JPH09239238A - Denitration apparatus - Google Patents

Denitration apparatus

Info

Publication number
JPH09239238A
JPH09239238A JP8049910A JP4991096A JPH09239238A JP H09239238 A JPH09239238 A JP H09239238A JP 8049910 A JP8049910 A JP 8049910A JP 4991096 A JP4991096 A JP 4991096A JP H09239238 A JPH09239238 A JP H09239238A
Authority
JP
Japan
Prior art keywords
ozone
fan
tunnel
nitrogen dioxide
denitration device
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
JP8049910A
Other languages
Japanese (ja)
Inventor
Atsushi Kataya
篤史 片谷
Akira Hashimoto
彰 橋本
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 Ecology Systems Co Ltd
Panasonic Holdings Corp
Original Assignee
Matsushita Seiko Co Ltd
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 Seiko Co Ltd, Matsushita Electric Industrial Co Ltd filed Critical Matsushita Seiko Co Ltd
Priority to JP8049910A priority Critical patent/JPH09239238A/en
Publication of JPH09239238A publication Critical patent/JPH09239238A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters

Landscapes

  • Ventilation (AREA)
  • Treating Waste Gases (AREA)

Abstract

PROBLEM TO BE SOLVED: To purify ozone flowing toward the roadway of a tunnel even when the simple operation of an ozone generator is performed during the stop of the fan of a denitration apparatus. SOLUTION: A denitration apparatus has a fan 1 sucking tunnel ventilation gas, an ozone generator oxidizing nitrogen monoxide to nitrogen dioxide, an ozone supply nozzle 3, a dry absorbent bed 4 containing active carbon as one component to absorb nitrogen dioxide, an ozone purifying unit 5 housing an ozone purifying agent and a changeover damper 6 for guiding ozone to the ozone purifying unit 5. Since the ozone-containing air 7 generated as the result of the simple operation of the ozone generator 2 during the stop of the fan 1 of the denitration apparatus is purified by the ozone purifying unit 5 without being allowed to flow toward the roadway of a tunnel, the simple operation of the ozone generator 2 and the disassembling and maintenance of the fan 1 can be performed at the same period and the disassembling and maintenance period of the whole of the denitration apparatus can be shortened.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は自動車道路トンネル
の換気ガス処理用の脱硝装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a denitration device for treating ventilation gas in an automobile road tunnel.

【0002】[0002]

【従来の技術】近年、自動車道路トンネルの換気口から
排出される窒素酸化物(NOx)の総量又は濃度を規制
しようという環境問題から、トンネルの換気口付近に脱
硝装置を設置することが求められている。
2. Description of the Related Art In recent years, it has been required to install a denitration device near a ventilation opening of a tunnel because of environmental problems such as limiting the total amount or concentration of nitrogen oxides (NOx) discharged from the ventilation opening of a road tunnel. ing.

【0003】従来、この種の脱硝装置は、特開平7−8
8326号公報に示すような構成が一般的であった。以
下、その構成について図4及び図5を参照しながら説明
する。
Conventionally, this type of denitration device is disclosed in Japanese Patent Laid-Open No. 7-8.
The configuration shown in Japanese Patent No. 8326 has been common. The configuration will be described below with reference to FIGS. 4 and 5.

【0004】図4に示すように、ファン101により引
き込まれたトンネル換気ガスに含まれるNOxの主成分
である一酸化窒素及び二酸化窒素の内、一酸化窒素はオ
ゾン発生装置102で生成されオゾン供給ノズル103
から供給されるオゾンにより二酸化窒素に酸化される。
この酸化により得られた二酸化窒素と、NOx中にもと
もと存在する二酸化窒素を乾式吸収剤層104で吸収し
ている。図5は図4と同様であるが、トンネル換気ガス
を地上で取りまわすための垂直ダクト113が設けてあ
る点のみが図4と異なっている。
As shown in FIG. 4, of nitric oxide and nitrogen dioxide, which are the main components of NOx contained in the tunnel ventilation gas drawn by the fan 101, nitric oxide is generated by the ozone generator 102 and is supplied to the ozone. Nozzle 103
Oxidized to nitrogen dioxide by ozone supplied from.
Nitrogen dioxide obtained by this oxidation and nitrogen dioxide originally present in NOx are absorbed by the dry absorbent layer 104. FIG. 5 is similar to FIG. 4, but differs from FIG. 4 only in that a vertical duct 113 is provided for routing tunnel ventilation gas on the ground.

【0005】上記構成においてトンネル換気ガス中のN
Oxを除去し脱硝を行なっている。
In the above structure, N in the tunnel ventilation gas
Ox is removed and denitration is performed.

【0006】[0006]

【発明が解決しようとする課題】このような従来の脱硝
装置の分解整備(オーバーホール)において、長期間を
要するオゾン発生装置の単体試運転(以下、単体運転と
記す)は、ファンを運転した状態で行なう必要があっ
た。その理由は、図6および図7に示すように、もしも
ファンを停止した状態でオゾン発生装置の単体運転を行
なうならば、オゾン供給ノズルから供給され脱硝装置の
内部に充満したオゾンが、途中のダクトを伝って、トン
ネルの車道側に向かって逆流し、環境基準に規定される
光化学オキシダント濃度(0.06 ppm)を上回る濃度のオゾ
ンが、車道内に流出する可能性が存在することになり、
車道内の人員にとって安全衛生上好ましからざる結果に
なりかねないからである。
In the disassembly and maintenance (overhaul) of such a conventional denitration device, a unit test operation (hereinafter, referred to as a unit operation) of an ozone generator, which requires a long period of time, is performed while a fan is operating. I had to do it. The reason is that, as shown in FIGS. 6 and 7, if the ozone generator is operated alone with the fan stopped, the ozone supplied from the ozone supply nozzle and filling the inside of the denitration device is There is a possibility that ozone will flow back through the duct toward the roadside of the tunnel, and the concentration of ozone that exceeds the photochemical oxidant concentration (0.06 ppm) specified in the environmental standards will flow out into the roadway.
This may result in unfavorable safety and health for personnel on the road.

【0007】一方、ファンを運転した状態で、オゾン発
生装置の単体運転を行なうのであれば、オゾン供給ノズ
ルから脱硝装置の内部に供給されたオゾンは、前述のト
ンネル換気ガス中の一酸化窒素を二酸化窒素に酸化する
反応で消費されるし、またこの反応で消費しきれなかっ
た余剰オゾンは、乾式吸収剤層を通過する際に、吸収剤
中の一成分である活性炭により、還元されて酸素になる
ので無害化できる。
On the other hand, if the ozone generator is operated as a single unit while the fan is operating, the ozone supplied from the ozone supply nozzle to the inside of the denitration unit is the nitric oxide in the tunnel ventilation gas. Excess ozone that was consumed in the reaction of oxidizing to nitrogen dioxide and that could not be consumed in this reaction was reduced to oxygen by activated carbon, which is one component in the absorbent, when passing through the dry absorbent layer. Therefore, it can be made harmless.

【0008】つまり、脱硝装置の通常運転時には、ファ
ンもオゾン発生装置も運転するので、オゾンが車道側に
逆流する恐れはないが、脱硝装置の分解整備時に行うオ
ゾン発生装置の単体運転を、ファンを停止した状態で行
なうと、オゾンが車道側に逆流する危険性を生じてしま
うことになる。これはファン停止を必ず伴うファンの分
解整備と、オゾン発生装置の単体運転とを同時期に行な
うことはできないということを意味している。即ち、こ
のような、従来の脱硝装置の分解整備では、オゾン発生
装置の単体運転期間と、ファンの分解整備期間とを重複
させることはできず、脱硝装置全体の分解整備期間を重
複を避けて長期化せざるを得ず、その分だけ、脱硝装置
の運転が行なえないことになるので、装置本来の目的で
ある環境対策の機能が充分に果たすことができないとい
う課題があった。
That is, during normal operation of the denitration device, both the fan and the ozone generator are operated, so there is no risk of ozone flowing back to the side of the roadway. If the operation is performed with the vehicle stopped, there is a risk that ozone will flow back to the roadway side. This means that the disassembly and maintenance of the fan, which always involves stopping the fan, and the standalone operation of the ozone generator cannot be performed at the same time. That is, in the conventional disassembly and maintenance of the denitration device, the single operation period of the ozone generator and the disassembly and maintenance period of the fan cannot be overlapped, and the disassembly and maintenance period of the entire denitration device should be avoided. Since there is no choice but to extend the period, and the operation of the denitration device cannot be performed correspondingly, there is a problem that the function of environmental measures, which is the original purpose of the device, cannot be fully fulfilled.

【0009】本発明は上記課題を解決するもので、脱硝
装置のファン停止中においてオゾン発生装置の単体運転
を行なった場合でも、トンネルの車道側に逆流するオゾ
ンを浄化することを第1の目的とする。
The present invention is intended to solve the above problems. A first object of the present invention is to purify ozone flowing back to the roadway side of a tunnel even when the ozone generator is operated alone while the fan of the denitration device is stopped. And

【0010】また、切換ダンパ等の駆動用電力を要する
機器を全く使用することなく、トンネルの車道側に逆流
するオゾンを浄化することを第2の目的とする。
A second object of the present invention is to purify ozone that flows back to the roadway side of the tunnel without using any equipment such as a switching damper that requires driving power.

【0011】[0011]

【課題を解決するための手段】この課題を解決するため
に本発明は、脱硝装置のファン停止中においてオゾン発
生装置の単体運転を行なったとき、トンネルの車道側に
逆流するオゾンが浄化できるように構成したものであ
る。
In order to solve this problem, the present invention makes it possible to purify the ozone flowing back to the roadway side of the tunnel when the ozone generator is operated alone while the fan of the denitration device is stopped. It is configured in.

【0012】これにより、脱硝装置の分解整備期間の短
縮化が図れる。
As a result, the disassembly and maintenance period of the denitration device can be shortened.

【0013】[0013]

【発明の実施の形態】本発明の請求項1に記載の発明
は、トンネル換気ガスを引き込むファンと、一酸化窒素
を二酸化窒素に酸化するオゾン発生装置及びオゾン供給
ノズルと、活性炭を成分の一つとして二酸化窒素を吸収
する乾式吸収剤層と、オゾン浄化剤を収納したオゾン浄
化ユニットと、オゾン浄化ユニットにオゾンを導くため
の切換ダンパを備えた脱硝装置の構成としたものであ
り、脱硝装置のファン停止中においてオゾン発生装置の
単体運転を行なった場合でも、トンネルの車道側に逆流
するオゾンを浄化するという作用を有する。
BEST MODE FOR CARRYING OUT THE INVENTION The invention according to claim 1 of the present invention comprises a fan for drawing in a tunnel ventilation gas, an ozone generator and an ozone supply nozzle for oxidizing nitric oxide into nitrogen dioxide, and activated carbon as one of the components. The denitration device is composed of a dry absorbent layer that absorbs nitrogen dioxide, an ozone purification unit that stores an ozone purifying agent, and a switching damper that guides ozone to the ozone purification unit. Even when the ozone generator is operated as a single unit while the fan is stopped, it has the effect of purifying ozone that flows back to the roadway side of the tunnel.

【0014】本発明の請求項2に記載の発明は、トンネ
ル換気ガスを引き込むファンと、一酸化窒素を二酸化窒
素に酸化するオゾン発生装置及びオゾン供給ノズルと、
活性炭を成分の一つとして二酸化窒素を吸収する乾式吸
収剤層と、オゾンは空気よりも重いという物理的性質を
利用して動力を用いずに内部に収納してある浄化剤でオ
ゾンが浄化できるオゾン浄化ダクトを備えた脱硝装置の
構成としたものであり、切換ダンパ等の駆動用電力を要
する機器を全く使用することなく、トンネルの車道側に
逆流するオゾンを浄化するという作用を有する。
According to a second aspect of the present invention, there is provided a fan for drawing in a tunnel ventilation gas, an ozone generator for oxidizing nitric oxide into nitrogen dioxide, and an ozone supply nozzle.
Ozone can be purified with a dry absorbent layer that uses activated carbon as one of the components to absorb nitrogen dioxide, and a purifying agent that is housed inside without using power, utilizing the physical property that ozone is heavier than air. The denitration device is provided with an ozone purifying duct, and has an effect of purifying ozone flowing back to the roadway side of the tunnel without using any equipment that requires driving power such as a switching damper.

【0015】以下、本発明の実施の形態について、図1
から図3を用いて説明する。 (実施の形態1)図1は、脱硝装置のファン1停止中に
おいて、オゾン発生装置2の単体運転の結果発生したオ
ゾンを、トンネルの車道側に流出することなく、オゾン
浄化ユニット5で浄化する作用を行なうもので、トンネ
ル換気ガスを引き込むファン1と、一酸化窒素を二酸化
窒素に酸化するオゾン発生装置2及びオゾン供給ノズル
3と、二酸化窒素を吸収する乾式吸収剤層4と、オゾン
浄化剤を収納したオゾン浄化ユニット5と、オゾン浄化
ユニット5にオゾンを導くための切換ダンパ6から構成
されている。
The embodiment of the present invention will be described below with reference to FIG.
This will be described with reference to FIG. (Embodiment 1) FIG. 1 shows that ozone generated as a result of a single operation of the ozone generator 2 is purified by the ozone purification unit 5 while the fan 1 of the denitration device is stopped, without flowing out to the road side of the tunnel. A fan 1 that draws in tunnel ventilation gas, an ozone generator 2 and an ozone supply nozzle 3 that oxidize nitric oxide into nitrogen dioxide, a dry absorbent layer 4 that absorbs nitrogen dioxide, and an ozone purifying agent. It is composed of an ozone purifying unit 5 that stores therein and a switching damper 6 for guiding ozone to the ozone purifying unit 5.

【0016】図2は、図1のAの部分の詳細図である。
オゾン浄化ユニット5には活性炭系のオゾン浄化剤9が
充填されており、切換ダンパ6は常時開ダンパ10と、
常時閉ダンパ11とで構成されている。切換ダンパ6
は、常時開ダンパ10が開状態の時は常時閉ダンパ11
は閉であり、常時開ダンパ10が閉状態の時は常時閉ダ
ンパ11は開である動作をする。したがって、常時開ダ
ンパ10を閉状態かつ常時閉ダンパ11を開状態にして
おけば、脱硝装置のファン1停止中にオゾン発生装置2
の単体運転の結果発生したオゾン含有空気7は、オゾン
浄化ユニット5を通過する過程において酸素に還元さ
れ、オゾン浄化された空気8となりトンネルの車道側へ
流出される。また、ファン1を運転する時には図2に示
すように、常時開ダンパ10を開状態かつ常時閉ダンパ
11を閉状態にしておけば、通常のトンネル換気が行な
える。
FIG. 2 is a detailed view of the portion A in FIG.
The ozone purifying unit 5 is filled with an activated carbon-based ozone purifying agent 9, and the switching damper 6 is a normally open damper 10.
It is composed of a normally closed damper 11. Switching damper 6
Is a normally closed damper 11 when the normally open damper 10 is open.
Is closed, and when the normally open damper 10 is in the closed state, the normally closed damper 11 operates to be open. Therefore, by keeping the normally open damper 10 closed and the normally closed damper 11 open, the ozone generator 2 can be operated while the fan 1 of the denitration device is stopped.
The ozone-containing air 7 generated as a result of the unit operation is reduced to oxygen in the process of passing through the ozone purification unit 5, becomes ozone-purified air 8 and flows out to the road side of the tunnel. Further, when the fan 1 is operated, as shown in FIG. 2, if the normally open damper 10 is in the open state and the normally closed damper 11 is in the closed state, normal tunnel ventilation can be performed.

【0017】従って、脱硝装置のファン停止中において
オゾン発生装置の単体運転を行なった場合でも、トンネ
ルの車道側に逆流するオゾンを浄化することができる。
Therefore, even when the ozone generator is operated alone while the fan of the denitration device is stopped, it is possible to purify the ozone flowing back to the roadway side of the tunnel.

【0018】(実施の形態2)図3は、脱硝装置のファ
ン1停止中において、オゾン発生装置2の単体運転の結
果発生したオゾンを、トンネルの車道側に流出すること
なく、オゾン浄化ダクト12内に収納したオゾン浄化剤
9で浄化する作用を行なうもので、トンネル換気ガスを
引き込むファン1と、一酸化窒素を二酸化窒素に酸化す
るオゾン発生装置2及びオゾン供給ノズル3と、二酸化
窒素を吸収する乾式吸収剤層4と、逆流するオゾン含有
空気7を浄化するためにオゾン浄化剤9を収納したオゾ
ン浄化ダクト12から構成されている。
(Embodiment 2) FIG. 3 shows that the ozone purifying duct 12 does not discharge ozone generated as a result of the operation of the ozone generator 2 alone while the fan 1 of the denitration device is stopped. It has a function of purifying with an ozone purifying agent 9 housed inside, a fan 1 that draws in tunnel ventilation gas, an ozone generator 2 and an ozone supply nozzle 3 that oxidize nitric oxide into nitrogen dioxide, and absorbs nitrogen dioxide. The dry absorbent layer 4 and the ozone purifying duct 12 containing the ozone purifying agent 9 for purifying the ozone-containing air 7 flowing back.

【0019】脱硝装置のファン1停止中にオゾン発生装
置2の単体運転の結果発生したオゾン含有空気7中のオ
ゾンの比重は、空気の約1.7倍重いという物理的性質を
利用するとともに、図3に示すようなオゾン浄化ダクト
12の配置をすれば、逆流するオゾン含有空気7中のオ
ゾンは、重力によりオゾン浄化ダクト12に自然に導か
れ、オゾン浄化ダクト12の中に設けたオゾン浄化剤9
を通過する過程において酸素に還元され、オゾン浄化さ
れた空気8となりトンネルの車道側へ流出される。
Utilizing the physical property that the specific gravity of ozone in the ozone-containing air 7 generated as a result of the standalone operation of the ozone generator 2 while the fan 1 of the denitrification device is stopped is about 1.7 times heavier than that of air. If the ozone purifying duct 12 is arranged as shown in FIG. 3, the ozone in the backflowing ozone-containing air 7 is naturally guided to the ozone purifying duct 12 by gravity, and the ozone purifying agent 9 provided in the ozone purifying duct 12 is provided.
In the process of passing through, the air is reduced to oxygen and becomes ozone-purified air 8 which flows out to the roadway side of the tunnel.

【0020】従って、脱硝装置のファン停止中において
オゾン発生装置の単体運転を行なった場合でも、動力や
制御を用いることなく、トンネルの車道側に逆流するオ
ゾンを浄化することができる。
Therefore, even when the ozone generator is operated as a single unit while the fan of the denitration device is stopped, it is possible to purify the ozone flowing back to the roadway side of the tunnel without using power or control.

【0021】[0021]

【発明の効果】以上のように本発明によれば、脱硝装置
のファン停止中においてオゾン発生装置の単体運転を行
なった場合でも、トンネルの車道側に逆流するオゾンを
浄化することができるので、オゾン発生装置の分解整備
とファンの分解整備とを同時期に行なうことが可能とな
り、脱硝装置全体の分解整備期間の短縮化が図れるとい
う有利な効果が得られる。
As described above, according to the present invention, it is possible to purify ozone that flows back to the roadway side of a tunnel even when the ozone generator is operated alone while the fan of the denitration device is stopped. It is possible to perform the disassembly maintenance of the ozone generator and the disassembly maintenance of the fan at the same time, and it is possible to obtain an advantageous effect that the disassembly maintenance period of the entire denitration device can be shortened.

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

【図1】本発明の実施の形態1の脱硝装置の縦断面図FIG. 1 is a vertical sectional view of a denitration device according to a first embodiment of the present invention.

【図2】本発明の実施の形態1の脱硝装置のオゾン浄化
の説明図
FIG. 2 is an explanatory diagram of ozone purification by the denitration device according to the first embodiment of the present invention.

【図3】本発明の実施の形態2の脱硝装置の縦断面図FIG. 3 is a vertical sectional view of a denitration device according to a second embodiment of the present invention.

【図4】従来の脱硝装置の縦断面図FIG. 4 is a vertical sectional view of a conventional denitration device.

【図5】従来の脱硝装置の縦断面図FIG. 5 is a vertical sectional view of a conventional denitration device.

【図6】従来の脱硝装置の縦断面図FIG. 6 is a vertical sectional view of a conventional denitration device.

【図7】従来の脱硝装置の縦断面図FIG. 7 is a vertical sectional view of a conventional denitration device.

【符号の説明】[Explanation of symbols]

1 ファン 2 オゾン発生装置 3 オゾン供給ノズル 4 乾式吸収剤層 5 オゾン浄化ユニット 6 切換ダンパ 7 オゾン含有空気 8 オゾン浄化された空気 1 Fan 2 Ozone Generator 3 Ozone Supply Nozzle 4 Dry Absorbent Layer 5 Ozone Purification Unit 6 Switching Damper 7 Ozone Containing Air 8 Ozone Purified Air

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 トンネル換気ガスを引き込むファンと、
一酸化窒素を二酸化窒素に酸化するオゾン発生装置及び
オゾン供給ノズルと、活性炭を成分の一つとして二酸化
窒素を吸収する乾式吸収剤層と、オゾン浄化剤を収納し
たオゾン浄化ユニットと、オゾン浄化ユニットにオゾン
を導くための切換ダンパを備えた脱硝装置。
1. A fan for drawing in ventilation gas for tunnel,
An ozone generator and an ozone supply nozzle that oxidize nitric oxide into nitrogen dioxide, a dry absorbent layer that absorbs nitrogen dioxide with activated carbon as one of the components, an ozone purification unit that contains an ozone purification agent, and an ozone purification unit A denitration device equipped with a switching damper for introducing ozone into the atmosphere.
【請求項2】 トンネル換気ガスを引き込むファンと、
一酸化窒素を二酸化窒素に酸化するオゾン発生装置及び
オゾン供給ノズルと、活性炭を成分の一つとして二酸化
窒素を吸収する乾式吸収剤層と、オゾンは空気よりも重
いという物理的性質を利用して動力や制御を用いずに内
部に収納してある浄化剤でオゾンが浄化できるオゾン浄
化ダクトを備えた脱硝装置。
2. A fan for drawing in ventilation gas for tunnel,
Utilizing an ozone generator and an ozone supply nozzle that oxidize nitric oxide to nitrogen dioxide, a dry absorbent layer that absorbs nitrogen dioxide with activated carbon as one of its components, and the physical property that ozone is heavier than air. A denitration device equipped with an ozone purification duct that can purify ozone with a purification agent stored inside without using power or control.
JP8049910A 1996-03-07 1996-03-07 Denitration apparatus Pending JPH09239238A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8049910A JPH09239238A (en) 1996-03-07 1996-03-07 Denitration apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8049910A JPH09239238A (en) 1996-03-07 1996-03-07 Denitration apparatus

Publications (1)

Publication Number Publication Date
JPH09239238A true JPH09239238A (en) 1997-09-16

Family

ID=12844177

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8049910A Pending JPH09239238A (en) 1996-03-07 1996-03-07 Denitration apparatus

Country Status (1)

Country Link
JP (1) JPH09239238A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999003564A3 (en) * 1997-07-18 1999-06-10 Enviro Energy Products Inc Method and apparatus for oxidizing no to no2 and apparatus and method for generating ozone
WO2012011393A1 (en) * 2010-07-23 2012-01-26 三菱重工メカトロシステムズ株式会社 Facility for treatment of gas in tunnel

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1999003564A3 (en) * 1997-07-18 1999-06-10 Enviro Energy Products Inc Method and apparatus for oxidizing no to no2 and apparatus and method for generating ozone
WO2012011393A1 (en) * 2010-07-23 2012-01-26 三菱重工メカトロシステムズ株式会社 Facility for treatment of gas in tunnel
JP2012024688A (en) * 2010-07-23 2012-02-09 Mitsubishi Heavy Industries Mechatronics Systems Ltd Facility for treatment of gas in tunnel

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