JPH0518529A - Purification system for exhaust gas - Google Patents

Purification system for exhaust gas

Info

Publication number
JPH0518529A
JPH0518529A JP3171024A JP17102491A JPH0518529A JP H0518529 A JPH0518529 A JP H0518529A JP 3171024 A JP3171024 A JP 3171024A JP 17102491 A JP17102491 A JP 17102491A JP H0518529 A JPH0518529 A JP H0518529A
Authority
JP
Japan
Prior art keywords
exhaust gas
adsorbent
oxidation catalyst
purification system
gas purification
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.)
Pending
Application number
JP3171024A
Other languages
Japanese (ja)
Inventor
Ikuo Matsumoto
郁夫 松本
Kenji Tabata
研二 田畑
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 JP3171024A priority Critical patent/JPH0518529A/en
Publication of JPH0518529A publication Critical patent/JPH0518529A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To purify exhaust gas containing contaminative constituents by a process having a long life span and good efficiency. CONSTITUTION:Absorbents 3 are placed in an exhaust gas duct 1, and oxidative catalysts 4 are located on both outsides thereof, and heaters 5 are, furthermore, located on both outsides of the oxidative catalysts 4. When exhaust gas is not flowing in the exhaust gas duct 1, an electric current is applied to the heaters 5, and the oxidative catalysts 4 are heated up to an active temperature thereof. In this way, contaminative constituents are separated from the absorbents 3 and are oxidized away with the oxidative catalysts 4.

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、家庭用、産業用などの
機器類で排気ガス中に含まれる臭気成分や、環境汚染成
分などに含まれる各種のガスを取り除き、クリーを排気
ガス成分となす排気ガス浄化システムに関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention removes odorous components contained in exhaust gas and various gases contained in environmental pollutant components in household and industrial equipment, and uses the cream as an exhaust gas component. The present invention relates to an exhaust gas purification system.

【0002】[0002]

【従来の技術】従来、排気ガスの汚染成分を取り除くに
は、大きく分けて次の二方法がある。すなわち、 酸
化触媒を排気ガス通路の途中に設置し、汚染成分を酸化
分解し、炭酸ガスと水にする。 活性炭の様な吸着材
を排気ガス通路に設置し、汚染成分を選択吸着させ、排
気ガスをクリーンにする。
2. Description of the Related Art Conventionally, there are roughly two methods for removing pollutant components of exhaust gas. That is, an oxidation catalyst is installed in the middle of the exhaust gas passage to oxidize and decompose pollutants into carbon dioxide and water. An adsorbent such as activated carbon is installed in the exhaust gas passage to selectively adsorb pollutants and clean the exhaust gas.

【0003】しかし、上記の前者の方法では酸化触媒を
所定の温度まで高める必要があり、また後者の方法の吸
着材では吸着量が限定されるため、長い期間使用するこ
とはできない。
However, in the former method, it is necessary to raise the oxidation catalyst to a predetermined temperature, and in the latter adsorbent, the adsorption amount is limited, so that it cannot be used for a long period of time.

【0004】[0004]

【発明が解決しようとする課題】そこでこの二方法を合
せたシステム(特願昭63−159981号など)が考
えられるが、排気ガスの流路を度々変更しなくてはなら
ず、またヒータ、ファンなどの切入のシーケンスが複雑
になってしまう欠点がある。
Therefore, a system combining these two methods (Japanese Patent Application No. 63-159981 and the like) is conceivable. However, the exhaust gas flow path must be frequently changed, and a heater, There is a drawback that the sequence of turning on and off the fan becomes complicated.

【0005】本発明は吸着材から脱離された汚染成分を
外部に洩れることなく簡単に処理できる排気ガス浄化シ
ステムを提供することを目的とする。
An object of the present invention is to provide an exhaust gas purification system which can easily treat pollutant components desorbed from an adsorbent without leaking to the outside.

【0006】[0006]

【課題を解決するための手段】上記課題を解決するた
め、本発明は排気ガス流路中に吸着材を設置し、その吸
着材を挟み込む様に吸着材の両端に酸化触媒を設置し、
さらにその近傍に酸化触媒を加熱するためのヒータを置
く構成としたものである。
In order to solve the above-mentioned problems, the present invention installs an adsorbent in an exhaust gas flow path, and installs an oxidation catalyst at both ends of the adsorbent so as to sandwich the adsorbent,
Further, a heater for heating the oxidation catalyst is placed in the vicinity thereof.

【0007】[0007]

【作用】上記した構成により、排気ガス中の汚染成分は
吸着材により捕捉され、排気ガスが流れていない時に酸
化触媒を加熱させるヒータが働らき、酸化触媒が加熱さ
れる。中央に設置された吸着材は酸化触媒の温度ほど高
くなくても、十分汚染成分が脱着され、隣接した酸化触
媒で分解することができる。この際、排気ガス流路には
強制的に風を送る必要はなく、その構成にもよるが、拡
散空気の補給で十分目的は達せられる。吸着材の両端に
酸化触媒を設置しているため、汚染成分がどちらの方向
に流れても、系外に洩れ出すことはなく、また構成的に
も簡単なものになり、運転時のシーケンスも非常に簡単
である。
With the above structure, the pollutant component in the exhaust gas is captured by the adsorbent, and the heater for heating the oxidation catalyst works when the exhaust gas is not flowing, and the oxidation catalyst is heated. Even if the temperature of the adsorbent placed in the center is not as high as the temperature of the oxidation catalyst, the pollutant components are sufficiently desorbed and can be decomposed by the adjacent oxidation catalyst. At this time, it is not necessary to forcibly blow the air into the exhaust gas flow path, and depending on the configuration, supplementation of diffused air can sufficiently achieve the purpose. Since the oxidation catalysts are installed at both ends of the adsorbent, no matter which direction pollutants flow, it will not leak out of the system, and the configuration will be simple, and the operation sequence will also be improved. Very easy.

【0008】[0008]

【実施例】以下、本発明の実施例を添付図面にもとづい
て説明する。図1は本発明の一実施例を示す断面図であ
る。
Embodiments of the present invention will be described below with reference to the accompanying drawings. FIG. 1 is a sectional view showing an embodiment of the present invention.

【0009】本発明の排気ガス浄化システムは図1の下
方より上方に向かって排気ガスが排気ガス流路1中を流
れる様になっており、排気ガス流路1に、その周囲をセ
ラミックフェルト2で巻いた活性炭を素材としたハニカ
カムからなる吸着材3を設置している。吸着材3の両端
に若干の空間をあけて同じくセラミックフェルト2で巻
いた酸化触媒4を設置している。酸化触媒4はコーディ
エライトハニカム(400cell/in2)を担体とし、γ−
Al2 3 を主体としたウォッシュコートを施し、その
上から白金(1g/l)を担持させた極く通常使用され
ている触媒である。酸化触媒の両端にはシーズヒータ5
を配し、酸化触媒4が加熱できる様な構成となってい
る。
In the exhaust gas purifying system of the present invention, the exhaust gas flows in the exhaust gas flow passage 1 from the lower side to the upper side in FIG. The adsorbent 3 made of hanikacam made of activated carbon wound in is installed. On both ends of the adsorbent 3, an oxidation catalyst 4 wound with a ceramic felt 2 is also installed with a slight space left between them. The oxidation catalyst 4 uses a cordierite honeycomb (400 cells / in 2 ) as a carrier and has a γ-
This is a catalyst which is usually used, in which a washcoat mainly composed of Al 2 O 3 is applied and platinum (1 g / l) is supported on the washcoat. A sheath heater 5 is provided at both ends of the oxidation catalyst.
Is arranged so that the oxidation catalyst 4 can be heated.

【0010】次に上記構成の排気ガス浄化システムの動
作について説明する。汚染成分を含んだ排気ガスは排気
ガス流路1を下方より上方に向かって流れ、その途中に
設置されている吸着材3により捕捉される。この時には
ヒータ5は働らかず、酸化触媒4は所定の活性温度にま
で上がっていないため触媒としての働きはない。次に排
気ガスが流れない時にシーズヒータ5に通電され、隣接
した酸化触媒4が加熱され、処理ガスの種類にもよるが
300〜400℃に達する。吸着材4はヒータ5より遠
い位置に設置されているため100〜200℃になり、
吸着されている汚染成分が脱着し始める。脱着された汚
染成分は拡散により酸化触媒4上に至り、外部の拡散空
気により酸化除去される。図1の例では排気ガス流路1
が縦型になっており、ヒータ5がオンした場合、上昇気
流により汚染成分は下方より上方に流れ、上方の酸化触
媒で処理することになるが、排気ガス流路が横型になっ
ていても、汚染成分はどちらかの酸化触媒に引っかか
り、処理することなしに系外に洩れ出ることはない。
Next, the operation of the exhaust gas purification system having the above structure will be described. The exhaust gas containing the pollutant flows from the lower part of the exhaust gas flow path 1 toward the upper part, and is trapped by the adsorbent 3 installed on the way. At this time, the heater 5 does not work, and the oxidation catalyst 4 does not work as a catalyst because it has not reached the predetermined activation temperature. Next, when the exhaust gas does not flow, the sheath heater 5 is energized to heat the adjacent oxidation catalyst 4, and the temperature reaches 300 to 400 ° C., depending on the type of the processing gas. Since the adsorbent 4 is installed at a position farther from the heater 5, the temperature is 100 to 200 ° C.,
The adsorbed pollutant begins to desorb. The desorbed pollutant component reaches the oxidation catalyst 4 by diffusion and is oxidized and removed by the diffusion air outside. In the example of FIG. 1, the exhaust gas flow path 1
Is a vertical type, and when the heater 5 is turned on, the pollutant components flow upward from the lower side due to the ascending air current and are processed by the upper oxidation catalyst, but even if the exhaust gas flow path is horizontal However, the pollutant is caught on either oxidation catalyst and will not leak out of the system without treatment.

【0011】また本実施例では汚染成分を処理する時に
は強制的にファンを働かせることはないが、若干の空気
を送り込んでも良い。ただしあまり大量の空気を送り込
む事は、ヒータからの熱を持ち出し量も多くなり、経済
的には得策ではなく、吸着されている成分及びその量に
もよるが、酸化反応するに足る酸素が供給できれば十分
である。
Further, in the present embodiment, the fan is not forced to work when treating the pollutant, but a small amount of air may be sent. However, sending in too much air is not a good idea economically because the amount of heat taken out from the heater is also large, and depending on the adsorbed component and its amount, sufficient oxygen is supplied for the oxidation reaction. It is enough if possible.

【0012】図2は別の実施例を示す断面図である。図
2は図1の実施例を模型にし、酸化触媒4の大きさを小
さくしたものである。本システムの通常運転時は吸着材
3が主要な働きをするわけで、またその量も大きなもの
を必要とするが、汚染成分を脱着させ、酸化触媒4で処
理する時は高濃度の汚染成分を時間をかけて少しづつ排
出されるため、酸化触媒4の大きさは小さくても良い。
図2の構成及びその働きは図2の実施例と同様であるの
で省略する。
FIG. 2 is a sectional view showing another embodiment. FIG. 2 is a model of the embodiment of FIG. 1 in which the size of the oxidation catalyst 4 is reduced. The adsorbent 3 plays a major role during normal operation of this system, and a large amount of adsorbent is required, but when desorbing pollutant components and treating them with the oxidation catalyst 4, a high concentration of pollutant components is required. Since it is discharged little by little over time, the size of the oxidation catalyst 4 may be small.
The structure and operation of FIG. 2 are similar to those of the embodiment of FIG.

【0013】また吸着材として以上の実施例では活性炭
を使用した例を挙げたが、低温である成分を吸着し、温
度を上げることにより脱着できる性質を有するものであ
れば、その物理的条件に合せて使用することができる。
従って活性炭の他に活性アルミナ、シリカゲル、及び各
種のゼオライトなどが使用できる。
In the above examples, activated carbon was used as the adsorbent. However, if the adsorbent has a property of adsorbing a component at a low temperature and desorbing it by raising the temperature, its physical condition is It can be used together.
Therefore, in addition to activated carbon, activated alumina, silica gel, and various zeolites can be used.

【0014】[0014]

【発明の効果】以上のように本発明の排気ガス浄化シス
テムは以下のような効果がある。 (1)低温度の排気ガスでも効率良く汚染成分を取り除
く事ができ、従来の酸化触媒だけの場合には排気ガス温
度を触媒活性温度にまで上げる必要はなく、省エネルギ
ー的である。 (2)システム自体が簡単な構成になっており、汚染成
分吸着および再生はそのまま同じ構成でよい。 (3)酸化触媒の容量は小さなもので良い。
As described above, the exhaust gas purification system of the present invention has the following effects. (1) Contaminant components can be efficiently removed even with low-temperature exhaust gas, and it is not necessary to raise the exhaust gas temperature to the catalyst activation temperature in the case of only the conventional oxidation catalyst, which is energy saving. (2) The system itself has a simple structure, and the adsorption of pollutant components and the regeneration may be the same. (3) The capacity of the oxidation catalyst may be small.

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

【図1】本発明の一実施例を示す排気ガス浄化システム
の断面図
FIG. 1 is a sectional view of an exhaust gas purification system showing an embodiment of the present invention.

【図2】本発明の他の実施例を示す排気ガス浄化システ
ムの断面図
FIG. 2 is a sectional view of an exhaust gas purification system showing another embodiment of the present invention.

【符号の説明】[Explanation of symbols]

1 排気ガス流路 3 吸着材 4 酸化触媒 5 シーズヒータ 1 Exhaust gas flow path 3 Adsorbent 4 Oxidation catalyst 5 sheathed heater

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】排気流路中に吸着性を有する吸着材を設置
し、その両端に酸化触媒を設置し、さらにその近傍に電
気ヒータを設置した排気ガス浄化システム。
1. An exhaust gas purification system in which an adsorbent having adsorptivity is installed in an exhaust passage, an oxidation catalyst is installed at both ends of the adsorbent, and an electric heater is installed in the vicinity thereof.
【請求項2】吸着材は活性炭、活性アルミナ、ゼオライ
ト、シリカゲルの少なくともいずれか一種類よりなり、
熱を加えることにより吸着成分が脱着される再生可能な
吸着材である請求項1記載の排気ガス浄化システム。
2. The adsorbent comprises at least one selected from activated carbon, activated alumina, zeolite and silica gel,
The exhaust gas purification system according to claim 1, wherein the exhaust gas purification system is a regenerable adsorbent in which adsorbed components are desorbed by applying heat.
JP3171024A 1991-07-11 1991-07-11 Purification system for exhaust gas Pending JPH0518529A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3171024A JPH0518529A (en) 1991-07-11 1991-07-11 Purification system for exhaust gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3171024A JPH0518529A (en) 1991-07-11 1991-07-11 Purification system for exhaust gas

Publications (1)

Publication Number Publication Date
JPH0518529A true JPH0518529A (en) 1993-01-26

Family

ID=15915676

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3171024A Pending JPH0518529A (en) 1991-07-11 1991-07-11 Purification system for exhaust gas

Country Status (1)

Country Link
JP (1) JPH0518529A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100342178C (en) * 2004-12-29 2007-10-10 上海交通大学 Oil smoke catalytic decomposition treating apparatus for range hoods
JP2013217639A (en) * 2013-04-26 2013-10-24 Sharp Corp Heating cooker
CN103742994A (en) * 2013-11-26 2014-04-23 南通华新环保设备工程有限公司 Novel air purifier
CN110375357A (en) * 2019-06-27 2019-10-25 宁波方太厨具有限公司 A kind of range hood and its control method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100342178C (en) * 2004-12-29 2007-10-10 上海交通大学 Oil smoke catalytic decomposition treating apparatus for range hoods
JP2013217639A (en) * 2013-04-26 2013-10-24 Sharp Corp Heating cooker
CN103742994A (en) * 2013-11-26 2014-04-23 南通华新环保设备工程有限公司 Novel air purifier
CN103742994B (en) * 2013-11-26 2016-05-04 南通华新环保设备工程有限公司 A kind of air purifier
CN110375357A (en) * 2019-06-27 2019-10-25 宁波方太厨具有限公司 A kind of range hood and its control method
CN110375357B (en) * 2019-06-27 2021-06-15 宁波方太厨具有限公司 Range hood and control method thereof

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