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JP3362891B2 - Adsorption / desorption type gas purifier - Google Patents
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JP3362891B2 - Adsorption / desorption type gas purifier - Google Patents

Adsorption / desorption type gas purifier

Info

Publication number
JP3362891B2
JP3362891B2 JP01136393A JP1136393A JP3362891B2 JP 3362891 B2 JP3362891 B2 JP 3362891B2 JP 01136393 A JP01136393 A JP 01136393A JP 1136393 A JP1136393 A JP 1136393A JP 3362891 B2 JP3362891 B2 JP 3362891B2
Authority
JP
Japan
Prior art keywords
belt
adsorption
suction
gas
desorption
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
JP01136393A
Other languages
Japanese (ja)
Other versions
JPH06218218A (en
Inventor
浩文 森本
雅夫 兵頭
信平 田中
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.)
Toyobo Co Ltd
Original Assignee
Toyobo 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 Toyobo Co Ltd filed Critical Toyobo Co Ltd
Priority to JP01136393A priority Critical patent/JP3362891B2/en
Publication of JPH06218218A publication Critical patent/JPH06218218A/en
Application granted granted Critical
Publication of JP3362891B2 publication Critical patent/JP3362891B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、塗装工場や半導体製造
工場などから排出される溶剤(トルエンやキシレンで代
表される有機溶剤等で30〜300ppm程度の濃度)
含有の排気を処理する、つまり、排気中の溶剤を除去処
理する技術のうち、最終処理量の減量を図るように溶剤
の濃度を濃縮する場合などに用いられる装置で、詳しく
は、通気性を備えた吸着ベルトを用い、溶剤などの除去
対象物を含有する処理対象ガスを、その吸着ベルト内を
厚さ方向で透過するように供給することによりその処理
対象ガス中の除去対象物を吸着ベルトに吸着させて処理
対象ガスを浄化する一方、前記の吸着ベルトに脱着用ガ
スを、その吸着ベルトの厚さ方向で透過するように供給
することにより吸着ベルトからそれに吸着されている除
去対象物を脱着して吸着ベルトの更新と除去対象物の濃
縮とを行う吸脱着式ガス浄化装置に関する。
The present invention relates to a solvent (concentration of about 30 to 300 ppm in an organic solvent represented by toluene or xylene) discharged from a coating factory, a semiconductor manufacturing factory or the like.
This is a device used to process the exhaust gas contained, that is, to remove the solvent in the exhaust gas and concentrate the concentration of the solvent so as to reduce the final treatment amount. By using the adsorption belt provided, a gas to be treated containing an object to be removed such as a solvent is supplied so as to pass through the adsorption belt in the thickness direction, so that the object to be eliminated in the gas to be treated is an adsorption belt. The desorption gas is supplied to the adsorption belt so that the desorption gas is permeated in the thickness direction of the adsorption belt to remove the object to be removed from the adsorption belt while purifying the gas to be treated by adsorbing the desorption gas to the adsorption belt. The present invention relates to an adsorption / desorption type gas purification device that desorbs and updates an adsorption belt and concentrates an object to be removed.

【0002】[0002]

【従来の技術】吸着ベルトを用いてガス浄化を行う本発
明対象の吸脱着式ガス浄化装置では、例えば、繊維状活
性炭をペーパ化し、段加工して多数のガス通路を有する
ハニカム状に成形し、それを枠に支持させたブロック状
の吸着体を用い、その吸着体のガス通路内に沿って処理
対象ガスを透過させることにより、繊維状活性炭が分散
するガス通路周囲壁に接触させて溶剤などの除去対象物
を吸着させるハニカムロータ式の吸脱着式ガス浄化装置
に比較して、次のような利点がある。つまり、ハニカム
ロータ式の吸脱着式ガス浄化装置による場合には、ガス
通路周囲壁に沿って処理対象ガスを流動させて吸着材に
接触させることで吸着させるため、吸着体の大きさの割
りには吸着材と処理対象ガスとの接触面積が小さくて、
吸着材と処理対象ガスとの接触効率が悪く、吸着体の大
きさの割りには処理能力が小さくてコストの高いものに
なる。しかも、吸着体を加熱して脱着する際、吸着体が
大きく、加えて、支持用の枠に熱を取られることによ
り、多量の熱量が必要であり、かつ、脱着後に吸着可能
状態に更新させる上で冷却を必要とすることもあり、ラ
ンニングコストが高くつく。これに対し、本発明が対象
とする上述の吸脱着式ガス浄化装置による場合には、吸
着ベルトを、繊維状活性炭のフェルトから構成したり、
或いは、活性炭を内部に分散させたフェルトから構成し
たりすることなどにより、吸着ベルトと処理対象ガスと
の接触面積を大きくして接触効率を優れたものにできる
割りには吸着ベルトの厚さを薄くでき、その結果、吸着
ベルトを加熱・冷却し易いものにできて、脱着のための
加熱に要するランニングコストが安くて済み、また、特
別な装置類を要することなく脱着後の吸着のための冷却
を行える。そのような利点を有する吸脱着式ガス浄化装
置として従来では、図28に示すように、吸着ベルト3
を第1のロールR1から繰り出すとともに、第2のロー
ルR2で巻き取り、その第1のロールR1から第2のロ
ールR2への移動途中で、処理対象ガスG1を供給して
溶剤などの除去対象物を吸着ベルト3に吸着させ、第2
のロールR2を収納する加熱室Hに脱着用ガスG2とし
ての加熱空気を供給して吸着ベルト3からそれの吸着さ
れている除去対象物を脱着する技術が知られている(例
えば特公昭53―9587号公報)。
2. Description of the Related Art In an adsorption / desorption type gas purifying apparatus according to the present invention for purifying gas using an adsorption belt, for example, fibrous activated carbon is made into paper and is step-processed to be formed into a honeycomb shape having a large number of gas passages. , A block-shaped adsorbent supporting it in a frame is used, and the gas to be treated is allowed to permeate along the gas passage of the adsorbent to bring it into contact with the peripheral wall of the gas passage in which the fibrous activated carbon is dispersed. Compared with a honeycomb rotor type adsorption / desorption type gas purifying apparatus that adsorbs an object to be removed such as the following, there are the following advantages. That is, in the case of the honeycomb rotor type adsorption / desorption type gas purifying apparatus, the gas to be treated is adsorbed by flowing along the gas passage peripheral wall and contacting the adsorbent, so that the size of the adsorbent is reduced. Has a small contact area between the adsorbent and the gas to be treated,
The contact efficiency between the adsorbent and the gas to be treated is poor, and the treatment capacity is small and the cost is high for the size of the adsorbent. Moreover, when the adsorbent is heated and desorbed, the adsorbent is large, and in addition, a large amount of heat is required because the supporting frame takes heat, and the adsorbable state is renewed after desorption. Cooling may be required at the top, and the running cost is high. On the other hand, in the case of the above-described adsorption / desorption type gas purifying apparatus targeted by the present invention, the adsorption belt is made of a fibrous activated carbon felt,
Alternatively, it is possible to increase the contact area between the adsorption belt and the gas to be treated and to improve the contact efficiency by, for example, composing a felt in which activated carbon is dispersed. It can be made thin, and as a result, the adsorption belt can be easily heated and cooled, and the running cost required for heating for desorption is low, and no special equipment is required for adsorption after desorption. Can be cooled. As a conventional adsorption / desorption type gas purifying apparatus having such an advantage, as shown in FIG.
Is unwound from the first roll R1 and wound up by the second roll R2, and in the middle of moving from the first roll R1 to the second roll R2, the processing target gas G1 is supplied to remove the solvent and the like. The object is sucked onto the suction belt 3 and the second
There is known a technique for supplying heated air as a desorption gas G2 to a heating chamber H accommodating the roll R2 of the roller R2 to desorb the adsorbed removal object from the adsorption belt 3 (for example, Japanese Patent Publication No. 53- 9587).

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来技術
によるときは、吸着ベルトを第1のロールから繰り出し
つつ第2のロールで巻き取ることで移動させて吸着ベル
トに除去対象物を吸着させるから、そのような移動時に
加熱室に加熱空気を並行して供給することにより、吸着
と同時に脱着を行えるものの、第2のロールに吸着ベル
トが最後まで巻き取られと、第1のロールに吸着ベル
トを巻き戻しする必要があって、処理形態が、吸脱着と
巻き戻しとを交互に繰り返す形態とならざるを得ない。
その結果、長時間の処理を行うには、第1のロールから
吸着ベルトの全部を繰り出しての1回の吸着作業時間を
長くしたり、或いは、複数の装置を設けて一方のものが
吸脱着しているときに他方のものが巻き戻しするように
交互に使用したりする必要がある。そして、前者の場合
には、吸着ベルトの巻き取り径が大きくなってそれに付
帯する装置の大型化、コストアップを招来するのみなら
ず、第2のロールに巻き取られた状態で加熱室で吸着ベ
ルトが除去対象物を吸着した状態で加熱される時間が長
くなることで、吸着ベルトの異常な昇温を招来すること
があって、それを防止するための構成が別途必要にな
り、装置の大型化、コストアップが不可避である。この
ことは、特に、高濃度の処理対象ガスを処理するために
吸着ベルトの移動速度を速くした場合に顕著である。他
方、後者の場合には、装置の数が増えて、やはり、装置
の大型化、コストアップが不可避である。本発明の目的
は、上記欠点を解消する点、つまり、たとえ前記従来例
の主使用領域濃度に比べて高濃度の処理対象ガスであっ
ても、装置の大型化、コストアップを招来することなく
長時間連続処理できるようにする点にある。
However, in the case of the above-mentioned prior art, the suction belt is moved by being unrolled from the first roll and taken up by the second roll so that the object to be removed is sucked onto the suction belt. by supplying in parallel heated air in the heating chamber in such a time of movement, but allows at the same time adsorption and desorption, the suction belt to the second roll that is taken either wound to the end, adsorbed on the first roll Since it is necessary to rewind the belt, the processing form must be a form in which adsorption / desorption and rewinding are alternately repeated.
As a result, in order to carry out a long-time treatment, one suction work time, in which the entire suction belt is unrolled from the first roll, is lengthened, or a plurality of devices are provided to absorb and desorb one. They need to be used alternately so that the other rewinds while they are doing. In the case of the former, not only the winding diameter of the suction belt becomes large and the device attached thereto becomes large and the cost increases, but also the suction belt sucks it in the heating chamber while being wound up on the second roll. If the belt is heated while adsorbing the object to be removed, it may cause an abnormal temperature rise of the adsorption belt, which requires a separate configuration to prevent it. Increasing size and increasing costs are inevitable. This is particularly remarkable when the moving speed of the adsorption belt is increased in order to process the high-concentration target gas. On the other hand, in the latter case, the number of devices increases, and it is inevitable that the devices will be large and the cost will be increased. An object of the present invention is to solve the above-mentioned drawback, that is, even if the gas to be treated has a higher concentration than the concentration in the main use region of the conventional example, it does not lead to an increase in the size and cost of the apparatus. The point is to enable continuous processing for a long time.

【0004】[0004]

【課題を解決するための手段】本発明の第1発明による
吸脱着式ガス浄化装置の特徴は、通気性を備えた吸着ベ
ルトを循環経路に沿うように巻きかけて回転移動させる
移動手段と、前記循環経路の設定箇所でその吸着ベルト
内を厚さ方向に透過するように処理対象ガスを給排する
吸着手段と、前記設定箇所とは異なる別の設定箇所で吸
着ベルト内を厚さ方向に透過するように脱着用ガスを給
排する脱着手段とを設け、前記吸着ベルトに、その吸着
ベルトの幅方向両端同士の相対接近を阻止する複数のベ
ルト幅規制体を回転移動方向に間隔を隔てて装着し、
記吸着ベルトのうちベルト幅規制体による幅規制箇所の
それぞれに、内周面側からベルト幅規制体に向かう通気
を阻止する通気制限帯状体を装着してある点にある。
The adsorption / desorption type gas purifying apparatus according to the first aspect of the present invention is characterized by a moving means for rotatively moving an adsorbing belt having air permeability by winding the adsorption belt along a circulation path. Adsorption means for supplying and exhausting the gas to be treated so as to pass through the adsorption belt in the thickness direction at the setting point of the circulation path, and in the adsorption belt in the thickness direction at another setting point different from the setting point. Desorption means for supplying and discharging desorption gas is provided so as to permeate, and the suction belt is provided with a plurality of belt width restricting bodies for preventing relative approach of both ends in the width direction of the suction belt at intervals in the rotational movement direction. Wear it in front
Of the suction belt,
For each, ventilation from the inner peripheral surface side toward the belt width regulation body
The point is that it is equipped with a ventilation-restricting strip .

【0005】本発明の第2発明による吸脱着式ガス浄化
装置の特徴は、上記第1発明において、前記吸着ベルト
の外周面に、ベルト幅方向に沿った姿勢でベルト幅の全
幅にわたる複数の切り込みをベルト回転移動方向に間隔
を隔てて形成し、 前記ベルト幅規制体を、前記切り込み
の形成箇所の夫々に配置して、前記通気制限帯状体を、
前記吸着ベルトにおける前記切り込みの形成箇所での通
気を防止する切り込み用の通気制限帯状体に兼用してあ
点にある。
A feature of the adsorption / desorption type gas purifying apparatus according to the second aspect of the present invention is that the adsorption belt according to the first aspect of the present invention.
On the outer peripheral surface of the
Spacing multiple notches across the width in the direction of belt rotation
The belt width regulating body, and the notch
Placed in each of the formation locations of the, the ventilation-limiting strip,
The passage at the location where the notch is formed in the suction belt
It is also used as a cut-out ventilation band to prevent air.
There to that point.

【0006】[0006]

【作用】上記本発明の第1発明によれば、吸着ベルトを
循環経路に沿って回転移動させるとともに、吸着手段と
脱着手段とを作動させることにより、処理対象ガスの供
給箇所と脱着用ガスの供給箇所とに交互に繰り返して吸
着ベルトを移動させて、吸着ベルトによる処理対象ガス
からの除去対象物の吸着と、その吸着した除去対象物の
脱着用ガスへの脱着とを行うことができるから、吸着ベ
ルトの回転移動と、その状態での処理対象ガスの供給及
び脱着用ガスの供給とを連続して行うことにより、吸脱
着を中断することなく連続して行うことができるととも
に、脱着時に吸着ベルトを過剰に加熱することがない。
しかも、吸着ベルトにはその循環経路に沿って確実円滑
に回転移動するために回転移動方向にテンションが掛け
られており、特に循環経路のうち上昇経路部分や下降経
路部分では自重自体がテンションとして作用し、そのよ
うなテンションは吸着ベルトの幅を狭めようとする力と
して作用するが、ベルト幅規制体を設けてあるから、テ
ンションや自重にかかわらず吸着ベルトの幅縮小方向へ
の変形を防止することができる。その結果、装置の小型
化・コンパクト化を進める上で、吸着部の処理対象ガス
供給口・処理ガス吸い込み口及び脱着部の脱着用ガス供
給口・濃縮ガス吸い込み口の幅を吸着ベルトの幅に匹敵
する大きさにしてあっても、吸着ベルトの幅内にそれら
の口を確実に対応位置させて、供給した処理対象ガスや
脱着用ガスが吸着ベルトを透過せずに吸着ベルト脇から
処理室内に漏出することを防止することができる。換言
すれば、吸着ベルトを最小限の幅に構成してあっても、
その吸着ベルトのほぼ全幅を吸脱着に確実に使用して効
率の良い吸脱着を行うことができる。
According to the first aspect of the present invention described above, the adsorption belt is rotated along the circulation path, and the adsorption means and the desorption means are actuated, so that the supply point of the gas to be treated and the desorption gas are removed. Since the adsorption belt can be moved alternately to the supply location, the adsorption target can be adsorbed by the adsorption belt and the adsorbed removal object can be desorbed to the desorption gas. By continuously rotating the adsorption belt and supplying the target gas and the desorption gas in that state, adsorption / desorption can be continuously performed without interruption, and at the time of desorption. Does not overheat the suction belt.
In addition, the suction belt is tensioned in the rotational movement direction in order to reliably and smoothly rotate along the circulation path, and the weight itself acts as the tension especially in the ascending path portion and the descending path portion of the circulation path. However, such a tension acts as a force for narrowing the width of the suction belt, but since a belt width regulator is provided, deformation of the suction belt in the width reduction direction is prevented regardless of the tension or its own weight. be able to. As a result, in advancing the downsizing and downsizing of the equipment, the width of the adsorption target processing gas supply port / processing gas suction port and the desorption unit desorption gas supply port / concentrated gas suction port should be the width of the adsorption belt. Even if they are of a comparable size, their openings are surely positioned within the width of the suction belt so that the gas to be treated and the desorption gas supplied do not pass through the suction belt and the side of the suction belt causes the processing chamber to move. It can be prevented from leaking out. In other words, even if the suction belt has a minimum width,
By using almost the entire width of the suction belt for adsorption and desorption, it is possible to perform efficient adsorption and desorption.

【0007】そしてまた、通気制限帯状体によりベルト
幅規制体への通気を阻止するようにしてあるから、ベル
ト幅規制体を設置しながらも、所期の吸脱着を阻害する
ことがない。つまり、ベルト幅規制体が脱着部を通過す
る際、高温の脱着用ガスにより加熱されると、その脱着
部通過後にそのベルト幅規制体によりその周囲の吸着ベ
ルト部分を加熱することになって吸着部での吸着性能の
低下を招来する一方、ベルト幅規制体に対する不要な加
熱で脱着用ガスのエネルギーを損失して吸着ベルトの加
熱効率の低下を招来する。ところが、第発明では、通
気制限帯状体により脱着部での脱着用ガスがベルト幅規
制体に接触することを防止してあるから、脱着用ガスで
ベルト幅規制体を不要に加熱することがなく、ベルト幅
規制体に起因した加熱ロス及び吸着性能の低下を防止す
ることができる。本発明の第2発明では、ベルト幅方向
に沿った姿勢でベルト幅の全幅にわたるように吸着ベル
トの外周面に形成した複数の切り込み夫々の開きによ
り、循環経路に沿った回転移動に伴う吸着ベルトの屈曲
変形を容易にして吸着ベルトの回転移動を円滑にする
が、ベルト幅規制体を切り込み形成箇所の夫々に配置し
て、内周面側からベルト幅規制体に向かう通気を阻止す
るベルト幅規制体用の通気制限 帯状体を、吸着ベルトに
おける切り込みの形成箇所での通気を防止する切り込み
用の通気制限帯状体に兼用するから、ベルト幅規制体を
切り込み形成箇所とは異なる箇所に配置して、切り込み
用の通気制限帯状体をベルト幅規制体用の通気制限帯状
体とは別個に設けるのに比べ、通気制限体の必要付設数
を少なくすることができる。
Further , since the ventilation restricting belt prevents the ventilation of the belt width regulating member, the desired adsorption / desorption can be prevented even when the belt width regulating member is installed. In other words, when the belt width regulator passes through the desorption section and is heated by the high temperature desorption gas, the belt width regulation body heats the adsorption belt portion around it after passing through the desorption section. On the other hand, the suction performance of the suction belt is deteriorated, but the heating of the suction belt is deteriorated due to the loss of energy of the desorption gas due to unnecessary heating of the belt width regulator. However, in the first invention, since the desorption gas at the desorption portion is prevented from coming into contact with the belt width regulation body by the ventilation restriction strip, the desorption gas can heat the belt width regulation body unnecessarily. Therefore, it is possible to prevent the heating loss and the deterioration of the adsorption performance due to the belt width regulator. In the second aspect of the present invention, the belt width direction
The suction bell so that it covers the entire width of the belt.
By opening each of the notches formed on the outer peripheral surface of the
The bending of the suction belt due to the rotational movement along the circulation path.
Deformation is facilitated and the suction belt is rotated smoothly.
However, place the belt width regulator at each of the cut formation points.
To prevent ventilation from the inner peripheral surface toward the belt width regulator.
Ventilation-restricted strips for belt width control
Notch that prevents ventilation at the notch formation point
Since it is also used as a ventilation restriction strip,
Place it in a place different from the notch formation point and make a notch
Ventilation-restricting strips for belts
The number of required ventilation restrictors compared to installing them separately from the body
Can be reduced.

【0008】[0008]

【発明の効果】従って、本発明によれば、吸着ベルトを
連続的に回転移動させて、装置の大型化及びコストアッ
プを招来することなく、高濃度の除去対象物含有ガスを
長時間連続処理でき、しかも、所期の吸脱着性能をも同
時に向上できるようになった。特に、請求項2のように
すれば、より一層、コストを低減することができる。
Therefore, according to the present invention, the adsorption belt is continuously rotatably moved to continuously process the gas containing a high concentration of the object to be removed for a long time without increasing the size and cost of the apparatus. In addition, the desired adsorption / desorption performance can be improved at the same time. Particularly, according to claim 2, the cost can be further reduced.

【0009】[0009]

【実施例】溶剤処理設備への適用例を示す。溶剤処理設
備は、図1に示すように、除去対象物の一例である溶剤
を含有する処理対象ガスG1を濃縮する前処理用の吸脱
着式ガス浄化装置1と、そこからの濃縮ガスg2中の溶
剤を除去する最終処理装置2とからなる。前記吸脱着式
ガス浄化装置1は、図2、図3に示すように、輪状(無
端帯状)に形成された通気性の吸着ベルト3と、その吸
着ベルト3を循環経路に沿うように巻きかけて回転移動
させる移動手段とを処理室4内に設け、吸着手段と、脱
着手段と、分離手段と、位置規制手段とを設けて構成さ
れている。前記循環経路は、上昇経路部と、それの上端
に連なる水平の上側経路部と、その終端に連なる下降経
路部と、その下降経路部から上昇経路部への水平な下側
経路部とからなる。前記吸着ベルト3は、活性炭を吸着
材として、常温で処理対象ガスG1中の溶剤を吸着し、
加熱(100〜130度)により脱着するものである。
具体的には、図4に示すように、繊維状活性炭をフェル
ト状に加工した通気性のマット3Aを設け、そのマット
3Aの内周面に、耐熱性(130℃程度に耐えられる性
能)及び通気性の不織布等からなる無端帯状の補強用の
基材3Bを重ねて固定し、マット3Aの外周面に耐熱性
(130℃程度に耐えられる性能)及び通気性の不織布
等からなる保護層3Cを重ねて固定し、ベルト幅規制体
3Dと第1及び第2の通気制限帯状体3E,3Fとを設
けて構成されている。前記マット3Aの実数値例を挙げ
ると、活性炭繊維の径は10〜20μm、厚さは10
20mm、目付け量は600g/m程度である。な
お、図では判りやすくする上で基材3B及び保護層3C
を厚く示してあるが、基材3B及び保護層3Cの実際の
厚さは非常に薄いものである。そして、吸着ベルト3の
外周面には、ベルト幅方向に沿った姿勢で、ベルト幅の
全幅にわたる幅及び基材3Bの外周面に達する深さを有
する複数の切り込み5が回転移動方向に間隔を隔てて形
成されている。つまり、マット3Aは、回転移動方向で
複数個に単位体3aに分割構成されており、保護層3C
は、単位体3aの回転移動方向の端面を覆うように折り
曲げ形成されている。もって、吸着ベルト3は、その各
部位がコーナー部を通過する際、回転移動方向で隣合う
マット3Aの外周面側同士が切り込み5を開くように回
転移動方向で相互に離間することにより外周面引張力
を吸収するように構成されている。前記ベルト幅規制体
3Dは、吸着ベルト3の幅方向両端同士の相対接近を阻
止するものであって、金属材料や合成樹脂(耐熱性を有
し、熱変形や熱膨張を起こしにくいものが好ましい。)
などからなり、丸棒状や角棒状、板状に形成されてい
る。なお、図では丸棒状のものを示してあるが、大き
形状は、可及的にガスの通過を阻害しないように設定
する。そして、吸着ベルト3の切り込み形成箇所のそれ
ぞれに配置されている。前記第1の通気制限帯状体3E
は、非通気性のもので、前記吸着ベルト3の切り込み形
成箇所の内周面それぞれにその吸着ベルト3の全幅にわ
たる状態に装着されて切り込み形成箇所での通気を防止
する切り込み用のものであり、耐熱性の合成樹脂シート
から構成されている。前記第2の通気制限帯状体3F
は、非通気性で、前記吸着ベルト3のうちベルト幅規制
体設置箇所の内周面それぞれにその吸着ベルト3の全幅
にわたる状態に装着されて内周面側からそれら各ベルト
幅規制体3Dに向かう通気を阻止するベルト幅規制体用
ものであり、前記第1の通気制限帯状体3Eと兼用構
成されている。前記移動手段は、前記吸着ベルト3をそ
の外周面に重ねた状態で前記の循環経路に沿って回転移
動することにより吸着ベルト3を循環経路に沿って移送
するネットコンベア6であり、コンベアネット6Aと、
それを移動案内するガイド機構と、駆動ローラ6Bと、
テンション機構とからなる。前記コンベアネット6A
は、図5〜図7に示すように、回転移動方向に沿う姿勢
の平帯状の縦ネット材6aと幅方向に沿う姿勢の横ネッ
ト材6bとを編織したネットを設け、このネットの幅方
向の両端に補強材6cを取り付けて構成されている。前
記縦ネット材6aは、抗張力が大きいアラミド樹脂製で
あり、横ネット材6bは、テフロン樹脂製である。そし
て、コンベアネット6Aの厚さtは、良好な可撓性を得
る上で0.5〜1mm程度としてあり、目の大きさは5
mm×5mm程度、ネット材の幅は1mm程度である。
前記ガイド機構は、循環経路のコーナ部に配置したガイ
ドローラ7と、上昇経路部、下降経路部、上側経路部の
それぞれに配置したガイドレール8とからなる。ガイド
レール8は、図6、図7に示すように、コンベアネット
6Aの補強ベルト6cに固定したピン9に係合すること
により、コンベアネット6Aの幅方向の位置ずれを規制
するガイド溝8aと、コンベアネット6Aの内周面に摺
動してそのコンベアネット6Aの厚さ方向での振れを防
止するガイド面8bとを備え、ガイド面8bのうち移動
上手側の端部分8cは、ガイドレール8の端面にピン9
が引っ掛からないようにするため傾斜姿勢に形成されて
いる。前記駆動ローラ6Bは、ガイドローラ7の一つを
モータ10などのアクチュエータに連動させることで構
成されており、その周面は、コンベアネット6Aの目に
入り込んで係合するようにゴム等の軟質材11から構成
されている。前記テンション機構は、循環経路のうち下
側経路部において、テンションローラ12でコンベアネ
ット6Aを上方に持ち上げてそのコンベアネット6Aに
テンションを付与するものであり、このテンション付与
の作用でコンベアネット6Aが吸着ベルト3から上方に
分離して吸着ベルト3が自由状態となる。つまり、テン
ション機構が、コンベアネット6Aを吸着ベルト3から
上方に分離して吸着ベルト3を自由状態にする前記分離
手段を構成している。前記吸着手段は、前記処理対象ガ
スG1中の溶剤を吸着ベルト3により吸着除去する手段
であって、前記循環経路のうち上昇経路部と下降経路部
とで前記吸着ベルト3内を厚さ方向に透過するように処
理対象ガスG1を外周面側から供給するとともに、その
吸着ベルト3で溶剤を吸着除去されて内周面側に透過し
てきた処理ガスg1を排出するように構成されている。
詳述すると、図8にも示すように、前記処理室4を形成
する外装ケース13のうち上昇経路部と下降経路部とに
対応する箇所に形成の処理対象ガス供給口14aを介し
て処理室4内のうち外装ケース13と吸着ベルト3の外
周面との間に処理対象ガスG1を供給するための吸着用
供給ダクト14と、吸着ベルト3で囲まれた箇所で吸着
ベルト3の内周面に近接位置する処理ガス吸い込み口1
5aを介して吸着ベルト3内から透過した処理ガスg1
を吸引して処理室4外に排出するための処理ガス排出ダ
クト15とを設け、処理対象ガスG1の供給ファンF1
と処理ガスg1の排気ファンf1とを設けて構成されて
いる。つまり、処理対象ガス供給口14a及び処理ガス
吸い込み口15aとから、処理室4内に位置して吸着ベ
ルト3に対して処理対象ガスG1を給排する吸着部が構
成されている。前記脱着手段は、前記吸着ベルト3に吸
着された溶剤を高温の脱着用ガスG2により脱着する手
段であって、前記循環経路のうち上側経路部で前記吸着
ベルト3内を厚さ方向に透過するように脱着用ガスG2
を内周面側から供給するとともに、吸着ベルト3から溶
剤を脱着して外周面側に透過してきた濃縮ガスg2を排
出するように構成されている。詳述すると、図8にも示
すように、処理室4内のうち前記吸着ベルト3で囲まれ
た箇所でその吸着ベルト3の内周面に近接位置する脱着
用ガス供給口16aを介して吸着ベルト3に内周面側か
ら脱着用ガスG2を供給するための脱着用供給ダクト1
6と、処理室4内のうちその脱着用供給ダクト16の脱
着用ガス供給口16aに吸着ベルト3を挟んで対向する
箇所で吸着ベルト3の外周面に近接位置する濃縮ガス吸
い込み口17aを介して吸着ベルト3を透過した濃縮ガ
スg2を処理室4外に排出するための濃縮ガス排出ダク
ト17とを設け、脱着用ガスG2の供給ファンF2と濃
縮ガスg2の排気ファンf2とを設けて構成されてい
る。つまり、脱着用ガス供給口16a及び濃縮ガス吸い
込み口17aとから、処理室4内に位置して吸着ベルト
3に対して脱着用ガスG2を給排する脱着部が構成され
ている。前記濃縮ガス排出ダクト17は濃縮ガスg2を
前記最終処理装置2に供給する排出ダクトである。そし
て、脱着用ガス供給口16aをその外郭が濃縮ガス吸い
込み口17aの内側に位置する大きさに構成し、供給口
16aと吸着ベルト3とに隙間d(2mm〜3mm程度
で、供給口を吸着ベルト3に接触させない寸法。)を形
成し、かつ、脱着用供給ダクト16内の圧力P3を外装
ケース13内の圧力、つまり、図8に示すように、吸着
用供給ダクト14内の圧力P1よりも高くして、脱着用
供給ダクト16から隙間dを介して若干の脱着用ガスG
2が処理室4内に排出されるようにすることにより、吸
着ベルト3に供給される脱着用ガスG2中に処理室4内
の冷たいガスが混入しないように構成してある。前記の
ように、隙間dから脱着用ガスG2を排出するための制
御は、脱着用供給ダクト16内の圧力P3と処理室4内
の圧力P1とを検出し、その差圧が設定値となるように
脱着用ガスG2の供給圧や濃縮ガスg2の吸引圧を制御
しても良いが、上記のように吸着部と脱着部とを配置し
た場合の処理室4内には、脱着用ガスG2の排出量に応
じて温度成層が形成される傾向にあるなど、処理室4内
の温度状況と脱着用ガスG2の排出量とを関係付けるこ
とができる場合には、温度に基づいて制御しても良い。
因みに、吸着用供給ダクト14の圧力P1と処理ガス排
出ダクト15の圧力P2と脱着用供給ダクト16の圧力
P3と濃縮ガス排出ダクト17の圧力P4とは、P2<
P1<P3、P4<P3の関係にある。また、吸着手段
及び脱着手段には、ガス吸引に伴う吸着ベルト3の変形
を防止する吸引変形防止手段が設けられている。吸着用
の吸引変形防止手段は、図9、図10に示すように、処
理ガス吸い込み口15aの全周において吸引に抗してコ
ンベアネット6A及び吸着ベルト3を支持するシール用
の支持板18と、支持体19とからなる。前記支持板1
8は、処理ガス吸い込み口15aの回転移動方向の前後
両端に位置するとともに、回転移動方向に設定長さLを
有する前後の支持部18Aと、処理ガス吸い込み口15
aの左右方向(幅方向)の両端に位置するとともに、左
右方向に設定長さLを有する左右の支持部18Bとから
なる。前記支持体19は、コンベアフレーム19Aの回
転移動方向に間隔を隔てた複数箇所それぞれに、コンベ
アネット6Aを支持するローラ19Bを、吸着ベルト3
の幅方向に沿った水平軸芯周りに自由回転自在に装着し
て構成されている。つまり、複数のローラ19Bがコン
ベアネット6Aの回転移動に伴い水平軸芯周りに回転す
ることにより、摺動抵抗なくコンベアネット6Aを支持
するように構成されている。前記脱着用の吸引変形防止
手段は、図11、図12に示すように、濃縮ガス吸い込
み口17aの全周において吸引に抗して吸着ベルト3を
支持するシール用の支持板20と、支持体21とからな
る。前記支持板20は、濃縮ガス吸い込み口17aの回
転移動方向の前後両端に位置するとともに、回転移動方
向に設定長さLを有する前後の支持部20Aと、濃縮ガ
ス吸い込み口17aの左右方向の両端に位置するととも
に、左右方向に設定長さLを有する左右の支持部20B
とからなる。前記支持体21は、コンベアフレーム21
Aの回転移動方向に間隔を隔てた複数箇所それぞれに、
吸着ベルト3を支持するローラ21Bを、吸着ベルト3
の幅方向に沿った水平軸芯周りに自由回転自在に装着し
て構成されている。つまり、複数のローラ21Bが吸着
ベルト3の回転移動に伴い水平軸芯周りに回転すること
により、摺動抵抗なく吸着ベルト3を支持するように構
成されている。なお、この脱着用の吸引変形防止手段の
ローラ21Bは、吸着用の吸引変形防止手段のローラ1
9Bよりも大径に構成してある。また、前記吸着用のロ
ーラ19B及び脱着用のローラ21Bの配置手段の例と
して、図9、図11に示すように、吸着ベルト3の幅に
相当する長さの長尺物を一列の状態に配置したものを示
したが、図13の(イ)(ロ)に示すように、短尺物を
幅方向に複数列の状態に設けても良い。この場合、
(イ)に示すように幅方向で隣合うものが回転移動方向
の同一箇所に位置する状態に配置する形態及び(ロ)に
示すように千鳥の状態に配置する形態のいずれを採用し
ても良い。前記位置規制手段は、図14に示すように、
下側経路部の左右両脇に、コンベアネット6Aから下方
に離脱して自由状態にある吸着ベルト3の左右の端縁、
詳しくは、ベルト幅規制体3Dのうち幅方向外方に突出
する長手方向の端部に摺動することにより、吸着ベルト
3の幅方向での位置を規制する規制板22を設けて構成
されている。
[Example] An example of application to a solvent treatment facility is shown. As shown in FIG. 1, the solvent treatment equipment includes a pretreatment adsorption / desorption gas purification device 1 for concentrating a treatment target gas G1 containing a solvent, which is an example of an object to be removed, and a concentrated gas g2 therefrom. And the final processing device 2 for removing the solvent. As shown in FIGS. 2 and 3, the adsorption / desorption type gas purification device 1 includes a breathable adsorption belt 3 formed in a ring shape (endless belt shape) and the adsorption belt 3 wound around along a circulation path. A moving means for rotating and moving is provided in the processing chamber 4, and an adsorbing means, a desorbing means, a separating means, and a position regulating means are provided. The circulation path includes an ascending path portion, a horizontal upper path portion connected to the upper end thereof, a descending path portion continuing to the end thereof, and a horizontal lower path portion from the descending path portion to the ascending path portion. . The adsorption belt 3 uses activated carbon as an adsorbent to adsorb the solvent in the gas G1 to be treated at room temperature,
It is desorbed by heating (100 to 130 degrees).
Specifically, as shown in FIG. 4, a breathable mat 3A obtained by processing fibrous activated carbon into a felt shape is provided, and the inner peripheral surface of the mat 3A has heat resistance (performance capable of withstanding about 130 ° C.) and An endless belt-like reinforcing base material 3B made of a breathable non-woven fabric is overlaid and fixed, and a protective layer 3C made of a non-woven fabric having heat resistance (performance up to about 130 ° C.) and breathable on the outer peripheral surface of the mat 3A. Are overlapped and fixed, and a belt width restricting body 3D and first and second ventilation limiting strips 3E and 3F are provided. To give an example of real numerical values of the mat 3A, the activated carbon fiber has a diameter of 10 to 20 μm and a thickness of 10 to
20 mm, and the basis weight is about 600 g / m 2 . In addition, in order to make it easy to understand in the figure, the base material 3B and the protective layer 3C
Although it is shown thick, the actual thickness of the base material 3B and the protective layer 3C is very thin. Then, on the outer peripheral surface of the suction belt 3, a plurality of notches 5 having a width over the entire width of the belt and a depth reaching the outer peripheral surface of the base material 3B are arranged along the belt width direction at intervals in the rotational movement direction. It is formed separately. That is, the mat 3A is divided into a plurality of unit bodies 3a in the rotational movement direction, and the protective layer 3C is formed.
Is bent and formed so as to cover the end face of the unit body 3a in the rotational movement direction. Therefore, the suction belt 3 is separated from each other in the rotational movement direction so that the outer peripheral surface sides of the mats 3A adjacent to each other in the rotational movement direction open the notches 5 when the respective parts pass through the corner portions. It is configured to absorb the tensile force of. The belt width restricting body 3D is for preventing the widthwise ends of the suction belt 3 from relatively approaching each other, and is preferably made of a metal material or synthetic resin (having heat resistance and being resistant to thermal deformation and thermal expansion). .)
Etc., and is formed into a round bar shape, a square bar shape, or a plate shape. Incidentally, there is shown what the round bar in the drawing, the size
The shape and shape should be set so as not to obstruct the passage of gas as much as possible. Then, the suction belt 3 is arranged at each of the cut forming portions. The first ventilation limiting strip 3E
Is of a non-breathable, the is intended for the cut to prevent the venting of the inner peripheral surface thereof is mounted in a state over the entire width of the suction belt 3, each notch area where the cut area where the suction belt 3 , A heat-resistant synthetic resin sheet. The second ventilation limiting strip 3F
Is non-breathable, and is attached to each inner peripheral surface of the belt width regulating body installation portion of the adsorption belt 3 so as to cover the entire width of the adsorption belt 3, and the belt width regulating bodies 3D are attached from the inner peripheral surface side. For belt width regulators that prevent airflow toward
Is of, is also used configured with said first vent restriction strip 3E. The moving means is a net conveyor 6 that transfers the suction belt 3 along the circulation path by rotating and moving the suction belt 3 along the circulation path in a state where the suction belt 3 is overlapped on the outer peripheral surface thereof. When,
A guide mechanism for moving and guiding it, a drive roller 6B,
It consists of a tension mechanism. The conveyor net 6A
As shown in FIGS. 5 to 7, a net formed by weaving a flat belt-shaped vertical net member 6a in a posture along the rotational movement direction and a horizontal net member 6b in a posture along the width direction is provided. The reinforcing material 6c is attached to both ends of the. The vertical net member 6a is made of aramid resin having high tensile strength, and the horizontal net member 6b is made of Teflon resin. The thickness t of the conveyor net 6A is about 0.5 to 1 mm in order to obtain good flexibility, and the size of the mesh is 5
mm × 5 mm, the width of the net material is about 1 mm.
The guide mechanism includes guide rollers 7 arranged at the corners of the circulation path, and guide rails 8 arranged on the ascending path portion, the descending path portion, and the upper path portion. As shown in FIGS. 6 and 7, the guide rail 8 engages with the pin 9 fixed to the reinforcing belt 6c of the conveyor net 6A, thereby forming a guide groove 8a for restricting the positional deviation of the conveyor net 6A in the width direction. , A guide surface 8b that slides on the inner peripheral surface of the conveyor net 6A to prevent the conveyor net 6A from swinging in the thickness direction, and the end portion 8c of the guide surface 8b on the movable side is a guide rail. Pin 9 on the end face of 8
It is formed in an inclined posture so that it is not caught. The drive roller 6B is configured by interlocking one of the guide rollers 7 with an actuator such as a motor 10, and the peripheral surface thereof is made of a soft material such as rubber so that it enters the eye of the conveyor net 6A and engages with it. It is composed of a material 11. In the lower side path portion of the circulation path, the tension mechanism lifts the conveyor net 6A upward by the tension roller 12 to apply a tension to the conveyor net 6A. The suction belt 3 is separated upward from the suction belt 3 and the suction belt 3 is in a free state. That is, the tension mechanism constitutes the separating means that separates the conveyor net 6A from the suction belt 3 upward so that the suction belt 3 is in a free state. The adsorbing means is means for adsorbing and removing the solvent in the gas to be treated G1 by the adsorbing belt 3, and the ascending path portion and the descending path portion of the circulation path are arranged in the adsorbing belt 3 in the thickness direction. The processing target gas G1 is supplied from the outer peripheral surface side so as to permeate, and the processing gas g1 which has absorbed and removed the solvent by the adsorption belt 3 and has permeated to the inner peripheral surface side is discharged.
More specifically, as shown in FIG. 8, the processing chamber is provided via a processing target gas supply port 14a formed in a portion corresponding to an ascending path portion and a descending path portion in the outer case 13 forming the processing chamber 4. 4, a suction supply duct 14 for supplying the processing target gas G1 between the outer case 13 and the outer peripheral surface of the suction belt 3, and an inner peripheral surface of the suction belt 3 in a portion surrounded by the suction belt 3. Gas inlet 1 close to
Processing gas g1 that has permeated from the inside of the adsorption belt 3 via 5a
And a processing gas discharge duct 15 for sucking and discharging the processing gas to the outside of the processing chamber 4, and a supply fan F1 for supplying the processing target gas G1.
And an exhaust fan f1 for processing gas g1. In other words, the processing target gas supply port 14a and the processing gas suction port 15a form an adsorption unit located in the processing chamber 4 for supplying and discharging the processing target gas G1 to and from the adsorption belt 3. The desorption means is a means for desorbing the solvent adsorbed on the adsorption belt 3 with a high-temperature desorption gas G2, and permeates the adsorption belt 3 in the thickness direction at the upper side path portion of the circulation path. Desorption gas G2
Is supplied from the inner peripheral surface side, and the concentrated gas g2 that has desorbed the solvent from the adsorption belt 3 and has permeated to the outer peripheral surface side is discharged. More specifically, as shown in FIG. 8, suction is performed through a desorption gas supply port 16a located in the processing chamber 4 and surrounded by the suction belt 3 in the vicinity of the inner peripheral surface of the suction belt 3. Desorption supply duct 1 for supplying the desorption gas G2 to the belt 3 from the inner peripheral surface side
6 and the concentrated gas suction port 17a located near the outer peripheral surface of the adsorption belt 3 at a position facing the desorption gas supply port 16a of the desorption supply duct 16 in the processing chamber 4 with the adsorption belt 3 interposed therebetween. A concentrated gas discharge duct 17 for discharging the concentrated gas g2 that has passed through the adsorption belt 3 to the outside of the processing chamber 4, and a supply fan F2 for the desorption gas G2 and an exhaust fan f2 for the concentrated gas g2. Has been done. That is, the desorption gas supply port 16a and the concentrated gas suction port 17a constitute a desorption unit located in the processing chamber 4 for supplying and discharging the desorption gas G2 to and from the adsorption belt 3. The concentrated gas exhaust duct 17 is an exhaust duct for supplying the concentrated gas g2 to the final processing device 2. Then, the desorption gas supply port 16a is configured to have a size such that the outer contour thereof is located inside the concentrated gas suction port 17a, and the supply port 16a and the suction belt 3 adsorb the supply port with a gap d (about 2 mm to 3 mm). (A size not to contact the belt 3) and the pressure P3 in the detachable supply duct 16 is greater than the pressure in the outer case 13, that is, the pressure P1 in the suction supply duct 14 as shown in FIG. Also, the desorption gas G is slightly increased from the desorption supply duct 16 through the gap d.
By allowing 2 to be discharged into the processing chamber 4, the desorption gas G2 supplied to the adsorption belt 3 is configured so that the cold gas in the processing chamber 4 does not mix. As described above, the control for discharging the desorption gas G2 from the gap d detects the pressure P3 in the desorption supply duct 16 and the pressure P1 in the processing chamber 4, and the differential pressure thereof becomes the set value. Although the supply pressure of the desorption gas G2 and the suction pressure of the concentrated gas g2 may be controlled as described above, the desorption gas G2 is provided in the processing chamber 4 when the adsorption unit and the desorption unit are arranged as described above. When it is possible to correlate the temperature inside the processing chamber 4 with the discharge amount of the desorption gas G2, such as when the temperature stratification tends to be formed according to the discharge amount of the Is also good.
By the way, the pressure P1 of the adsorption supply duct 14, the pressure P2 of the processing gas discharge duct 15, the pressure P3 of the desorption supply duct 16 and the pressure P4 of the concentrated gas discharge duct 17 are P2 <
There is a relationship of P1 <P3 and P4 <P3. Further, the suction means and the desorption means are provided with suction deformation preventing means for preventing deformation of the suction belt 3 due to gas suction. As shown in FIGS. 9 and 10, the suction-deformation preventing means for suction includes a support plate 18 for sealing which supports the conveyor net 6A and the suction belt 3 against suction over the entire circumference of the processing gas suction port 15a. , Support 19. The support plate 1
8 are located at the front and rear ends of the processing gas suction port 15a in the rotational movement direction, and the front and rear support portions 18A having a set length L in the rotational movement direction and the processing gas suction port 15 are provided.
It is composed of left and right support portions 18B located at both ends in the left-right direction (width direction) of a and having a set length L in the left-right direction. The support body 19 includes rollers 19B for supporting the conveyor net 6A at a plurality of positions spaced apart in the rotational movement direction of the conveyor frame 19A, and the suction belt 3
It is configured to be freely rotatable around a horizontal axis along the width direction of the. That is, the plurality of rollers 19B are configured to support the conveyor net 6A without sliding resistance by rotating around the horizontal axis along with the rotational movement of the conveyor net 6A. As shown in FIGS. 11 and 12, the suction-deformation preventing means for detachment includes a support plate 20 for sealing which supports the suction belt 3 against the suction in the entire circumference of the concentrated gas suction port 17a, and a support member. 21 and. The support plates 20 are located at the front and rear ends of the concentrated gas suction port 17a in the rotational movement direction, and the front and rear support portions 20A having a set length L in the rotational movement direction and the left and right ends of the concentrated gas suction port 17a. And the left and right support portions 20B having a set length L in the left-right direction.
Consists of. The support 21 is a conveyor frame 21.
At each of a plurality of locations spaced in the rotational movement direction of A,
The roller 21B supporting the suction belt 3 is attached to the suction belt 3
It is configured to be freely rotatable around a horizontal axis along the width direction of the. That is, the plurality of rollers 21B are configured to support the suction belt 3 without sliding resistance by rotating around the horizontal axis along with the rotation movement of the suction belt 3. The roller 21B of the suction deformation preventing means for detachment is the roller 1B of the suction deformation preventing means for suction.
It has a larger diameter than 9B. In addition, as an example of the arrangement means of the suction roller 19B and the detaching roller 21B, as shown in FIGS. 9 and 11, a long object having a length corresponding to the width of the suction belt 3 is arranged in a line. Although the arrangement is shown, as shown in FIGS. 13A and 13B, the short objects may be provided in a plurality of rows in the width direction. in this case,
Whichever of the form shown in (a) is arranged in a state where adjacent ones in the width direction are located at the same position in the rotational movement direction and the form is arranged in zigzag as shown in (b) good. As shown in FIG. 14, the position regulating means is
On both the left and right sides of the lower path portion, the left and right edges of the suction belt 3 which is free from the conveyor net 6A,
More specifically, a regulation plate 22 that regulates the position of the suction belt 3 in the width direction by sliding on the end portion of the belt width regulation body 3D that projects outward in the width direction is provided. There is.

【0010】〔別実施例〕 上記実施例では、循環経路として、上昇経路部と下降経
路部と上側経路部と下側経路部とを備えたものを示した
が、循環経路の形状は適宜変更自在である。上記実施例
では、吸着を循環経路の2箇所で、脱着を1箇所で行う
ものを示したが、それらの数は不問である。上記実施例
では、切り込み形成箇所にベルト幅規制体3Dを配置し
たが、図15に示すように、切り込み形成箇所とは異な
る箇所にベルト幅規制体3Dを配置してもよい。この場
合、第1の通気制限帯状体3Eと第2の通気制限帯状体
3Fとを別個に設置することになる。上記実施例では、
マット3Aを、回転移動方向で隣合うもの同士が相互に
分離する単位体3aから構成したが、図16に示すよう
に、切り込み5をマット3Aの厚さ方向の中間までの深
さのものにして、マット3Aがそれ自身で一連に一体化
していても良い。上記実施例では、切り込み5付きの吸
着ベルト3を示したが、吸着ベルト3は、図17に示す
ように、マット3Aの幅方向両端に「コ」の字形の補強
材3Gを取り付け、幅方向中間の内外周に、平板状の補
強材3Hをマット3Aを挟む状態に取り付けて、対引張
性能を向上し、かつ、マット3Aの幅方向の端部を保護
するように構成したものや、図18に示すように、マッ
ト3Aの内周面に、補強用のガラス繊維製のネット3J
を取り付けたものであっても良い。前記コンベアネット
6Aを次のように構成しても良い。図19、図20に示
すように、循環径路に沿って回転移動自在なフレームに
上記実施例で示したネットを取り付ける。前記フレーム
は、2本の補強兼用の駆動ベルト6dを幅方向に間隔を
隔てて配置し、回転移動方向に間隔を隔てた箇所それぞ
れでそれら駆動ベルト6d同士を繋いでそれらの間隔を
保持するとともに駆動ベルト6d同士の回転方向の位置
づれを抑制する補強材6eを設けて構成されている。6
fは、補強材6e及びネットを厚さ方向から挟む状態で
ネットに取り付けた内外一対の非通気性のシートであ
り、これは、補強材6eとネット特に縦ネット材6aと
を固定連結して一体化するとともに、補強材6eにガス
が接触しないようにその補強材6eへの通気を制限する
ものである。前記駆動ベルト6dは、Vベルトやタイミ
ングベルトなどであり、従って、このコンベアネット6
Aを駆動並びに移動案内するものは、V溝付きのプーリ
ーや歯付きのプーリーなどである。また、補強材6e
は、金属材料や合成樹脂材料などからなり、平板状や棒
状(丸や角などの形状)のものであり、曲げ剛性に優れ
たものであることが好ましい。上記コンベアネット6A
の場合、回転移動する際、補強材6eそれぞれによりネ
ットがその全幅で引っ張られ、その結果、ネットを全幅
で均等に回転移動させやすく、かつ、ネットには補強材
6e間分のテンションのみが作用し、ネットの寿命が長
くなる。また、上記のコンベアネット6Aを次のように
しても良い。すなわち、図21、図22に示すように、
補強材6eの両端を外方に延長する。この場合、コンベ
アネット6Aの駆動構成として、コンベアネット6Aの
両脇に駆動チェーンCHを設け、この駆動チェーンCH
に、補強材6eの延長端部6gに連結、或いは、係合す
る連係部Lを装備させて、チェーン駆動によりコンベア
ネット6Aを駆動する形式を採用することができる。上
記実施例では、吸着用の吸引変形防止手段の支持体19
として、コンベアフレーム19Aとローラ19Bとから
なるいわゆるローラコンベアを示したが、この支持体1
9としては、図23に示すように、処理ガス吸い込み口
15a内の幅方向に間隔を隔てた複数箇所それぞれにV
ベルトやタイミングベルト(滑り止め用の歯付きベル
ト)で代表されるベルトBをプーリP間に巻き掛けたベ
ルトコンベアの複数を、吸着ベルト3の回転移動に伴い
追従回動しながらそのベルトBで吸着ベルト3を支持す
るように配置して構成されたものであっても良い。上記
実施例では、脱着用の吸引変形防止手段の支持体21と
して、コンベアフレーム21Aとローラ21Bとからな
るいわゆるローラコンベアを示したが、この支持体21
としては、図24に示すように、ローラR間にコンベア
ネットNを巻き掛けたネットコンベアを、吸着ベルト3
の回転移動に伴い追従回動しながらそのコンベアネット
Nで吸着ベルト3を支持するように配置して構成された
ものであっても良い。前記吸着用の吸引変形防止手段の
支持体19を脱着用の吸引変形防止手段の支持体21と
して用いたり、反対に、脱着用の吸引変形防止手段の支
持体21を吸着用の吸引変形防止手段の支持体19とし
て用いたりする。上記実施例では、吸着ベルト3とし
て、繊維状活性炭をフェルト状に加工したものを示した
が、吸着ベルト3としては、(イ)図25に示すよう
に、通気性及び可撓性を有する不織布などの基材Bの表
面に粒状活性炭cを接着により担持させたものや、
(ロ)図26に示すように、通気性及び可撓性を有する
不織布などの基材Bの複数を重ね、それら基材B間に粒
状活性炭や繊維活性炭・粉状活性炭cを挟み込んだも
の、(ハ)図27に示すように、通気性及び可撓性を有
する不織布などの基材B中に粒状活性炭cを分散させて
保持させたものであってもよい。これら構造の吸着ベ
ルト3では、基材B自体に吸着能が要求されず、ベルト
として使用できる機能が基材B備わっていればよいか
ら、基材Bの材質選定の自由度が高く、その結果、耐久
性に優れたものを得やすい。なお、図では、判りやすく
するために、活性炭を大きく誇張して示してある。上記
実施例及び別の実施例では、吸着物質として活性炭を示
したが、吸着物質は、天然や合成のゼオライトであって
もよい。この場合、ゼオライトが不燃性であるため、脱
着用ガスG2による加熱に起因した吸着物質の損傷を考
える必要がなく、脱着用ガスG2の温度設定の自由度を
上げることができる。
[Other Embodiments] In the above embodiment, the circulation path is provided with the ascending path portion, the descending path portion, the upper side path portion and the lower side path portion, but the shape of the circulation path is appropriately changed. You are free. In the above embodiment, the adsorption is performed at two points in the circulation path and the desorption is performed at one point, but the number of them is not critical. In the above-described embodiment, the belt width restricting body 3D is arranged at the cut forming portion, but as shown in FIG. 15, the belt width restricting body 3D may be arranged at a position different from the cut forming portion. In this case, the first ventilation limiting strip 3E and the second ventilation limiting strip 3F are installed separately. In the above example,
The mat 3A is composed of the unit bodies 3a in which adjacent ones are separated from each other in the rotational movement direction. As shown in FIG. 16, the notch 5 has a depth up to the middle of the mat 3A in the thickness direction. Then, the mat 3A may be integrated in series by itself. Although the suction belt 3 with the notch 5 is shown in the above embodiment, as shown in FIG. 17, the suction belt 3 is provided with the U-shaped reinforcing members 3G at both ends in the width direction of the mat 3A. A flat reinforcing member 3H is attached to the inner and outer circumferences of the middle so as to sandwich the mat 3A, thereby improving anti-pullability and protecting the widthwise end of the mat 3A. As shown in FIG. 18, a reinforcing glass fiber net 3J is formed on the inner peripheral surface of the mat 3A.
May be attached. The conveyor net 6A may be configured as follows. As shown in FIGS. 19 and 20, the net shown in the above embodiment is attached to a frame that is rotatable and movable along the circulation path. In the frame, two reinforcing driving belts 6d are arranged at intervals in the width direction, and the driving belts 6d are connected to each other at positions separated in the rotational movement direction to maintain the distance. The reinforcing member 6e is provided so as to prevent the drive belts 6d from being misaligned in the rotational direction. 6
f is a pair of inner and outer non-breathable sheets attached to the net while sandwiching the reinforcing member 6e and the net from the thickness direction. This is a sheet for fixing and connecting the reinforcing member 6e and the net, especially the vertical net member 6a. In addition to being integrated, ventilation is restricted to the reinforcing material 6e so that gas does not come into contact with the reinforcing material 6e. The drive belt 6d is a V-belt, a timing belt, or the like.
The one that drives and moves and guides A is a pulley with a V groove or a pulley with teeth. Also, the reinforcing material 6e
Is made of a metal material, a synthetic resin material, or the like, has a flat plate shape or a rod shape (shape such as a circle or a corner), and preferably has excellent bending rigidity. The above conveyor net 6A
In the case of, the nets are pulled by their respective reinforcing members 6e at their full widths when rotating, and as a result, the nets are easily rotated and moved uniformly over their entire widths, and only the tension between the reinforcing members 6e acts on the nets. However, the life of the net is extended. Further, the above conveyor net 6A may be configured as follows. That is, as shown in FIGS. 21 and 22,
Both ends of the reinforcing member 6e are extended outward. In this case, as a drive configuration of the conveyor net 6A, drive chains CH are provided on both sides of the conveyor net 6A.
In addition, it is possible to adopt a type in which a linking portion L that is connected to or engages with the extended end portion 6g of the reinforcing member 6e is provided and the conveyor net 6A is driven by chain drive. In the above embodiment, the support 19 of the suction deformation preventing means for suction is used.
A so-called roller conveyor including a conveyor frame 19A and rollers 19B is shown as the above.
As shown in FIG. 23, the reference numeral 9 indicates V at each of a plurality of positions in the processing gas suction port 15a spaced in the width direction.
A plurality of belt conveyors in which a belt B typified by a belt or a timing belt (a toothed belt for anti-slip) is wound between pulleys P are rotated by the suction belt 3 while following the rotation of the suction belt 3. It may be arranged so as to support the suction belt 3. In the above-described embodiment, the so-called roller conveyor including the conveyor frame 21A and the rollers 21B is shown as the support 21 of the suction-deformation preventing means for detachment.
As shown in FIG. 24, as shown in FIG.
The suction belt 3 may be arranged so as to be supported by the conveyor net N while following the rotation of the suction belt 3. The support 19 of the suction deformation preventing means for suction is used as the support 21 of the suction deformation preventing means for detachment, or conversely, the support 21 of the suction deformation preventing means for detachment is used for suction attraction deformation prevention. It is also used as the support 19 of In the above-described embodiment, the adsorption belt 3 is made of fibrous activated carbon processed into a felt shape. However, as the adsorption belt 3, as shown in (a) FIG. 25, a nonwoven fabric having air permeability and flexibility. Such as the one in which granular activated carbon c is carried on the surface of the base material B by adhesion,
(B) As shown in FIG. 26, a plurality of base materials B such as nonwoven fabric having air permeability and flexibility are stacked, and granular activated carbon or fiber activated carbon / powdered activated carbon c is sandwiched between the base materials B, (C) As shown in FIG. 27, a granular activated carbon c may be dispersed and held in a base material B such as a breathable and flexible nonwoven fabric. In the suction belt 3 of these structures is not required adsorption ability to the substrate B itself, because functions that can be used as a belt has only to come to the substrate B, high degree of freedom in material selection of the base material B, As a result, it is easy to obtain a product with excellent durability. In the figure, the activated carbon is greatly exaggerated for easy understanding. Although activated carbon was shown as the adsorbing material in the above-mentioned embodiment and another embodiment, the adsorbing material may be natural or synthetic zeolite. In this case, since the zeolite is nonflammable, it is not necessary to consider damage to the adsorbed substance due to heating by the desorption gas G2, and the degree of freedom in setting the temperature of the desorption gas G2 can be increased.

【0011】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configuration of the accompanying drawings by the entry.

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

【図1】溶剤処理設備の概念構成を示すブロック図FIG. 1 is a block diagram showing a conceptual configuration of a solvent treatment facility.

【図2】吸脱着式ガス処理装置の切り欠き正面図FIG. 2 is a cutaway front view of the adsorption / desorption type gas treatment device.

【図3】吸脱着式ガス処理装置の切り欠き側面図FIG. 3 is a cutaway side view of the adsorption / desorption type gas treatment device.

【図4】要部の拡大断面図FIG. 4 is an enlarged sectional view of a main part.

【図5】コンベアネット要部の平面図FIG. 5 is a plan view of the main part of the conveyor net.

【図6】コンベアネットとガイド機構との関係を示す要
部の横断正面図
FIG. 6 is a cross-sectional front view of essential parts showing the relationship between the conveyor net and the guide mechanism.

【図7】コンベアネットとガイド機構との関係を示す要
部の縦断正面図
FIG. 7 is a vertical cross-sectional front view of essential parts showing the relationship between the conveyor net and the guide mechanism.

【図8】吸脱着ガス処理装置の概略構成図FIG. 8 is a schematic configuration diagram of an adsorption / desorption gas treatment device.

【図9】吸着部を示す要部の正面図FIG. 9 is a front view of a main portion showing a suction unit.

【図10】吸着部を示す要部の拡大縦断正面図FIG. 10 is an enlarged vertical sectional front view of an essential part showing a suction part.

【図11】脱着部を示す要部の平面図FIG. 11 is a plan view of an essential part showing a detachable part.

【図12】脱着部を示す要部の拡大縦断正面図FIG. 12 is an enlarged vertical sectional front view of an essential part showing a detachable part.

【図13】吸着用・脱着用の吸引変形防止手段の支持体
の他の配置例を示す平面図
FIG. 13 is a plan view showing another arrangement example of the support of the suction deformation preventing means for suction / desorption.

【図14】位置規制手段を示す要部の拡大側面図FIG. 14 is an enlarged side view of a main part showing a position regulating means.

【図15】別の実施例を示す吸着ベルト要部縦断面図FIG. 15 is a vertical cross-sectional view of a main part of a suction belt showing another embodiment.

【図16】別の実施例を示す吸着ベルト要部縦断面図FIG. 16 is a vertical cross-sectional view of a main part of a suction belt showing another embodiment.

【図17】別の実施例を示す吸着ベルトの斜視図FIG. 17 is a perspective view of a suction belt showing another embodiment.

【図18】別の実施例を示す吸着ベルトの斜視図FIG. 18 is a perspective view of a suction belt showing another embodiment.

【図19】別の実施例を示す要部の横断面図FIG. 19 is a transverse cross-sectional view of the main part showing another embodiment.

【図20】別の実施例を示す要部の縦断面図FIG. 20 is a vertical cross-sectional view of a main part showing another embodiment.

【図21】別の実施例を示す要部の横断面図FIG. 21 is a cross-sectional view of the main part showing another embodiment.

【図22】別の実施例を示す要部の縦断面図FIG. 22 is a vertical cross-sectional view of a main part showing another embodiment.

【図23】別の実施例を示す吸着部の斜視図FIG. 23 is a perspective view of a suction unit showing another embodiment.

【図24】別の実施例を示す脱着部の斜視図FIG. 24 is a perspective view of a detachable portion showing another embodiment.

【図25】別の実施例を示す吸着ベルト要部(マット)
の拡大断面図
FIG. 25 is a main part (mat) of a suction belt showing another embodiment.
Enlarged sectional view of

【図26】別の実施例を示す吸着ベルト要部(マット)
の拡大断面図
FIG. 26 is a main part (mat) of a suction belt showing another embodiment.
Enlarged sectional view of

【図27】別の実施例を示す吸着ベルト要部(マット)
の拡大断面図
FIG. 27 is a main part (mat) of a suction belt showing another embodiment.
Enlarged sectional view of

【図28】従来例を示す断面図FIG. 28 is a sectional view showing a conventional example.

【符号の説明】[Explanation of symbols]

3 吸着ベルト G1 処理対象ガス G2 脱着用ガス 3D ベルト幅規制体 3F 通気制限帯状体 切り込み 3E 通気制限帯状体 3 Adsorption belt G1 Gas to be treated G2 Desorption gas 3D Belt width regulator 3F Ventilation limiting strip 5 Cut 3E Ventilation limiting strip

フロントページの続き (72)発明者 兵頭 雅夫 東京都新宿区西新宿2丁目6番1号 株 式会社大氣社内 (72)発明者 田中 信平 東京都新宿区西新宿2丁目6番1号 株 式会社大氣社内 (56)参考文献 特開 昭51−32482(JP,A) 特開 昭50−147480(JP,A) (58)調査した分野(Int.Cl.7,DB名) B01D 53/06 B01D 53/34 Front page continuation (72) Inventor Masao Hyodo 2-6-1, Nishishinjuku, Shinjuku-ku, Tokyo Incorporated company Oki (72) Innovator Shinpei Tanaka 2-6-1 Nishishinjuku, Shinjuku-ku, Tokyo Stock company In-house (56) Reference JP-A-51-32482 (JP, A) JP-A-50-147480 (JP, A) (58) Fields investigated (Int.Cl. 7 , DB name) B01D 53/06 B01D 53/34

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 通気性を備えた吸着ベルト(3)を循環
経路に沿うように巻きかけて回転移動させる移動手段
と、前記循環経路の設定箇所でその吸着ベルト(3)内
を厚さ方向に透過するように処理対象ガス(G1)を給
排する吸着手段と、前記設定箇所とは異なる別の設定箇
所で吸着ベルト(3)内を厚さ方向に透過するように脱
着用ガス(G2)を給排する脱着手段とを設け、前記吸
着ベルト(3)に、その吸着ベルト(3)の幅方向両端
同士の相対接近を阻止する複数のベルト幅規制体(3
D)を回転移動方向に間隔を隔てて装着し、 前記吸着ベルト(3)のうちベルト幅規制体(3D)に
よる幅規制箇所のそれぞれに、内周面側からベルト幅規
制体(3D)に向かう通気を阻止する通気制限帯状体
(3F)を装着してある 吸脱着式ガス浄化装置。
1. A moving means for winding and rotating a suction belt (3) having air permeability along a circulation path, and a suction belt (3) inside the suction belt (3) in a thickness direction at a setting position of the circulation path. Adsorption means for supplying / discharging the gas to be treated (G1) so as to permeate through the adsorption belt (3) and a desorption gas (G2) so as to permeate through the adsorption belt (3) in the thickness direction at a different setting position from the setting position A plurality of belt width regulators (3) for preventing the suction belt (3) from relatively approaching each other in the width direction of the suction belt (3).
D) is mounted at intervals in the rotational movement direction, and is attached to the belt width regulating body (3D) of the suction belt (3).
The belt width regulation from the inner peripheral surface side
Ventilation-restricting strips that prevent ventilation toward the control body (3D)
Adsorption / desorption type gas purifier equipped with (3F) .
【請求項2】 前記吸着ベルト(3)の外周面に、ベル
ト幅方向に沿った姿勢でベルト幅の全幅にわたる複数の
切り込み(5)をベルト回転移動方向に間隔を隔てて形
成し、 前記ベルト幅規制体(3D)を、前記切り込み(5)の
形成箇所の夫々に配置して、前記通気制限帯状体(3
F)を、前記吸着ベルト(3)における前記切り込み
(5)の形成箇所での通気を防止する切り込み用の通気
制限帯状体(3E)に兼用してある 請求項1記載の吸脱
着式ガス浄化装置。
2. A bell is provided on the outer peripheral surface of the suction belt (3).
In the posture along the width direction,
Form notches (5) at intervals in the direction of belt rotation movement.
The belt width regulating body (3D) of the notch (5)
The ventilation limiting strips (3) are arranged at the respective formation locations.
F) the notch in the suction belt (3)
Ventilation for notches that prevent ventilation at the formation location of (5)
The adsorption / desorption gas purifier according to claim 1, which is also used as the restriction strip (3E) .
JP01136393A 1993-01-27 1993-01-27 Adsorption / desorption type gas purifier Expired - Lifetime JP3362891B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP01136393A JP3362891B2 (en) 1993-01-27 1993-01-27 Adsorption / desorption type gas purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP01136393A JP3362891B2 (en) 1993-01-27 1993-01-27 Adsorption / desorption type gas purifier

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP2002239324A Division JP3563068B2 (en) 2002-08-20 2002-08-20 Adsorption / desorption type gas purifier

Publications (2)

Publication Number Publication Date
JPH06218218A JPH06218218A (en) 1994-08-09
JP3362891B2 true JP3362891B2 (en) 2003-01-07

Family

ID=11775949

Family Applications (1)

Application Number Title Priority Date Filing Date
JP01136393A Expired - Lifetime JP3362891B2 (en) 1993-01-27 1993-01-27 Adsorption / desorption type gas purifier

Country Status (1)

Country Link
JP (1) JP3362891B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5966646B2 (en) * 2012-06-13 2016-08-10 東洋紡株式会社 Solvent treatment equipment

Also Published As

Publication number Publication date
JPH06218218A (en) 1994-08-09

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