JP2734824B2 - Noxious gas heating purification equipment - Google Patents

Noxious gas heating purification equipment

Info

Publication number
JP2734824B2
JP2734824B2 JP3217487A JP21748791A JP2734824B2 JP 2734824 B2 JP2734824 B2 JP 2734824B2 JP 3217487 A JP3217487 A JP 3217487A JP 21748791 A JP21748791 A JP 21748791A JP 2734824 B2 JP2734824 B2 JP 2734824B2
Authority
JP
Japan
Prior art keywords
exhaust gas
heat
temperature
heating
main body
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
JP3217487A
Other languages
Japanese (ja)
Other versions
JPH0557133A (en
Inventor
彰 橋本
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 JP3217487A priority Critical patent/JP2734824B2/en
Publication of JPH0557133A publication Critical patent/JPH0557133A/en
Application granted granted Critical
Publication of JP2734824B2 publication Critical patent/JP2734824B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Treating Waste Gases (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、各種燃焼機器の排ガス
中に含まれる一酸化炭素(CO),炭化水素(HC)な
どの悪臭成分や有害成分を加熱し酸化浄化する加熱浄化
装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a heating and purifying apparatus for heating and oxidizing and purifying malodorous and harmful components such as carbon monoxide (CO) and hydrocarbons (HC) contained in exhaust gas from various types of combustion equipment.

【0002】[0002]

【従来の技術】近年、各種の燃焼機器や乾燥,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。
またバンド機の動作中や樹脂,ビニールなどの融着時に
も有害ガスが発生し、その浄化が求められている。CO
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。一般に、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。酸
化触媒を用いる方法では200〜400℃の温度範囲で
反応を進めることができ熱エネルギーの消費を節減する
ことができる。
2. Description of the Related Art In recent years, it has become essential to purify and discharge CO and HC components generated during various types of combustion equipment and during drying and heat treatment due to their harmfulness and odor.
In addition, harmful gases are generated during the operation of the band machine or during fusion of resin, vinyl, and the like, and purification of the gases is required. CO
As a method for purifying the exhaust gas and HC components, a method in which the exhaust gas itself is heated and reacted with oxygen in the gas has the highest purification efficiency and high reliability. Generally, in order for oxygen in air to react with CO or HC, a temperature of 800 to 900 ° C. or higher is required. In the method using the oxidation catalyst, the reaction can proceed in a temperature range of 200 to 400 ° C., and the consumption of heat energy can be reduced.

【0003】以下に従来の有害ガス浄化装置について図
面を参照しながら説明する。図3(A),(B)に従来
の触媒浄化装置の構成を示す。図3(A)は触媒浄化装
置本体、図3(B)は熱交換器も含めたシステムの構成
を示す。図に示すように触媒浄化装置本体10中には熱
交換機16,加熱装置12,触媒13が設けられてい
る。排ガスはガス入口11から触媒加熱装置本体10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器を用いたシステムが
図3(B)である。図に示すようにガス流入口17から
導入され熱交換器16で昇温された排ガスは、矢印に沿
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、再び熱交換器16に入り冷却されガス流出口
18から排出される。この熱交換器により排ガスの昇温
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
なくすることができる。
A conventional harmful gas purifying apparatus will be described below with reference to the drawings. FIGS. 3A and 3B show the configuration of a conventional catalyst purifying device. FIG. 3A shows the configuration of a catalyst purification device main body, and FIG. 3B shows the configuration of a system including a heat exchanger. As shown in the figure, a heat exchanger 16, a heating device 12, and a catalyst 13 are provided in the catalyst purification device main body 10. The exhaust gas is introduced from the gas inlet 11 into the catalyst heating device main body 10, the temperature is raised to a predetermined temperature by the heating device 12, CO and HC are oxidized and purified by the catalyst 13, and the outlet 14
Is discharged from At this time, the energy required for raising the temperature of the exhaust gas is discharged together with the gas. FIG. 3B shows a system that uses a heat exchanger to recover a part of this energy. As shown in the figure, the exhaust gas introduced from the gas inlet 17 and heated in the heat exchanger 16 flows along the arrow and proceeds to the catalyst purification device main body 10. The purified gas enters the heat exchanger 16 again, is cooled, and is discharged from the gas outlet 18. With this heat exchanger, a part of the energy required for raising the temperature of the exhaust gas can be recovered and the energy loss can be reduced.

【0004】これに対し図4(A),(B)は、蓄熱体
を用いた加熱浄化装置の例で、図4(A)の状態と図4
(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。熱交換は蓄熱体2,加熱
装置4で行われる。有害な排ガスの流れはダンパー9に
より制御される。図4(A)では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
置本体5内に入る。さらに、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から排出されガスの流
出口20へ進む。一定時間経過後図4(B)に示すよう
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。すなわち図4(A)で排ガスから熱を奪った
上部の蓄熱体2が今度は排ガスを加熱するように働き、
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。上記の工程を繰り返すことにより浄化装置内に熱が
閉じこめられ省エネルギーとなる。
On the other hand, FIGS. 4A and 4B show an example of a heating and purifying apparatus using a heat accumulator, in which the state of FIG.
The heat energy is reduced by alternately repeating the state of (B). Heat exchange is performed by the heat storage unit 2 and the heating device 4. The flow of the harmful exhaust gas is controlled by the damper 9. In FIG. 4A, the exhaust gas is the gas inlet 1
From FIG. 9, proceed as indicated by an arrow 7 and enter the purifier main body 5 from the gas inlet / outlet 1. Further, the heat passes through the lower heat storage body 2 and is heated and purified by the heating device 4. The heat is taken away by the upper heat storage body 2, cooled, discharged from the gas inlet / outlet 8, and proceeds to the gas outlet 20. After a certain period of time, as shown in FIG. 4B, the dampers 9 are respectively operated so as to change the flow of the exhaust gas. That is, in FIG. 4 (A), the upper heat storage body 2 which has taken heat from the exhaust gas works to heat the exhaust gas,
Supplement some or most of the energy that heats the exhaust gas. By repeating the above steps, heat is trapped in the purification device, and energy is saved.

【0005】[0005]

【発明が解決しようとする課題】しかし、図3(B)の
浄化装置に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おり、熱交換効
率は50〜60%が限界である。また、SOxやNOx
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。図4(A),
(B)の浄化装置では耐食性の蓄熱材を用いることによ
り、図3(B)の浄化装置の欠点を解消することがで
き、熱交換効率の高い浄化装置を実現できる。しかし、
排ガスの中に含まれるHCやCO成分の濃度が高い場
合、加熱浄化時に発生するHC,COの発熱分が浄化装
置内部の蓄熱材に蓄積され蓄熱材が異常高温になること
があった。特に触媒を用いた装置では、触媒の性能劣化
が起こり浄化能力が低下するという問題があった。
However, the heat exchanger 16 used in the purifying apparatus shown in FIG. 3B is usually made of thin aluminum having good heat conductivity, and has a heat exchange efficiency of 50-60. % Is the limit. Further, aluminum cannot be used for exhaust gas containing corrosive gas such as SO x and NO x because aluminum corrodes. FIG. 4 (A),
By using a corrosion-resistant heat storage material in the purifier of FIG. 3B, the disadvantage of the purifier of FIG. 3B can be eliminated, and a purifier with high heat exchange efficiency can be realized. But,
When the concentrations of HC and CO components contained in the exhaust gas are high, heat generated by HC and CO generated during heating purification is accumulated in the heat storage material inside the purification device, and the heat storage material sometimes becomes abnormally high in temperature. Particularly, in a device using a catalyst, there is a problem that the performance of the catalyst is deteriorated and the purification ability is reduced.

【0006】本発明は、このような課題を解決するもの
で、有害成分が高濃度で発熱量の多い排ガスの場合でも
安心して使用できる加熱浄化装置を提供することを目的
とするものである。
An object of the present invention is to provide a heating and purifying apparatus which can be used safely even in the case of exhaust gas having a high concentration of harmful components and a large amount of heat generation.

【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、浄化装置本体中を
流れる排ガスの流れ方向を、一定時間毎に交互に変換す
るダンパーと、前記浄化装置本体中央に設けた加熱装置
と、両端から中央への排ガス流路の途中にそれぞれ設け
た蓄熱体とを備えた加熱浄化装置であって、出口と入口
を切り替えて排ガスの流れ方向を反転させる制御手段と
して、時間的なものに加え浄化装置本体の中央部分に設
けた温度センサーにより温度を検出し、温度により排ガ
スの流れ方向を反転させるようにしたものである。
To achieve this object, a harmful gas heating and purifying apparatus according to the present invention comprises: a damper for alternately changing a flow direction of exhaust gas flowing in a purifying apparatus main body at regular intervals; A heating and purifying device comprising a heating device provided at the center of the purifier main body and a heat storage element provided in the middle of the exhaust gas flow path from both ends to the center, wherein the flow direction of the exhaust gas is reversed by switching the outlet and the inlet. As a control means for controlling the temperature, a temperature sensor is provided at a central portion of the main body of the purification device in addition to a time-dependent one, and the temperature is detected, and the flow direction of the exhaust gas is reversed according to the temperature.

【0008】[0008]

【作用】この構成により、一定時間有害成分を含んだ排
ガスを一端(入り口)から浄化装置内に導入し、蓄熱体
を経て加熱装置により加熱浄化し、もう一方の蓄熱体層
で冷却され他端(出口)から排出する。タイマーにより
浄化装置本体の両端に設けられたダンパーを操作し、排
ガスの流れを逆転する。この構成により蓄熱材は、吸熱
と放熱の役割を交替し、浄化装置本体から熱が逃げない
ようにできる。
According to this structure, exhaust gas containing harmful components is introduced into the purifier from one end (entrance) for a certain period of time, and is purified by heating through the heat accumulator, cooled by the other heat accumulator layer and cooled by the other heat accumulator layer. (Exit). A damper provided at both ends of the purifier body is operated by a timer to reverse the flow of the exhaust gas. With this configuration, the heat storage material alternates between the functions of heat absorption and heat radiation, so that heat cannot escape from the purification device body.

【0009】また、排ガス中に高濃度のHCやCO成分
が混入していると加熱浄化時に発熱を伴い、その熱が熱
ロス分とつりあうまで浄化装置内が高温になる。ここで
浄化装置内部の温度制御機構により、定めた温度以上に
なった場合、排ガスの流れ方向が逆転しないように制御
すると定められた温度以下になるまで一方向に流れ続け
出口部分から熱エネルギーが放出し浄化装置内が異状高
温になることがない。浄化装置内の温度が定めた温度を
下回ると排ガスの流れ方向を逆転し、余分な熱を加熱装
置により与えることを避けることとなる。
Further, if high concentrations of HC and CO components are mixed in the exhaust gas, heat is generated at the time of heat purification, and the temperature inside the purification device becomes high until the heat balances with the heat loss. Here, when the temperature becomes higher than the specified temperature by the temperature control mechanism inside the purification device, if the flow direction of the exhaust gas is controlled so as not to be reversed, the exhaust gas continues to flow in one direction until the temperature becomes equal to or lower than the predetermined temperature, and the heat energy from the outlet portion is generated. There is no abnormal high temperature inside the purifier. When the temperature in the purification device is lower than the predetermined temperature, the flow direction of the exhaust gas is reversed, and it is possible to avoid applying extra heat by the heating device.

【0010】[0010]

【実施例】以下に本発明の一実施例の有害ガス浄化装置
を図面を参照しながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A harmful gas purifying apparatus according to one embodiment of the present invention will be described below with reference to the drawings.

【0011】(実施例1)図1(A),(B)に本発明
の実施例の加熱浄化装置の構成を示す。図に示すよう
に、排ガスはガスの入り口側流路19よら入り排ガスの
出口側流路20から出て行く。浄化装置本体5は蓄熱体
2と加熱装置4を備え、ダンパー9により浄化装置内の
排ガスの流れ方向を逆転させるように構成されている。
温度センサ21は加熱装置の動作を制御し、温度センサ
22は過昇温を制御する。もちろんこの2つのセンサー
を同一のもので兼用しても良い。図1(A)と図1
(B)は浄化装置内部の排ガスの流れが逆になった状態
を示す。まず図1(A)の状態を説明する。排ガスは排
ガスの流入口19から入り、矢印7で示したように排ガ
スの入口1から浄化装置本体5に入り、下部の蓄熱材2
を通り加熱装置4により加熱浄化される。上部の蓄熱材
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排ガスの出口8から排ガスの
流出口20の方向へ排出される。通常は一定時間後ダン
パー9を操作し、浄化装置本体5内を排ガスが上から下
へ流れるようにする。この状態を図1(B)に示す。し
かし、排ガス中に高濃度のHCやCO成分が含まれてい
ると下部の蓄熱材2により加熱されて反応し温度が上が
る。この熱は上下の蓄熱材によって蓄えられるため、サ
イクルを重ねるたびに高温になる。温度センサー22が
異常高温を感知した場合、温度が下がるまで排ガスの流
れを逆転せず一定方向でガスを流し続ける。風下側に位
置している蓄熱材にも蓄熱できる限界があり、徐々に熱
を出口方向に放出することになり冷却浄化装置が危険な
状態にならないようにする。
(Embodiment 1) FIGS. 1A and 1B show a configuration of a heating and purifying apparatus according to an embodiment of the present invention. As shown in the figure, the exhaust gas exits through an inlet-side flow path 19 of the gas and enters through an outlet-side flow path 20 of the exhaust gas. The purifying device main body 5 includes the heat storage body 2 and the heating device 4, and is configured so that the flow direction of the exhaust gas in the purifying device is reversed by the damper 9.
The temperature sensor 21 controls the operation of the heating device, and the temperature sensor 22 controls overheating. Of course, the same two sensors may be used in common. FIG. 1 (A) and FIG.
(B) shows a state in which the flow of the exhaust gas inside the purification device is reversed. First, the state of FIG. The exhaust gas enters through the exhaust gas inlet 19, enters the purifier main body 5 from the exhaust gas inlet 1 as shown by the arrow 7, and enters the lower heat storage material 2.
And is heated and purified by the heating device 4. When passing through the upper heat storage material 2, the thermal energy of the exhaust gas is taken away, and the exhaust gas is cooled and discharged from the exhaust gas outlet 8 toward the exhaust gas outlet 20. Normally, after a certain time, the damper 9 is operated so that the exhaust gas flows from the top to the bottom in the purification device main body 5. This state is shown in FIG. However, if the exhaust gas contains a high concentration of HC or CO components, it is heated by the lower heat storage material 2 and reacts to increase the temperature. Since this heat is stored by the upper and lower heat storage materials, the temperature rises with each cycle. When the temperature sensor 22 detects an abnormally high temperature, the gas continues to flow in a certain direction without reversing the flow of the exhaust gas until the temperature decreases. There is a limit to heat storage in the heat storage material located on the leeward side, and heat is gradually released in the direction of the outlet, so that the cooling and purifying device is not put into a dangerous state.

【0012】(実施例2)つぎに本発明の実施例2につ
いて、図面を参照しながら説明する。
Second Embodiment Next, a second embodiment of the present invention will be described with reference to the drawings.

【0013】本実施例2の構成は、図2に示すように実
施例1に対してそれぞの蓄熱材の間に酸化触媒3を配置
したものである。この酸化触媒の働きは低い温度で有害
ガスを浄化することである。しかし、高温になると触媒
能力が低下するので、注意する必要がある。本実施例で
は実施例1と同様にして過昇温を検知し、ダンパーを制
御する温度センサー22が設置されている。この制御手
段により信頼性の高い有害ガス浄化装置を実現すること
ができる。
The structure of the second embodiment is different from the first embodiment in that an oxidation catalyst 3 is arranged between the heat storage materials as shown in FIG. The function of this oxidation catalyst is to purify harmful gases at low temperatures. However, attention must be paid to the fact that as the temperature increases, the catalytic ability decreases. In this embodiment, a temperature sensor 22 for detecting an excessive temperature rise and controlling a damper is provided in the same manner as in the first embodiment. With this control means, a highly reliable harmful gas purifying device can be realized.

【0014】[0014]

【発明の効果】以上の実施例の説明からも明らかなよう
に本発明によれば、浄化装置本体中を流れる排ガスの流
れ方向を一定時間毎に交互に変換するダンパーと、浄化
装置本体中央に加熱装置を設け、両端から中央への排ガ
ス流路の途中にそれぞれ蓄熱体を設けた加熱浄化装置で
あって、出口,入り口を切り替え排ガスの流れ方向を反
転させる命令制御として、タイマー制御に加え本体の中
央部分に設けた温度センサーの温度情報を読みとり、定
められた温度以上になった場合排ガスの流れ方向を反転
させないで熱をガスと一緒に排出する。これにより排ガ
ス中に高濃度のHCやCO成分が混入した場合の加熱浄
化時に起こる異常昇温とそれに伴う浄化装置の劣化や破
壊および触媒,蓄熱材の破損を防ぐことができ、信頼性
の高い有害ガス加熱浄化装置を提供することができる。
As is apparent from the above description of the embodiment, according to the present invention, a damper for alternately changing the flow direction of the exhaust gas flowing in the purification device main body at regular intervals, and a damper at the center of the purification device main body. A heating and purifying device provided with a heating device and provided with a heat storage element in the middle of an exhaust gas flow path from both ends to the center. In addition to the timer control, the main body is used as a command control for switching an outlet and an inlet to reverse a flow direction of the exhaust gas. The temperature information provided by the temperature sensor provided at the center of the device is read, and when the temperature exceeds a predetermined temperature, heat is discharged together with the gas without reversing the flow direction of the exhaust gas. As a result, it is possible to prevent abnormal temperature rise that occurs at the time of heating and purification when high concentrations of HC and CO components are mixed in the exhaust gas, and to prevent deterioration and destruction of the purification device and damage to the catalyst and the heat storage material due to the high temperature. A harmful gas heating purification device can be provided.

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

【図1】(A)は本発明の実施例1の有害ガス加熱浄化
装置の構成図 (B)は(A)の排気ガスの流れを反転した状態を示す
構成図
FIG. 1A is a configuration diagram of a harmful gas heating / purifying apparatus according to a first embodiment of the present invention. FIG. 1B is a configuration diagram showing a state in which the flow of exhaust gas in FIG.

【図2】(A)は本発明の実施例2の有害ガス加熱浄化
装置の構成図 (B)は(A)の排気ガスの流れを反転した状態を示す
構成図
FIG. 2A is a configuration diagram of a harmful gas heating / purifying apparatus according to a second embodiment of the present invention. FIG. 2B is a configuration diagram showing a state in which the flow of exhaust gas in FIG.

【図3】(A)は従来の触媒浄化装置本体の構成図 (B)は熱交換機も含めた従来の触媒浄化システムの構
成図
FIG. 3A is a configuration diagram of a conventional catalyst purification device main body, and FIG. 3B is a configuration diagram of a conventional catalyst purification system including a heat exchanger.

【符号の説明】[Explanation of symbols]

1 排ガスの入口 2 蓄熱材 3 触媒 4 加熱装置 5 浄化装置本体 6 排ガスの流路 7 排ガスの流れ方向 8 排ガスの出口 9 ダンパー 19 排ガスの流入口 20 排ガスの流出口 21 加熱装置のセンサー 22 過昇温感知センサー DESCRIPTION OF SYMBOLS 1 Exhaust gas inlet 2 Heat storage material 3 Catalyst 4 Heater 5 Purifier main body 6 Exhaust gas flow path 7 Exhaust gas flow direction 8 Exhaust gas outlet 9 Damper 19 Exhaust gas inlet 20 Exhaust gas outlet 21 Heater sensor 22 Excessive rise Temperature sensing sensor

フロントページの続き (51)Int.Cl.6 識別記号 FI B01D 53/87 Continued on the front page (51) Int.Cl. 6 Identification code FI B01D 53/87

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 浄化装置本体中を流れる排ガスの流れ方
向を一定時間毎に交互に変換するダンパーと、前記浄化
装置本体中央に設けた加熱装置と、両端から中央へ排ガ
ス流路の途中に設けた畜熱体と、前記浄化装置本体の中
央部に設けた温度センサーを備えた加熱浄化装置であっ
て、一定時間毎に排ガスの流れ方向を切り替える制御手
段と、浄化装置本体内の前記温度センサーでの温度検出
により排ガスの流れ方向を切り替える制御手段とをとも
備えた有害ガス加熱浄化装置。
1. A damper for alternately changing the flow direction of exhaust gas flowing through a purification device main body at regular intervals, a heating device provided at the center of the purification device main body, and a heating device provided in the middle of the exhaust gas flow path from both ends to the center. Inside the body of the purification device
A heating and purifying apparatus having a temperature sensor provided in a central portion, wherein the control means switches a flow direction of exhaust gas at predetermined time intervals, and the flow direction of the exhaust gas is switched by temperature detection by the temperature sensor in the main body of the purification apparatus. A harmful gas heating and purifying apparatus including both control means.
JP3217487A 1991-08-28 1991-08-28 Noxious gas heating purification equipment Expired - Lifetime JP2734824B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3217487A JP2734824B2 (en) 1991-08-28 1991-08-28 Noxious gas heating purification equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3217487A JP2734824B2 (en) 1991-08-28 1991-08-28 Noxious gas heating purification equipment

Publications (2)

Publication Number Publication Date
JPH0557133A JPH0557133A (en) 1993-03-09
JP2734824B2 true JP2734824B2 (en) 1998-04-02

Family

ID=16705011

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3217487A Expired - Lifetime JP2734824B2 (en) 1991-08-28 1991-08-28 Noxious gas heating purification equipment

Country Status (1)

Country Link
JP (1) JP2734824B2 (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5345090Y2 (en) * 1973-03-09 1978-10-28

Also Published As

Publication number Publication date
JPH0557133A (en) 1993-03-09

Similar Documents

Publication Publication Date Title
US6280691B1 (en) Indoor air purification system
JP2004530488A (en) High performance air cleaning system and method
US4877592A (en) Method of catalytic cleaning of exhaust gases
JP5270912B2 (en) Catalytic oxidation treatment apparatus and catalytic oxidation treatment method
JP2007154717A (en) Exhaust emission control device and exhaust emission control method for internal combustion engine
JPH04326924A (en) Intermittent type apparatus and method for purifying catalyst
WO2007010985A1 (en) Exhaust gas purifier
JP2734824B2 (en) Noxious gas heating purification equipment
JP2734823B2 (en) Noxious gas heating purification equipment
JP2789871B2 (en) Catalyst purification device
JP3500802B2 (en) Noxious gas heating purification equipment
JP2616516B2 (en) Harmful component heating purification device and purification method
CN110778384B (en) Control method and control device of post-processing system and post-processing system
JPH09122446A (en) Gas heating and purifying apparatus
WO2016084564A1 (en) Engine exhaust purification control method
JP2743632B2 (en) Noxious gas heating purification equipment
JP2720648B2 (en) Hazardous gas heating purification apparatus and operation method thereof
JP2692425B2 (en) Catalyst purification device and purification method
JP2743641B2 (en) Catalyst purification device
JPH04326941A (en) Catalytic cleaning apparatus and cleaning method
JP6753151B2 (en) Exhaust gas purification system for internal combustion engine and exhaust gas purification method for internal combustion engine
JP4348020B2 (en) Method for regenerating catalyst for exhaust gas treatment
JPS6115740A (en) Regeneration of oxidizing catalyst
JP2831910B2 (en) Method for regenerating CO oxidation catalyst
JP3055270B2 (en) Exhaust gas purification device for internal combustion engine

Legal Events

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

Free format text: PAYMENT UNTIL: 20080109

Year of fee payment: 10

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

Free format text: PAYMENT UNTIL: 20090109

Year of fee payment: 11

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

Free format text: PAYMENT UNTIL: 20090109

Year of fee payment: 11

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

Free format text: PAYMENT UNTIL: 20100109

Year of fee payment: 12

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

Free format text: PAYMENT UNTIL: 20110109

Year of fee payment: 13

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

Free format text: PAYMENT UNTIL: 20110109

Year of fee payment: 13

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

Free format text: PAYMENT UNTIL: 20120109

Year of fee payment: 14

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

Free format text: PAYMENT UNTIL: 20120109

Year of fee payment: 14