JP2003245521A - Catalytic combustion type deodorizing apparatus - Google Patents
Catalytic combustion type deodorizing apparatusInfo
- Publication number
- JP2003245521A JP2003245521A JP2002049130A JP2002049130A JP2003245521A JP 2003245521 A JP2003245521 A JP 2003245521A JP 2002049130 A JP2002049130 A JP 2002049130A JP 2002049130 A JP2002049130 A JP 2002049130A JP 2003245521 A JP2003245521 A JP 2003245521A
- Authority
- JP
- Japan
- Prior art keywords
- catalytic combustion
- heat
- combustion type
- catalyst
- type deodorizing
- 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
Links
Landscapes
- Incineration Of Waste (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【０００１】[0001]
【発明の属する技術分野】本発明は、触媒燃焼式脱臭装
置の構造に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to the structure of a catalytic combustion type deodorizing device.
【０００２】[0002]
【従来の技術】臭気性ガスの処理方法として該臭気ガス
を燃焼させて脱臭する処理方法が知られており、該処理
方法に用いられる装置として、図５に示す触媒燃焼式の
ものが知られている。該装置では、必要な温度に予熱さ
れた臭気ガスを、管路２０を通して管路２０内に設けた
触媒層２１に導入し酸化無臭化する。その際、触媒層２
１の温度低下を極力防ぎ、予熱のためのエネルギー消費
を少なくするため管路２０を断熱材２２で覆っている。2. Description of the Related Art As a method for treating odorous gas, a method for burning the odorous gas to deodorize is known, and as a device used in the method, a catalytic combustion type apparatus shown in FIG. 5 is known. ing. In this apparatus, the odorous gas preheated to the required temperature is introduced into the catalyst layer 21 provided in the pipe 20 through the pipe 20 to deoxidize it by oxidation. At that time, the catalyst layer 2
The pipe 20 is covered with a heat insulating material 22 in order to prevent the temperature decrease of 1 as much as possible and reduce the energy consumption for preheating.
【０００３】[0003]
【発明が解決しようとする課題】しかし、従来の触媒脱
臭装置は以上のように構成されているので、触媒燃焼に
より触媒層の温度が上昇し、触媒側面からの放熱損失が
大きくなり、損失を抑制するには触媒層の周辺の断熱材
を厚くするなどの必要があった。特に炭化水素など発熱
量の高い臭気成分が含まれている場合にこのような問題
が顕著である。However, since the conventional catalyst deodorizing device is constructed as described above, the temperature of the catalyst layer rises due to the catalytic combustion, and the heat radiation loss from the side surface of the catalyst increases, resulting in a loss. In order to suppress it, it was necessary to increase the thickness of the heat insulating material around the catalyst layer. Such a problem is particularly remarkable when an odorous component having a high calorific value such as hydrocarbon is contained.
【０００４】本発明は、上記のような従来のものの課題
を解決するためになされたもので、触媒部の設置部分を
二重管構造にすることにより、放熱損失を抑制し、また
放熱された熱を有効に利用して省エネルギー化を実現で
きる装置を提供することを目的としている。The present invention has been made in order to solve the above-mentioned problems of the conventional ones, and the heat dissipation loss is suppressed and the heat is dissipated by making the installation part of the catalyst part a double pipe structure. It is an object of the present invention to provide a device that can effectively use heat to realize energy saving.
【０００５】[0005]
【課題を解決するための手段】上記課題を解決するため
本発明の触媒燃焼式脱臭装置のうち、請求項１記載の発
明は、臭気ガスを触媒部に導入して触媒燃焼により脱臭
する触媒燃焼式脱臭装置において、前記触媒部を二重管
の内管内に設置し、その周囲であって前記二重管の外管
と前記内管との間の空隙に臭気ガスの通過が可能である
ように蓄熱体を設け、該蓄熱体を通過した臭気ガスが前
記触媒部に導入されるように構成したことを特徴とす
る。In order to solve the above-mentioned problems, among the catalytic combustion type deodorizing apparatus of the present invention, the invention according to claim 1 is a catalytic combustion in which an odorous gas is introduced into the catalytic portion to deodorize by catalytic combustion. In the deodorizing device, the catalyst portion is installed in the inner pipe of the double pipe, and odorous gas can pass through the space around the catalyst pipe between the outer pipe and the inner pipe of the double pipe. Is provided with a heat storage body, and the odorous gas that has passed through the heat storage body is introduced into the catalyst section.
【０００６】請求項２記載の発明は、請求項１記載の発
明において、前記外管は、内管先端の先に伸長してガス
流が折り返されるように閉じられていることを特徴とす
る。The invention according to claim 2 is characterized in that, in the invention according to claim 1, the outer pipe is closed so as to extend beyond the tip of the inner pipe and to fold back the gas flow.
【０００７】請求項３記載の発明は、請求項１または２
に記載の発明において、触媒部の上流側に予熱用バーナ
ーが設置されていることを特徴とする。The invention according to claim 3 is the invention according to claim 1 or 2.
In the invention described in (1), a preheating burner is installed on the upstream side of the catalyst section.
【０００８】請求項４記載の発明は、請求項１〜３のい
ずれかに記載の発明において、触媒部の上流側に予熱用
バーナーと燃料供給口が設置されていることを特徴とす
る。The invention according to claim 4 is characterized in that, in the invention according to any one of claims 1 to 3, a preheating burner and a fuel supply port are installed upstream of the catalyst portion.
【０００９】すなわち本発明によれば、触媒部を二重管
の内管内に設置し、触媒部周囲にあたる、外管と内管と
の間の空隙に蓄熱体を設置することで、触媒からの放熱
分を蓄熱体に蓄熱させ、その外管内に臭気ガスを通すこ
とで放熱分により臭気ガスを予熱することが可能にな
り、消費エネルギーの低減を可能としたものである。That is, according to the present invention, the catalyst section is installed in the inner tube of the double tube, and the heat storage body is installed in the space between the outer tube and the inner tube, which is the periphery of the catalyst section. By storing the radiated heat in the heat storage body and letting the odorous gas pass through the outer tube, the odorous gas can be preheated by the radiated heat and the energy consumption can be reduced.
【００１０】上記二重管は、請求項２に記載するよう
に、内管先端の先に外管を伸長させ、外管の先端をガス
流が折り返されるように閉じることにより、内管と外管
との間の蓄熱体を通るガスは、外管の先端側で折り返さ
れて内管の先端から内部に流入し触媒部に導入されて触
媒燃焼に供される。According to the second aspect of the present invention, the outer tube is extended beyond the tip of the inner tube, and the tip of the outer tube is closed so that the gas flow is folded back. The gas passing through the heat storage between the tube and the tube is folded back at the tip side of the outer tube, flows into the inside from the tip of the inner tube, is introduced into the catalyst portion, and is provided for catalytic combustion.
【００１１】[0011]
【発明の実施の形態】以下、本発明の一実施形態を図に
基づいて説明する。筒状に形成され両端が閉じられた外
管２の外周壁に断熱材３が覆われて装置本体１が構成さ
れており、該装置本体１の一端に処理対象となる臭気ガ
スと燃焼後の処理ガスとの間で熱交換して臭気ガスを予
熱する熱交換器４が設置されており、該熱交換器４に
は、臭気ガス入口５と処理後ガス出口６とが設けられて
いる。熱交換器４の装置本体１内に位置する外周部に
は、予熱された臭気ガスを脱臭装置本体１内で外周方向
に放出する放出部４ａが設けられている。BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings. A heat insulating material 3 is covered on an outer peripheral wall of an outer tube 2 which is formed in a tubular shape and whose both ends are closed to form a device main body 1. One end of the device main body 1 is an odor gas to be treated and an odor gas after combustion. A heat exchanger 4 for exchanging heat with the processing gas to preheat the odorous gas is installed, and the heat exchanger 4 is provided with an odorous gas inlet 5 and a post-processing gas outlet 6. At the outer peripheral portion of the heat exchanger 4 located inside the device body 1, there is provided a discharge portion 4a for discharging preheated odorous gas in the deodorizing device body 1 in the outer peripheral direction.
【００１２】また、装置本体１の外管２内には、外管２
とほぼ同軸に内管７が配置されており、外管２と内管７
とで二重管構造になっている。なお、内管７の一端は上
記熱交換器２の下端部に接続されて内部の処理後ガス通
路（図示しない）に連通しており、内管７の先端側は、
外管２の先端に達しない長さで外管２の下方側に伸長し
て、外管２内で開口している。上記内管７の先端側で
は、先端からやや奥まった位置に触媒部として触媒層８
が設けられており、該触媒層８を上下に挟んで内管７の
先端部と触媒層８の奥側に蓄熱体９１、９２が配置され
ている。また、触媒層８の周囲であって内管７と外管２
との間の空隙に、輪状に同じく蓄熱体９０が配置されて
いる。また、外管２の下端は閉じられてガス流が折り返
されるように構成されており、該下方部空間がバーナー
燃焼室１０に割り当てられている。このバーナー燃焼室
１０に露出するようにして該外管２に予熱用バーナー１
１が設けられている。In addition, the outer tube 2 of the apparatus main body 1 is provided in the outer tube 2.
The inner pipe 7 is arranged almost coaxially with the outer pipe 2 and the inner pipe 7.
It has a double tube structure. In addition, one end of the inner pipe 7 is connected to the lower end of the heat exchanger 2 and communicates with an internal post-treatment gas passage (not shown).
It extends below the outer tube 2 with a length that does not reach the tip of the outer tube 2 and opens inside the outer tube 2. On the tip side of the inner pipe 7, a catalyst layer 8 is formed as a catalyst portion at a position slightly recessed from the tip.
Is provided, and the heat storage bodies 91 and 92 are arranged at the tip of the inner tube 7 and at the back side of the catalyst layer 8 with the catalyst layer 8 sandwiched vertically. In addition, the inner tube 7 and the outer tube 2 are provided around the catalyst layer 8.
A heat storage body 90 is also arranged in a ring shape in the space between and. The lower end of the outer tube 2 is closed so that the gas flow is folded back, and the lower space is assigned to the burner combustion chamber 10. The outer tube 2 is exposed to the burner combustion chamber 10 and the preheating burner 1 is attached to the outer tube 2.
1 is provided.
【００１３】上記装置の動作について説明すると、処理
すべき臭気ガスは、臭気ガス入口５から熱交換器４内に
導入され、同じく熱交換器４内に導入された高温の処理
後ガスと熱交換されて予熱される。なお、処理後ガス
は、処理後ガス出口６より熱交換器４の外部に排気され
る。上記熱交換器４で予熱された臭気ガスは、放出部４
ａを通して外管２と内管７との間の空隙に放出され、該
空隙を下方に移動して、蓄熱体９０を通過する。蓄熱体
９０〜９２には、先に触媒層８で臭気ガスが通過して触
媒燃焼した際の熱が伝えられており、該熱によって蓄熱
体９０を通る臭気ガスが予熱される。これにより熱が有
効に利用されている。The operation of the above apparatus will be described. The odorous gas to be treated is introduced into the heat exchanger 4 through the odorous gas inlet 5 and exchanges heat with the high-temperature treated gas also introduced into the heat exchanger 4. And is preheated. The treated gas is exhausted from the treated gas outlet 6 to the outside of the heat exchanger 4. The odorous gas preheated by the heat exchanger 4 is discharged from the discharge unit 4
It is discharged into the space between the outer tube 2 and the inner tube 7 through a, moves downward in the space, and passes through the heat storage body 90. The heat when the odorous gas first passes through the catalyst layer 8 and is catalytically burned is transferred to the heat storage bodies 90 to 92, and the odorous gas passing through the heat storage body 90 is preheated by the heat. This makes effective use of heat.
【００１４】予熱された臭気ガスは、蓄熱体９０を通過
してバーナー燃焼室１０に至り、該バーナー燃焼室１０
で折り返される。該バーナー燃焼室１０では必要に応じ
て予熱用バーナー１１を動作させ、臭気ガスを加熱す
る。通常は、装置稼働初期に触媒層８の温度が充分に上
昇していないときに、該予熱用バーナー１１を用いて臭
気ガスを加熱し、触媒層８での触媒燃焼を補助する。The preheated odorous gas passes through the heat storage body 90 and reaches the burner combustion chamber 10, where it is burned.
Will be folded back. In the burner combustion chamber 10, the preheating burner 11 is operated as needed to heat the odorous gas. Normally, when the temperature of the catalyst layer 8 has not risen sufficiently at the beginning of the operation of the apparatus, the odorous gas is heated by the preheating burner 11 to assist the catalytic combustion in the catalyst layer 8.
【００１５】臭気ガスは上記にようにしてバーナー燃焼
室１０で折り返されるようにして内管７の先端より内部
に流入し、上昇する。その際に、蓄熱体９１を通過して
予熱される。さらに上昇する臭気ガスは触媒層８内に導
入される。触媒層８では、触媒の酸化作用により臭気ガ
スが燃焼して無臭化される。触媒層８を通過した燃焼後
の処理後ガスは、さらに蓄熱体９２を通過して予熱さ
れ、内管７を上昇して熱交換器４に導入される。処理後
ガスは、上記したように熱交換器４で新たに処理の対象
となる臭気ガスに熱を伝達し、さらに熱利用がなされ
る。熱交換された処理後ガスは、処理後ガス出口６より
排気される。The odorous gas is flown back into the burner combustion chamber 10 as described above, flows into the inside from the tip of the inner pipe 7, and rises. At that time, it passes through the heat storage body 91 and is preheated. Further rising odorous gas is introduced into the catalyst layer 8. In the catalyst layer 8, the odorous gas is burned and deodorized by the oxidizing action of the catalyst. The post-combustion treated gas that has passed through the catalyst layer 8 further passes through the heat storage body 92 to be preheated, rises in the inner pipe 7 and is introduced into the heat exchanger 4. As described above, the heat-treated gas transfers heat to the odorous gas to be newly treated in the heat exchanger 4, and the heat is further utilized. The heat-treated processed gas is exhausted from the processed gas outlet 6.
【００１６】上記のように本発明の脱臭装置では、触媒
層８で発生した熱が蓄熱体９０〜９２に伝達され、さら
に臭気ガスに伝えられるので、エネルギ損失を大幅に低
減することができる。As described above, in the deodorizing device of the present invention, the heat generated in the catalyst layer 8 is transferred to the heat storage bodies 90 to 92 and further transferred to the odorous gas, so that the energy loss can be greatly reduced.
【００１７】次に、図２は他の実施形態を示す図であ
る。なお、この実施形態で上記実施形態と同様の構造に
ついては同一の符号を付してその説明を省略する。この
実施形態では、上記実施形態と同様の構造のバーナー燃
焼室１０に燃料を供給できるように外管２に燃料供給口
１２が設けられている。上記脱臭装置では、装置稼働初
期に予熱用バーナー１１を用いることにより触媒層８の
昇温が充分になされ、その後、予熱用バーナー１１によ
る加熱が不要となり、定常運転へと移行する。その際
に、予熱用バーナー１１による加熱を停止するととも
に、予熱された臭気ガスに燃料供給口１２から燃料を供
給し、燃料を爆発限界以下適量で臭気ガスに混合する。
燃料が混合された臭気ガスは、触媒層８において触媒燃
焼し、触媒燃焼の発熱のみで装置の連続運転がなされ
る。Next, FIG. 2 is a diagram showing another embodiment. In addition, in this embodiment, the same reference numerals are given to the same structures as those in the above-mentioned embodiment, and the description thereof will be omitted. In this embodiment, a fuel supply port 12 is provided in the outer pipe 2 so that fuel can be supplied to the burner combustion chamber 10 having the same structure as that of the above embodiment. In the above deodorizing device, the temperature of the catalyst layer 8 is sufficiently raised by using the preheating burner 11 at the initial stage of the operation of the device, and thereafter, the heating by the preheating burner 11 becomes unnecessary and the operation shifts to the steady operation. At that time, heating by the preheating burner 11 is stopped, and fuel is supplied to the preheated odorous gas from the fuel supply port 12 to mix the fuel with the odorous gas in an appropriate amount below the explosion limit.
The odorous gas mixed with the fuel is catalytically burned in the catalyst layer 8, and the device is continuously operated only by the heat generated by the catalytic combustion.
【００１８】図３はさらに他の実施形態を示す図であ
り、この図で上記実施形態と同様の構造についても同一
の符号を付してその説明を省略または簡略化する。本実
施形態では、装置本体１に熱交換器４が設置されておら
ず、外部から供給される臭気ガスが臭気ガス入口５０を
通して直接装置本体１に供給されている。該臭気ガス
は、図示しない熱交換器で予熱した後、装置本体１に供
給されるものであっても良い。FIG. 3 is a view showing still another embodiment. In this figure, the same structures as those in the above embodiment are designated by the same reference numerals, and the description thereof will be omitted or simplified. In the present embodiment, the heat exchanger 4 is not installed in the device body 1, and the odor gas supplied from the outside is directly supplied to the device body 1 through the odor gas inlet 50. The odorous gas may be supplied to the apparatus main body 1 after being preheated by a heat exchanger (not shown).
【００１９】図４はさらに他の実施形態を示す図であ
り、図３の装置においてバーナー燃焼室１０に燃料供給
口１２を設置したものである。該燃料供給口１２は、図
２の装置と同様に、定常運転時に燃料を爆発限界以下適
量で臭気ガスに供給し、連続運転を触媒燃焼の発熱のみ
で行うことを可能にするものである。FIG. 4 is a view showing still another embodiment, in which the fuel supply port 12 is installed in the burner combustion chamber 10 in the apparatus of FIG. Similar to the device of FIG. 2, the fuel supply port 12 supplies the fuel to the odorous gas in an appropriate amount below the explosion limit during steady operation and enables continuous operation only by the heat generation of catalytic combustion.
【００２０】[0020]
【発明の効果】以上のように、本発明によれば、臭気ガ
スを触媒部に導入して触媒燃焼により脱臭する触媒燃焼
式脱臭装置において、前記触媒部を二重管の内管内に設
置し、その周囲であって前記二重管の外管と前記内管と
の間の空隙に臭気ガスの通過が可能であるように蓄熱体
を設け、該空隙を通過した臭気ガスが前記触媒部に導入
されるように構成したので、触媒部からの放熱損失を蓄
熱体に蓄熱し、予熱に利用することができるので、高温
の触媒部からの熱損失を回収することで従来の技術と比
較してエネルギー損失が抑制される。即ち、エネルギー
消費量を抑制することができ、低ランニングコストを実
現できる。As described above, according to the present invention, in the catalytic combustion type deodorizing device for introducing odorous gas into the catalyst section to deodorize by catalytic combustion, the catalyst section is installed in the inner pipe of the double pipe. , A heat storage body is provided in a space around the outer pipe and the inner pipe of the double pipe so that the odorous gas can pass therethrough, and the odorous gas passing through the space is passed to the catalyst portion. Since it is configured to be introduced, the heat radiation loss from the catalyst part can be stored in the heat storage body and used for preheating, so by recovering the heat loss from the hot catalyst part, it is possible to compare with the conventional technology. Energy loss is suppressed. That is, energy consumption can be suppressed and low running cost can be realized.
【図１】 本発明の一実施形態の触媒燃焼式脱臭装置を
示す断面図である。FIG. 1 is a cross-sectional view showing a catalytic combustion type deodorizing apparatus according to an embodiment of the present invention.
【図２】 同じく他の実施形態の触媒燃焼式脱臭装置の
断面図である。FIG. 2 is a sectional view of a catalytic combustion type deodorizing apparatus according to another embodiment of the present invention.
【図３】 同じく他の実施形態の触媒燃焼式脱臭装置の
断面図である。FIG. 3 is a sectional view of a catalytic combustion type deodorizing apparatus of another embodiment of the present invention.
【図４】 同じく他の実施形態の触媒燃焼式脱臭装置の
断面図である。FIG. 4 is a sectional view of a catalytic combustion type deodorizing apparatus according to another embodiment of the present invention.
【図５】 従来の触媒燃焼式脱臭装置を示す断面図であ
る。FIG. 5 is a cross-sectional view showing a conventional catalytic combustion type deodorizing device.
１ 装置本体 ２ 外管 ３ 断熱材 ４ 熱交換器 ５ 臭気ガス入口 ６ 処理後ガス出口 ７ 内管 ８ 触媒層 １０ バーナー燃焼室 １１ 予熱用バーナー １２ 燃料供給口 ９０ 蓄熱体 ９１ 蓄熱体 ９２ 蓄熱体 1 device body 2 outer tube 3 insulation 4 heat exchanger 5 Odor gas inlet 6 Gas outlet after processing 7 inner tube 8 catalyst layers 10 burner combustion chamber 11 Preheating burner 12 Fuel supply port 90 heat storage 91 heat storage 92 Heat storage
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 ＦＩ テーマコート゛(参考） Ｆ２３Ｇ 7/06 １０５ Ｆ２３Ｇ 7/06 ＺＡＢ ＺＡＢ Ｂ０１Ｄ 53/36 Ｈ ─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) F23G 7/06 105 F23G 7/06 ZAB ZAB B01D 53/36 H
Claims (4)
より脱臭する触媒燃焼式脱臭装置において、前記触媒部
を二重管の内管内に設置し、その周囲であって前記二重
管の外管と前記内管との間の空隙に臭気ガスの通過が可
能であるように蓄熱体を設け、該空隙を通過した臭気ガ
スが前記触媒部に導入されるように構成したことを特徴
とする触媒燃焼式脱臭装置。1. A catalytic combustion type deodorizing device for introducing odorous gas into a catalyst part to deodorize by catalytic combustion, wherein the catalyst part is installed in an inner pipe of a double pipe, and the periphery thereof is the double pipe. A heat storage body is provided in a gap between the outer pipe and the inner pipe so that the odorous gas can pass through, and the odorous gas that has passed through the gap is introduced into the catalyst portion. A catalytic combustion type deodorizing device.
ス流が折り返されるように閉じられていることを特徴と
する請求項１記載の触媒燃焼式脱臭装置。2. The catalytic combustion type deodorizing device according to claim 1, wherein the outer tube is closed so as to extend to the tip of the inner tube and to fold back the gas flow.
されていることを特徴とする請求項１または２に記載の
触媒燃焼式脱臭装置。3. The catalytic combustion type deodorizing apparatus according to claim 1, wherein a preheating burner is installed on the upstream side of the catalyst section.
供給口が設置されていることを特徴とする請求項１〜３
のいずれかに記載の触媒燃焼式脱臭装置。4. A preheating burner and a fuel supply port are installed on the upstream side of the catalyst section.
5. A catalytic combustion type deodorizing device according to any one of 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002049130A JP2003245521A (en) | 2002-02-26 | 2002-02-26 | Catalytic combustion type deodorizing apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002049130A JP2003245521A (en) | 2002-02-26 | 2002-02-26 | Catalytic combustion type deodorizing apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2003245521A true JP2003245521A (en) | 2003-09-02 |
Family
ID=28661723
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2002049130A Pending JP2003245521A (en) | 2002-02-26 | 2002-02-26 | Catalytic combustion type deodorizing apparatus |
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| Country | Link |
|---|---|
| JP (1) | JP2003245521A (en) |
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| JP2008304112A (en) * | 2007-06-07 | 2008-12-18 | Koyo Thermo System Kk | Heat recovery device |
| JP2009063210A (en) * | 2007-09-05 | 2009-03-26 | Chubu Electric Power Co Inc | Treatment device of volatile organic compound |
| WO2010074154A1 (en) * | 2008-12-25 | 2010-07-01 | 独立行政法人産業技術総合研究所 | Reactor with integrated heat exchange unit |
| JP2011058375A (en) * | 2009-09-07 | 2011-03-24 | Isuzu Motors Ltd | Method for controlling exhaust emission control device for internal combustion engine, exhaust emission control device for internal combustion engine, and internal combustion engine |
| KR101357177B1 (en) | 2012-11-27 | 2014-02-03 | 주식회사 파나시아 | A reactor with double-casing structure having by-pass and pre-heating function |
| CN107906543A (en) * | 2017-12-20 | 2018-04-13 | 安徽省升泰节能科技服务有限公司 | A kind of heat accumulating type tar disposes burner |
| CN109099446A (en) * | 2018-08-31 | 2018-12-28 | 佛山市锐拓环境工程设备有限公司 | A kind of catalysis burning processing device |
| CN111828995A (en) * | 2020-06-01 | 2020-10-27 | 沈阳环境科学研究院 | Phase-change heat-storage catalytic combustion device and combustion method |
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2002
- 2002-02-26 JP JP2002049130A patent/JP2003245521A/en active Pending
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008304112A (en) * | 2007-06-07 | 2008-12-18 | Koyo Thermo System Kk | Heat recovery device |
| JP2009063210A (en) * | 2007-09-05 | 2009-03-26 | Chubu Electric Power Co Inc | Treatment device of volatile organic compound |
| WO2010074154A1 (en) * | 2008-12-25 | 2010-07-01 | 独立行政法人産業技術総合研究所 | Reactor with integrated heat exchange unit |
| JP5495066B2 (en) * | 2008-12-25 | 2014-05-21 | 独立行政法人産業技術総合研究所 | Heat exchanger integrated reactor |
| JP2011058375A (en) * | 2009-09-07 | 2011-03-24 | Isuzu Motors Ltd | Method for controlling exhaust emission control device for internal combustion engine, exhaust emission control device for internal combustion engine, and internal combustion engine |
| KR101357177B1 (en) | 2012-11-27 | 2014-02-03 | 주식회사 파나시아 | A reactor with double-casing structure having by-pass and pre-heating function |
| WO2014084533A1 (en) * | 2012-11-27 | 2014-06-05 | 주식회사 파나시아 | Reactor having double casing structure and having bypass and preheating functions |
| CN107906543A (en) * | 2017-12-20 | 2018-04-13 | 安徽省升泰节能科技服务有限公司 | A kind of heat accumulating type tar disposes burner |
| CN107906543B (en) * | 2017-12-20 | 2024-04-12 | 南京硬核科技服务有限公司 | Tar disposal burner |
| CN109099446A (en) * | 2018-08-31 | 2018-12-28 | 佛山市锐拓环境工程设备有限公司 | A kind of catalysis burning processing device |
| CN111828995A (en) * | 2020-06-01 | 2020-10-27 | 沈阳环境科学研究院 | Phase-change heat-storage catalytic combustion device and combustion method |
| CN111828995B (en) * | 2020-06-01 | 2022-12-06 | 沈阳环境科学研究院 | Phase-change heat-storage catalytic combustion device and combustion method |
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