JP2000054833A - NOx REDUCTION SYSTEM FOR COMBUSTION EXHAUST GAS - Google Patents

NOx REDUCTION SYSTEM FOR COMBUSTION EXHAUST GAS

Info

Publication number
JP2000054833A
JP2000054833A JP10254486A JP25448698A JP2000054833A JP 2000054833 A JP2000054833 A JP 2000054833A JP 10254486 A JP10254486 A JP 10254486A JP 25448698 A JP25448698 A JP 25448698A JP 2000054833 A JP2000054833 A JP 2000054833A
Authority
JP
Japan
Prior art keywords
exhaust gas
air
fuel
ozone
air supply
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
JP10254486A
Other languages
Japanese (ja)
Other versions
JP3531489B2 (en
Inventor
Yoshinori Takahashi
嘉則 高橋
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.)
Mitsubishi Motors Corp
Original Assignee
Mitsubishi Motors Corp
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 Mitsubishi Motors Corp filed Critical Mitsubishi Motors Corp
Priority to JP25448698A priority Critical patent/JP3531489B2/en
Publication of JP2000054833A publication Critical patent/JP2000054833A/en
Application granted granted Critical
Publication of JP3531489B2 publication Critical patent/JP3531489B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2240/00Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being
    • F01N2240/38Combination or association of two or more different exhaust treating devices, or of at least one such device with an auxiliary device, not covered by indexing codes F01N2230/00 or F01N2250/00, one of the devices being an ozone (O3) generator, e.g. for adding ozone after generation of ozone from air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/03Adding substances to exhaust gases the substance being hydrocarbons, e.g. engine fuel
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/08Adding substances to exhaust gases with prior mixing of the substances with a gas, e.g. air
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N2610/00Adding substances to exhaust gases
    • F01N2610/10Adding substances to exhaust gases the substance being heated, e.g. by heating tank or supply line of the added substance
    • 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
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Abstract

PROBLEM TO BE SOLVED: To easily and inexpensively improve the NOX purifying performance by partially changing oxygen in the air to ozone, heating a gas oil added to the air in the presence of ozone to partially oxidize it, and adding them into an exhaust gas passage on the upstream side of a NOx catalytic converter. SOLUTION: In a diesel engine 10, fuel gas oil is supplied from a fuel injection pump 14 to each cylinder through a fuel injection pipe 16 and a fuel injection nozzle 12. The exhaust gas is carried in an exhaust gas passage 26 including an exhaust manifold 24 and exhausted to the outside after NOx is removed by the NOx catalyst 30 of a NOx catalytic converter 28. At this time, the air regulated by a flow control valve 34 is supplied to an air supplying passage 32 communicating with the exhaust gas passage 26 on the upstream side of the NOx catalyst 30 responding to the operating condition of the engine 10. The oxygen in the air is partially changed to ozone through an ozone generating device 40. Thereafter, the mixture of the resulting air and the fuel gas oil is heated by a heating device 46 to partially oxidize the gas oil.

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、種々の工業用燃焼
炉、ディーゼルエンジン等の燃焼排ガス(以下場合によ
り、単に排ガスと略称する)中に含まれるNOを効果
的に浄化することができる燃焼排ガス用NO還元シス
テムに関するものである。
BACKGROUND OF THE INVENTION The present invention provides various industrial combustion furnace, (optionally hereinafter, simply referred to as exhaust gas) combustion exhaust gas such as a diesel engine can be effectively purifying NO x contained in the it relates the NO x reduction system for a combustion exhaust gas.

【0002】[0002]

【従来の技術】従来、ディーゼルエンジンのNO及び
酸素過剰の酸素を含む排ガス中のNOを浄化する手段
として、例えば、実開平4−54926号公報に記載さ
れているように、排ガス中に還元剤を添加して分子篩構
造を有するメタロシリケート系等のNO触媒に接触さ
せることが有効であるとされている。
Conventionally, as a means for purifying the NO x in the exhaust gas containing NO x and oxygen excess oxygen diesel engines, for example, as described in the real Hei 4-54926, JP-in the exhaust gas be brought into contact with the NO x catalyst of the metallosilicate type or the like having a molecular sieve structure is to be effective by adding a reducing agent.

【0003】上記NO触媒のNO浄化性能を向上す
る還元剤として、ディーゼルエンジンの燃料軽油を使用
することが最も簡便であるが、図3の概略構成図に示さ
れているように、ディーゼルエンジンの排ガス通路01
に介装され、その内部にNO触媒02が収蔵されたN
コンバータ03の上流側排ガス通路に、燃料噴射装
置04を設けて、排ガス中に直接燃料軽油を噴射して添
加する通常の方法では、図4のNO浄化率線図に示さ
れているように、十分なNO浄化性能を得ることがで
きない。
As a reducing agent to improve the NO x purification performance of the the NO x catalyst, it is the most convenient to use a fuel gas oil of the diesel engine, as shown in the schematic diagram of FIG. 3, Diesel Exhaust gas passage 01 of the engine
A is interposed, is the NO x catalyst 02 therein is collection N
Upstream exhaust gas passage of O x converter 03, provided with a fuel injector 04, in the conventional method of adding by injecting fuel directly light oil into the exhaust gas are shown in the NO x purification rate diagram of Figure 4 as such, it is impossible to obtain sufficient the nO x purification performance.

【0004】上記NO浄化率線図は、縦軸にNO
化効率(%)をとり、かつ横軸に、実際のディーゼルエ
ンジンの排ガス成分と略同様の組成を有する試験ガスの
温度をとって、NO浄化性能を調べたものである。上
記試験ガスの流量はSV=4000h−1であり、この
試験ガス中にエンジン用燃料の軽油が3000ppmの
濃度で添加されている。通常のトラック用ディーゼルエ
ンジンの排ガス温度は、アイドル運転時において100
〜200℃、全力運転時に500℃程度であり、エンジ
ンの運転状態と排ガス中のNO濃度との関係から、図
4中に台形の折れ線Aで示したようなNO浄化性能を
得ることが理想的であるが、上記排気ガス中に直接軽油
を噴射する通常の方法では、同図4中に曲線Bで示され
ているように、目標性能線Aに対して、遥かに低い浄化
率しか得られず、排ガス濃度が400℃付近の狭い領域
でNO浄化率が30%を僅かに越える程度であって、
実用上不十分である。なお、図中試験ガス温度500℃
以上の領域は、エンジンの運転中稀にしか発生しない過
負荷運転領域である。
[0004] The the NO x purification rate diagram takes the NO x purification efficiency (%) on the vertical axis, and the horizontal axis, taking the temperature of the test gas having an actual substantially the same composition as the exhaust gas components of the diesel engine Te is obtained by examining the the NO x purification performance. The flow rate of the test gas was SV = 4000 h −1 , and light oil of engine fuel was added to the test gas at a concentration of 3000 ppm. The exhaust gas temperature of a normal truck diesel engine is 100
To 200 DEG ° C., is about 500 ° C. at the time of full power operation, the relationship between the concentration of NO x operating conditions and in the exhaust gas of the engine, to obtain the the NO x purification performance, as shown in trapezoidal polygonal line A in FIG. 4 Although it is ideal, the conventional method of directly injecting light oil into the exhaust gas has a much lower purification rate than the target performance line A as shown by a curve B in FIG. not obtained, NO x purification rate in the narrow region around the exhaust gas concentration 400 ° C. is a degree slightly exceeding 30%,
Practically insufficient. In the figure, the test gas temperature is 500 ° C.
The above region is an overload operation region that rarely occurs during operation of the engine.

【0005】そこで、上記実開平4−54926号公報
に記載された装置(以下、場合により既提案の装置とい
う)では、ディーゼルエンジンの燃料軽油を熱分解して
排ガスに添加しNO触媒コンバータに供給することに
よって、NO浄化率を向上することが意図されてい
る。
[0005] Therefore, the actual Hei apparatus described in 4-54926 JP (hereinafter, the case that the apparatus already proposed by), the in the NO x catalyst converter fuel light oil diesel engine was added pyrolyzed in the exhaust gas by feeding, it is intended to improve the NO x purification rate.

【0006】上記既提案の装置の概略構成を示す図5に
おいて、05は車両用の4サイクルディーゼルエンジ
ン、06は同ディーゼルエンジン05の各気筒に設けら
れた燃料噴射ノズル07に燃料噴射管08を介して燃料
を供給する列型燃料噴射ポンプ、09は燃料タンク内の
燃料を燃料供給管010を介して上記燃料噴射ポンプ0
6に供給するフィードポンプ、011は上記ディーゼル
エンジン05の排気マニホールド012を含む排ガス通
路、013は同排ガス通路011に介装されたNO
媒コンバータであって、同触媒コンバータ013の内部
には、メタロシリケート系NO触媒014が収蔵され
ている。
In FIG. 5 showing the schematic configuration of the above-mentioned proposed device, reference numeral 05 denotes a four-cycle diesel engine for a vehicle, and reference numeral 06 denotes a fuel injection pipe 08 to a fuel injection nozzle 07 provided in each cylinder of the diesel engine 05. A line type fuel injection pump 09 for supplying fuel through the fuel injection pump 09 supplies the fuel in the fuel tank via the fuel supply pipe 010 to the fuel injection pump 0.
Feed pump supplies the 6, 011 exhaust gas passage including an exhaust manifold 012 of the diesel engine 05, 013 is a the NO x catalyst converter interposed in the exhaust gas passage 011, inside of the catalytic converter 013, metallosilicate type the NO x catalyst 014 is collection.

【0007】上記NO触媒コンバータ013の上流側
における排ガス通路011に熱分解装置015が接続さ
れ、同熱分解装置015は、外周を電熱ピータ016に
よって囲まれた分解室017と、同分解室017内に燃
料軽油を噴射する燃料噴射弁018と、上記排ガス通路
011内の排ガスを流量制御弁019を介して上記分解
室017に供給する排ガス供給通路020とを備え、上
記燃料噴射弁018には、上記燃料供給管010から分
岐燃料供給管021を経て燃料軽油が供給される。
[0007] The NO pyrolyzer 015 to the exhaust gas passage 011 upstream of x catalytic converter 013 is connected, the pyrolyzer 015 includes a decomposition chamber 017 surrounded the outer periphery by heating repeater 016, the cracking chamber 017 A fuel injection valve 018 for injecting fuel gas oil therein, and an exhaust gas supply passage 020 for supplying the exhaust gas in the exhaust gas passage 011 to the decomposition chamber 017 via a flow control valve 019. The fuel light oil is supplied from the fuel supply pipe 010 through the branch fuel supply pipe 021.

【0008】上記既提案の装置では、排ガス供給通路0
20から分解室017に供給された排ガスが、電熱ヒー
タ016により1000℃近くの高温度に加熱され、こ
の高温雰囲気内に燃料噴射弁018から噴射された燃料
軽油が熱分解されて、NO還元用の不飽和低級炭化水
素が生成され、この還元用HCの存在により、NO
媒014のNO浄化性能の向上が図られている。
In the above-mentioned proposed device, the exhaust gas supply passage 0
Exhaust gas supplied to the decomposition chamber 017 from 20 is heated to a high temperature near 1000 ° C. The electric heater 016, a fuel light oil is injected from the fuel injection valve 018 into the high-temperature atmosphere is thermally decomposed, NO x reduction And the presence of this reducing HC improves the NO x purification performance of the NO x catalyst 014.

【0009】しかしながら、通常のディーゼルエンジン
05の排ガス中の酸素量は、アイドル運転状態で18〜
20%程度、全力運転状態で3〜5%程度に過ぎず、特
に排ガス中のNO量が多い部分負荷ないし全力運転時
の酸素量が少ないため、分解室017の雰囲気温度を1
000℃近くの高温としてもNO還元に有効なHCの
生成量が少なく、NO触媒014のNO浄化性能が
なお不十分な不具合があり、また、熱分解雰囲気温度を
1000℃近くの高温にする必要があるため、電熱ヒー
タ016の消費電力が大きい不都合がある。
However, the amount of oxygen in the exhaust gas of the normal diesel engine 05 is 18 to 18 in the idling state.
About 20%, only about 3-5% at full operating conditions, in particular for small amount of oxygen of the NO x amount is larger portion when load or full power operation in the exhaust gas, the ambient temperature of the decomposition chamber 017 1
Even when the temperature is as high as about 000 ° C., the amount of generated HC effective for NO x reduction is small, and there is a problem that the NO x purification performance of the NO x catalyst 014 is still insufficient. Therefore, there is a disadvantage that the power consumption of the electric heater 016 is large.

【0010】[0010]

【発明が解決しようとする課題】本発明は、ディーゼル
エンジンの燃焼排ガス等、NO及び過剰酸素を含む燃
焼排ガス通路に介装されたNO触媒コンバータの上流
側における排ガス通路内に直接燃料軽油を噴射するよう
にした従来装置、及び雰囲気ガスとして排ガスを使用し
1000℃近くの高温雰囲気中に燃料軽油を噴射して熱
分解し、生成した不飽和低級炭化水素をNO還元用H
CとしてNO触媒コンバータの上流側における排ガス
通路内に添加する既提案の装置における上記不具合を改
良し、従来より優れたNO浄化性能を有する構造簡単
かつ安価な燃焼排ガス用還元システムを提供することを
目的とするものである。
[0008] The present invention is a combustion exhaust gas or the like of a diesel engine, NO x and fuel directly light oil into the exhaust gas passageway upstream of the NO x catalytic converter interposed in the combustion exhaust gas passage containing excess oxygen conventional apparatus designed to inject, and a high-temperature atmosphere near 1000 ° C. using an exhaust gas by injecting fuel light oil is thermally decomposed as the atmospheric gas, the generated unsaturated lower hydrocarbons the NO x reduction for H
Improved defect above the device already proposed to be added to the exhaust gas passageway upstream of the NO x catalytic converter as C, and provides a simple structure and inexpensive flue gas for reduction system with excellent the NO x purification performance than conventional The purpose is to do so.

【0011】[0011]

【課題を解決するための手段】上記目的を達成するた
め、本発明は、NO及び過剰酸素を含む燃焼排ガス通
路に介装され燃焼排ガス中のNOを還元することがで
きる触媒を収蔵したNO触媒コンバータと、一端を上
記NO触媒コンバータ上流側の燃焼排ガス通路に連通
されると共に他端を空気供給源に接続された空気供給通
路と、上記空気供給通路の途中に設けられ上記空気供給
源から供給された空気中の酸素の一部をオゾンに変化さ
せるオゾン発生装置と、上記空気供給通路の途中に設け
られ上記空気供給源から供給された空気に軽油を添加す
る軽油添加装置と、上記空気に添加された軽油をオゾン
の存在下に加熱して部分酸化させる加熱装置とを備えた
ことを特徴とする燃焼排ガス用NO還元システムを提
供するものである。
To achieve To achieve the object described above, the present invention has a collection of over a catalyst capable of reducing NO x in combustion exhaust gas passage is interposed combustion exhaust gas containing NO x and excess oxygen and the NO x catalyst converter, and an air supply passage connected to an air supply source and the other end with one end communicates with the combustion exhaust gas passage of the the NO x catalyst converter upstream, the air provided in the middle of the air supply passage An ozone generation device that converts a part of oxygen in the air supplied from the supply source into ozone, and a light oil addition device that is provided in the middle of the air supply passage and adds light oil to the air supplied from the air supply source. , der provides a the NO x reduction system for a combustion exhaust gas, characterized in that it comprises a heating device and to the gas oil which is added to the air is heated to partial oxidation in the presence of ozone .

【0012】[0012]

【発明の実施の形態】以下本発明の好ましい実施形態を
図1および図2について具体的に説明する。先ず、図1
の概略構成図において、符号10はトラック等車両用の
4サイクル多気筒ディーゼルエンジン(図では、一例と
して4気筒エンジンが示されている)であって、同エン
ジン10の各気筒に設けられた燃料噴射ノズル12に
は、燃料噴射ポンプ14の対応するポンプユニットから
燃焼噴射管16を介して燃料軽油が供給される。また、
上記燃料噴射ポンプ14には、燃料タンク18内に貯溜
された軽油が、フィードポンプ20により燃料供給管2
2を介して供給される。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A preferred embodiment of the present invention will be specifically described below with reference to FIGS. First, FIG.
In the schematic configuration diagram, reference numeral 10 denotes a four-cycle multi-cylinder diesel engine for a vehicle such as a truck (a four-cylinder engine is shown as an example in the figure), and a fuel provided in each cylinder of the engine 10 is shown. Fuel light oil is supplied to the injection nozzle 12 from a corresponding pump unit of the fuel injection pump 14 via a combustion injection pipe 16. Also,
Light oil stored in a fuel tank 18 is supplied to the fuel injection pump 14 by a feed pump 20 through a fuel supply pipe 2.
2 is provided.

【0013】上記ディーゼルエンジン10の運転中、そ
の排ガスは排気マニホールド24を含む排ガス通路26
に排出され、同排ガス通路26の適所にNO触媒コン
バータ28が介装されている。上記NO触媒コンバー
タ28内には、適宜のNO触媒、好ましくはコージェ
ライト製のハニカム構造の担体に、銀アルミネート(A
gAlO)のような銀複合酸化物を主成分とする触媒
を担持させたNO触媒30が収蔵されている。
During the operation of the diesel engine 10, the exhaust gas is exhausted through an exhaust gas passage 26 including an exhaust manifold 24.
Is discharged, place in the NO x catalyst converter 28 in the exhaust gas channel 26 are interposed. Within the the NO x catalyst converter 28, suitably of the NO x catalyst, preferably a carrier of a honeycomb structure of cordierite, silver aluminate (A
Galo 2) silver composite oxide the NO x catalyst 30 which is supported a catalyst mainly composed of are collections like.

【0014】上記NO触媒コンバータ28の上流側の
排ガス通路26に空気供給通路32の一端が接続され、
同空気供給通路32の他端は流量制御弁34を介して空
気供給源又はエアタンク36に接続されている。空気供
給源36には、エアコンプレッサ又はエアポンプ38に
より加圧された空気が供給される。また、上記流量制御
弁34より下流側の空気供給通路32に、コロナ放電
式、紫外線照射方式、アーク放電方式、電子線或いはX
線照射方式等適宜方式のオゾン発生装置40が配設さ
れ、上記空気供給通路32に供給された空気中の酸素の
一部がオゾンに変化するように設けられている。
[0014] One end of the air supply passage 32 is connected to the exhaust gas passage 26 on the upstream side of the the NO x catalyst converter 28,
The other end of the air supply passage 32 is connected to an air supply source or an air tank 36 via a flow control valve 34. Air compressed by an air compressor or an air pump 38 is supplied to the air supply source 36. Further, a corona discharge type, an ultraviolet irradiation type, an arc discharge type, an electron beam or X-ray is supplied to the air supply passage 32 downstream of the flow control valve 34.
An ozone generator 40 of an appropriate type such as a line irradiation type is provided, and a part of oxygen in the air supplied to the air supply passage 32 is changed to ozone.

【0015】さらに、上記オゾン発生装置40より下流
側の空気供給通路32に軽油添加装置を形成する燃料噴
射弁42が配設され、同燃料噴射弁42は分岐燃料供給
管44を介して上記燃料供給管22に連結されている。
なおまた、上記空気供給通路32のオゾン発生装置40
より下流側の部分に、好ましくは電熱ヒータ或いは赤外
線炉からなる加熱装置46が設けられ、同加熱装置46
により空気供給通路32内を流れるオゾンを含んだ空気
及び燃料噴射弁42から噴射された軽油噴霧が加熱され
る。
Further, a fuel injection valve 42 forming a light oil addition device is disposed in the air supply passage 32 downstream of the ozone generation device 40, and the fuel injection valve 42 is connected via the branch fuel supply pipe 44 to the fuel injection valve 42. It is connected to the supply pipe 22.
In addition, the ozone generator 40 of the air supply passage 32
A heating device 46, which preferably comprises an electric heater or an infrared furnace, is provided at a portion on the further downstream side.
Accordingly, the air containing ozone flowing in the air supply passage 32 and the light oil spray injected from the fuel injection valve 42 are heated.

【0016】上記流量制御弁34の開度、従って空気供
給源36から空気供給通路32に供給される空気流量、
上記オゾン発生装置40の作動、燃料噴射弁42の開
閉、即ち空気供給通路32に供給される燃料軽油の流
量、加熱装置46に対する電力供給、従って空気供給通
路32内を流れる燃料噴霧及びオゾンを含む空気の温度
は、夫々コントロールユニット48によって制御され
る。
The opening degree of the flow control valve 34, and thus the flow rate of air supplied from the air supply source 36 to the air supply passage 32,
The operation of the ozone generator 40, the opening and closing of the fuel injection valve 42, that is, the flow rate of the fuel oil supplied to the air supply passage 32, the power supply to the heating device 46, and the fuel spray and ozone flowing in the air supply passage 32 are included. The temperature of the air is controlled by the control unit 48, respectively.

【0017】上記コントロールユニット48は、ディー
ゼルエンジン10の運転状態を表わすエンジン回転数を
検出する回転数センサー50の出力信号Ne、エンジン
負荷を検出する負荷センサー52の出力信号Le、その
他エンジン冷却水の温度等の補助的信号を受容して、排
ガス通路26内に排出される排ガスの流量、温度等を検
知して、上記流量制御弁34、オゾン発生装置40、燃
料噴射弁42、及び加熱装置46に夫々エンジンの運転
状態に応じた駆動出力を供給する。なお、上記負荷セン
サー52は、図示の実施形態では燃料噴射ポンプ14の
燃料供給量制御用ラックの位置検出センサーとして示さ
れているが、勿論、車両のアクセルペダル踏込量を検知
するセンサーで代替することができる。
The control unit 48 includes an output signal Ne of a rotation speed sensor 50 for detecting an engine rotation speed indicating an operation state of the diesel engine 10, an output signal Le of a load sensor 52 for detecting an engine load, and other engine cooling water. The flow rate control valve 34, the ozone generator 40, the fuel injection valve 42, and the heating device 46 detect the flow rate, the temperature, and the like of the exhaust gas discharged into the exhaust gas passage 26 by receiving an auxiliary signal such as the temperature. To each of which a drive output corresponding to the operating state of the engine is supplied. In the illustrated embodiment, the load sensor 52 is shown as a position detection sensor of the fuel supply amount control rack of the fuel injection pump 14, but it is needless to say that a sensor that detects the accelerator pedal depression amount of the vehicle is used instead. be able to.

【0018】なお、必要に応じ、上記空気供給通路32
の一端が排ガス通路26に連通する部分の下流側及び上
流側に、第1及び第2の温度センサー54及び56が設
けられ、NO触媒30の直上流における排ガスと供給
空気との混合気体の温度及び排気ガス自体の温度が、上
記コントロールユニット48内に供給され、上記流量制
御弁34等に供給される駆動出力の補正が行なわれる。
If necessary, the air supply passage 32
The end on the downstream side and the upstream side of the portion which communicates with the exhaust gas passage 26, first and second temperature sensors 54 and 56 are provided, the gas mixture of the exhaust gas and the feed air in immediately upstream of the NO x catalyst 30 The temperature and the temperature of the exhaust gas itself are supplied into the control unit 48, and the drive output supplied to the flow control valve 34 and the like is corrected.

【0019】上記装置において、ディーゼルエンジン1
0は、燃料噴射ポンプ14から燃料噴射管16及び燃料
噴射ノズル12を介して各気筒に燃料軽油が供給され、
排ガスは、排気マニホールド24を含む排ガス通路26
内を流れ、同排ガス通路26内に配設されたNO触媒
コンバータ28を通りNO触媒30により含有するN
の相当部分を還元し除去されたのち、外気に排出さ
れる。
In the above device, the diesel engine 1
0 indicates that fuel oil is supplied from a fuel injection pump 14 to each cylinder via a fuel injection pipe 16 and a fuel injection nozzle 12,
The exhaust gas passes through an exhaust gas passage 26 including an exhaust manifold 24.
The inner flow, containing the street the NO x catalyst 30 to the NO x catalyst converter 28 disposed in the exhaust gas passage 26 N
After reducing a substantial portion of the O x is removed, it is discharged to the outside air.

【0020】良く知られているように、トラック等車両
用のディーゼルエンジンは、アイドル運転から全力運転
まで、広範かつ頻繁に変化する運転状態で作動し、運転
状態によって排ガスの温度、流量、過剰酸素及びNO
の含有量が大幅に変化し、一例として、アイドル運転
時、排ガス温度は100〜200℃、過剰酸素量は18
〜20%(重量比)、また全力運転時、排ガス温度は略
500℃前後、過剰酸素量は僅かに3〜5%(重量比)
程度である。また、排ガス中のNO量は、アイドル運
転時は少なく、部分負荷運転時及び全力運転時は大幅に
増加する一般的傾向があり、従って、排ガス中のNO
を浄化するという観点からは、部分負荷ないし全力運転
時が重要であり、このとき排ガス中の過剰酸素量は空気
と較べて著しく少ない。
As is well known, a diesel engine for a vehicle such as a truck operates in a wide and frequently changing operation state from an idling operation to a full power operation. And NO x
Is greatly changed. For example, during idling operation, the exhaust gas temperature is 100 to 200 ° C., and the excess oxygen amount is 18
-20% (weight ratio), and at full power operation, the exhaust gas temperature is about 500 ° C, and the excess oxygen amount is only 3-5% (weight ratio)
It is about. Further, NO x amount in the exhaust gas, idling operation is small, and during full power operation part load operation has generally tends to increase significantly, therefore, NO x in the exhaust gas
From the viewpoint of purifying the exhaust gas, partial load or full power operation is important. At this time, the amount of excess oxygen in the exhaust gas is significantly smaller than that in the air.

【0021】上記ディーゼルエンジン10の運転状態
は、回転数センサー50の出力信号Ne及び負荷センサ
ー52の出力信号Le、その他必要に応じエンジン冷却
水温等の補助信号が、コントロールユニット48に供給
されることによって検知され、同コントロールユニット
48に内蔵されたマップにより排気ガス温度、排ガス流
量等が検知され、流量制御弁34、オゾン発生装置4
0、燃料噴射弁42及び加熱装置46に駆動出力が供給
される。
The operation state of the diesel engine 10 is such that an output signal Ne of the rotation speed sensor 50, an output signal Le of the load sensor 52, and other auxiliary signals such as an engine cooling water temperature are supplied to the control unit 48 as necessary. The exhaust gas temperature, the exhaust gas flow rate, and the like are detected by a map built in the control unit 48, and the flow control valve 34, the ozone generator 4
0, the drive output is supplied to the fuel injection valve 42 and the heating device 46.

【0022】エンジン10の運転状態に応じて、NO
触媒30の上流側の排ガス通路26に連通する空気供給
通路32に流量制御弁34により調量された空気が供給
される。空気供給通路32内に流入した空気は、オゾン
発生装置40を通り、含有する酸素の一部がオゾンに変
化して下流に流れる。ディーゼルエンジンの排ガスに較
べて多量の酸素を含み、かつオゾンを含んだ空気内にそ
の流量に応じた量の燃料軽油が、燃料噴射弁42から噴
射され、同燃料噴射弁42には、燃料タンク18内の燃
料軽油が分岐燃料供給管44を介して供給される。
Depending on the operating state of the engine 10, NO x
Air metered by a flow control valve 34 is supplied to an air supply passage 32 communicating with the exhaust gas passage 26 on the upstream side of the catalyst 30. The air that has flowed into the air supply passage 32 passes through the ozone generator 40, and a part of the contained oxygen is changed to ozone and flows downstream. A light quantity of fuel oil containing a large amount of oxygen compared to the exhaust gas of the diesel engine and containing ozone is injected from a fuel injection valve 42 into the air containing ozone, and the fuel injection valve 42 has a fuel tank. The fuel light oil in 18 is supplied via a branch fuel supply pipe 44.

【0023】上記多量の酸素及びオゾンを含んだ空気と
燃料軽油噴霧との混合体は、加熱装置46により適宜の
温度、好ましくは300℃ないし480℃程度に加熱さ
れ、多量の酸素を含みかつオゾンを含む供給空気中の軽
油は効果的に部分酸化されてNO還元性が強いアセト
アルデヒド、フォルムアルデヒド等のアルデヒド類、プ
ロピレン、エチレン等多量に含む分解ガスとなって、排
ガスに添加される。
The mixture of the air containing a large amount of oxygen and ozone and the fuel gas oil spray is heated to an appropriate temperature, preferably about 300 ° C. to 480 ° C., by a heating device 46, and contains a large amount of oxygen and ozone. The gas oil in the supply air containing is effectively partially oxidized to become a cracked gas containing a large amount of aldehydes such as acetaldehyde and formaldehyde, propylene, ethylene, etc., which have a strong NO x reducing property, and is added to the exhaust gas.

【0024】一例として、流量制御弁34によって制御
される空気供給通路32内の空気流量は、排ガス流量の
20%(容積比)に調整され、燃料噴射弁42から空気
供給通路32内に噴射される燃料軽油は、エンジン10
に供給される燃料軽油に対して3〜6%程度(重量比)
であり、また加熱装置46により供給された空気及び燃
料軽油噴霧の混合体は350℃に加熱される。軽油噴霧
は上記のように部分酸化された分解ガスとなって供給空
気と共に排ガスに添加され、上記NO触媒30と接触
して、排ガス中のNOが効率的に還元され浄化され
る。
As an example, the air flow rate in the air supply passage 32 controlled by the flow control valve 34 is adjusted to 20% (volume ratio) of the exhaust gas flow rate, and is injected from the fuel injection valve 42 into the air supply passage 32. Fuel oil is supplied to the engine 10
3 to 6% (by weight) of fuel light oil supplied to
And the mixture of air and fuel gas oil spray supplied by the heating device 46 is heated to 350 ° C. Gas oil spray is added to the exhaust gas with partially oxidized decomposition gas and turned by supplying air, as described above, in contact with the the NO x catalyst 30, NO x in the exhaust gas is efficiently reduced and purified.

【0025】図2は、実際のディーゼルエンジンの排ガ
スを模した試験ガスの温度(℃)を横軸にとり、かつN
浄化率(%)を縦軸にとって、上記軽油を部分酸化
した分解ガスと空気との混合体(350℃)をNO
媒30の上流側において排ガスに添加してNO浄化率
を調べた結果を示したものである。なお、前記図4のN
浄化率線図と同様に、試験ガスの流量はSV=40
00h−1、添加軽油の濃度は3000ppmであり、
比較のために、軽油を直接排ガス中に同じ濃度添加した
場合の浄化率曲線Bが図中に記載されている。
FIG. 2 shows the temperature (° C.) of the test gas simulating the exhaust gas of an actual diesel engine on the horizontal axis,
O x purification rate (%) ordinate, examined the NO x purification rate by adding to the exhaust gas at the upstream side of the mixture of cracked gas and air was partially oxidizing the light oil (350 ° C.) NO x catalyst 30 FIG. Note that N in FIG.
As in the Ox purification rate diagram, the flow rate of the test gas was SV = 40.
00h -1 , the concentration of the added light oil is 3000 ppm,
For comparison, the purification rate curve B when light oil is directly added to the exhaust gas at the same concentration is shown in the figure.

【0026】図2の右上方に記載されているように、上
記オゾン発生装置40の出力を種々変化させて、オゾン
濃度0ppm(白抜き三角Δを連ねた折れ線)、50p
pm(黒丸●を連ねた折れ線)、400ppm(白抜き
正方形□を連ねた折れ線)、750ppm(×印を連ね
た折れ線)、及び1000ppm(点線の折れ線)とN
浄化率との関係を調べた結果、オゾン濃度0pp
m、即ちオゾン発生装置40が作動していない場合で
も、従来の排気ガス中に直接軽油を噴射した場合のNO
浄化率曲線Bに較べて遥かに浄化率が良く、エンジン
の部分負荷運転状態から全力運転の全領域において目標
性能線Aに近い優れた浄化率を得ることができ、特に試
験ガス温度が380〜450℃の領域で、略60%に近
い高い浄化率を達成し得ることが確認され、さらに、オ
ゾン濃度が50ppmから1000ppmに増加するに
つれ、NO浄化率が向上し、特に400〜1000p
pmでは、350〜480℃の試験ガス温度領域におい
て前記目標性能線Aを超え、最高60%近い優れた浄化
率が得られることが確認され、かつ試験ガス温度が30
0℃程度の低温領域でも目標性能に近い浄化率が得られ
ることが認められた。
As shown in the upper right part of FIG. 2, the output of the ozone generator 40 is varied to obtain an ozone concentration of 0 ppm (a polygonal line connecting the open triangles Δ) and 50 p.
pm (a polygonal line connecting black circles), 400 ppm (a polygonal line connecting white squares), 750 ppm (a polygonal line connecting x marks), and 1000 ppm (a dotted line).
As a result of examining the relationship with the O x purification rate, the ozone concentration was 0 pp.
m, that is, NO when the light oil is directly injected into the conventional exhaust gas even when the ozone generator 40 is not operating.
x The purification rate is much better than the purification rate curve B, and an excellent purification rate close to the target performance line A can be obtained in the entire region of full-power operation from the partial load operation state of the engine. It has been confirmed that a high purification rate close to about 60% can be achieved in the range of about to 450 ° C., and further, as the ozone concentration increases from 50 ppm to 1000 ppm, the NOx purification rate improves, particularly 400 to 1000 p.
pm, it is confirmed that an excellent purification rate exceeding the target performance line A in the test gas temperature range of 350 to 480 ° C. and close to 60% at maximum is obtained, and the test gas temperature is 30 ° C.
It was recognized that a purification rate close to the target performance could be obtained even in a low temperature range of about 0 ° C.

【0027】なお、上記試験結果から明らかなように、
試験ガス温度が300〜480℃の領域で高いNO
去効率が得られるので、第1及び第2温度センサー54
及び56により排ガス温度を調べ、NO触媒30の直
上流の排ガス温度が480℃より高い場合、流量制御弁
34の開度を増大して空気供給量を増大させ、NO
媒30の直上流における排ガスの温度を上記300〜4
80℃の温度領域に低下させることが有利である。
As apparent from the above test results,
Since test gas temperature is obtained a high NO x removal efficiency in the region of three hundred to four hundred eighty ° C., the first and second temperature sensors 54
And 56 examine the exhaust gas temperature by, when the exhaust gas temperature immediately upstream of the NO x catalyst 30 is higher than 480 ° C., by increasing the opening degree of the flow control valve 34 to increase the air supply amount, immediately upstream of the NO x catalyst 30 Temperature of the exhaust gas at 300 to 4
Advantageously, the temperature is reduced to a temperature range of 80 ° C.

【0028】なお、前記既提案の装置ではディーゼルエ
ンジンの排ガス通路から一部の排気を分岐して取出し、
当該分岐排ガス内に燃料軽油を噴射し加熱することによ
り、軽油を改質してNO触媒の上流側排ガス通路内に
流入させるように構成されているが、NOの発生量が
多い部分負荷ないし全力運転時の排ガス中の酸素量は空
気と較べて著しく少ないので、改質された軽油に含まれ
るアルデヒド類等還元性が強い成分が少なく、十分なN
浄化効率を得ることができない不具合があり、また
添加する軽油の改質のために、軽油噴霧を含む排ガスを
1000℃近くの高温に加熱する必要があるので、電力
消費が大きく、車両用ディーゼルエンジンの場合、発電
負荷が増大して燃費が悪化する欠点がある。
In the above-mentioned proposed device, a part of the exhaust gas is branched out from the exhaust gas passage of the diesel engine and taken out.
By heating the fuel is injected light oil to the branch in the exhaust gas, is configured so as diesel fuel is reformed to flow into the upstream side exhaust gas passage of the NO x catalyst, the amount is large partial load of the NO x In addition, since the amount of oxygen in the exhaust gas at the time of full power operation is significantly smaller than that of air, there are few components having strong reducing properties such as aldehydes contained in the reformed gas oil, and sufficient N
Ox purification efficiency cannot be obtained, and exhaust gas including light oil spray must be heated to a high temperature of about 1000 ° C. for reforming the light oil to be added. In the case of a diesel engine, there is a disadvantage that the power generation load increases and fuel efficiency deteriorates.

【0029】なおまた、本発明は上記実施形態に限定さ
れるものではなく、本発明の特許請求の範囲内で種々の
変更、修正を加え実施することができる。一例として、
オゾン発生装置40の配置位置を、図1に示されている
燃料噴射弁42の上流側位置から同燃料噴射弁42の下
流側における空気供給通路32に配置することができ
る。さらに、本発明はディーゼルエンジンの排ガス用N
還元システムのみならず、種々の工業用燃焼炉等か
ら発生する燃焼排ガスのNO還元に広く適用すること
ができる。
The present invention is not limited to the above embodiment, and various changes and modifications can be made within the scope of the claims of the present invention. As an example,
The arrangement position of the ozone generator 40 can be arranged in the air supply passage 32 on the downstream side of the fuel injection valve 42 from the position on the upstream side of the fuel injection valve 42 shown in FIG. Furthermore, the present invention relates to a diesel engine
O x not reduction system only, it can be widely applied to the NO x reduction of the combustion exhaust gas generated from various industrial combustion furnace.

【0030】[0030]

【発明の効果】叙上のように、本発明に係る燃焼排ガス
用NO還元システムは、NO及び過剰酸素を含む燃
焼排ガス通路に介装され燃焼排ガス中のNOを還元す
ることができる触媒を収蔵したNO触媒コンバータ
と、一端を上記NO触媒コンバータ上流側の燃焼排ガ
ス通路に連通されると共に他端を空気供給源に接続され
た空気供給通路と、上記空気供給通路の途中に設けられ
上記空気供給源から供給された空気中の酸素の一部をオ
ゾンに変化させるオゾン発生装置と、上記空気供給通路
の途中に設けられ上記空気供給源から供給された空気に
軽油を添加する軽油添加装置と、上記空気に添加された
軽油をオゾンの存在下に加熱して部分酸化させる加熱装
置とを備えたことを特徴とし、ディーゼルエンジンや種
々の工業用燃焼炉等から発生する燃焼排ガス、特に車両
用ディーゼルエンジンのNO発生量が多い運転領域に
おいて、従来のNO還元システムより著しく優れたN
浄化効率を達成し得る構造簡単かつ安価なNO
元システムを提供することができるので、産業上有益で
ある。
According to the present invention as the ordination combustion the NO x reduction system for exhaust gas according to the present invention can be interposed in the combustion exhaust gas passage including NO x and excess oxygen to reduce NO x in the combustion exhaust gas and the NO x catalyst converter with collection of the catalyst, an air supply passage connected to an air supply source and the other end with one end communicates with the combustion exhaust gas passage of the the NO x catalyst converter upstream, in the middle of the air supply passage An ozone generator that is provided to change a part of oxygen in the air supplied from the air supply source to ozone, and that is provided in the middle of the air supply passage and adds light oil to air supplied from the air supply source It is characterized by comprising a light oil addition device and a heating device for heating light oil added to the air in the presence of ozone to partially oxidize the light oil. Generated from such combustion exhaust gas, particularly in the NO x generation amount is large operating range of the diesel engine for a vehicle, conventional the NO x reduction system than significantly better N
Since the structure simple and inexpensive the NO x reduction system can achieve the O x purification efficiency can be provided, it is beneficial industrially.

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

【図1】本発明の好ましい実施形態を示す概略構成図で
ある。
FIG. 1 is a schematic configuration diagram showing a preferred embodiment of the present invention.

【図2】本発明に係る排気浄化装置のNO浄化率を従
来の排ガス浄化装置のNO浄化率と対比して示した線
図である。
2 is a diagram of the NO x purification rate shown in comparison with the NO x purification rate of the conventional exhaust gas purifying device for an exhaust gas purification apparatus of the present invention.

【図3】NO触媒の上流側排ガス通路内に直接軽油を
噴射する従来の装置を示す概略構成図である。
Figure 3 is a schematic diagram showing a conventional apparatus for injecting directly light oil to the upstream side exhaust gas passage of the NO x catalyst.

【図4】図3に示した従来の排ガス浄化装置のNO
化率を示した線図である。
4 is a diagram showing the the NO x purification rate of the conventional exhaust gas purifying apparatus shown in FIG.

【図5】既提案のNO浄化装置を示す概略構成図であ
る。
FIG. 5 is a schematic configuration diagram showing an already proposed NO x purification device.

【符号の説明】[Explanation of symbols]

10…ディーゼルエンジン、12…燃料噴射ノズル、1
4…燃料噴射ポンプ、18…燃料タンク、20…フィー
ドポンプ、24…排気マニホールド、26…排ガス通
路、28…NO触媒コンバータ、30…NO触媒、
32…空気供給通路、34…流量制御弁、36…空気供
給源、40…オゾン発生装置、42…燃料噴射弁(軽油
添加装置)、46…加熱装置、48…コントロールユニ
ット、50…回転数センサー、52…負荷センサー。
10: diesel engine, 12: fuel injection nozzle, 1
4 ... fuel injection pump, 18 ... Fuel tank, 20 ... feed pump, 24 ... exhaust manifold, 26 ... exhaust passage, 28 ... NO x catalytic converter, 30 ... NO x catalyst,
32 ... air supply passage, 34 ... flow control valve, 36 ... air supply source, 40 ... ozone generator, 42 ... fuel injection valve (light oil addition device), 46 ... heating device, 48 ... control unit, 50 ... rotation speed sensor , 52 ... load sensor.

───────────────────────────────────────────────────── フロントページの続き Fターム(参考) 3G091 AA02 AA18 AA28 AB05 BA01 BA04 BA14 BA22 CA18 CA22 CB02 CB08 DA01 DA02 DA05 EA01 EA03 EA07 EA08 EA16 EA17 FA11 FB10 FC04 GA06 GB01W GB10W GB17X HA36 HA42 HB07  ──────────────────────────────────────────────────続 き Continued on the front page F term (reference) 3G091 AA02 AA18 AA28 AB05 BA01 BA04 BA14 BA22 CA18 CA22 CB02 CB08 DA01 DA02 DA05 EA01 EA03 EA07 EA08 EA16 EA17 FA11 FB10 FC04 GA06 GB01W GB10W GB17X HA36 HA42 HB07

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 NO及び過剰酸素を含む燃焼排ガス通
路に介装され燃焼排ガス中のNOを還元することがで
きる触媒を収蔵したNO触媒コンバータと、一端を上
記NO触媒コンバータ上流側の燃焼排ガス通路に連通
されると共に他端を空気供給源に接続された空気供給通
路と、上記空気供給通路の途中に設けられ上記空気供給
源から供給された空気中の酸素の一部をオゾンに変化さ
せるオゾン発生装置と、上記空気供給通路の途中に設け
られ上記空気供給源から供給された空気に軽油を添加す
る軽油添加装置と、上記空気に添加された軽油をオゾン
の存在下に加熱して部分酸化させる加熱装置とを備えた
ことを特徴とする燃焼排ガス用NO還元システム。
1. A NO x and the the NO x catalyst converter with a collection of over a catalyst capable of excess oxygen is interposed in the combustion exhaust gas channel comprising reducing NO x in the combustion exhaust gas, the the NO x catalyst converter upstream side end An air supply passage connected to the combustion exhaust gas passage and having the other end connected to the air supply source, and a part of the oxygen contained in the air supplied from the air supply source provided in the middle of the air supply passage. An ozone generator, which is provided in the middle of the air supply passage, for adding light oil to the air supplied from the air supply source, and heating the light oil added to the air in the presence of ozone. the NO x reduction system for a combustion exhaust gas, characterized in that it comprises a heating device and which is partially oxidized.
JP25448698A 1998-08-05 1998-08-05 NOx reduction system for flue gas Expired - Fee Related JP3531489B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25448698A JP3531489B2 (en) 1998-08-05 1998-08-05 NOx reduction system for flue gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25448698A JP3531489B2 (en) 1998-08-05 1998-08-05 NOx reduction system for flue gas

Publications (2)

Publication Number Publication Date
JP2000054833A true JP2000054833A (en) 2000-02-22
JP3531489B2 JP3531489B2 (en) 2004-05-31

Family

ID=17265731

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25448698A Expired - Fee Related JP3531489B2 (en) 1998-08-05 1998-08-05 NOx reduction system for flue gas

Country Status (1)

Country Link
JP (1) JP3531489B2 (en)

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002221024A (en) * 2001-01-22 2002-08-09 Kawasaki Heavy Ind Ltd METHOD AND DEVICE FOR SUPPLYING LIQUID REDUCING AGENT FOR NOx REMOVAL SYSTEM
JP2005517853A (en) * 2002-02-15 2005-06-16 ボルボ テクニスク ウートヴェクリング アクチボラゲット Equipment for processing gas streams
JP2007289844A (en) * 2006-04-24 2007-11-08 Toyota Motor Corp Exhaust gas cleaning device of internal combustion engine
JP2008031927A (en) * 2006-07-28 2008-02-14 Mazda Motor Corp Failure diagnostic system of exhaust emission control device
WO2008081734A1 (en) * 2006-12-28 2008-07-10 Toyota Jidosha Kabushiki Kaisha Exhaust gas purifying apparatus for internal combustion engine
WO2013035663A1 (en) * 2011-09-05 2013-03-14 日野自動車株式会社 Exhaust gas purification apparatus
JP2015108354A (en) * 2013-12-05 2015-06-11 株式会社デンソー High-active substance adding device
JP2015108351A (en) * 2013-12-05 2015-06-11 株式会社デンソー High-active substance adding device
JP2015108350A (en) * 2013-12-05 2015-06-11 株式会社デンソー High-active substance adding device
US20150211400A1 (en) * 2014-01-30 2015-07-30 Denso Corporation Reducing agent supplying device
CN104819037A (en) * 2014-01-30 2015-08-05 株式会社电装 Reducing agent supplying device
JP2015200228A (en) * 2014-04-08 2015-11-12 株式会社デンソー reducing agent addition device
JP2016035246A (en) * 2014-08-04 2016-03-17 株式会社日本自動車部品総合研究所 Reducing agent addition device
EP2998532A2 (en) 2014-09-18 2016-03-23 Denso Corporation Reducing agent supplying device
DE102015116013A1 (en) 2014-09-25 2016-03-31 Denso Corporation Reducing agent supplying device
DE102015115656A1 (en) 2014-09-25 2016-03-31 Denso Corporation Ozonzuführvorrichtung
JP2016065538A (en) * 2014-09-25 2016-04-28 株式会社日本自動車部品総合研究所 Reducer addition device
JP2016191305A (en) * 2015-03-30 2016-11-10 株式会社日本自動車部品総合研究所 Nox elimination system control device and reducing agent addition system
WO2017098906A1 (en) * 2015-12-11 2017-06-15 株式会社デンソー Ozone supply control device and ozone supply device
US20180251374A1 (en) * 2015-09-08 2018-09-06 Denso Corporation Ozone supply device
CN110199094A (en) * 2016-12-19 2019-09-03 庄信万丰股份有限公司 NO is improved by introducing ozonexConversion ratio

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6107748B2 (en) 2014-06-20 2017-04-05 株式会社デンソー Reducing agent addition device

Cited By (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002221024A (en) * 2001-01-22 2002-08-09 Kawasaki Heavy Ind Ltd METHOD AND DEVICE FOR SUPPLYING LIQUID REDUCING AGENT FOR NOx REMOVAL SYSTEM
JP2005517853A (en) * 2002-02-15 2005-06-16 ボルボ テクニスク ウートヴェクリング アクチボラゲット Equipment for processing gas streams
JP2007289844A (en) * 2006-04-24 2007-11-08 Toyota Motor Corp Exhaust gas cleaning device of internal combustion engine
JP2008031927A (en) * 2006-07-28 2008-02-14 Mazda Motor Corp Failure diagnostic system of exhaust emission control device
JP4706589B2 (en) * 2006-07-28 2011-06-22 マツダ株式会社 Failure diagnosis system for exhaust gas purification equipment
WO2008081734A1 (en) * 2006-12-28 2008-07-10 Toyota Jidosha Kabushiki Kaisha Exhaust gas purifying apparatus for internal combustion engine
WO2013035663A1 (en) * 2011-09-05 2013-03-14 日野自動車株式会社 Exhaust gas purification apparatus
JP5465361B2 (en) * 2011-09-05 2014-04-09 日野自動車株式会社 Exhaust gas purification device
EP2754866A1 (en) * 2011-09-05 2014-07-16 Hino Motors Ltd. Exhaust gas purification apparatus
EP2754866A4 (en) * 2011-09-05 2015-04-22 Hino Motors Ltd Exhaust gas purification apparatus
US9145805B2 (en) 2011-09-05 2015-09-29 Hino Motors, Ltd. Exhaust gas purifier
JP2015108354A (en) * 2013-12-05 2015-06-11 株式会社デンソー High-active substance adding device
JP2015108351A (en) * 2013-12-05 2015-06-11 株式会社デンソー High-active substance adding device
JP2015108350A (en) * 2013-12-05 2015-06-11 株式会社デンソー High-active substance adding device
CN104819037A (en) * 2014-01-30 2015-08-05 株式会社电装 Reducing agent supplying device
US9528410B2 (en) * 2014-01-30 2016-12-27 Denso Corporation Reducing agent supplying device
JP2015140792A (en) * 2014-01-30 2015-08-03 株式会社デンソー reducing agent addition device
US20150211400A1 (en) * 2014-01-30 2015-07-30 Denso Corporation Reducing agent supplying device
CN104819038A (en) * 2014-01-30 2015-08-05 株式会社电装 Reducing agent supplying device
US9605575B2 (en) 2014-01-30 2017-03-28 Denso Corporation Reducing agent supplying device
JP2015200228A (en) * 2014-04-08 2015-11-12 株式会社デンソー reducing agent addition device
JP2016035246A (en) * 2014-08-04 2016-03-17 株式会社日本自動車部品総合研究所 Reducing agent addition device
JP2016061233A (en) * 2014-09-18 2016-04-25 株式会社デンソー Reducing agent addition device
US9488082B2 (en) 2014-09-18 2016-11-08 Denso Corporation Reducing agent supplying device
EP2998532A2 (en) 2014-09-18 2016-03-23 Denso Corporation Reducing agent supplying device
DE102015115656A1 (en) 2014-09-25 2016-03-31 Denso Corporation Ozonzuführvorrichtung
JP2016065538A (en) * 2014-09-25 2016-04-28 株式会社日本自動車部品総合研究所 Reducer addition device
DE102015116013A1 (en) 2014-09-25 2016-03-31 Denso Corporation Reducing agent supplying device
JP2016191305A (en) * 2015-03-30 2016-11-10 株式会社日本自動車部品総合研究所 Nox elimination system control device and reducing agent addition system
US20180251374A1 (en) * 2015-09-08 2018-09-06 Denso Corporation Ozone supply device
WO2017098906A1 (en) * 2015-12-11 2017-06-15 株式会社デンソー Ozone supply control device and ozone supply device
JP2017106420A (en) * 2015-12-11 2017-06-15 株式会社デンソー Ozone supply control device and ozone supply device
CN110199094A (en) * 2016-12-19 2019-09-03 庄信万丰股份有限公司 NO is improved by introducing ozonexConversion ratio

Also Published As

Publication number Publication date
JP3531489B2 (en) 2004-05-31

Similar Documents

Publication Publication Date Title
JP3565035B2 (en) NOx reduction system for combustion exhaust gas
JP3531489B2 (en) NOx reduction system for flue gas
US5586433A (en) Process and apparatus for selective catalyzed no-reduction in oxygen-containing exhaust gases
JP4122849B2 (en) Catalyst degradation detector
JP3557928B2 (en) Internal combustion engine having lean NOx catalyst
US20130239554A1 (en) Exhaust gas treatment system having a solid ammonia gas producing material
US20120060480A1 (en) Exhaust gas purifiying apparatus in internal combustion engine
KR102518593B1 (en) CORRECTION METHOD OF NOx PURIFYING EFFICIENCY OF SDPF
KR20180029678A (en) Exhaust gas purification device of vehicle and control method thereof
JP2000240441A (en) NOx REDUCTION DEVICE FOR ENGINE EXHAUST GAS
JP3577946B2 (en) Compression ignition type internal combustion engine having a combustion type heater
US20090308056A1 (en) Procedure and device for the purification of exhaust gas
JP2543736Y2 (en) Exhaust gas purification device for internal combustion engine
KR101836287B1 (en) Catalyst heating control apparatus and the method
JP4893493B2 (en) Exhaust gas purification device for internal combustion engine
US6318076B1 (en) Apparatus for treating the exhaust gas of an internal combustion engine
JPH1193647A (en) Device for diagnosing deterioration of catalyst for internal combustion engine
JP3552561B2 (en) Internal combustion engine with exhaust gas purification device
KR20240009563A (en) Apparatus for purifying exhaust gas
JP3551779B2 (en) Internal combustion engine having lean NOx catalyst
KR20220135376A (en) Exhaust gas reducing system and control method thereof
JPH10141048A (en) Method and device for controlling nox in exhaust gas from diesel engine
JPH08281069A (en) Method of purifying exhaust gas from internal combustion engine
JP3292117B2 (en) Injection control device for internal combustion engine
JP3508532B2 (en) Internal combustion engine having lean NOx catalyst

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20040129

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20040210

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20040223

R150 Certificate of patent or registration of utility model

Free format text: JAPANESE INTERMEDIATE CODE: R150

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R371 Transfer withdrawn

Free format text: JAPANESE INTERMEDIATE CODE: R371

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

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

Free format text: PAYMENT UNTIL: 20090312

Year of fee payment: 5

LAPS Cancellation because of no payment of annual fees