JPH05222923A - Nox-in-engine-exhaust-gas reducing device by means of catalyst - Google Patents

Nox-in-engine-exhaust-gas reducing device by means of catalyst

Info

Publication number
JPH05222923A
JPH05222923A JP4056366A JP5636692A JPH05222923A JP H05222923 A JPH05222923 A JP H05222923A JP 4056366 A JP4056366 A JP 4056366A JP 5636692 A JP5636692 A JP 5636692A JP H05222923 A JPH05222923 A JP H05222923A
Authority
JP
Japan
Prior art keywords
hydrocarbon
nox
catalyst
reducing agent
engine
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
JP4056366A
Other languages
Japanese (ja)
Inventor
Mitsuru Hosoya
満 細谷
Isao Uemitsu
勲 上光
Tetsuya Otani
哲也 大谷
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.)
Hino Motors Ltd
Original Assignee
Hino Motors 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 Hino Motors Ltd filed Critical Hino Motors Ltd
Priority to JP4056366A priority Critical patent/JPH05222923A/en
Publication of JPH05222923A publication Critical patent/JPH05222923A/en
Pending 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
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/24Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
    • F01N3/36Arrangements for supply of additional 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
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • 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
    • F01N2240/18Combination 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 adsorber or absorber
    • 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
    • F01N2570/00Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
    • F01N2570/12Hydrocarbons
    • 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
    • F01N2610/04Adding substances to exhaust gases the substance being hydrogen
    • 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
    • F01N2610/14Arrangements for the supply of substances, e.g. conduits
    • F01N2610/1473Overflow or return means for the substances, e.g. conduits or valves for the return path
    • 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To supply a proper quantity of reducing agents in accordance the operating condition of an engine, even if a hydrocarbon reducing agent having a low invert ratio of NOx to N2 in respect of component constitution is used, by reforming it so as to efficiently reduce NOx. CONSTITUTION:The exhaust pipe 12 of an engine 10 is provided with a NOx catalyst 14 and an injection nozzle 18 arranged upstream thereof. A reducing agent supply means 20 for supplying a hydrocarbon reducing agent to the injection nozzle 18 is provided with a storage tank 22 for storing liquid hydrocarbon 21, a force-feeding pump 24 for forcibly feeding the hydrocarbon 21 stored in this tank 22 through a liquid feeding pipe 23, a reactor 26 for reforming the forcibly fed hydrocarbon 21 so as to reduce the number of carbons thereof, a hydrocarbon separating chamber 27 for separating the reformed hydrocarbon from the unreformed hydrocarbon, and a compressor 29 for forcibly feeding the reformed hydrocarbon to the injection nozzle 18 through a pneumatic tube 28.

Description

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

【0001】[0001]

【産業上の利用分野】本発明は、エンジンの排ガスに含
まれる窒素酸化物(以下、NOxという)を触媒により
低減する装置に関する。更に詳しくは車両用エンジンの
排ガス中のNOx低減装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for reducing nitrogen oxides (hereinafter referred to as NOx) contained in exhaust gas of an engine by a catalyst. More specifically, it relates to a device for reducing NOx in exhaust gas of a vehicle engine.

【0002】[0002]

【従来の技術】この種のNOx低減装置として、エンジ
ンの排気管にNOx触媒を収容する触媒室を設け、この
NOx触媒の排ガス上流側より噴射ノズルでNOxの還
元剤を噴射して、触媒によりNOxを無害なN2に転化
する装置が知られている。従来、この還元剤にはアンモ
ニアが用いられてきた。
2. Description of the Related Art As a NOx reducing device of this type, a catalyst chamber for accommodating a NOx catalyst is provided in an exhaust pipe of an engine, and a NOx reducing agent is injected from an exhaust gas upstream side of the NOx catalyst by an injection nozzle so that the catalyst is used. Devices for converting NOx to harmless N 2 are known. Conventionally, ammonia has been used as the reducing agent.

【0003】[0003]

【発明が解決しようとする課題】しかし、アンモニアは
車載性に劣り、かつ漏洩したときの臭気の問題から車両
用エンジンのNOx還元剤には不向きであった。また還
元剤として軽油を用いた場合には、軽油は炭素数が16
の炭化水素成分を多く含み、この点で効率良くNOxを
2に転化することができず、そのまま大気に放出され
てしまうNOxの割合が高い不具合があった。本発明の
目的は、成分組成の点でNOxのN2への転化率が低い
炭化水素系還元剤であってもこれを改質して効率良くN
Oxを低減し得る、エンジン排ガスの触媒によるNOx
低減装置を提供することにある。本発明の別の目的は、
エンジンの運転状態に応じて適量の還元剤を供給し得る
NOx低減装置を提供することにある。
However, ammonia is unsuitable as a NOx reducing agent for vehicle engines because of its poor vehicle mountability and the problem of odor when it leaks. When light oil is used as the reducing agent, the light oil has 16 carbon atoms.
However, in this respect, NOx could not be efficiently converted to N 2 , and the proportion of NOx that was directly released to the atmosphere was high. The object of the present invention is to efficiently reform a hydrocarbon-based reducing agent that has a low NOx conversion rate to N 2 in terms of composition.
NOx by catalyst of engine exhaust gas that can reduce Ox
It is to provide a reduction device. Another object of the present invention is to
An object of the present invention is to provide a NOx reduction device that can supply an appropriate amount of reducing agent according to the operating state of the engine.

【0004】[0004]

【課題を解決するための手段】上記目的を達成するため
の本発明の構成を実施例に対応する図1に基づいて説明
する。本発明は、エンジン10の排気管12に設けられ
NOx触媒14を収容する触媒室16と、NOx触媒1
4の排ガス上流側に設けられこのNOx触媒14に向け
て炭化水素系還元剤を噴射可能な噴射ノズル18と、噴
射ノズル18に前記還元剤を供給する還元剤供給手段2
0とを備えたエンジン排ガスの触媒によるNOx低減装
置の改良である。その特徴ある構成は、還元剤供給手段
20が液状の炭化水素21を貯える貯蔵タンク22と、
このタンク22に貯えられた炭化水素21を液送管23
を介して圧送する圧送ポンプ24と、この圧送された炭
化水素21をその炭素数を減少するように改質するリア
クタ26と、改質された炭化水素と改質されなかった炭
化水素とを分離する炭化水素分離室27と、改質された
炭化水素を気送管28を介して噴射ノズル18に圧送す
るコンプレッサ29とを備えたことにある。なお、この
NOx低減装置に、NOx触媒14の排ガス上流側に設
けられた温度センサ46と、エンジン10の負荷を検出
する負荷センサ44と、エンジン10の回転速度を検出
する回転センサ42と、液送管23に設けられた第1流
量調整弁31と、気送管28に設けられた第2流量調整
弁32と、温度センサ46、負荷センサ44及び回転セ
ンサ42の検出出力に基づいて圧送ポンプ24、コンプ
レッサ29、第1及び第2流量調整弁31,32を制御
するコントローラ40とを備えることが好ましい。更
に、このNOx低減装置の炭化水素分離室27の底部に
改質されなかった液状の炭化水素を回収する回収タンク
33を設け、この回収タンク33の液状の炭化水素を貯
蔵タンク22に戻す回収ポンプ36を設けることが好ま
しい。
A structure of the present invention for achieving the above object will be described with reference to FIG. 1 corresponding to an embodiment. The present invention includes a catalyst chamber 16 provided in an exhaust pipe 12 of an engine 10 for accommodating a NOx catalyst 14, and a NOx catalyst 1.
4, an injection nozzle 18 provided upstream of the exhaust gas and capable of injecting a hydrocarbon-based reducing agent toward the NOx catalyst 14, and a reducing agent supply means 2 for supplying the reducing agent to the injection nozzle 18.
Is an improvement of the NOx reduction device by the catalyst of the engine exhaust gas provided with 0. The characteristic configuration is that the reducing agent supply means 20 has a storage tank 22 for storing a liquid hydrocarbon 21,
Hydrocarbon 21 stored in this tank 22
And a reactor 26 for reforming the pumped hydrocarbon 21 so as to reduce its carbon number, and a reformed hydrocarbon and a non-reformed hydrocarbon are separated from each other. That is, it is provided with a hydrocarbon separation chamber 27 that operates and a compressor 29 that pressure-feeds the reformed hydrocarbons to the injection nozzle 18 through the air delivery pipe 28. In this NOx reduction device, a temperature sensor 46 provided on the exhaust gas upstream side of the NOx catalyst 14, a load sensor 44 for detecting the load of the engine 10, a rotation sensor 42 for detecting the rotation speed of the engine 10, and a liquid sensor A first flow rate adjusting valve 31 provided in the delivery pipe 23, a second flow rate adjusting valve 32 provided in the air delivery pipe 28, and a pressure feed pump based on detection outputs of the temperature sensor 46, the load sensor 44, and the rotation sensor 42. 24, a compressor 29, and a controller 40 for controlling the first and second flow rate adjusting valves 31, 32 are preferably provided. Further, a recovery tank 33 for recovering unreformed liquid hydrocarbons is provided at the bottom of the hydrocarbon separation chamber 27 of the NOx reduction device, and a recovery pump for returning the liquid hydrocarbons in the recovery tank 33 to the storage tank 22. It is preferable to provide 36.

【0005】[0005]

【作用】エンジン10から排出されたガスは排気管12
を通り、噴射ノズル18から供給された還元剤とともに
触媒室16に流入し、そこで排ガス中のNOxはNOx
触媒14により還元処理されて無害のN2に転化した
後、大気に放出される。噴射ノズル18から供給される
還元剤は、質的にはリアクタ26でクラッキングされ、
分離室27で精製分離された炭素数の減少した低分子量
の炭化水素であるため、高い効率でNOxをN2に転化
する。また量的にはコントローラ40が運転状態に応じ
て記憶される排ガス中のNOx含有量に見合った適量の
還元剤を流量調整弁31,32等を制御して噴射ノズル
18から供給する。
The gas discharged from the engine 10 is discharged to the exhaust pipe 12
Through the injection nozzle 18 and the reducing agent supplied to the catalyst chamber 16, where NOx in the exhaust gas is converted to NOx.
After being reduced by the catalyst 14 and converted into harmless N 2 , it is released into the atmosphere. The reducing agent supplied from the injection nozzle 18 is qualitatively cracked in the reactor 26,
Since it is a low molecular weight hydrocarbon having a reduced number of carbons, which has been purified and separated in the separation chamber 27, NOx is converted to N 2 with high efficiency. In terms of quantity, the controller 40 supplies an appropriate amount of reducing agent corresponding to the NOx content in the exhaust gas stored according to the operating state from the injection nozzle 18 by controlling the flow rate adjusting valves 31, 32 and the like.

【0006】[0006]

【実施例】次に本発明の一実施例を図面に基づいて詳し
く説明する。図1に示すように、ディーゼルエンジン1
0の排気マニホルド11には排気管12が接続される。
この排気管12の途中にはエンジン側から還元剤噴射室
13と、NOx触媒14を収容する触媒室16と、マフ
ラー17がこの順に設けられる。この例では、NOx触
媒14は銅イオン交換ゼオライト(Cu−ZSM−5)
により構成される。この銅イオン交換ゼオライトはゼオ
ライトが含んでいるナトリウムイオンを銅イオンに置き
換えた物質であって、NOxを炭化水素により還元する
性質を有する。還元剤噴射室13には噴射ノズル18が
NOx触媒14に向けて設けられる。
An embodiment of the present invention will be described in detail with reference to the drawings. As shown in FIG. 1, a diesel engine 1
An exhaust pipe 12 is connected to the exhaust manifold 11 of 0.
A reducing agent injection chamber 13, a catalyst chamber 16 accommodating the NOx catalyst 14, and a muffler 17 are provided in this order from the engine side in the middle of the exhaust pipe 12. In this example, the NOx catalyst 14 is a copper ion exchanged zeolite (Cu-ZSM-5).
It is composed of This copper ion-exchanged zeolite is a substance in which sodium ions contained in zeolite are replaced with copper ions, and has a property of reducing NOx with hydrocarbons. An injection nozzle 18 is provided in the reducing agent injection chamber 13 toward the NOx catalyst 14.

【0007】噴射ノズル18に炭化水素系還元剤を供給
する還元剤供給手段20は、軽油21を貯える貯蔵タン
ク22と、この軽油21を液送管23を介して圧送する
圧送ポンプ24と、圧送された軽油の炭素数を減少する
ように改質するリアクタ26と、改質された炭化水素と
改質されなかった炭化水素とを分離する炭化水素分離室
27と、改質された炭化水素を気送管28を介して噴射
ノズル18に圧送するコンプレッサ29とにより構成さ
れる。この例では、コンプレッサ29はモータ30によ
り駆動される。ポンプ24の吐出側の液送管23には第
1流量調整弁31が、またコンプレッサ29の吐出側の
気送管28には第2流量調整弁32がそれぞれ設けられ
る。これらの調整弁31及び32は電磁弁であって、調
整弁31及び32にはタンク22への戻り管31a及び
炭化水素分離室27への戻り管32aがそれぞれ接続さ
れる。
A reducing agent supply means 20 for supplying a hydrocarbon reducing agent to the injection nozzle 18 includes a storage tank 22 for storing light oil 21, a pressure pump 24 for pressure-transmitting the light oil 21 via a liquid-feeding pipe 23, and a pressure-feeding device. The reactor 26 for reforming the reformed light oil so as to reduce the carbon number thereof, the hydrocarbon separation chamber 27 for separating the reformed hydrocarbons from the unreformed hydrocarbons, and the reformed hydrocarbons. It is configured by a compressor 29 that pressure-feeds to the injection nozzle 18 via an air feeding pipe 28. In this example, the compressor 29 is driven by the motor 30. The liquid delivery pipe 23 on the discharge side of the pump 24 is provided with a first flow rate adjusting valve 31, and the air delivery pipe 28 on the discharge side of the compressor 29 is provided with a second flow rate adjusting valve 32. The adjusting valves 31 and 32 are electromagnetic valves, and the adjusting valves 31 and 32 are connected to a return pipe 31a to the tank 22 and a returning pipe 32a to the hydrocarbon separation chamber 27, respectively.

【0008】リアクタ26はポンプ24から圧送された
炭素数16の炭化水素を主成分とする軽油をクラッキン
グして主として炭素数3〜10の成分に改質する。この
例では、リアクタ26は粒状のゼオライトが充填された
カラム26aと、このカラム26aを加熱するヒータ2
6bとを備える。炭化水素分離室27は炭素数3〜10
に改質された軽油とそれ以外の軽油とに分離するセパレ
ータ27aと、周囲にヒータ27bとを備える。カラム
26aの入口は前記液送管23に接続され、その出口は
炭化水素分離室27のセパレータ27aに向けられる。
この分離室27の底部には改質されなかった液状の炭化
水素を回収する回収タンク33が設けられ、分離室27
の頂部には改質され気化した炭化水素を吸引する前述し
た気送管28と戻り管32aが接続される。この回収タ
ンク33と貯蔵タンク22の間には回収管34が接続さ
れ、回収管34の途中には回収ポンプ36が設けられ
る。
The reactor 26 cracks the light oil containing a hydrocarbon having 16 carbon atoms as a main component, which is pumped from the pump 24, and reforms it mainly into a component having 3 to 10 carbon atoms. In this example, the reactor 26 includes a column 26a filled with granular zeolite and a heater 2 for heating the column 26a.
6b. The hydrocarbon separation chamber 27 has 3 to 10 carbon atoms.
A separator 27a for separating the light oil that has been reformed into light oil and the other light oil, and a heater 27b are provided around the separator 27a. The inlet of the column 26a is connected to the liquid delivery pipe 23, and the outlet thereof is directed to the separator 27a of the hydrocarbon separation chamber 27.
A recovery tank 33 for recovering unreformed liquid hydrocarbons is provided at the bottom of the separation chamber 27.
The aforesaid air feeding pipe 28 for sucking the reformed and vaporized hydrocarbons and the return pipe 32a are connected to the top of the. A recovery pipe 34 is connected between the recovery tank 33 and the storage tank 22, and a recovery pump 36 is provided in the recovery pipe 34.

【0009】第1及び第2流量調整弁31及び32、圧
送ポンプ24、コンプレッサ駆動用モータ30、ヒータ
26a及び27b、及び回収ポンプ36にはコントロー
ラ40の制御出力が接続される。このコントローラ40
の制御入力にはエンジン10の回転速度を検出する回転
センサ42と、エンジンの負荷を検出する噴射ポンプ4
3のロードレバー位置センサ44と、触媒室16のNO
x触媒14に流入する排気温度を検出する温度センサ4
6とが接続される。コントローラ40は図示しないメモ
リを備える。このメモリにはエンジンの回転速度、負荷
及び排気温度に応じて噴射ノズル18からNOx触媒1
4に供給すべき炭化水素の量が予め記憶され、コントロ
ーラ40はこの供給量に基づいて調整弁31及び32、
圧送ポンプ24、コンプレッサ駆動用モータ30等を制
御する。
The control output of the controller 40 is connected to the first and second flow rate adjusting valves 31 and 32, the pressure feed pump 24, the compressor driving motor 30, the heaters 26a and 27b, and the recovery pump 36. This controller 40
The control inputs of the rotation sensor 42 for detecting the rotation speed of the engine 10 and the injection pump 4 for detecting the load of the engine.
Load lever position sensor 44 of No. 3 and NO of the catalyst chamber 16
x Temperature sensor 4 for detecting the temperature of exhaust gas flowing into the catalyst 14.
6 and 6 are connected. The controller 40 includes a memory (not shown). This memory stores the NOx catalyst 1 from the injection nozzle 18 according to the engine speed, load and exhaust temperature.
4, the amount of hydrocarbons to be supplied is stored in advance, and the controller 40 adjusts the control valves 31 and 32 based on this supply amount.
It controls the pressure pump 24, the compressor driving motor 30, and the like.

【0010】このような構成のNOx低減装置の動作を
説明する。先ず、エンジン10から排出されたガスは排
気管12を通り、還元剤噴射室13に入り、ここで噴射
ノズル18により炭化水素系還元剤の供給を受ける。こ
の還元剤の供給を受けた排ガスは触媒室16に入り、N
Ox触媒14で排ガス中のNOxを還元処理して無害の
2に転化した後、大気に放出される。ここで噴射ノズ
ル18から噴射される還元剤は次の方法によりその品質
が改良される。先ず、軽油が貯蔵タンク22から圧送ポ
ンプ24によりリアクタ26のカラム26aに送られ、
400〜500℃の温度でゼオライト触媒に接触して分
解し、気化する。この軽油のクラッキングにより軽油が
主として炭素数3〜10の低分子量の炭化水素に改質さ
れる。リアクタ26で改質されなかった高分子量の炭化
水素は炭化水素分離室27のセパレータ27aで改質さ
れた炭化水素と分離される。この精製分離された改質還
元剤はコンプレッサ29で圧縮され噴射ノズル18から
噴射される。この炭素数の減少した炭化水素系還元剤
は、NOx触媒14において、NOxをN2に高い効率
で転化する。
The operation of the NOx reducing device having such a configuration will be described. First, the gas discharged from the engine 10 passes through the exhaust pipe 12 and enters the reducing agent injection chamber 13, where the injection nozzle 18 receives the supply of the hydrocarbon-based reducing agent. The exhaust gas supplied with this reducing agent enters the catalyst chamber 16,
The NOx in the exhaust gas is reduced by the Ox catalyst 14 to be converted into harmless N 2 and then released to the atmosphere. Here, the quality of the reducing agent injected from the injection nozzle 18 is improved by the following method. First, light oil is sent from the storage tank 22 to the column 26a of the reactor 26 by the pressure pump 24,
The zeolite catalyst is decomposed and vaporized at a temperature of 400 to 500 ° C. By cracking the light oil, the light oil is mainly reformed into a low molecular weight hydrocarbon having 3 to 10 carbon atoms. The high molecular weight hydrocarbons that have not been reformed in the reactor 26 are separated from the reformed hydrocarbons in the separator 27a of the hydrocarbon separation chamber 27. The refined and reduced reforming reducing agent is compressed by the compressor 29 and injected from the injection nozzle 18. This hydrocarbon-based reducing agent having a reduced carbon number converts NOx to N 2 in the NOx catalyst 14 with high efficiency.

【0011】また噴射ノズル18から噴射される還元剤
の量は次の方法により制御される。コントローラ40が
センサ42,44,46の検出出力により運転状態に応
じてメモリに記憶される排ガス中のNOx含有量に見合
った適量の還元剤を読出し、この還元剤の量に応じて流
量調整弁31,32,圧送ポンプ24,コンプレッサ駆
動用モータ30等を制御して適量の還元剤を噴射ノズル
18から供給する。具体的には、コントローラ40はエ
ンジン10が低速回転域で軽負荷のときには噴射量を絞
り、中高速回転域で中高負荷のときには噴射量を増大す
るように制御する。更に炭化水素分離室27で改質され
なかった高沸点の炭化水素系還元剤は回収タンク33に
回収され、回収ポンプ36により貯蔵タンク22に戻さ
れる。なお、上記例ではNOx触媒として銅イオン交換
ゼオライトを挙げたが、他のゼオライト系、酸化物系の
触媒でもよい。また、リアクタにおいて軽油をゼオライ
ト触媒を用いて接触分解する例を示したが、酸化チタ
ン、シリカ−アルミナ触媒等他の触媒を用いてもよい。
The amount of reducing agent injected from the injection nozzle 18 is controlled by the following method. The controller 40 reads out an appropriate amount of reducing agent corresponding to the NOx content in the exhaust gas stored in the memory according to the operating states by the detection outputs of the sensors 42, 44, 46, and according to the amount of the reducing agent, the flow rate adjusting valve. An appropriate amount of reducing agent is supplied from the injection nozzle 18 by controlling 31, 32, the pressure feed pump 24, the compressor driving motor 30, and the like. Specifically, the controller 40 controls so that the injection amount is reduced when the engine 10 has a light load in the low speed rotation range, and increases when the engine 10 has a medium and high load in the medium and high speed rotation range. Further, the high-boiling-point hydrocarbon-based reducing agent that has not been reformed in the hydrocarbon separation chamber 27 is recovered in the recovery tank 33 and returned to the storage tank 22 by the recovery pump 36. In the above example, copper ion-exchanged zeolite is used as the NOx catalyst, but other zeolite-based or oxide-based catalysts may be used. Although an example of catalytic cracking of light oil using a zeolite catalyst in the reactor is shown, other catalysts such as titanium oxide and silica-alumina catalyst may be used.

【0012】[0012]

【発明の効果】以上述べたように、本発明によれば、炭
化水素系還元剤が成分組成の点でNOxのN2への転化
率が低い高沸点の炭化水素を含む軽油等であっても、リ
アクタで改質し、炭化水素分離室で精製分離して、有効
な炭化水素系還元剤を選択的に取出し噴射ノズルから噴
射するため、NOx触媒上で排ガス中のNOxが効率良
くN2に転化する。また、エンジンの運転状態に応じて
還元剤の噴射量が制御され、結果として排ガス中のNO
xに応じて適量の還元剤を供給されるため、排ガスに含
まれるNOxを有効に低減することができる。
As described above, according to the present invention, the hydrocarbon-based reducing agent is a gas oil or the like containing a high-boiling hydrocarbon having a low NOx conversion to N 2 in terms of component composition. Also, since it is reformed in the reactor, refined and separated in the hydrocarbon separation chamber, and the effective hydrocarbon-based reducing agent is selectively taken out and injected from the injection nozzle, NOx in the exhaust gas is efficiently converted to N 2 on the NOx catalyst. Convert to. Further, the injection amount of the reducing agent is controlled according to the operating state of the engine, and as a result, NO in the exhaust gas is reduced.
Since an appropriate amount of reducing agent is supplied according to x, NOx contained in the exhaust gas can be effectively reduced.

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

【図1】本発明の一実施例のNOx低減装置の構成図。FIG. 1 is a configuration diagram of a NOx reduction device according to an embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10 エンジン 12 排気管 13 還元剤噴射室 14 NOx触媒 16 触媒室 18 噴射ノズル 20 還元剤供給手段 21 軽油(炭化水素系還元剤) 22 貯蔵タンク 23 液送管 24 圧送ポンプ 26 リアクタ 27 炭化水素分離室 28 気送管 29 コンプレッサ 31 第1流量調整弁 32 第2流量調整弁 33 回収タンク 36 回収ポンプ 40 コントローラ 42 回転センサ 44 負荷センサ 46 温度センサ 10 engine 12 exhaust pipe 13 reducing agent injection chamber 14 NOx catalyst 16 catalyst chamber 18 injection nozzle 20 reducing agent supply means 21 light oil (hydrocarbon-based reducing agent) 22 storage tank 23 liquid feed pipe 24 pressure feed pump 26 reactor 27 hydrocarbon separation chamber 28 Pneumatic tube 29 Compressor 31 First flow rate adjusting valve 32 Second flow rate adjusting valve 33 Recovery tank 36 Recovery pump 40 Controller 42 Rotation sensor 44 Load sensor 46 Temperature sensor

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 エンジン(10)の排気管(12)に設けられN
Ox触媒(14)を収容する触媒室(16)と、 前記NOx触媒(14)の排ガス上流側に設けられ前記NO
x触媒(14)に向けて炭化水素系還元剤を噴射可能な噴射
ノズル(18)と、 前記噴射ノズル(18)に前記還元剤を供給する還元剤供給
手段(20)とを備えたエンジン排ガスの触媒によるNOx
低減装置において、 前記還元剤供給手段(20)が液状の炭化水素(21)を貯える
貯蔵タンク(22)と、 前記貯蔵タンク(22)に貯えられた炭化水素(21)を液送管
(23)を介して圧送する圧送ポンプ(24)と、 前記圧送された炭化水素(21)をその炭素数を減少するよ
うに改質するリアクタ(26)と、 前記改質された炭化水素と改質されなかった炭化水素と
を分離する炭化水素分離室(27)と、 前記改質された炭化水素を気送管(28)を介して前記噴射
ノズル(18)に圧送するコンプレッサ(29)とを備えたこと
を特徴とするエンジン排ガスの触媒によるNOx低減装
置。
1. An N provided in an exhaust pipe (12) of an engine (10)
A catalyst chamber (16) for accommodating the Ox catalyst (14) and the NOx catalyst (14) provided on the exhaust gas upstream side of the NOx catalyst (14).
x Engine exhaust gas provided with an injection nozzle (18) capable of injecting a hydrocarbon-based reducing agent toward the catalyst (14) and a reducing agent supply means (20) for supplying the reducing agent to the injection nozzle (18) NOx by catalyst
In the reducing device, the reducing agent supply means (20) stores a liquid hydrocarbon (21) in a storage tank (22) and a liquid feed pipe for the hydrocarbon (21) stored in the storage tank (22).
(23) a pressure-fed pump (24) for pressure-fed, a reactor (26) for reforming the pressure-fed hydrocarbon (21) so as to reduce the carbon number thereof, and the reformed hydrocarbon A hydrocarbon separation chamber (27) for separating unreformed hydrocarbons, and a compressor (29) for pressure-feeding the reformed hydrocarbons to the injection nozzle (18) via a pneumatic pipe (28). An NOx reduction device using a catalyst for engine exhaust gas, comprising:
【請求項2】 NOx触媒(14)の排ガス上流側に設けら
れた温度センサ(46)と、 エンジン(10)の負荷を検出する負荷センサ(44)と、 エンジン(10)の回転速度を検出する回転センサ(42)と、 液送管(23)に設けられた第1流量調整弁(31)と、 気送管(28)に設けられた第2流量調整弁(32)と、 前記温度センサ(46)、負荷センサ(44)及び回転センサ(4
2)の検出出力に基づいて圧送ポンプ(24)、コンプレッサ
(29)、前記第1及び第2流量調整弁(31,32)を制御する
コントローラ(40)とを備えた請求項1記載のエンジン排
ガスの触媒によるNOx低減装置。
2. A temperature sensor (46) provided on the exhaust gas upstream side of the NOx catalyst (14), a load sensor (44) for detecting the load of the engine (10), and a rotational speed of the engine (10). Rotation sensor (42), the first flow rate adjusting valve (31) provided in the liquid delivery pipe (23), the second flow rate adjusting valve (32) provided in the air delivery pipe (28), and the temperature Sensor (46), load sensor (44) and rotation sensor (4
Compressed pump (24), compressor based on the detection output of 2)
The NOx reduction device according to claim 1, further comprising: (29) a controller (40) for controlling the first and second flow rate adjusting valves (31, 32).
JP4056366A 1992-02-06 1992-02-06 Nox-in-engine-exhaust-gas reducing device by means of catalyst Pending JPH05222923A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4056366A JPH05222923A (en) 1992-02-06 1992-02-06 Nox-in-engine-exhaust-gas reducing device by means of catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4056366A JPH05222923A (en) 1992-02-06 1992-02-06 Nox-in-engine-exhaust-gas reducing device by means of catalyst

Publications (1)

Publication Number Publication Date
JPH05222923A true JPH05222923A (en) 1993-08-31

Family

ID=13025260

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4056366A Pending JPH05222923A (en) 1992-02-06 1992-02-06 Nox-in-engine-exhaust-gas reducing device by means of catalyst

Country Status (1)

Country Link
JP (1) JPH05222923A (en)

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