics, and the term “fluid medium” is a generic term for refractory particles such as alumina filled in a predetermined amount in the bed. The fluid medium is uniformly supplied to the bed through a gas dispersion plate. 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きるが、これを加熱は、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。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℃〜500℃に、ま
た、ポリプロピレンの場合は425℃〜500℃、更に、シリ
コン樹脂の場合は520℃〜560℃に夫々加熱すればよい。
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、セラミック製以外のものであっ
てもよく、その形態も特定のものに限定されない。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パック、これの構成
部品である紡糸口金や口金フイルタ等が挙げられる。
As the fluidized bed furnace, various types of furnaces generally known in the past can be used, but the heating may be any of electric heating with a heater, gas heating with a burner, etc. Controlled at 400 ℃ -600 ℃. When treated at other high temperatures, when the most common alumina is used, it tends to adhere to the object to be treated, and when the object to be treated is a metal, the risk of damage to it increases. On the other hand, if the treatment is performed at a low temperature other than this, it becomes difficult to sufficiently decompose the organic polymer material. Although it is a standard temperature,
For example, in the case of polyvinyl chloride, it may be heated to 400 ° C to 500 ° C, in the case of polypropylene, it may be heated to 425 ° C to 500 ° C, and in the case of silicone resin, it may be heated to 520 ° C to 560 ° C.
Further, the object to be treated is one in which the organic polymer material is attached to the penetrating pores, but if it can withstand the treatment temperature, it may be other than metal or ceramic. Also, the form is not limited to a particular one. As a typical example of the object to be treated in which the organic polymer material is attached to the penetrating pores, a used spinneret pack, a spinneret and a spinner filter which are components of the spinneret pack, and the like can be mentioned.

更に、蓋付き容器は、耐熱性金属材等の非通気性材製の
蓋及び容器本体で構成され、かつ蓋及び容器本体の底
に、流動媒体の通過を阻止してエアーガスだけを通過さ
せ得るフイルタを装着するが、このフイルタは、耐熱性
のいかなるフイ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、フエルト状あるいは不織布状等の
各種のフイ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もよい。
Further, the lidded container is composed of a lid and a container body made of a non-breathable material such as a heat-resistant metal material, and can prevent passage of a fluidized medium and allow only air gas to pass through the bottom of the lid and the container body. A filter is attached, and this filter may be any heat-resistant filter, and various types of filters such as ceramic, stainless steel plate-like, felt-like or non-woven fabric-like can be used. For example, a plurality of materials may be used, such as a combination of a wire mesh and a ceramic sheet.

第1図において、これの一例を示すが、蓋付き容器1
は、耐熱性金属製の容器本体2の底に、セラミック製の
フイルタ3を固着していると共に耐熱性金属製の蓋4に
も同一のフイルタ3を固着しており、蓋4の下端は、容
器本体2の上端近くに固着されている耐熱性金属製の蓋
受け5によって形成されるシール部6内に挿入されてい
る。このシール部6に、流動層への浸漬時に流動媒体が
滞留してここをシールする。
An example of this is shown in FIG.
Has a ceramic filter 3 fixed to the bottom of the heat-resistant metal container body 2 and the same filter 3 fixed to the heat-resistant metal lid 4, and the lower end of the lid 4 is It is inserted in a seal portion 6 formed by a lid receiver 5 made of a heat-resistant metal fixed near the upper end of the container body 2. The fluid medium stays in this seal portion 6 when immersed in the fluidized bed, and seals the fluid medium.

同図中、7は被処理物である使用済みの紡糸口金パック
を示し、このパック7は容器本体2の底で支持、すなわ
ち、底内面と接触されて収容されている。なお、紡糸口
金パック7は、雌ユニオン8、雄ユニオン9、サンド1
0、口金フイルタ11、多孔板12及び紡糸口金13で構成さ
れ、かつパック入口14及びパック出口15を有している
が、口金フイルタ11、多孔板12及び紡糸口金13の貫通細
孔16には有機性高分子材が付着されている。
In the figure, reference numeral 7 denotes a used spinneret pack which is an object to be treated, and the pack 7 is supported by the bottom of the container body 2, that is, is brought into contact with the inner surface of the bottom and is accommodated therein. The spinneret pack 7 includes a female union 8, a male union 9 and a sand 1
0, the spinneret filter 11, the perforated plate 12 and the spinneret 13, and has a pack inlet 14 and a pack outlet 15, but in the spinneret 11 of the spinneret 11, the porous plate 12 and the spinneret 13. Organic polymer material is attached.

次に、このように被処理物を蓋付き容器に収容し、次い
でこれを、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7を収容した蓋付き容器1の場合
においては、容器本体2の底が下側に位置されるように
流動層中に浸漬して処理する。なお、蓋付き容器を懸吊
して直接、流動層中に浸漬してもよいが、一般には、流
動媒体が通過し得る網目状のバスケツトに収容して浸漬
すればよく、いずれの場合においても、流動層中に完全
に没されるように浸漬される。
Next, the object to be treated is housed in a container with a lid in this way, and then this is dipped in a fluidized bed for processing. At that time, for example, in the case of the container 1 with a lid containing the spinneret pack 7. In step 1, the container body 2 is immersed in a fluidized bed so that the bottom of the container body 2 is located on the lower side. The lidded container may be suspended and directly immersed in the fluidized bed, but in general, it may be immersed in a netted basket through which the fluid medium can pass, and in any case. , To be completely submerged in the fluidized bed.

而して、浸漬された紡糸口金パック等の被処理物は流動
層によって加熱され、細孔等に付着されれている有機高
分子材が熱分解されて除去される。すなわち、紡糸口金
パック7の場合においては、床の加熱されている流動
媒体及びエアーガスのうち、流動媒体は容器本体2に固
着されているフイルタ3により通過が阻止されてエアー
ガスだけが通過し、パック出口15を経て紡糸口金13の細
孔16に流入し、更に、多孔板12、口金フイルタ11、サン
ド10を経てパック入口14から排出され、更に、蓋4に固
着されているフイルタ3を通過して蓋付き容器1外(流
動層内)に排出される。
Thus, the object to be treated such as the immersed spinneret pack is heated by the fluidized bed, and the organic polymer material attached to the pores is thermally decomposed and removed. That is, in the case of the spinneret pack 7, out of the fluidized medium and the air gas heated on the floor, the fluidized medium is prevented from passing by the filter 3 fixed to the container body 2, and only the air gas passes through the pack. It flows into the fine holes 16 of the spinneret 13 through the outlet 15, is further discharged from the pack inlet 14 through the perforated plate 12, the spinner filter 11 and the sand 10, and further passes through the filter 3 fixed to the lid 4. And is discharged to the outside of the container with lid 1 (inside the fluidized bed).

その為、この加熱ガス単体流によって各構成部品に付着
されている有機高分子材が加熱されて分解除去される。
なお、除去に際し、紡糸口金13の細孔3が付着の有機高
分子材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 organic polymer material attached to each component is heated and decomposed and removed by this heating gas simple substance flow.
In addition, when the pores 3 of the spinneret 13 are clogged with the attached organic polymer material during the removal, the pyrolysis removal is first performed here, and when the pores are penetrated, the perforated plate arranged in the upper stage. It flows into 12 pores and can be removed by thermal decomposition one after another.

このように、本発明においては、エアーガスだけを、し
かも、このガスを強制的に細孔へ流入させ得るようにし
ているのであり、これによって付着されている有機高分
子材を迅速、かつ良好に熱分解除去(空気酸化の効果が
顕著)することができる。
As described above, in the present invention, only the air gas can be forced to flow into the pores, and the organic polymer material attached by this can be swiftly and satisfactorily. It can be removed by thermal decomposition (the effect of air oxidation is remarkable).

すなわち、詳述すると、非通気性材で構成され、かつ蓋
と容器本体の底とに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イルタを装着した蓋付き容器を
用いるから、エアーガスの流れ方向を、蓋と容器本体の
底とが対向される方向だけに特定化することができ、従
って、流動層への浸漬時においては、両フイルタ間の圧
力差△Pは、両フイルタ間の距離をL、流動媒体の密度
をρとした場合、△P=L×ρになるが、これは、特公
昭42−18892号公報において開示されているような、全
周壁を、流動媒体の通過を阻止してガスだけを通過させ
得る通気性壁で構成した容器を使用する場合のそれと比
較して一段と大きく(計算上においては2倍になる)、
その為、細孔が蓋と容器本体の底とが対向される方向
(上下方向)に配されるように被処理物を容器本体の底
内面に接触若しくは近接せしめて収容することにより、
細孔に対してエアーガスを強力に供給するすることがで
きてここに付着されている有機高分子材を迅速、かつ良
好に熱分解除去することができる。具体的には、処理時
間については、1/2〜1/5程度短縮することができる。
That is, to be more specific, since a container with a lid, which is made of a non-breathable material and has a lid and a bottom of the container body, which is equipped with a filter capable of passing only the air gas to prevent passage of the fluid medium, is used. The flow direction can be specified only in the direction in which the lid and the bottom of the container body are opposed to each other. Therefore, when immersed in the fluidized bed, the pressure difference ΔP between the filters is equal to the pressure difference between the filters. When the distance is L and the density of the fluid medium is ρ, ΔP = L × ρ, which means that the fluid medium passes through the entire peripheral wall as disclosed in Japanese Examined Patent Publication (Kokoku) No. 42-18892. Is much larger than that in the case of using a container made of a gas permeable wall that can block gas and allow only gas to pass (double in calculation),
Therefore, by accommodating the object to be processed in contact with or close to the inner surface of the bottom of the container body so that the pores are arranged in the direction in which the lid and the bottom of the container body are opposed (vertical direction),
Air gas can be strongly supplied to the pores, and the organic polymer material attached thereto can be rapidly and satisfactorily removed by thermal decomposition. Specifically, the processing time can be reduced by about 1/2 to 1/5.

加えて、流動層への浸漬時において、特公昭42−18892
号公報において開示されているような、全周壁を、流動
媒体の通過を阻止してガスだけを通過させ得る通気性壁
で構成した容器を用いる場合においては、容器中に多方
向からエアーガスが流入する為、本来、上下方向に流れ
るべきエアーガス流が乱されて局部的に流動媒体の良好
な流動化が妨げられ、従って、流動層の均一な温度制御
が困難になるのに対し、上述の蓋付き容器を使用する場
合においては、エアーガス流方向を常に上下方向に保つ
ことができるから、このような問題が発生するのを阻止
することができる。
In addition, when dipping in a fluidized bed,
In the case of using a container whose entire peripheral wall is formed of a gas permeable wall which prevents passage of a fluid medium and allows only gas to pass, air gas flows into the container from multiple directions as disclosed in Japanese Patent Publication No. Therefore, the air gas flow that should originally flow in the vertical direction is disturbed to locally hinder good fluidization of the fluidized medium, thus making it difficult to uniformly control the temperature of the fluidized bed. In the case of using the attached container, the air gas flow direction can always be maintained in the vertical direction, so that the occurrence of such a problem can be prevented.

なお、第2図において、蓋付き容器中に、容器本体2の
底内面に近接させて被処理物を収容する一例を示す。図
中、被処理物は鎖線で示され、容器本体2の底内面に固
着されているサポート17上に載置されている。サポート
17の背丈は出来る限り低いほうが好ましい。第1図中、
18は脚を示している。
Note that FIG. 2 shows an example of accommodating an object to be processed in a container with a lid in proximity to the inner surface of the bottom of the container body 2. In the figure, the object to be processed is shown by a chain line and is placed on a support 17 fixed to the inner surface of the bottom of the container body 2. support
It is preferable that the height of 17 is as low as possible. In Figure 1,
18 indicates a leg.

[実施例1] 第1図において示されているように、細孔16等にナイロ
ン6が付着している使用済みの紡糸口金パック7を蓋付
き容器1中に収容すると共にこれを網目状のバスケット
中に収容し、予め470℃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、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5時間処理し、次
いで炉内から取り出して放冷後、パック解体して検査し
たところ、紡糸口金13、多孔板12及び口金フイルタ11の
全ての細孔に付着物の残留(除去不良)が見当らなかっ
た。
[Example 1] As shown in Fig. 1, a used spinneret pack 7 having nylon 6 attached to pores 16 and the like was housed in a container 1 with a lid, and the spinneret pack 7 was reticulated. It is housed in a basket and immersed in an electrically heated fluidized bed furnace (alumina is used as the fluid medium and air gas is supplied to the floor) preheated to 470 ° C so that it is completely submerged and treated for 5 hours, then the furnace After taking out from the inside and allowing to cool, the pack was disassembled and inspected, and no residue (poor removal) of deposits was found in all the pores of the spinneret 13, the perforated plate 12, and the spinneret filter 11.

[実施例2] 容器本体2の底内面上に、ナイロン6が付着している紡
糸口金13を10個積み重ねて蓋付き容器1中に収容したこ
と及び6時間処理した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、実施例1と同一結果であった。
[Example 2] Conditions other than that 10 spinnerets 13 to which nylon 6 was attached were stacked on the inner surface of the bottom of the container body 2 and housed in the container with a lid 1 and treated for 6 hours. When treated under the same conditions as in Example 1, the same results as in Example 1 were obtained.

[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
去方法に関し、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, a method for removing organic matter by a fluidized bed furnace is provided, in which an attached organic polymer material is removed from a processed object having pores such as a used spinneret pack and a spinneret. A suitable method of removal is obtained.

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

第1図は被処理物である紡糸口金パック7を蓋付き容器
1中に収容した態様を示す縦断面図、第2図は容器本体
2の底内面に近接させて被処理物を収容する態様を示す
縦断面図である。 1……蓋付き容器、2……容器本体、3……フイルタ、
4……蓋、7……紡糸口金パック(被処理物)、13……
紡糸口金、16……細孔、17……サポート
FIG. 1 is a vertical cross-sectional view showing a mode in which a spinneret pack 7 which is an object to be processed is housed in a container 1 with a lid, and FIG. 2 is a mode in which an object to be processed is housed in close proximity to an inner bottom surface of a container body 2. FIG. 1 ... container with lid, 2 ... container body, 3 ... filter,
4 ... Lid, 7 ... Spinneret pack (workpiece), 13 ...
Spinneret, 16 ... Pore, 17 ... Support

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】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、非通気性材で構成され、かつ蓋と容器
本体の底とに流動媒体の通過を阻止してエアーガスだけ
を通過させ得るフイルタを装着した蓋付き容器の中に、
前記細孔が前記蓋と前記容器本体の底とが対向される方
向に配されるように前記被処理物を前記容器本体の底内
面に接触若しくは近接せしめて収容すると共にこれを、
前記容器本体の底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. An organic substance in a fluidized bed furnace in which an object to be treated having an organic polymer material attached to its perforated pores is immersed in a heated fluidized bed to thermally decompose and remove the organic polymer material. In the removal method, in a container with a lid, which is made of a non-air-permeable material, and in which a lid and a bottom of the container body are equipped with a filter that prevents passage of a fluid medium and allows only air gas to pass,
While accommodating the object to be processed in contact with or close to the inner surface of the bottom of the container body so that the pores are arranged in the direction in which the lid and the bottom of the container body are opposed to each other,
A method of removing organic substances by a fluidized bed furnace, which comprises immersing the container body in the fluidized bed so that the bottom of the container body is located on the lower side, and treating it.
JP2153044A 1990-06-06 1990-06-11 Organic matter removal method by fluidized bed furnace Expired - Lifetime JPH0752004B2 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP2153044A JPH0752004B2 (en) 1990-06-11 1990-06-11 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
JP2153044A JPH0752004B2 (en) 1990-06-11 1990-06-11 Organic matter removal method by fluidized bed furnace

Publications (2)

Publication Number Publication Date
JPH0445310A JPH0445310A (en) 1992-02-14
JPH0752004B2 true JPH0752004B2 (en) 1995-06-05

Family

ID=15553747

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2153044A Expired - Lifetime JPH0752004B2 (en) 1990-06-06 1990-06-11 Organic matter removal method by fluidized bed furnace

Country Status (1)

Country Link
JP (1) JPH0752004B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4659098B2 (en) 2009-02-13 2011-03-30 ファナック株式会社 Parallel link robot with posture change mechanism with 3 degrees of freedom
JP4653848B1 (en) * 2009-10-26 2011-03-16 ファナック株式会社 Parallel link robot
CN104941960A (en) * 2015-06-06 2015-09-30 安徽瀚洋节能科技有限公司 Granular-substance cooling and cleaning fluidized bed

Also Published As

Publication number Publication date
JPH0445310A (en) 1992-02-14

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