JPH0538417A - Apparatus for heating and cleaning harmful gas - Google Patents

Apparatus for heating and cleaning harmful gas

Info

Publication number
JPH0538417A
JPH0538417A JP3196421A JP19642191A JPH0538417A JP H0538417 A JPH0538417 A JP H0538417A JP 3196421 A JP3196421 A JP 3196421A JP 19642191 A JP19642191 A JP 19642191A JP H0538417 A JPH0538417 A JP H0538417A
Authority
JP
Japan
Prior art keywords
gas
heating
main body
exhaust gas
outside air
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP3196421A
Other languages
Japanese (ja)
Other versions
JP2743632B2 (en
Inventor
Akira Hashimoto
彰 橋本
Junjiro Awano
順二郎 粟野
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP3196421A priority Critical patent/JP2743632B2/en
Publication of JPH0538417A publication Critical patent/JPH0538417A/en
Application granted granted Critical
Publication of JP2743632B2 publication Critical patent/JP2743632B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Abstract

PURPOSE:To provide an apparatus for heating and cleaning a harmful gas in which harmful components including carbon monooxide (CO) and hydrocarbons (HC) in various kinds of exhaust gases are heated and eliminated by oxidation at a low level of energy loss and at a high cleaning efficiency. CONSTITUTION:The gas inlet and outlet 1, 8 at the ends of the main body 5 of an apparatus for heating and cleaning a harmful gas are interchanged every given time by a damper 9 to reverse the gas flow direction 7 in the main body of the apparatus. In the apparatus including a heater 4 at the middle, a catalyst layer 3, and heat accumulator layers 2 fixed respectively on the way of gas passages from each end to the middle, an exhaust gas is introduced by a fan 22 placed on the exhaust side apart from the main body of the apparatus. A damper 21a fixed at an opening 21 for the introduction of outside air is opened just before the reversion of the gas flow direction. The outside air is introduced into the main body of the apparatus by the fan 22 so that the discharge of an uncleaned exhaust gas is prevented.

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、有害ガス加熱浄化装置
に関し、特に各種排ガス中に混入したCO(一酸化炭
素),HC(炭化水素)などの悪臭成分や有害成分を適
正温度に加熱し酸化浄化する有害ガス加熱浄化装置に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a harmful gas heating and purification device, and in particular, it heats malodorous and harmful components such as CO (carbon monoxide) and HC (hydrocarbons) mixed in various exhaust gases to an appropriate temperature. The present invention relates to a harmful gas heating / purification device for oxidative purification.

【0002】[0002]

【従来の技術】近年、各種の燃焼機や乾燥,熱処理時に
発生するCOやHC成分は、その有害性や臭気のため浄
化し排出することが必要不可欠なものになっている。C
OやHC成分の浄化方法としては、排ガス自身を加熱し
ガス中の酸素と反応させる方法が最も浄化効率が高く信
頼性も高い。ここで排ガスの温度を上げ空気中の酸素が
COやHCと反応するには、800〜900℃以上の温
度が必要になるが酸化触媒を用いる方法では200〜4
00℃の温度範囲で反応を進めることができ熱エネルギ
ーの無駄を省くことができる。
2. Description of the Related Art In recent years, it has become indispensable to purify and discharge CO and HC components generated in various combustors, drying and heat treatment due to their harmfulness and odor. C
As a method of purifying O and HC components, a method of heating exhaust gas itself and reacting it with oxygen in gas has the highest purification efficiency and high reliability. Here, in order to raise the temperature of the exhaust gas and allow oxygen in the air to react with CO and HC, a temperature of 800 to 900 ° C. or higher is required, but 200 to 4 in the method using the oxidation catalyst.
The reaction can proceed in the temperature range of 00 ° C. and waste of thermal energy can be eliminated.

【0003】以下に従来の有害ガス浄化装置について説
明する。図3は、従来例1の触媒浄化装置である。図3
において、(a)は触媒浄化装置本体、(b)は熱交換
機も含めたシステムを示す。10は触媒浄化装置本体、
16は熱交換機、12は加熱装置、13は触媒を示す。
(a)で排ガスは入り口11から触媒加熱装置本体に導
入され、加熱装置12により所定の温度に昇温し、触媒
13によりCO,HCなどが酸化浄化され、出口14か
ら排出される。この時排ガスの昇温に要したエネルギー
はガスと一緒に排出されることになる。このエネルギー
の一部を回収する目的で熱交換機を用いたシステムが
(b)である。この場合ガス流入口17から導入され熱
交換機16で昇温された排ガスは、矢印15に沿って流
れ触媒浄化装置本体10に進む。ここで浄化されたガス
は、再び熱交換機16に入り冷却されガス流出口18か
ら排出される。すなわち排ガスの昇温に要したエネルギ
ーの一部を回収し、エネルギーロスを少なくしようとす
るものである。
A conventional harmful gas purifying apparatus will be described below. FIG. 3 is a catalyst purification device of Conventional Example 1. Figure 3
In FIG. 1, (a) shows the main body of the catalyst purifying device, and (b) shows the system including the heat exchanger. 10 is the main body of the catalyst purifier,
16 is a heat exchanger, 12 is a heating device, and 13 is a catalyst.
In (a), the exhaust gas is introduced into the main body of the catalyst heating device from the inlet 11, heated to a predetermined temperature by the heating device 12, CO, HC and the like are oxidized and purified by the catalyst 13, and discharged from the outlet 14. At this time, the energy required to raise the temperature of the exhaust gas is discharged together with the gas. A system using a heat exchanger for the purpose of recovering a part of this energy is (b). In this case, the exhaust gas introduced from the gas inlet 17 and heated by the heat exchanger 16 flows along the arrow 15 and proceeds to the catalyst purifying apparatus main body 10. The gas purified here enters the heat exchanger 16 again, is cooled, and is discharged from the gas outlet 18. That is, part of the energy required to raise the temperature of the exhaust gas is recovered to reduce energy loss.

【0004】一方これに対し図4は、蓄熱体をもちいた
従来例2の加熱浄化装置で、(a)の状態と(b)の状
態を交互に繰り返すことにより熱エネルギーの削減を図
ったものである。図4において、2が触媒を含む蓄熱
体、4が加熱装置である。9は有害な排ガスの流れを制
御するダンパーを示す。(a)で排ガスはガス流入口1
9から矢印7のように進みガスの出入口1から浄化装置
内に入る。下部の蓄熱体2を通過し加熱装置4により加
熱,浄化され、上部の蓄熱体2で熱を奪われ冷却されて
ガスの出入口8から排出されガス流出口20へ進む、一
定時間後(b)のように排ガスの流れを変えるようにダ
ンパー9をそれぞれ操作する。すなわち(a)で排ガス
から熱を奪った上部の蓄熱体2が今度は排ガスに熱を与
えるように働き、排ガスを加熱するエネルギーの一部ま
たは大部分を補う。すなわちこの浄化装置本体5内で熱
が循環し省エネルギーとなる。
On the other hand, FIG. 4 shows a heating and purifying apparatus of the conventional example 2 using a heat storage body, in which the state of (a) and the state of (b) are alternately repeated to reduce heat energy. Is. In FIG. 4, 2 is a heat storage body containing a catalyst, and 4 is a heating device. Reference numeral 9 denotes a damper that controls the flow of harmful exhaust gas. In (a), the exhaust gas is the gas inlet 1
From 9 as shown by arrow 7, gas enters into the purifier through the inlet / outlet 1. After passing through the lower heat storage body 2, it is heated and purified by the heating device 4, is deprived of heat by the upper heat storage body 2, is cooled, is discharged from the gas inlet / outlet 8 and proceeds to the gas outlet 20, after a certain time (b). The dampers 9 are operated so as to change the flow of the exhaust gas as described above. That is, the upper heat storage body 2 which has taken heat from the exhaust gas in (a) works to give heat to the exhaust gas, and supplements a part or most of the energy for heating the exhaust gas. That is, heat is circulated in the purifying device body 5 to save energy.

【0005】[0005]

【発明が解決しようとする課題】しかしながら上記の従
来例1(図3)の構成で用いられる熱交換機16は、通
常熱伝導率の良い薄肉のアルミニウムが主体となって構
成されており熱交換効率は50〜60%が限界であり、
またSOxやNOxなどの腐食性のガスを含んだ排ガス
に対してはアルミニウムが腐食するため使用できなかっ
た。従来例2(図4)では触媒を含む耐食性の蓄熱体2
を用いることにより従来例1の欠点を解消できるもので
あり、熱交換効率の高い浄化装置を実現できるが、ガス
の流れ方向を逆転するとき最後に入り口から浄化装置本
体5に導入されたガスは下流側の蓄熱体2や加熱装置4
に到達する前に上流側の蓄熱体2やガス出入口1付近で
停滞し、ガス流れ方向の逆転と同時にガスの出入口8か
ら排出される。すなわちガスの一部は浄化されないまま
排出されることになり100%の浄化は理論的に不可能
であった。
However, the heat exchanger 16 used in the configuration of the above-mentioned conventional example 1 (FIG. 3) is usually composed mainly of thin-walled aluminum having good thermal conductivity, and the heat exchange efficiency is high. Is limited to 50-60%,
Also, aluminum cannot be used for exhaust gas containing corrosive gases such as SOx and NOx because aluminum corrodes. In Conventional Example 2 (FIG. 4), a corrosion-resistant heat storage body 2 containing a catalyst
It is possible to eliminate the drawbacks of Conventional Example 1 by using, and it is possible to realize a purification device with high heat exchange efficiency. However, when the gas flow direction is reversed, the gas introduced into the purification device main body 5 from the last inlet is Downstream heat storage body 2 and heating device 4
Before it reaches the heat storage unit 2, it is stagnated in the vicinity of the heat storage body 2 and the gas inlet / outlet 1 on the upstream side, and is discharged from the gas inlet / outlet 8 simultaneously with the reversal of the gas flow direction. That is, a part of the gas is discharged without being purified, and 100% purification was theoretically impossible.

【0006】本発明は、上記従来例2の加熱浄化装置の
問題点を解決するもので、有害ガス成分を含んだ排ガス
は100%触媒層および加熱装置を通過して排出される
ようにする構造および操作を与える有害ガス加熱浄化装
置を提供することを目的としている。
The present invention solves the problems of the heating and purifying device of the above-mentioned conventional example 2, in which exhaust gas containing harmful gas components is exhausted through 100% catalyst layer and heating device. It is also an object of the present invention to provide a toxic gas heating and purifying device that gives an operation.

【0007】[0007]

【課題を解決するための手段】この目的を達成するため
に本発明の有害ガス加熱浄化装置は、ガスの流入口、ガ
スの流出口および加熱浄化装置本体からなる構成に対し
て、ガスの流出口側にファンと、加熱浄化装置本体の両
端にダンパーにより一定時間毎にガスの流れ方向を逆転
させ交互に変換するガスの出入口と、外気導入のための
開口部を設けた構成としたものである。
In order to achieve this object, the harmful gas heating and purifying apparatus of the present invention has a structure that includes a gas inlet, a gas outlet, and a heating and purifying apparatus main body. A fan is provided on the outlet side, gas inlets and outlets are provided at both ends of the heating and purifying apparatus main body for alternately reversing the gas flow direction by a damper at regular intervals, and openings for introducing outside air. is there.

【0008】[0008]

【作用】この構成により本発明の有害ガス加熱浄化装置
は、ガスの流出口側に設けられたファンによりガスの流
入口から導入される排ガスは、一定時間の間、浄化装置
本体の一端(一方のガスの出入口)から浄化装置本体内
に導入され、蓄熱体層を経て加熱装置および触媒層によ
り加熱浄化され、もう一方の蓄熱体層で冷却され他端
(他方のガスの出入口)から排出され、ファンを通過し
てガスの流出口から排出される。一定時間経過後ガスの
流入口から加熱浄化装置本体のガスの入口への流路を閉
じ、同時に外気導入のための開口部のダンパーを開ける
ことによって外気がファンにより加熱浄化装置本体内に
吸引される。この時の外気の吸引量は、最後に加熱浄化
装置本体内に導入された排ガス成分が加熱浄化装置本体
内の触媒層および加熱装置に送られるのに十分な量であ
れば良い。次に外気導入のための開口部を閉じ、排ガス
がそれまでとは逆方向に加熱浄化装置本体内を通過する
ように加熱浄化装置本体の両端部分に設置したダンパー
を操作する。このモードでも一定時間経過後、ガスの流
入口から加熱浄化装置本体のガスの出入口への流路を閉
じ、同時に外気が一定量加熱浄化装置本体内に吸引され
るようにダンパーを操作する。この操作を繰り返すこと
により、排ガスは加熱浄化装置本体の両サイドのそれぞ
れの蓄熱体層が吸熱及び放熱の役割を交換することによ
って加熱、および冷却されて排出される。また排ガスの
流れ方向が逆転するときも、外気により排ガスは触媒層
や加熱装置に送られているので100%浄化することが
できることとなる。
With this configuration, the harmful gas heating and purifying apparatus of the present invention is such that the exhaust gas introduced from the gas inlet by the fan provided on the gas outlet side is kept at one end (one side Gas is introduced into the main body of the purifier through the heat storage layer, heated and purified by the heating device and the catalyst layer, cooled by the other heat storage layer, and discharged from the other end (the other gas inlet and outlet). After passing through the fan, the gas is discharged from the outlet. After a certain period of time, the flow path from the gas inlet to the gas inlet of the heating and purifying apparatus main body is closed, and at the same time, the damper at the opening for introducing the outside air is opened to suck the outside air into the heating and purifying apparatus main body by the fan. It The amount of outside air sucked at this time may be an amount sufficient for the exhaust gas component finally introduced into the heating and purifying device body to be sent to the catalyst layer and the heating device in the heating and purifying device body. Next, the opening for introducing the outside air is closed, and the dampers installed at both ends of the heat purifying apparatus main body are operated so that the exhaust gas passes through the inside of the heat purifying apparatus main body in the opposite direction. Even in this mode, after a certain period of time, the flow path from the gas inlet to the gas inlet / outlet of the heating / purifying device main body is closed, and at the same time, the damper is operated so that a certain amount of outside air is sucked into the heating / purifying device main body. By repeating this operation, the exhaust gas is heated and cooled by the heat storage layers on both sides of the main body of the heat purifying apparatus exchanging the roles of heat absorption and heat radiation, and then exhausted. Further, even when the flow direction of the exhaust gas is reversed, the exhaust gas is sent to the catalyst layer and the heating device by the outside air, so that it can be purified 100%.

【0009】[0009]

【実施例】以下本発明の一実施例の有害ガス加熱浄化装
置について、図面を参照しながら説明する。
DESCRIPTION OF THE PREFERRED EMBODIMENTS A harmful gas heating and purifying apparatus according to an embodiment of the present invention will be described below with reference to the drawings.

【0010】図1において、19は排ガスの流入口、2
0は排ガスの流出口を示す。5は加熱浄化装置本体、2
は蓄熱体層、4は加熱装置、3は触媒層を示す。9は加
熱浄化装置内の排ガスの流れ方向を逆転させるためのダ
ンパーを示す。21は外気導入のための開口部、21a
はそのダンパーを示す。(b)は(a)の状態で浄化装
置内部に排ガスを流し一定時間経過した直後に外気を加
熱浄化装置本体5内部に導入する状態を示す。(a)の
状態を説明する。排ガスはファン22によりガス流入口
19から入り矢印7で示したように流れ、ガスの出入口
1から加熱浄化装置本体5内に入り下方の蓄熱体層2を
通り加熱装置4により加熱され触媒層3により浄化され
る。上方の蓄熱体層2を通過するとき、排ガスの持って
いる熱エネルギーが奪われ排ガスは冷却されてガスの出
入口8からガスの流出口20の方向へ排出される。一定
時間後、浄化装置の下方のダンパー9を閉じ、排ガスが
加熱浄化装置本体5内に流れないようにし、同時に図の
下方の開口部21のダンパー21aを開き外気を加熱浄
化装置本体5内に導入するようにしたのが(b)の状態
である。外気の導入量はガスの出入口1と下方の蓄熱体
層2内部に停滞する排ガス成分を加熱装置4、および触
媒層3まで追いやる量で十分である。次のモードを図2
に示した。外気導入のための開口部21のダンパー21
aを閉じ、上下のダンパー9を操作し、加熱浄化装置本
体5内の排ガスの流れ方向が図1の(a)と逆転してい
るのが、図2の(a)である。この状態では排ガスは上
方の蓄熱体層2により熱を奪い加熱装置4および触媒層
3により浄化された後、下方の蓄熱体層2に熱を奪われ
冷却されてガスの流出口20から排出される。すなわち
排ガスを加熱するための熱エネルギーの一部または大部
分は二層の蓄熱体層2によって加熱浄化装置本体5内部
に閉じこめられる。一定時間経過後外気を加熱浄化装置
本体5内に導入するように図の上方の開口部21のダン
パー21aを操作した状態を(b)に示す。この操作に
よって未浄化の状態で排出される排ガスを防ぐことがで
き、有害成分の浄化効率を高めることができる。
In FIG. 1, 19 is an exhaust gas inlet, 2
0 indicates the outlet of the exhaust gas. 5 is the main body of the heat purifying device, 2
Is a heat storage layer, 4 is a heating device, and 3 is a catalyst layer. Reference numeral 9 denotes a damper for reversing the flow direction of the exhaust gas in the heat purification device. 21 is an opening for introducing outside air, 21a
Indicates the damper. (B) shows a state in which exhaust gas is allowed to flow inside the purifying device in the state of (a) and outside air is introduced into the heating purifying device main body 5 immediately after a lapse of a certain time. The state of (a) will be described. The exhaust gas enters from the gas inlet 19 by the fan 22 as shown by the arrow 7, enters the heating purifying device main body 5 from the gas inlet / outlet 1 and passes through the heat storage layer 2 below and is heated by the heating device 4 and the catalyst layer 3 Purified by. When passing through the upper heat storage layer 2, the heat energy of the exhaust gas is removed and the exhaust gas is cooled and discharged from the gas inlet / outlet 8 toward the gas outlet 20. After a certain period of time, the damper 9 below the purifier is closed to prevent the exhaust gas from flowing into the heat purifier main body 5, and at the same time, the damper 21a of the lower opening 21 in the figure is opened to let the outside air enter the heat purifier main body 5. The state of (b) was introduced. The amount of the outside air introduced is sufficient to drive the exhaust gas component stagnating inside the gas inlet / outlet 1 and the lower heat storage layer 2 to the heating device 4 and the catalyst layer 3. Figure 2 for the next mode
It was shown to. Damper 21 of opening 21 for introducing outside air
It is FIG. 2A that the flow direction of the exhaust gas in the heating and purifying device main body 5 is reversed from that of FIG. 1A by closing a and operating the upper and lower dampers 9. In this state, the exhaust gas is deprived of heat by the upper heat storage layer 2 and purified by the heating device 4 and the catalyst layer 3, and then deprived of heat by the lower heat storage layer 2 and cooled and discharged from the gas outlet 20. It That is, a part or most of the thermal energy for heating the exhaust gas is confined inside the heating and purifying apparatus main body 5 by the two layers of the heat storage layer 2. The state where the damper 21a of the upper opening 21 in the figure is operated so as to introduce the outside air into the heating and purifying apparatus main body 5 after a certain time has elapsed is shown in (b). By this operation, exhaust gas discharged in an unpurified state can be prevented and the efficiency of purification of harmful components can be increased.

【0011】[0011]

【発明の効果】以上の実施例の説明により明らかなよう
に、本発明の有害ガス加熱浄化装置によれば、加熱浄化
装置本体の両端がダンパーにより排ガスの流れ方向を一
定時間毎に逆転させることにより、入口または出口とし
て交互に変換するガスの出入口を有し、中央に加熱装置
とその加熱装置を介して一対の触媒層を設け、この触媒
層の外側にそれぞれ蓄熱体層を有した加熱浄化装置であ
ってガスの出口,入口を切り替え排ガスの流れ方向を逆
転させることにより、二層の蓄熱体層で排ガスを加熱す
るための熱エネルギーを加熱浄化装置本体内部に閉じこ
めることを可能にした構成であるが、排ガスの流れ方向
を逆転させるとき浄化されずに排出され、浄化効率を低
下させていた排ガス成分がないように、外気を導入する
ことによって全ての排ガスが加熱装置および触媒層を通
過する構造を提供することができ、排ガスの浄化効率を
大きく向上させることができる。
As is apparent from the above description of the embodiments, according to the harmful gas heating and purifying apparatus of the present invention, both ends of the heating and purifying apparatus main body have dampers to reverse the flow direction of exhaust gas at regular intervals. Has an inlet / outlet for gas to be alternately converted as an inlet or an outlet, a heating device and a pair of catalyst layers are provided in the center through the heating device, and heat purification having a heat storage layer on each outside of the catalyst layer A device that switches the gas outlet and inlet and reverses the flow direction of the exhaust gas so that the thermal energy for heating the exhaust gas in the two heat storage layers can be confined inside the heating purification device body. However, by introducing the outside air so that there is no exhaust gas component that was not purified when the flow direction of the exhaust gas was reversed and was not purified, and the purification efficiency was reduced. Can provide a structure that exhaust gas passes through the heating device and the catalyst layer, it is possible to greatly improve the efficiency of purifying the exhaust gas.

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

【図1】(a)本発明の一実施例の有害ガス加熱浄化装
置の1つのモードの構成の概念を示す説明図 (b)(a)モードを終了した直後に外気を加熱浄化装
置本体に導入した状態を示す説明図
FIG. 1 (a) is an explanatory view showing the concept of the configuration of one mode of the harmful gas heating and purifying apparatus of one embodiment of the present invention. (B) (a) Outside air is introduced into the heating and purifying apparatus main body immediately after the mode is finished. Explanatory diagram showing the installed state

【図2】(a)同次のモードの構成の概念を示す説明図 (b)(a)モードを終了した直後に外気を加熱浄化装
置本体に導入した状態を示す説明図
FIG. 2 (a) is an explanatory view showing the concept of the configuration of the same mode. (B) An explanatory view showing a state in which outside air is introduced into the heating and purifying apparatus main body immediately after the (a) mode is finished.

【図3】(a)第1の従来例の触媒浄化装置本体の構成
の概念を示す説明図 (b)(a)の触媒浄化装置本体に熱交換機も含めた触
媒浄化システム全体の構成の概念を示す説明図
FIG. 3 (a) is an explanatory view showing the concept of the configuration of the catalyst purifying apparatus main body of the first conventional example. (B) The concept of the overall configuration of the catalyst purifying system including the heat exchanger in the catalyst purifying apparatus main body of FIG. 3 (a). Explanatory diagram showing

【図4】(a)第2の従来例の触媒浄化装置本体の構成
の概念を示す説明図 (b)(a)から排ガスの流れ方向を逆転した状態を示
す説明図
FIG. 4 (a) is an explanatory view showing the concept of the configuration of a catalyst purifying apparatus main body of a second conventional example. FIG. 4 (b) is an explanatory view showing a state in which the flow direction of exhaust gas is reversed from FIG.

【符号の説明】 1,8 ガスの出入口 2 蓄熱体層 3 触媒層 4 加熱装置 5 加熱浄化装置本体 7 ガスの流れ方向 9 ダンパー 19 ガスの流入口 20 ガスの流出口 21 開口部 22 ファン[Explanation of symbols] 1,8 Gas inlet / outlet 2 Heat storage layer 3 Catalyst layer 4 Heating device 5 Heating / purifying device main body 7 Gas flow direction 9 Damper 19 Gas inlet 20 Gas outlet 21 Opening 22 Fan

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】ガスの流入口、ガスの流出口、および加熱
浄化装置本体からなり、前記加熱浄化装置本体の両端
に、ダンパーにより一定時間毎にガスの流れ方向を逆転
させ交互に変換するガスの出入口と、中央に加熱装置
と、この加熱装置を介して一対の触媒層と、この触媒層
の外側にそれぞれ蓄熱体層を有した加熱浄化装置におい
て、前記ガスの流出口側に設けたファンと、前記ガスの
出入口近傍に、前記加熱浄化装置本体内へ浄化を対象と
した排ガス以外の外気導入のための開口部を具備した有
害ガス加熱浄化装置。
1. A gas comprising a gas inflow port, a gas outflow port, and a heating / purifying device main body, wherein the dampers are provided at both ends of the heating / purifying device main body so that the flow direction of the gas is reversed at regular intervals to alternate conversion. In the heating and purifying device having the inlet / outlet, the heating device in the center, the pair of catalyst layers via the heating device, and the heat storage layer on the outside of the catalyst layer, the fan provided on the gas outlet side. And a harmful gas heating and purifying apparatus having an opening near the inlet and outlet of the gas for introducing outside air other than exhaust gas into the heating and purifying apparatus main body.
【請求項2】一定時間毎に加熱浄化装置本体内のガスの
流れ方向を逆転させるとき、入口側のガス流路を遮断す
ると同時に、外気導入のための開口部を開き一定量の外
気が前記加熱浄化装置本体内に導入されてのち、ダンパ
ーの操作によってガスの流れ方向を制御して逆転させる
ように構成した請求項1記載の有害ガス加熱浄化装置。
2. When reversing the flow direction of the gas in the main body of the heating and purifying apparatus at regular intervals, the gas flow path on the inlet side is blocked, and at the same time, an opening for introducing outside air is opened to allow a certain amount of outside air to flow. 2. The harmful gas heating and purifying apparatus according to claim 1, wherein after being introduced into the heating and purifying apparatus main body, the gas flow direction is controlled by the operation of the damper to reverse the direction.
JP3196421A 1991-08-06 1991-08-06 Noxious gas heating purification equipment Expired - Lifetime JP2743632B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3196421A JP2743632B2 (en) 1991-08-06 1991-08-06 Noxious gas heating purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3196421A JP2743632B2 (en) 1991-08-06 1991-08-06 Noxious gas heating purification equipment

Publications (2)

Publication Number Publication Date
JPH0538417A true JPH0538417A (en) 1993-02-19
JP2743632B2 JP2743632B2 (en) 1998-04-22

Family

ID=16357576

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3196421A Expired - Lifetime JP2743632B2 (en) 1991-08-06 1991-08-06 Noxious gas heating purification equipment

Country Status (1)

Country Link
JP (1) JP2743632B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09262436A (en) * 1996-03-29 1997-10-07 Cataler Kogyo Kk Regenerative waste gas purifier
WO1998020238A1 (en) * 1996-11-08 1998-05-14 Matros Technologies, Inc. Emission control system
DE102014220264A1 (en) 2013-10-17 2015-04-23 Ford Global Technologies, Llc A method of operating an exhaust aftertreatment device with a lean NOx trap

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH09262436A (en) * 1996-03-29 1997-10-07 Cataler Kogyo Kk Regenerative waste gas purifier
WO1998020238A1 (en) * 1996-11-08 1998-05-14 Matros Technologies, Inc. Emission control system
DE102014220264A1 (en) 2013-10-17 2015-04-23 Ford Global Technologies, Llc A method of operating an exhaust aftertreatment device with a lean NOx trap

Also Published As

Publication number Publication date
JP2743632B2 (en) 1998-04-22

Similar Documents

Publication Publication Date Title
JPH11123318A (en) Device for cleaning gas containing nitrogen oxide
US8318115B2 (en) Systems and methods for high efficiency regenerative selective catalytic reduction
ATE458134T1 (en) NOX CATALYST WITH EXHAUST TEMPERATURE CONTROL
KR100414430B1 (en) Rotary heat transfer devices applied to gas emissions and methods for continuously purifying gaseous emissions
JPH04326924A (en) Intermittent type apparatus and method for purifying catalyst
KR100597695B1 (en) A Selective Catalyst And Non-Catalyst Reduction System Using Regenerative Heat Recovery
JP4435417B2 (en) Pollution control equipment
JP2743632B2 (en) Noxious gas heating purification equipment
JP2004337781A (en) Exhaust gas treating method, exhaust gas treating system, and catalyst oxidation apparatus
JP2616516B2 (en) Harmful component heating purification device and purification method
RU2002129372A (en) METHOD FOR CLEANING AIR FOR FUEL ELEMENTS AND DEVICE FOR ITS IMPLEMENTATION
JP2720648B2 (en) Hazardous gas heating purification apparatus and operation method thereof
JPH10192657A (en) Catalyst regeneration
JP2692425B2 (en) Catalyst purification device and purification method
JP2789871B2 (en) Catalyst purification device
JP3500802B2 (en) Noxious gas heating purification equipment
JPH0557132A (en) Device for heating and purifying harmful gas
JP3771758B2 (en) CO gas-containing hazardous gas treatment equipment for closed spaces
JP2743641B2 (en) Catalyst purification device
JPS6115740A (en) Regeneration of oxidizing catalyst
JPH04326941A (en) Catalytic cleaning apparatus and cleaning method
JPH09122444A (en) Harmful gas heating and purifying apparatus
JPH0557147A (en) Equipment for heating and purifying harmful gas
JPS60238153A (en) Regeneration of catalyst used in oxidation of carbon monoxide
CN114811623A (en) Heat storage oxidation device for treating low-concentration volatile organic compound exhaust gas

Legal Events

Date Code Title Description
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080206

Year of fee payment: 10

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090206

Year of fee payment: 11

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090206

Year of fee payment: 11

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100206

Year of fee payment: 12

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100206

Year of fee payment: 12

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110206

Year of fee payment: 13

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120206

Year of fee payment: 14

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120206

Year of fee payment: 14