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JP3448548B2 - How to remove high boiling substances - Google Patents

How to remove high boiling substances

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Publication number
JP3448548B2
JP3448548B2 JP2000141537A JP2000141537A JP3448548B2 JP 3448548 B2 JP3448548 B2 JP 3448548B2 JP 2000141537 A JP2000141537 A JP 2000141537A JP 2000141537 A JP2000141537 A JP 2000141537A JP 3448548 B2 JP3448548 B2 JP 3448548B2
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JP
Japan
Prior art keywords
gas
heat storage
temperature
treated
storage chamber
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
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JP2000141537A
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Japanese (ja)
Other versions
JP2001324121A (en
Inventor
祐三 田中
球夫 渡辺
保 村上
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.)
Chugai Ro Co Ltd
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Chugai Ro Co Ltd
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Priority to JP2000141537A priority Critical patent/JP3448548B2/en
Publication of JP2001324121A publication Critical patent/JP2001324121A/en
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Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、蓄熱式脱臭装置を
構成する切換弁および蓄熱室、ならびに、蓄熱式脱臭装
置に連通する配管内に付着したヤニ、タール等の高沸点
物質の除去方法に関するものである。 【0002】 【従来の技術】従来、たとえば、塗装乾燥炉から排出さ
れる悪臭成分である高沸点物質等を含む排ガス(被処理
ガス)は、熱効率が良い等の理由から蓄熱式脱臭装置に
供給して脱臭処理されている。 【0003】この蓄熱式脱臭装置は、たとえば、複数の
蓄熱室と、バーナ、ヒータ等の加熱手段を備えた燃焼室
とからなる脱臭炉本体と、切換弁装置とからなる。 【0004】そして、塗装乾燥炉からの被処理ガスは、
途中、被処理ガス供給管内で降温し、たとえば約50℃
となって切換弁装置を通り、先の工程で昇温した蓄熱室
を通ることにより昇温したのち燃焼室に至り、ここで加
熱手段、たとえばバーナにより約820℃に加熱されて
高沸点物質が燃焼して脱臭処理される。 【0005】一方、前記のようにして脱臭処理された高
温の処理ガスは、被処理ガスが供給されていない他の蓄
熱室を通過する際、該蓄熱室の蓄熱体に熱を奪われて降
温し、切換弁装置を通ってガス排出管から炉外へ排出さ
れる。なお、前記処理ガスの排出は排気ファンにより行
われる。 【0006】そして、前記各蓄熱室への被処理ガスの供
給と処理ガスの排出とを前記切換弁装置をタイマにより
所定時間毎に切換えて交互に実施するとともに、前記工
程を繰り返して行うことにより被処理ガス中の高沸点物
質を脱臭処理する。なお、前記切換弁装置の切換えは、
タイマによる切換えだけでなく、蓄熱室出口における処
理ガスの温度が所定温度(たとえば100℃)になる毎
に切換えるようにしてもよい。 【0007】塗装乾燥炉の1日の操業が終了すると、バ
ーナを停止するとともに、被処理ガス供給管の供給弁を
閉じ、被処理ガス供給管に高沸点物質を含まない清浄ガ
ス(空気)を切換弁装置を介して前述のように蓄熱式脱
臭装置に供給・排気して燃焼室内を約250℃以下と
し、火炎検知装置を保護するようにしている。 【0008】ところで、前記タール等の高沸点物質は凝
縮温度が比較的高い(50℃程度)ため、被処理ガスが
被処理ガス供給管内面、切換弁装置内部や蓄熱室入口部
等で冷却されて凝縮付着し、蓄熱体を閉塞したり、切換
弁装置の作動の不良を引き起こしたりする原因となって
いた。 【0009】そこで、従来は、前記被処理ガスが切換弁
装置等で冷却されても高沸点物質の凝縮温度以下に降温
しないよう被処理ガス供給管の所定位置に予熱器を設け
て被処理ガスを加熱することにより、被処理ガス中の高
沸点物質が前述の各個所に付着することを防止するよう
にしている。 【0010】 【発明が解決しようとする課題】しかしながら、予熱器
により被処理ガスを予熱する方法では、蓄熱式脱臭装置
の操業中、被処理ガスを予熱し続けなければならないた
め、大量の燃料を必要とするという課題を有する。 【0011】ところで、切換弁装置等に付着した高沸点
物質は、蓄熱式脱臭装置が操業・停止を繰り返すことに
より加熱・冷却を繰り返され、炭化して固着することが
知られている。 【0012】しかも、高沸点物質が一旦固着するとさま
ざまな気化温度を有する物質に変化するため、これを完
全に気化除去するには固着した高沸点物質を500℃程
度まで加熱しなければならない。ところが、固着した高
沸点物質には種々の着火温度のものがあるので、場合に
よっては一気に500℃まで加熱すると火災を引き起こ
す危険性があり、また回転弁方式の切換弁装置では、シ
ール部材の耐熱性の点からも500℃まで加熱すること
は困難である。 【0013】そこで、本発明者らが種々検討した結果、
高沸点物質は、加熱・冷却の繰り返しにより切換弁装置
等に固着した状態となっていなければ、すなわち、単に
凝縮しているだけの状態であれば、高沸点物質の気化温
度(たとえば250℃)以上で、かつ、着火温度(たと
えば300℃)以下の温度で容易に気化させることがで
きることを見出した。 【0014】そこで、本発明は、前記蓄熱式脱臭装置の
操業を停止した際に、燃焼室を構成する断熱材や蓄熱室
の蓄熱体に残存する熱に着目し、これを利用することで
別途熱を供給することなく、蓄熱式脱臭装置を構成する
切換弁および蓄熱室、ならびに、蓄熱式脱臭装置に連通
する配管内に付着した高沸点物質を気化し、除去するよ
うにした蓄熱式脱臭装置に付着した高沸点物質の除去方
法を提供することを目的とする。 【0015】 【課題を解決するための手段】本発明は、前記目的を達
成するために、加熱手段を有する燃焼室に連通する複数
の蓄熱室へ切換弁の切換えにより高沸点物質を含む被処
理ガスを順次供給し、この被処理ガスを前記蓄熱室の蓄
熱体により昇温したのち前記燃焼室へ供給して燃焼脱臭
処理するとともに、前記被処理ガスが供給されていない
他の蓄熱室から前記脱臭処理した処理ガスを排出するこ
とにより当該蓄熱体を昇温して排出する蓄熱式脱臭装置
による被処理ガス中の高沸点物質の脱臭処理に際し、前
記被処理ガスの供給を停止するとともに、前記加熱手段
を停止する一方、高沸点物質を含まない清浄ガスを燃焼
室へ所定量供給したのちその供給を停止し、蓄熱室から
の処理ガスの蓄熱室出側での温度が前記高沸点物質の気
化温度以上で、かつ、着火温度以下の所定温度となるよ
うに前記切換弁を切換えて制御し、この所定温度となっ
た蓄熱室出側からの処理ガスを前記蓄熱式脱臭装置に循
環供給して高沸点物質を除去するようにしたものであ
る。 【0016】 【発明の実施の形態】つぎに、本発明の実施の形態を図
にしたがって説明する。図は、本発明にかかる蓄熱式脱
臭装置に付着した高沸点物質の除去方法に適用する蓄熱
式脱臭設備を示す概略図である。 【0017】図において、1は公知の蓄熱式脱臭装置
で、脱臭炉本体2と切換弁装置7とからなる。 【0018】前記脱臭炉本体2は、上部に加熱手段、た
とえばバーナ4を有する燃焼室3と、この燃焼室3に連
通するとともに、内部に蓄熱体6を備えた第1蓄熱室5
Aと第2蓄熱室5Bとから構成されている。 【0019】前記切換弁装置7は第1切換弁8Aと第2
切換弁8Bとからなり、第1、第2切換弁8A,8B
は、弁箱9内に所定間隔をもって配設された中央部に開
口11を有する2つの弁座10a,10bと、この弁座
10a,10b間をシリンダ12の進退により昇降して
弁座10aあるいは10bのいずれかを閉塞する弁体1
3とからなり、図示しない塗装乾燥炉から蓄熱式脱臭装
置1へ高沸点物質を含有する被処理ガス(排ガス)を供
給するガス供給管P1は、前記弁座10a,10bで区
画される第1、第2切換弁8A,8Bの上室Ra,Ra
に連通するとともに、第1、第2切換弁8A,8Bの下
室Rb,Rbは排気ファン14を備えたガス排出管P2
に連通している。また、第1、第2切換弁8A,8Bの
中室Rc,Rcは、それぞれ第1蓄熱室5Aと第2蓄熱
室5BのチャンバーCa,Cbに連通している。 【0020】さらに、前記ガス供給管P1の所定位置に
は被処理ガス供給弁V1が設けられるとともにその下流
には清浄ガス供給弁V2が配設されている。なお、15
は排気塔である。 【0021】そして、前記ガス供給管P1の清浄ガス供
給弁V2下流側の所定位置とガス排出管P2の排気ファン
14下流側の所定位置とは開閉弁V3を備えた循環配管
3で連通してあり、循環路を形成している。 【0022】つぎに、前記蓄熱式脱臭装置1により高沸
点物質を有する被処理ガスの脱臭方法を説明する。 【0023】図1に示すように、前記開閉弁V3が閉、
第1切換弁8Aの弁体13が弁座10bの開口11を、
第2切換弁8Bの弁体13が弁座10aの開口11をそ
れぞれ閉塞した状態にあり、バーナ4を点火するととも
に排気ファン14を駆動し、被処理ガス供給弁V1を開
とする。 【0024】高沸点物質を有する被処理ガスは、第1切
換弁8Aの上室Raから中室Rcを通って第1蓄熱室5
Aから燃焼室3に至り、ここでバーナ4により約820
℃に保持された燃焼室3内で高沸点物質は燃焼脱臭処理
され、その後、処理ガスは第2蓄熱室5Bを通り、その
間に蓄熱体6と熱交換して冷却され、第2切換弁8Bの
中室Rc、下室Rb、ガス排出管P2を経て排気塔15
から大気放出される。 【0025】そして、所定時間が経過すると、図示しな
いタイマにより前記両シリンダ12,12を操作して、
つまり、第1切換弁8Aにおいては弁座10aの開口1
1を弁体13で閉じ、第2切換弁8Bにおいては弁座1
0bの開口11を弁体13で閉じ、被処理ガスを第2蓄
熱室5Bに供給する一方、処理ガスを第1蓄熱室5Aか
らガス排出管P2へ排出する。 【0026】前記のように、被処理ガスと処理ガスの供
給・排出経路を変更すると、前工程で処理ガスの通過に
より加熱された蓄熱体6に被処理ガスが供給されるため
予熱され、他方、高温(たとえば820℃)となった処
理ガスは前工程で被処理ガスにより冷却された蓄熱体6
を通過する際に熱を奪われ、100〜150℃以下に冷
却されて大気に放出される。この工程を繰り返して被処
理ガス中の高沸点物質を連続して燃焼除去する。 【0027】つぎに、蓄熱式脱臭装置1を構成する切換
弁装置7および蓄熱室5A,5B、ならびに、蓄熱式脱
臭装置1に連通するガス供給管P1内に付着した高沸点
物質の除去方法を説明する。 【0028】前記塗装乾燥炉の1日の操業(1回/日の
バッチ操業とした場合)が終了すると、燃焼室3のバー
ナ4を停止するとともに前記被処理ガス供給弁V1
閉、清浄ガス供給弁V2を開とし、ガス供給管P1から清
浄ガスたとえば空気を供給してガス供給管P1内および
蓄熱体6内の被処理ガスをパージする。なお、この場
合、燃焼室3内はまだ高温のため高沸点物質は燃焼脱臭
される。 【0029】その後、前記清浄ガス供給弁V2を閉とす
るとともに開閉弁V3を開とする。開閉弁V3が開となる
と、循環配管P3のガス排出管P2との連通部aには前記
排気ファン14の吸引力が作用して負圧となっているた
め、排気ファン14からの処理ガスの一部は循環配管P
3を通って蓄熱式脱臭装置1に至り、以後、これを繰り
返すことにより処理ガスの循環路が形成される。 【0030】そして、第1、第2蓄熱室5A,5Bの一
方から排出される処理ガスの温度が蓄熱室5A、5Bの
チャンバCa,Cbで設定温度になれば切換弁装置7を
切換える。ここで,設定温度は高沸点物質の気化温度以
上で、かつ、着火温度以下である、たとえば、300℃
にする。これにより、高沸点物質を気化させるのに充分
な熱量を有する処理ガスが蓄熱式脱臭装置1を循環する
こととなり、その間に、特に、先の脱臭処理中に高沸点
物質が付着していた蓄熱式脱臭装置1に連通するガス供
給管P1内や切換弁装置7内部、あるいは蓄熱室内に付
着した高沸点物質は気化し、燃焼室3内で脱臭処理され
ることとなる。 【0031】前記処理ガスの循環は放熱により燃焼室3
内の温度が約250℃になるまで続行され、その後、排
気ファン14を停止するとともに開閉弁V3を閉とし高
沸点物質の除去作業を終了する。 【0032】なお、前記説明では、被処理ガスと処理ガ
スの供給・排出を2つの切換弁8A、8Bからなる切換
弁装置7により行ったが、これに限らず3つ以上の切換
弁で構成してもよいし、複数通路を備えた回転弁であっ
てもよい。 【0033】また、前記説明では、脱臭処理をバッチ操
業のサイクルに合わせて1日1回行うようにしたが、高
沸点物質の付着状況により何日かに1回の実施でもよい
し、さらに、脱臭処理が連続的に行われる場合であれ
ば、高沸点物質が固着しないうちに一時脱臭処理の操業
を停止して行ってもよい。 【0034】 【発明の効果】以上の説明で明らかなように、本発明に
よれば、高沸点物質が低温部に固着する以前に蓄熱式脱
臭装置の保有する熱を利用して、高沸点物質の気化温度
以上に昇温した処理ガスを低温部に循環させることによ
り高沸点物質を気化除去するものであって、予熱器等を
必要とせず、構造が簡単で、かつ省エネルギーを図るこ
とができる。 【0035】また、気化した高沸点物質は着火温度以上
の燃焼室で燃焼するため、気化した高沸点物質が外部に
放出されることはない。 【0036】さらに、高沸点物質の除去作業を、蓄熱式
脱臭装置の操業終了時において容易に行えるので、操業
時間を無駄にすることがない等の効果を奏する。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a switching valve and a heat storage chamber that constitute a regenerative deodorizing apparatus, and a dust attached to a pipe communicating with the regenerative deodorizing apparatus. The present invention relates to a method for removing high-boiling substances such as tar. 2. Description of the Related Art Conventionally, for example, an exhaust gas (gas to be treated) containing a high-boiling substance, which is a malodorous component, discharged from a coating and drying furnace is supplied to a regenerative deodorizer because of its high thermal efficiency. It has been deodorized. [0003] This regenerative deodorizing apparatus comprises, for example, a deodorizing furnace main body comprising a plurality of regenerative chambers, a combustion chamber provided with a heating means such as a burner and a heater, and a switching valve device. The gas to be treated from the coating and drying furnace is
On the way, the temperature is lowered in the gas supply pipe to be treated, for example, about 50 ° C.
Then, it passes through the switching valve device, passes through the heat storage chamber heated in the previous step, and then reaches the combustion chamber, where it reaches the combustion chamber, where it is heated to about 820 ° C. by a heating means, for example, a burner, and the high-boiling substance is removed. It burns and is deodorized. On the other hand, when the high-temperature processing gas that has been deodorized as described above passes through another heat storage chamber to which the gas to be processed is not supplied, heat is taken by the heat storage body of the heat storage chamber and the temperature is lowered. Then, the gas is discharged from the gas discharge pipe to the outside of the furnace through the switching valve device. The exhaust of the processing gas is performed by an exhaust fan. [0006] The supply of the gas to be treated to each of the heat storage chambers and the discharge of the gas to be treated are alternately performed by switching the switching valve device at predetermined time intervals by a timer, and the above steps are repeated. Deodorize high boiling substances in the gas to be treated. The switching of the switching valve device is performed as follows.
In addition to the switching by the timer, the switching may be performed every time the temperature of the processing gas at the outlet of the heat storage chamber reaches a predetermined temperature (for example, 100 ° C.). After one day of operation of the coating and drying oven, the burner is stopped, the supply valve of the gas supply pipe is closed, and clean gas (air) containing no high boiling point substance is supplied to the gas supply pipe. As described above, the combustion chamber is supplied to and exhausted from the regenerative deodorizing device via the switching valve device to keep the temperature in the combustion chamber at about 250 ° C. or less, thereby protecting the flame detecting device. Since the high-boiling substances such as tar have a relatively high condensation temperature (about 50 ° C.), the gas to be treated is cooled at the inner surface of the gas supply pipe to be treated, inside the switching valve device, at the inlet of the heat storage chamber, and the like. Condensed and adhered, causing a blockage of the heat storage body and a malfunction of the switching valve device. Therefore, conventionally, a preheater is provided at a predetermined position of a gas supply pipe to be treated so that the gas to be treated does not fall below the condensation temperature of the high boiling point substance even if the gas to be treated is cooled by a switching valve device or the like. Is heated to prevent the high-boiling substances in the gas to be treated from adhering to the above-described locations. [0010] However, in the method of preheating the gas to be treated by the preheater, the gas to be treated must be kept preheated during the operation of the regenerative deodorizer, so that a large amount of fuel must be used. There is a problem of need. By the way, it is known that the high-boiling substance adhering to the switching valve device or the like is repeatedly heated and cooled by the regenerative deodorizing device being repeatedly operated and stopped, and is carbonized and fixed. Moreover, once the high-boiling substance is fixed, it changes to a substance having various vaporization temperatures. Therefore, to completely vaporize and remove the high-boiling substance, the fixed high-boiling substance must be heated to about 500 ° C. However, since there are various ignition temperatures among the high-boiling substances adhered, there is a risk of causing a fire if heated up to 500 ° C at a stretch. It is difficult to heat to 500 ° C. also from the viewpoint of properties. Therefore, as a result of various studies by the present inventors,
If the high-boiling substance is not fixed to the switching valve device or the like by repeated heating and cooling, that is, if it is simply condensed, the vaporization temperature of the high-boiling substance (for example, 250 ° C.) As described above, it has been found that vaporization can be easily performed at a temperature lower than the ignition temperature (for example, 300 ° C.). Therefore, the present invention focuses on the heat remaining in the heat insulating material constituting the combustion chamber and the heat storage body of the heat storage chamber when the operation of the heat storage type deodorizing apparatus is stopped, and utilizes this to separately A regenerative deodorizer that vaporizes and removes high-boiling substances adhering to a switching valve and a regenerator that constitute a regenerative deodorizer and a pipe connected to the regenerative deodorizer without supplying heat. It is an object of the present invention to provide a method for removing a high-boiling substance adhered to water. According to the present invention, in order to achieve the above object, the present invention relates to a treatment target containing a high-boiling substance by switching a switching valve to a plurality of heat storage chambers communicating with a combustion chamber having a heating means. The gas is sequentially supplied, and after the temperature of the gas to be treated is increased by the heat storage body of the heat storage chamber, the gas is supplied to the combustion chamber to perform the combustion deodorization treatment. During the deodorization of the high-boiling substances in the gas to be treated by the regenerative deodorizing device that raises the temperature of the heat storage body by discharging the deodorized treatment gas, the supply of the gas to be treated is stopped, While the heating means is stopped, a predetermined amount of clean gas containing no high-boiling substance is supplied to the combustion chamber, then the supply is stopped, and the temperature of the processing gas from the heat storage chamber at the exit side of the heat-storage chamber is changed to the high-boiling substance. Vaporization temperature Degree, and controls the switching valve so as to be a predetermined temperature equal to or lower than the ignition temperature, and circulates and supplies the processing gas from the heat storage chamber outlet side at the predetermined temperature to the heat storage type deodorizer. High boiling substances are removed. Next, an embodiment of the present invention will be described with reference to the drawings. The figure is a schematic view showing a heat storage type deodorizing facility applied to a method for removing high boiling substances attached to a heat storage type deodorizing apparatus according to the present invention. In FIG. 1, reference numeral 1 denotes a known heat storage type deodorizing device, which comprises a deodorizing furnace main body 2 and a switching valve device 7. The deodorization furnace main body 2 has a combustion chamber 3 having a heating means, for example, a burner 4 at an upper part thereof, and a first heat storage chamber 5 communicating with the combustion chamber 3 and having a heat storage body 6 therein.
A and the second heat storage chamber 5B. The switching valve device 7 includes a first switching valve 8A and a second switching valve 8A.
A first and a second switching valve 8A, 8B.
Are two valve seats 10a, 10b having openings 11 in the center arranged at predetermined intervals in the valve box 9; and the valve seat 10a or 10b is moved up and down between the valve seats 10a, 10b by moving the cylinder 12 forward and backward. Valve body 1 for closing any of 10b
A gas supply pipe P1 for supplying a gas to be treated (exhaust gas) containing a high-boiling substance from a coating / drying furnace (not shown) to the regenerative deodorizing apparatus 1 is defined by the valve seats 10a and 10b. 1. Upper chambers Ra, Ra of second switching valves 8A, 8B
And the lower chambers Rb and Rb of the first and second switching valves 8A and 8B are provided with a gas exhaust pipe P 2 provided with an exhaust fan 14.
Is in communication with The middle chambers Rc, Rc of the first and second switching valves 8A, 8B communicate with the chambers Ca, Cb of the first heat storage chamber 5A and the second heat storage chamber 5B, respectively. Further, a gas supply valve V 1 is provided at a predetermined position of the gas supply pipe P 1 , and a clean gas supply valve V 2 is provided downstream thereof. Note that 15
Is an exhaust tower. [0021] Then, the circulation pipe provided with a closing valve V 3 and the predetermined position and the exhaust fan 14 downstream of the predetermined position of the gas discharge pipe P 2 of the clean gas supply valve V 2 downstream of the gas supply pipe P 1 P They are connected by 3 and form a circulation path. Next, a method for deodorizing a gas to be treated having a high-boiling substance by the regenerative deodorizer 1 will be described. As shown in FIG. 1, the on-off valve V 3 is closed,
The valve body 13 of the first switching valve 8A closes the opening 11 of the valve seat 10b,
In a state where the valve body 13 of the second switch valve 8B is closed, respectively the opening 11 of the valve seat 10a, and drives the exhaust fan 14 together with igniting the burner 4, the treated gas supply valve V 1 open. The gas to be treated having a high boiling point substance flows from the upper chamber Ra of the first switching valve 8A through the middle chamber Rc to the first heat storage chamber 5A.
From A to the combustion chamber 3 where the burner 4 provides about 820
The high-boiling-point substances are burned and deodorized in the combustion chamber 3 maintained at a temperature of 2 ° C., and then the processing gas passes through the second heat storage chamber 5B, during which it exchanges heat with the heat storage body 6 to be cooled, and the second switching valve 8B through the middle chamber Rc, lower chamber Rb, a gas discharge pipe P 2 exhaust tower 15
Emitted from the atmosphere. When a predetermined time has elapsed, the two cylinders 12 and 12 are operated by a timer (not shown).
That is, in the first switching valve 8A, the opening 1 of the valve seat 10a
1 is closed by the valve body 13 and the valve seat 1 is provided in the second switching valve 8B.
It closes the opening 11 of the 0b in the valve body 13, while supplying the gas to be treated into the second regenerator 5B, to discharge the process gas from the first heat storage chamber 5A to the gas discharge pipe P 2. As described above, when the supply and discharge paths of the gas to be processed and the processing gas are changed, the gas to be processed is supplied to the heat storage unit 6 heated by the passage of the processing gas in the previous process, so that the preheating is performed. , The high temperature (for example, 820 ° C.) processing gas is cooled by the gas to be processed in the previous process.
When passing through, heat is taken away, cooled to 100 to 150 ° C. or lower, and released to the atmosphere. This process is repeated to continuously burn and remove high-boiling substances in the gas to be treated. Next, the switching valve 7 and the heat storage chamber 5A constituting the regenerative deodorizing apparatus 1, 5B, and, a method for removing the high boiling point substance adhering to the regenerative deodorizing device a gas supply pipe P 1 which communicates with the 1 Will be described. [0028] When the (case of the batch operation once / day) the painting operation daily drying furnace is finished, closing the gas to be treated supply valve V 1 stops the burner 4 of the combustion chamber 3, the clean the gas supply valve V 2 is opened to purge the gas to be treated of supplying clean gas such as air from a gas supply pipe P 1 gas supply pipe P and in the regenerator 6 1. In this case, since the inside of the combustion chamber 3 is still at a high temperature, high-boiling substances are burned and deodorized. [0029] Then, the clean gas supply valve V 2 to the on-off valve V 3 opened with a closed. Opening and closing valve V 3 is opened, since the suction force of the exhaust fan 14 is the communicating portion a between the gas discharge pipe P 2 of the circulation pipe P 3 is in the act by negative pressure, from the exhaust fan 14 Part of the processing gas is circulation pipe P
3 to the regenerative deodorizer 1, and thereafter, by repeating this, a circulation path of the processing gas is formed. When the temperature of the processing gas discharged from one of the first and second heat storage chambers 5A and 5B reaches the set temperature in the chambers Ca and Cb of the heat storage chambers 5A and 5B, the switching valve device 7 is switched. Here, the set temperature is equal to or higher than the vaporization temperature of the high boiling substance and equal to or lower than the ignition temperature, for example, 300 ° C.
To As a result, the processing gas having a sufficient amount of heat to vaporize the high-boiling substance circulates through the regenerative deodorizing apparatus 1, and during that time, particularly, the heat storage where the high-boiling substance has adhered during the previous deodorizing treatment. high-boiling materials attached inside the gas supply pipe P 1 in and switching valve 7 which communicates with the formula deodorizing apparatus 1, or the heat storage chamber is vaporized, and thus is deodorized in the combustion chamber 3. The processing gas circulates through the combustion chamber 3 by heat radiation.
Then, the internal temperature is maintained at about 250 ° C., and thereafter, the exhaust fan 14 is stopped, the on-off valve V 3 is closed, and the operation of removing high-boiling substances is completed. In the above description, the supply and discharge of the gas to be processed and the processing gas are performed by the switching valve device 7 including the two switching valves 8A and 8B. However, the present invention is not limited to this. Or a rotary valve having a plurality of passages. In the above description, the deodorizing treatment is performed once a day in accordance with the cycle of the batch operation. However, the deodorizing treatment may be performed once every several days depending on the adhesion state of the high boiling point substance. When the deodorizing treatment is performed continuously, the operation of the deodorizing treatment may be temporarily stopped before the high-boiling substance is fixed, and then performed. As is apparent from the above description, according to the present invention, before the high-boiling substance adheres to the low-temperature part, the heat of the regenerative deodorizing device is utilized to utilize the high-boiling substance. A high-boiling substance is vaporized and removed by circulating the processing gas heated to a temperature higher than the vaporization temperature to a low-temperature portion, and does not require a preheater, etc., and has a simple structure and energy saving. . Further, since the vaporized high-boiling substance is burned in a combustion chamber having a temperature equal to or higher than the ignition temperature, the vaporized high-boiling substance is not released to the outside. Further, since the operation of removing the high-boiling substances can be easily performed at the end of the operation of the regenerative deodorizer, the operation time is not wasted.

【図面の簡単な説明】 【図1】 本発明を実施するための蓄熱式脱臭設備の概
略図である。 【符号の説明】 1〜蓄熱式脱臭装置、3〜燃焼室、4〜加熱手段、5A
〜第1蓄熱室、5B〜第2蓄熱室、6〜蓄熱体、7〜切
換弁装置、14〜排気ファン、P1〜ガス供給管、P2
ガス排気管、P3〜循環配管、V1〜被処理ガス供給弁、
2〜清浄ガス供給弁、V3〜開閉弁。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a schematic diagram of a regenerative deodorizing facility for carrying out the present invention. [Description of Signs] 1-regenerative deodorizer, 3-combustion chamber, 4-heating means, 5A
~ The first regenerator, 5B through the second regenerator, 6 regenerator, 7 switching valve device, 14 an exhaust fan, P 1 ~ gas supply pipe, P 2 -
Gas exhaust pipe, P 3 ~ circulation pipe, V 1 ~ treated gas supply valve,
V 2 ~ clean gas supply valve, V 3 ~ off valve.

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平10−47636(JP,A) 特開 平11−51358(JP,A) (58)調査した分野(Int.Cl.7,DB名) F23G 7/06 103 F23G 7/06 ZAB F23G 5/50 ZAB ────────────────────────────────────────────────── ─── Continuation of the front page (56) References JP-A-10-47636 (JP, A) JP-A-11-51358 (JP, A) (58) Fields investigated (Int. Cl. 7 , DB name) F23G 7/06 103 F23G 7/06 ZAB F23G 5/50 ZAB

Claims (1)

(57)【特許請求の範囲】 【請求項1】 加熱手段を有する燃焼室に連通する複数
の蓄熱室へ切換弁の切換えにより高沸点物質を含む被処
理ガスを順次供給し、この被処理ガスを前記蓄熱室の蓄
熱体により昇温したのち前記燃焼室へ供給して燃焼脱臭
処理するとともに、前記被処理ガスが供給されていない
他の蓄熱室から前記脱臭処理した処理ガスを排出するこ
とにより当該蓄熱体を昇温して排出する蓄熱式脱臭装置
による被処理ガス中の高沸点物質の脱臭処理に際し、 前記被処理ガスの供給を停止するとともに、前記加熱手
段を停止する一方、高沸点物質を含まない清浄ガスを燃
焼室へ所定量供給したのちその供給を停止し、蓄熱室か
らの処理ガスの蓄熱室出側での温度が前記高沸点物質の
気化温度以上で、かつ、着火温度以下の所定温度となる
ように前記切換弁を切換えて制御し、この所定温度とな
った蓄熱室出側からの処理ガスを前記蓄熱式脱臭装置に
循環供給することを特徴とする高沸点物質の除去方法。
(57) [Claim 1] A gas to be treated containing a high-boiling substance is sequentially supplied to a plurality of heat storage chambers communicating with a combustion chamber having a heating means by switching a switching valve, and the gas to be treated is Is heated by the heat storage body of the heat storage chamber, and then supplied to the combustion chamber to perform combustion deodorization processing, and by discharging the deodorized processing gas from another heat storage chamber to which the gas to be processed is not supplied. In the deodorizing treatment of the high-boiling substance in the gas to be treated by the regenerative deodorizing device which raises the temperature of the heat storage body and discharges the same, the supply of the gas to be treated is stopped, and the heating means is stopped. After a predetermined amount of clean gas containing no is supplied to the combustion chamber, the supply is stopped, and the temperature of the processing gas from the heat storage chamber at the exit side of the heat storage chamber is equal to or higher than the vaporization temperature of the high boiling substance and equal to or lower than the ignition temperature. Of the specified temperature A method for removing high-boiling substances, characterized in that the switching valve is switched and controlled as described above, and the processing gas from the outlet side of the heat storage chamber at the predetermined temperature is circulated and supplied to the regenerative deodorizer.
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