JPH054026A - Harmful component heating and cleaning device - Google Patents

Harmful component heating and cleaning device

Info

Publication number
JPH054026A
JPH054026A JP3156472A JP15647291A JPH054026A JP H054026 A JPH054026 A JP H054026A JP 3156472 A JP3156472 A JP 3156472A JP 15647291 A JP15647291 A JP 15647291A JP H054026 A JPH054026 A JP H054026A
Authority
JP
Japan
Prior art keywords
gas
chamber
heat storage
heat
heating
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
JP3156472A
Other languages
Japanese (ja)
Other versions
JP2616516B2 (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 JP3156472A priority Critical patent/JP2616516B2/en
Publication of JPH054026A publication Critical patent/JPH054026A/en
Application granted granted Critical
Publication of JP2616516B2 publication Critical patent/JP2616516B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To provide the cleaning device which is small in energy loss and is simple in construction as the cleaning device which heats, oxidizes and cleans the harmful components, such as CO (carbon monoxide), HC (hydrocarbon), bacteria, ticks, etc., in various kids of gases. CONSTITUTION:The apertures of the two chambers of the cleaning device body consisting of the two chambers which are communicated with each other at the closed other ends and have heaters and catalysts exist on the same plane and allow the inflow and outflow of gases or the communication with the outdoor air by means of dampers which can be controlled by one driving system. Heat accumulating body layers which are respectively resistant to corrosion are installed to the mid-ways of the gas flow passages from the opening ends to the heaters. The gases are applied with heat from the one heat accumulating body layer and are thereby heated and cleaned. The gases are deprived of the heat by another heat accumulating body layer and are thereby cooled and discharged. The flow of the gases is reversed through the process introducing the outdoor air by driving the dampers at every specified time, by which the respective heat accumulating body layers are subjected to an exchange of the heating or cooling. The heat energy necessary for heating of the gases is confined into the cleaning device in this way and the short passing of the uncleaned harmful components is obviated.

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、各種排ガス中に混入し
たCO(一酸化炭素),HC(炭化水素)等の悪臭成分
や有害成分、細菌,ダニ等を適正温度に加熱し酸化浄
化、死滅する加熱浄化装置に関するものである。
BACKGROUND OF THE INVENTION The present invention is directed to oxidative purification by heating malodorous or harmful components such as CO (carbon monoxide) and HC (hydrocarbons) mixed in various exhaust gases, bacteria, mites, etc. to an appropriate temperature. The present invention relates to a heat purifying device that is dead.

【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
化しは排出することが必要不可欠なものになっている。
バンド機や樹脂,ビニール等の融着時に有害ガスが発生
し、その浄化が求められている。また生活環境の中で
は、タバコの煙や細菌,ダニ等の浄化も必要となってい
る。COやHC成分の浄化や細菌,ダニ等の死滅方法と
しては、有害成分を含んだ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。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。
酸化触媒を用いる方法では200〜400℃の温度範囲
で反応を進める事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.
Hazardous gas is generated during fusion of band machines, resins, vinyl, etc., and its purification is required. Also, in the living environment, it is necessary to purify tobacco smoke, bacteria, mites and the like. As a method of purifying CO and HC components and killing bacteria, mites and the like, a method of heating a gas containing a harmful component itself and reacting it with oxygen in the gas has the highest purification efficiency and high reliability. In order to raise the temperature of the gas and allow oxygen in the air to react with CO and HC, a temperature of 800 to 900 ° C. or higher is required.
With the method using an oxidation catalyst, the reaction can proceed in the temperature range of 200 to 400 ° C. and waste of thermal energy can be eliminated.

【0003】以下、従来の加熱による有害成分浄化装置
について説明する。図3は、従来の触媒加熱浄化装置の
一例で、(a)は触媒浄化装置本体、(b)は熱交換も
含めたシステムを示す。図中、25は触媒浄化装置本
体、27は熱交換機、22は加熱装置、23は触媒を示
す。(a)で有害成分を含んだガスは20の入口から触
媒加熱装置本体に導入され、22の加熱装置により所定
の温度に昇温され、23の触媒によりCO,HC等が酸
化浄化され、24の出口から排出される。この時ガスの
昇温に要したエネルギーはガスと一緒に排出される事に
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26から導
入され27の熱交換機で昇温されたガスは、矢印に沿っ
て流れ、25の触媒浄化装置本体に進む。ここで加熱浄
化されたガスは、再び27の熱交換機に入り冷却され2
8から排出する。すなわち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
物である。
A conventional heating harmful substance purification apparatus will be described below. FIG. 3 shows an example of a conventional catalyst heating and purifying apparatus, (a) shows the main body of the catalytic purifying apparatus, and (b) shows a system including heat exchange. In the figure, 25 is a catalyst purifying device main body, 27 is a heat exchanger, 22 is a heating device, and 23 is a catalyst. In (a), the gas containing harmful components is introduced into the main body of the catalyst heating device through the inlet of 20, heated to a predetermined temperature by the heating device of 22, and CO, HC, etc. are oxidized and purified by the catalyst of 23, and 24 Is discharged from the exit of. At this time, the energy required to raise the temperature of the 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 gas introduced from 26 and heated by the heat exchanger of 27 flows along the arrow and proceeds to the main body of the catalyst purifying device of 25. The gas that has been heated and purified here enters the heat exchanger 27 again and is cooled.
Discharge from 8. That is, it is an object to reduce energy loss by recovering a part of the energy required for heating the gas.

【0004】一方これに対し図4は、蓄熱体を用いた加
熱浄化装置の例で、(a)の状態と(b)の状態を交互
に繰り返す事により熱エネルギーの削減をはかったもの
である。6が蓄熱体、10が加熱装置である。29,3
0は有害成分を含んだガスの流れを制御するダンパーを
示す。(a)でガスは1の流入口から3の矢印のように
進み27の入口から下部の蓄熱体を通過する。そして1
0の加熱装置により加熱,浄化され上部の蓄熱体で冷却
されて28の出口から11の流出口へ進む。次に一定時
間後(b)のようなガスの流れになるようにダンパー2
9,30をそれぞれ操作する。すなわち(a)で加熱浄
化されたガスから熱を奪った上部の蓄熱体が今度はガス
に熱を与えるように働き、ガスを加熱するエネルギーの
一部または大部分を補うように働く。すなわちこの浄化
装置内で熱が往復し省エネルギーとなる。触媒を用いる
場合は上下の蓄熱体層の間に置くことができる。
On the other hand, FIG. 4 shows an example of a heat purifying apparatus using a heat storage body, in which the state of (a) and the state of (b) are alternately repeated to reduce heat energy. . 6 is a heat storage body, and 10 is a heating device. 29,3
0 indicates a damper that controls the flow of gas containing harmful components. In (a), the gas advances from the inlet 1 as shown by the arrow 3 and passes from the inlet 27 to the lower heat storage body. And 1
It is heated and purified by the heating device No. 0, cooled by the upper heat storage body, and proceeds from the outlet 28 to the outlet 11. Next, after a certain period of time, the damper 2 is adjusted so that the gas flows as shown in (b).
Operate 9, 30 respectively. That is, the upper heat storage body, which has removed heat from the gas that has been heated and purified in (a), now works to give heat to the gas, and works to supplement a part or most of the energy for heating the gas. That is, the heat is reciprocated in the purifying device to save energy. When a catalyst is used, it can be placed between the upper and lower heat storage layers.

【0005】[0005]

【発明が解決しようとする課題】しかしながら上記(図
3)で示す従来例1の構成で用いられる熱交換機27
は、通常伝導率のよ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S
OxやNOx等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)に示す従来例2では耐食性の蓄熱体を用いる事によ
り従来例1の欠点を解消できるものであるが蓄熱体や加
熱装置の側壁からの放熱やダンパー等の構成が複雑であ
ったりする欠点があった。また浄化装置内部でガスの流
れを切り替えるとき、ガスの出入口や風上側の蓄熱体層
に溜まったガスが浄化されないまま排出される構成であ
った。
However, the heat exchanger 27 used in the configuration of the conventional example 1 shown in the above (FIG. 3).
Is usually mainly composed of thin aluminum with good conductivity, and the heat exchange efficiency is limited to 50 to 60%. Also S
Aluminum cannot be used for exhaust gas containing corrosive gases such as Ox and NOx because aluminum corrodes. The conventional example 2 shown in FIG. 4 can solve the drawbacks of the conventional example 1 by using a corrosion-resistant heat storage material, but the heat radiation from the heat storage material and the side wall of the heating device, the configuration of the damper, etc. may be complicated. There was a drawback to Further, when the gas flow is switched inside the purifier, the gas accumulated in the inlet / outlet of the gas and the heat storage layer on the windward side is discharged without being purified.

【0006】本発明は、上記従来例2の問題点を解決す
るもので、放熱によるロスを最小限に抑えるとともにダ
ンパーの構造等を簡素化し、未浄化のまま有害成分が排
出される事がない有害成分浄化装置を提供することを目
的としている。
The present invention solves the problem of the above-mentioned conventional example 2, in which the loss due to heat dissipation is minimized and the structure of the damper is simplified so that no harmful components are discharged without being purified. It is intended to provide a harmful component purification device.

【0007】[0007]

【課題を解決するための手段】上記の目的を達成するた
めに本発明の有害成分浄化装置は、本体の一端が開口し
他端が閉じた構造であり、閉じられた部分で互いに連通
した2室を有し、それぞれの室の開口部側に蓄熱体層を
配置し、閉じられた側に加熱装置および触媒を配置する
とともに、それぞれの室の開口部が同一面上に配置され
1つの駆動系で制御されるダンパーを介して、それぞれ
の室がガスの流入流路および流出流路、外気雰囲気のい
ずれかと連通できる構成を有している。
In order to achieve the above object, the harmful component purifying apparatus of the present invention has a structure in which one end of the main body is open and the other end is closed, and the closed parts communicate with each other. The chamber has a chamber, the heat storage layer is arranged on the opening side of each chamber, the heating device and the catalyst are arranged on the closed side, and the openings of the chambers are arranged on the same plane to form one drive. Each chamber is configured to be able to communicate with any of the gas inflow passage and the outflow passage and the outside air atmosphere via a damper controlled by the system.

【0008】[0008]

【作用】この構成による有害成分を含んだガスの浄化に
ついて説明する。この浄化装置本体の2室は同一面上に
配置した開口部でそれぞれガスの流出流路、流入流路ま
たは外気雰囲気の一方とのみ連通した状態で作動する。
まず1のパターンとして有害成分を含んだガスは流入流
路から一方の室に流入し蓄熱体及び加熱装置、触媒によ
り加熱浄化されもう一方の室の蓄熱体層で冷却されガス
流出流路に排出される。この時ガスの冷却側で使われる
蓄熱体層は、ガスから熱を奪い蓄熱する。
The function of purifying the gas containing the harmful component by this structure will be described. The two chambers of the main body of the purifying device operate at the openings arranged on the same plane, respectively in communication with only one of the gas outflow passage, the inflow passage or the outside air atmosphere.
First, as a first pattern, a gas containing harmful components flows into one chamber from an inflow passage, is heated and purified by a heat storage body, a heating device, and a catalyst, is cooled by a heat storage layer in the other chamber, and is discharged to a gas outflow passage. To be done. At this time, the heat storage layer used on the cooling side of the gas takes heat from the gas and stores the heat.

【0009】2のパターンは、1つの駆動系で動作する
ダンパーによりガスの流入流路と連通していた室の開口
部を外気雰囲気と連通するように切り替える。流出流路
と連通している側は、そのまま連通している状態を維持
することでガスの代わりに外気が導入され浄化装置本体
内部をいままでと同じ方向に流れ蓄熱体,加熱装置,触
媒を経てもう一方の室の蓄熱体層で冷却されガス流出流
路に排出される。すなわちガスの入り口付近や蓄熱体層
中の未浄化の有害成分が外気により加熱装置、触媒に追
いやられ、浄化される。
The pattern 2 is switched so that the opening of the chamber, which has been communicated with the gas inflow passage, is communicated with the outside air atmosphere by the damper operated by one drive system. On the side that communicates with the outflow passage, by maintaining the state where it communicates as it is, outside air is introduced instead of gas and flows in the same direction as before in the main body of the purification device, and the heat storage body, heating device, and catalyst are After that, it is cooled by the heat storage layer in the other chamber and discharged to the gas outflow passage. That is, unpurified harmful components in the vicinity of the gas inlet and in the heat storage layer are expelled by the outside air to the heating device and the catalyst for purification.

【0010】3のパターンは、同様にダンパーを操作し
浄化装置本体内のガスの流れがそれぞれの室で1のパタ
ーンと逆転するように切り替える。有害成分を含んだガ
スは、1のパターンとは反対の室から浄化装置本体内部
に入り、その室の蓄熱体層を通過する。この蓄熱体層は
1のパターンのとき熱を蓄えているのでこのパターンで
はガスに熱を与えるように働く。ガスは加熱装置によっ
てさらに加熱され浄化される。そしてもう一方の室の蓄
熱体層によって冷却され、排出される。
Similarly, the pattern of 3 is switched by operating the damper so that the flow of gas in the main body of the purifying device is reversed to the pattern of 1 in each chamber. The gas containing the harmful component enters the inside of the purifying apparatus main body from the chamber opposite to the pattern of 1, and passes through the heat storage layer in the chamber. Since this heat storage layer stores heat in the pattern 1, it works to give heat to the gas in this pattern. The gas is further heated and purified by the heating device. Then, it is cooled by the heat storage layer in the other chamber and discharged.

【0011】最後の4のパターンは、2のパターンと同
様にダンパーによりガスの流入流路と連通していた室の
開口部を外気雰囲気と連通するように切り替え、外気が
この室から導入され、蓄熱体層,加熱装置,触媒を経て
もう一方の室の蓄熱体層で冷却され、ガス流出流路に排
出されることで、ガスの入り口付近や蓄熱体層中の未浄
化の有害成分を外気により加熱装置、触媒に追いやり浄
化する。
In the last 4 patterns, as in the case of the 2 pattern, the damper is switched so that the opening of the chamber communicating with the gas inflow passage communicates with the outside air atmosphere, and the outside air is introduced from this chamber. After passing through the heat storage layer, heating device, and catalyst, it is cooled by the heat storage layer in the other chamber and discharged to the gas outflow passage, so that unpurified harmful components near the gas inlet and in the heat storage layer are released to the outside air. Purifies by pursuing the heating device and catalyst.

【0012】以上の4つのパターンを一定時間毎に繰り
返す事は、1つのダンパーを操作することによって有害
成分を含んだガスが浄化に必要な温度まで加温されるた
めの熱エネルギーを加熱浄化装置本体の内部で閉じこめ
る事ができ、またガスの流れの切り替え時に未浄化の有
害成分が排出される事がなく、蓄熱体や加熱装置からの
放熱も最外壁からの放熱のみであるため、エネルギー効
率および浄化効率の高い有害成分浄化装置である事がわ
かる。
By repeating the above four patterns at regular intervals, the heating and purifying device for heating the heat energy for heating the gas containing harmful components to the temperature required for purification by operating one damper. It can be confined inside the main body, no unpurified harmful components are emitted when switching the gas flow, and heat radiation from the heat storage body and heating device is only from the outermost wall, so energy efficiency And it is understood that it is a harmful component purification device with high purification efficiency.

【0013】[0013]

【実施例】【Example】

(実施例1)以下本発明の一実施例について、図面を参
照しながら説明する。
(Embodiment 1) An embodiment of the present invention will be described below with reference to the drawings.

【0014】図1(a)において、1は有害成分を含ん
だガスの流入口、2はその流入流路、11はガスの流出
口を示す。7は触媒浄化装置本体、6は蓄熱体層、10
は加熱装置、9は触媒を示す。(b)は(a)のA−B
線の断面図を示す。左右の2室の開口部は31の同一面
上にあり1つの駆動系で制御できる12のスライド部お
よび13の本体部からなるダンパーで流入流路、流出流
路または外気雰囲気と連通する(それぞれ5,4,33
で示した)。図1(b)は装置の下方が閉じられた一端
を示し、8の分割壁で分けられた左右の2室がここで連
通している。排ガスの流れは矢印3で示した。34は開
いた開口部を示す。この図1(a)および(b)の状態
を説明する。有害成分を含んだガスは(a)の1から入
り左に進み矢印から34の開口部を通過して加熱浄化装
置本体に導入される。そして(b)の矢印で示したよう
にガスは流れる。この時左の室の蓄熱体層6によりガス
は加熱され、触媒を通過して下部の加熱装置10により
更に必要な温度まで加熱され右の室の触媒によって浄化
される。そして右の室の蓄熱体層6で熱交換し、冷却さ
れた状態で開口部34から流出流路11に排出される。
(c)および(c)のA−B線に沿った断面図(d)
は、(a)および(b)の状態から一定時間後スライド
ダンパーの操作により外気が左側の室に導入される状態
を示した。この操作によって左側の室には未浄化の有害
成分が無い状態をつくり出す事ができる。
In FIG. 1 (a), reference numeral 1 is an inlet for gas containing a harmful component, 2 is an inflow passage thereof, and 11 is an outlet for gas. 7 is a catalyst purifying apparatus main body, 6 is a heat storage layer, 10
Is a heating device, and 9 is a catalyst. (B) is AB of (a)
A sectional view of the line is shown. The openings of the two chambers on the left and right are on the same plane of 31 and are connected to the inflow passage, the outflow passage or the outside air atmosphere by a damper consisting of 12 slide portions and 13 main body portions that can be controlled by one drive system (each 5,4,33
). FIG. 1B shows one end where the lower part of the device is closed, and two left and right chambers divided by eight dividing walls communicate with each other. The flow of exhaust gas is shown by arrow 3. Reference numeral 34 indicates an open opening. The states of FIGS. 1A and 1B will be described. The gas containing a harmful component enters from 1 of (a), proceeds to the left, passes through the opening of 34 from the arrow, and is introduced into the main body of the heat purifying apparatus. Then, the gas flows as shown by the arrow in (b). At this time, the gas is heated by the heat storage layer 6 in the left chamber, passes through the catalyst, is further heated to a required temperature by the lower heating device 10, and is purified by the catalyst in the right chamber. Then, heat is exchanged in the heat storage layer 6 in the right chamber, and the heat is discharged from the opening 34 to the outflow passage 11 in a cooled state.
(C) And sectional drawing along the AB line of (c) (d).
Shows a state in which outside air is introduced into the left chamber by operating the slide damper after a certain period of time from the states of (a) and (b). By this operation, it is possible to create a state where there is no unpurified harmful component in the left chamber.

【0015】次にダンパーを操作し(e)および(f)
の状態になるようにし、再びガスを流す。
Next, the damper is operated (e) and (f).
Then, let gas flow again.

【0016】この時はガスは(e)で流入流路を右に流
れ、(f)の右の室を上から下へ流れて左の室に移り、
下から上へ流れて流出流路に排出される。右室の蓄熱体
層は(b)及び(d)の状態の時に十分熱エネルギーを
蓄熱しており、(f)の状態ではガスを熱交換によって
加熱する働きをする。(g)および(h)は、(e)お
よび(f)の状態から一定時間後スライドダンパーの操
作により外気が右側の室に導入される状態を示した。
(c),(d)と同様にこの操作によって右側の室には
未浄化の有害成分がない状態を作り出すことができる。
以上の4つのパターンを繰り返すことは、1つのスライ
ドダンパーを操作することにより熱エネルギーは加熱浄
化装置内に閉じ込められ、ロスする量が非常に少なく、
また有害成分が未浄化のまま排出されることがないこと
を意味する。図2に本実施例のダンパーについて示し
た。(a)がダンパーのスライド部分12を示し、
(b)がダンパーの本体部13を示す。14はスライド
部の開口、16はガスの流入流路、17は外気雰囲気、
18はガスの流出流路と連通している。図2の(c)の
状態は図1の(a)(b)の状態に相当する。浄化装置
本体の左の室の開口部がガスの流入流路と連通し、右の
室がガスの流出流路と連通している。図2の(d)・
(e)・(f)がそれぞれ図1の(c)(d)・(e)
(f)・(g)(h)の状態に相当する。すなわちダン
パーのスライド部を1つの駆動系で操作することによっ
て、浄化装置本体内部でガスの流れを逆転でき、しかも
外気を導入するパターンを組み入れる事ができて未浄化
のガスが排出される事がない。
At this time, the gas flows to the right in the inflow passage in (e), flows from the top to the bottom in the right chamber in (f), and moves to the left chamber,
It flows from bottom to top and is discharged to the outflow passage. The heat storage layer in the right chamber stores sufficient heat energy in the states (b) and (d), and in the state (f), it functions to heat the gas by heat exchange. (G) and (h) show the state where the outside air is introduced into the right chamber by the operation of the slide damper after a certain period of time from the states of (e) and (f).
Similar to (c) and (d), this operation can create a state where there is no unpurified harmful component in the right chamber.
By repeating the above four patterns, the thermal energy is confined in the heating and purifying device by operating one slide damper, and the amount lost is very small.
It also means that harmful components are not discharged unpurified. FIG. 2 shows the damper of this embodiment. (A) shows the slide part 12 of the damper,
(B) shows the main body 13 of the damper. 14 is an opening of the slide portion, 16 is a gas inflow passage, 17 is an outside air atmosphere,
18 communicates with the gas outflow passage. The state of (c) of FIG. 2 corresponds to the states of (a) and (b) of FIG. The opening of the left chamber of the purification device body communicates with the gas inflow passage, and the right chamber communicates with the gas outflow passage. 2 (d)
(E) and (f) are (c), (d), and (e) of FIG. 1, respectively.
This corresponds to the states of (f), (g) and (h). That is, by operating the slide part of the damper with one drive system, the flow of gas can be reversed inside the purifier main body, and a pattern for introducing the outside air can be incorporated to discharge unpurified gas. Absent.

【0017】本実施例における有害成分の浄化効果と熱
効率を測定した結果を(表1)に示す。
The results of measuring the purification effect of harmful components and thermal efficiency in this example are shown in (Table 1).

【0018】[0018]

【表1】 [Table 1]

【0019】加熱浄化装置は、蓄熱体としてそれぞれの
室に粒状アルミナ(5〜10mmφ)のものは5リット
ル、触媒はハニカム状の白金触媒をそれぞれ1リット
ル、加熱装置はmax1kwのシーズーヒーターを用い60
0℃で温度調節を行った。ガスは100ppmのスチレン
ガスを含み、送風量500リットルl/minとした。ガ
スの浄化率はスチレンガスの触媒による分解率で示し、
熱効率は簡易的に排ガスが600℃まで昇温されたとし
て600℃への昇温温度に対して出口温度と入口温度の
差を比較して算出した。外気導入時間は、2秒間とし
た。
The heating and purifying device uses 5 liters of granular alumina (5 to 10 mmφ) in each chamber as a heat storage body, 1 liter of honeycomb-shaped platinum catalyst for each catalyst, and a heating device of a max 1 kw Shihzu heater.
The temperature was adjusted at 0 ° C. The gas contained 100 ppm of styrene gas, and the air flow rate was 500 liters / min. The purification rate of gas is indicated by the decomposition rate of styrene gas with a catalyst,
The thermal efficiency was calculated by simply comparing the difference between the outlet temperature and the inlet temperature with respect to the temperature rising to 600 ° C., assuming that the exhaust gas was heated to 600 ° C. The outside air introduction time was 2 seconds.

【0020】この(表1)から明らかなように、本実施
例による加熱浄化装置は、90%以上のスチレンガス排
ガスの浄化を80%以上の熱交換効率で達成することが
できている。
As is clear from (Table 1), the heating and purifying apparatus according to the present embodiment can achieve purification of styrene gas exhaust gas of 90% or more with heat exchange efficiency of 80% or more.

【0021】また本実施例では、蓄熱材としてアルミナ
を用いており耐腐食性に優れているため排ガス中に金属
を腐食するような成分(たとえば酸性ガス等)が含まれ
ていても十分使用に耐える。
Further, in this embodiment, since alumina is used as the heat storage material and the corrosion resistance is excellent, even if the exhaust gas contains a component that corrodes a metal (for example, acid gas, etc.), it can be sufficiently used. Endure.

【0022】[0022]

【発明の効果】以上のように、本発明は浄化装置本体が
蓄熱体層を有した2室に別れ、開口する一端が同一面上
で1つの駆動系で制御できるダンパーによって、ガスの
流入流路,流出流路または外気雰囲気とそれぞれ相反し
て連通できる構造を有するとともに、閉じられた他端部
分で互いに連通し加熱装置,触媒が設けられた構造で、
1室の開口部から導入されたガスは、蓄熱体層から熱エ
ネルギーを供給されて、加熱装置,触媒で有害成分を浄
化された後、もう一方の室の蓄熱体層で熱交換し冷却さ
れて開口部からの流出流路に排出される。一定時間の後
ダンパーのスライドを移動させる事により外気を導入す
る過程を経てガスの流れ方向を逆転することができ、そ
れぞれの室の蓄熱体層が逆の熱交換作用を行うようにす
る。この操作を交互に繰り返すことにより熱エネルギー
のロスを最小限に抑え、かつ排ガス中の有害成分をショ
ートパスすることなく効率よく浄化することができる有
害成分加熱浄化装置を実現するものである。
As described above, according to the present invention, the purifying apparatus main body is divided into two chambers having the heat storage layer, and the inflow flow of gas is controlled by the damper whose one open end can be controlled by one drive system on the same plane. The structure has a structure capable of communicating with the channel, the outflow channel, or the atmosphere of the outside air in a mutually opposite manner, and has a structure in which a heating device and a catalyst are provided so as to communicate with each other at the closed other end portion,
The gas introduced from the opening of one chamber is supplied with thermal energy from the heat storage layer, purified of harmful components by the heating device and the catalyst, and then heat-exchanged and cooled by the heat storage layer of the other chamber. And is discharged to the outflow passage from the opening. By moving the slide of the damper after a certain period of time, the flow direction of the gas can be reversed through the process of introducing the outside air, so that the heat storage layer in each chamber performs an opposite heat exchange action. By repeating this operation alternately, it is possible to realize a harmful component heating and purifying apparatus that can minimize the loss of thermal energy and efficiently purify the harmful components in the exhaust gas without short-passing.

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

【図1】(a)本発明の第1の実施例における有害成分
加熱浄化装置の全体構成を示す図 (b)(a)のA−B線に沿った断面図 (c),(e),(g)はダンパーの操作によって
(a)のガスの流れを変化させた状態を示す図 (d),(f),(h)はそれぞれ(c),(e),
(g)のA−B線に沿った断面図
FIG. 1 (a) is a sectional view taken along the line AB of FIG. 1 (b) showing the overall configuration of a harmful component heating / purifying device according to the first embodiment of the present invention (c), (e). , (G) shows the state where the gas flow in (a) is changed by the operation of the damper, (d), (f), (h) are (c), (e), respectively.
Sectional drawing which followed the AB line of (g).

【図2】(a)本発明の同一面上に配置されたダンパー
のスライド部を示す図 (b)ダンパーの本体部を示す図 (c),(d),(e),(f)はダンパーと本体部の
重なりによる開口部の状態を示す図
FIG. 2 (a) is a view showing a slide part of a damper arranged on the same surface of the present invention, (b) is a view showing a main body part of the damper, (c), (d), (e) and (f) are FIG. Diagram showing the state of the opening due to the overlap of the damper and the main body

【図3】(a)従来の触媒浄化装置本体の構成を示す図 (b)熱交換機も含めた従来の触媒浄化システム全体の
構成を示す図
FIG. 3 (a) is a diagram showing the configuration of a conventional catalyst purifying apparatus main body, and FIG. 3 (b) is a diagram showing the overall configuration of a conventional catalyst purifying system including a heat exchanger.

【図4】(a)従来の蓄熱型浄化装置本体の構成を示す
図 (b)排ガスの流れを逆転した状態を示す図
FIG. 4 (a) is a view showing a configuration of a conventional heat storage-type purification apparatus main body, and FIG. 4 (b) is a view showing a state in which a flow of exhaust gas is reversed.

【符号の説明】[Explanation of symbols]

6 蓄熱体層 9 触媒 10 加熱装置 31 同一面上に配置された開口部 12 ダンパーのスライド部 13 ダンパーの本体部 6 heat storage layer 9 catalyst 10 heating device 31 Openings arranged on the same plane 12 Damper slide 13 Damper body

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】一端が開口し多端が閉じているとともにそ
の部分で互いに連通した2室に分けられた本体を有し、
それぞれの室の開口部側に蓄熱体層を配置し、閉じられ
た側に加熱装置と触媒を配置するとともに、それぞれの
室が開口部を同一面上に配置されることで1つの駆動系
が動作するダンパーを介して有害成分を含んだガスの流
入流路,流出流路または外気雰囲気と連通することを特
徴とする有害成分加熱浄化装置。
1. A main body divided into two chambers, one end of which is open and the other end of which is closed, and which communicates with each other at that portion,
The heat storage layer is arranged on the opening side of each chamber, the heating device and the catalyst are arranged on the closed side, and the opening parts of the chambers are arranged on the same plane, whereby one drive system is formed. A harmful component heating and purifying device characterized by being connected to an inflow passage, an outflow passage of a gas containing a harmful component or an outside air atmosphere through an operating damper.
【請求項2】2室はそれぞれのガスの流出流路,流入流
路または外気雰囲気の一方とのみ連通した状態で作動
し、次のパターンで浄化操作を交互に繰り返す請求項1
記載の有害成分加熱浄化装置。 1パターン−−有害成分を含んだガスは流入流路から一
方の室に流入し蓄熱体及び加熱装置,触媒により加熱浄
化されもう一方の室の蓄熱体層で冷却されガス流出流路
に排出される 2パターン−−1つの駆動系で動作するダンパーにより
ガスの流入流路と連通していた室の開口部を外気雰囲気
と連通するように切り替え、外気がこの室に導入され蓄
熱体層,加熱装置,触媒を経て一方の室の蓄熱体層で冷
却されガス流出流路に排出される 3パターン−−ダンパーにより浄化装置本体内のガスの
流れがそれぞれの室で前記1パターンと逆転するように
切り替え、有害成分は加熱,浄化,冷却過程を経て排出
される 4パターン−−ダンパーによりガスの流入流路と連通し
ていた室の開口部を外気雰囲気と連通するように切り替
え外気がこの室に導入され、蓄熱体層,加熱装置,触媒
を経てもう一方の室の蓄熱体層で冷却されガス流出流路
に排出される
2. The two chambers are operated in a state in which they communicate with only one of the gas outflow passages, the inflow passages, or the outside air atmosphere, and the cleaning operation is repeated alternately in the following pattern.
Heat treatment device for harmful components described. 1 pattern-Gas containing harmful components flows into the one chamber from the inflow passage, is heated and purified by the heat storage body, the heating device and the catalyst, is cooled by the heat storage layer in the other chamber and is discharged to the gas outflow passage. 2 patterns --- The damper operated by one drive system switches the opening of the chamber that was in communication with the gas inflow passage so that it communicates with the atmosphere of the outside air, and the outside air is introduced into this chamber and the heat storage layer, heating 3 patterns that are cooled by the heat storage layer in one chamber and discharged to the gas outflow passage through the device and the catalyst-By the damper, the gas flow in the purifying device main body is reversed to the one pattern in each chamber. Switching, the harmful components are discharged through the heating, purification and cooling processes. 4 patterns-The damper is switched so that the opening of the chamber that was in communication with the gas inflow passage is communicated with the outside air atmosphere. Guide Is, the heat storage layer, is discharged to the heating device, it is cooled by the heat storage layer of the other chamber through the catalytic gas outflow passages
JP3156472A 1991-06-27 1991-06-27 Harmful component heating purification device and purification method Expired - Lifetime JP2616516B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3156472A JP2616516B2 (en) 1991-06-27 1991-06-27 Harmful component heating purification device and purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3156472A JP2616516B2 (en) 1991-06-27 1991-06-27 Harmful component heating purification device and purification method

Publications (2)

Publication Number Publication Date
JPH054026A true JPH054026A (en) 1993-01-14
JP2616516B2 JP2616516B2 (en) 1997-06-04

Family

ID=15628502

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JP2616516B2 (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08318164A (en) * 1995-03-17 1996-12-03 Hideo Kameyama Catalyst structural body and gas combustion/ decomposition device using the same
JPH09262436A (en) * 1996-03-29 1997-10-07 Cataler Kogyo Kk Regenerative waste gas purifier
JPH11226342A (en) * 1997-04-22 1999-08-24 Johannes Schedler Method and apparatus for cleaning gas
JP2008105875A (en) * 2006-10-24 2008-05-08 Nippon Oil Corp Method for reducing concentration of carbon monoxide and fuel cell system
JP2013521098A (en) * 2010-03-11 2013-06-10 イー.エム.ダブリュ.エナジー カンパニー リミテッド Air purification module
JP2016121859A (en) * 2014-12-25 2016-07-07 株式会社島川製作所 Harmful component heating and purifying device
JP6814494B1 (en) * 2020-03-06 2021-01-20 株式会社島川製作所 Hazardous component heating purification device

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4996968A (en) * 1973-01-20 1974-09-13

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4996968A (en) * 1973-01-20 1974-09-13

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08318164A (en) * 1995-03-17 1996-12-03 Hideo Kameyama Catalyst structural body and gas combustion/ decomposition device using the same
JPH09262436A (en) * 1996-03-29 1997-10-07 Cataler Kogyo Kk Regenerative waste gas purifier
JPH11226342A (en) * 1997-04-22 1999-08-24 Johannes Schedler Method and apparatus for cleaning gas
JP2008105875A (en) * 2006-10-24 2008-05-08 Nippon Oil Corp Method for reducing concentration of carbon monoxide and fuel cell system
JP2013521098A (en) * 2010-03-11 2013-06-10 イー.エム.ダブリュ.エナジー カンパニー リミテッド Air purification module
JP2016121859A (en) * 2014-12-25 2016-07-07 株式会社島川製作所 Harmful component heating and purifying device
JP6814494B1 (en) * 2020-03-06 2021-01-20 株式会社島川製作所 Hazardous component heating purification device

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