JPH0658058B2 - Diesel engine - Google Patents

Diesel engine

Info

Publication number
JPH0658058B2
JPH0658058B2 JP2061898A JP6189890A JPH0658058B2 JP H0658058 B2 JPH0658058 B2 JP H0658058B2 JP 2061898 A JP2061898 A JP 2061898A JP 6189890 A JP6189890 A JP 6189890A JP H0658058 B2 JPH0658058 B2 JP H0658058B2
Authority
JP
Japan
Prior art keywords
nox
absolute humidity
value
exhaust gas
amount
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.)
Expired - Fee Related
Application number
JP2061898A
Other languages
Japanese (ja)
Other versions
JPH03264732A (en
Inventor
憲一 瀬角
道興 原
博美 近藤
Original Assignee
ダイハツデイーゼル株式会社
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 ダイハツデイーゼル株式会社 filed Critical ダイハツデイーゼル株式会社
Priority to JP2061898A priority Critical patent/JPH0658058B2/en
Publication of JPH03264732A publication Critical patent/JPH03264732A/en
Publication of JPH0658058B2 publication Critical patent/JPH0658058B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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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
    • F01N3/18Exhaust 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
    • F01N3/2053By-passing catalytic reactors, e.g. to prevent overheating
    • 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
    • F01N3/206Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B47/00Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines
    • F02B47/04Methods of operating engines involving adding non-fuel substances or anti-knock agents to combustion air, fuel, or fuel-air mixtures of engines the substances being other than water or steam only
    • 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
    • F01N2610/02Adding substances to exhaust gases the substance being ammonia or urea
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02BINTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
    • F02B3/00Engines characterised by air compression and subsequent fuel addition
    • F02B3/06Engines characterised by air compression and subsequent fuel addition with compression ignition
    • 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

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Air Humidification (AREA)

Description

【発明の詳細な説明】 〈産業上の利用分野〉 本発明は、大気の絶対湿度の季節変化による給気の乾湿
に伴って増減する排気中の窒素酸化物濃度を一定の低い
レベルまで減少できるディーゼル機関に関する。
DETAILED DESCRIPTION OF THE INVENTION <Industrial field of application> The present invention can reduce the concentration of nitrogen oxides in the exhaust gas, which increases or decreases with the dryness or humidity of the supply air due to seasonal changes in the absolute humidity of the atmosphere, to a certain low level. Regarding diesel engine.

〈従来の技術〉 排気ガス中の窒素酸化物濃度を減少させる装置として、
例えばボイラなどの排気ガスに適用される選択還元アン
モニア脱硝装置がある。この脱硝装置は、触媒を充填し
た容器内に空気を含む320〜450℃程度の排気ガス
を通すとともに、反応に必要かつ十分な量のアンモニア
ガスを注入し、下記の還元反応により排気ガス中のNO
を低減させるものである。
<Prior Art> As a device for reducing the concentration of nitrogen oxides in exhaust gas,
For example, there is a selective reduction ammonia denitration device applied to exhaust gas from a boiler or the like. This denitrification device allows an exhaust gas containing air of about 320 to 450 ° C. to pass through a container filled with a catalyst, and injects a sufficient amount of ammonia gas necessary for the reaction, and reduces the exhaust gas in the exhaust gas by the following reduction reaction. NO
Is to reduce.

4NO+4NH+O→4N+6HO 〈発明が解決しようとする課題〉 ところが、上記従来の脱硝装置は、出力の大きいディー
ゼル機関には適用の可能性とメリットがある反面、構造
が比較的大規模で高価なため、中小型のディーゼル機関
には事実上適用が難しいという欠点がある。また、排気
中の窒素酸化物濃度は、給気の乾湿に伴って増減する特
性があるので、排気中のNOを一定レベルまで低減させ
るには、第7図に示すようにNH注入量を冬期に多く
なるように制御しなければならず、この制御が容易でな
い。さらに、脱硝装置を過給機よりも下流側の排気管に
設ける場合は、排気ガス加熱装置を設けるか、マッチン
グにより排気ガス温度を上昇させる必要があるため、実
質上燃費が増加したり、機関の信頼性が低下するという
問題がある。
4NO + 4NH 3 + O 2 → 4N 2 + 6H 2 O <Problems to be solved by the invention> However, the conventional denitration device has applicability and merit to a diesel engine with a large output, but has a relatively large structure. Due to its large scale and cost, it has a drawback that it is practically difficult to apply to small and medium-sized diesel engines. Further, the concentration of nitrogen oxides in the exhaust gas has a characteristic of increasing and decreasing with the dryness and humidity of the supply air. Therefore, in order to reduce NO in the exhaust gas to a certain level, the amount of NH 3 injection should be adjusted as shown in FIG. It must be controlled so that it increases during winter, and this control is not easy. Furthermore, when the denitration device is installed in the exhaust pipe downstream of the supercharger, it is necessary to install an exhaust gas heating device or raise the exhaust gas temperature by matching, which substantially increases fuel consumption and There is a problem in that the reliability of

さらに、国による排気ガス中のNOx排出基準値が、気筒
径400mm未満ではO2:13%換算で現在の950ppmであ
るが、地方自治体においては114ppmに厳しく規制さ
れる予定であり、中小型ディーゼル機関では現状の排気
NOxレベルからさらに、NOx濃度の低減が急務になってい
る。
Furthermore, the national standard for NOx emissions in exhaust gas is 950 ppm, which is the current O 2 : 13% conversion when the cylinder diameter is less than 400 mm, but local governments will strictly regulate it to 114 ppm. Exhaust as it is in the organization
There is an urgent need to further reduce the NOx concentration from the NOx level.

そこで、本発明の目的は、選択還元アンモニア脱硝装置
にこの装置の脱硝負荷を低減し、かつアンモニア注入の
制御を容易化できる新規なNOx低減手段を組み合わせる
とともに、脱硝装置の配置を工夫することによって、季
節により変動する排気中のNOx濃度を上記規制値に近い
一定のレベルまで大幅に減少することができるディーゼ
ル機関を提供することにある。
Therefore, an object of the present invention is to combine a NOx reduction means capable of reducing the denitration load of this device with the selective reduction ammonia denitration device and facilitating the control of ammonia injection, and devising the arrangement of the denitration device. The purpose of the present invention is to provide a diesel engine capable of greatly reducing the NOx concentration in the exhaust gas, which varies depending on the season, to a certain level close to the above regulated value.

〈課題を解決するための手段〉 上記目的を達成するため、発明者らは、自らが最近提案
した給気への加湿によるNOx低減方法(特願昭63−3
31985号)に着目し、研究を重ねた結果、上記方法
が選択還元アンモニア脱硝装置の脱硝負荷の低減と、ア
ンモニア注入制御の容易化に最適であることを見出し、
本発明を構成するに至った。
<Means for Solving the Problems> In order to achieve the above object, the inventors have recently proposed a NOx reduction method by humidifying air supply (Japanese Patent Application No. 63-3.
As a result of repeated studies focusing on No. 31985), the above method was found to be optimal for reducing the denitration load of the selective reduction ammonia denitration device and facilitating the ammonia injection control,
The present invention has been completed.

即ち、本発明によるディーゼル機関は、設置環境におけ
る大気の絶対湿度の季節変化による給気の乾湿に伴って
増減する排気中の窒素酸化物濃度を一定の低レベルまで
減少できるものにおいて、上記ディーゼル機関の給気配
管系に設けられ、吸い込まれた大気に所定量の水分を加
えて加湿する加湿器と、上記ディーゼル機関の排気配管
系に設けられ、排気中の窒素酸化物をアンモニアと触媒
により還元する還元装置と、給気の絶対湿度と,機関の
運転条件で一義的に定まる給気温度と,使用燃料の比重
および窒素含有量の関数で定義されるNOx濃度の支配式
に出荷調整時における上記諸変数値を代入して関数値を
求める初期関数値算出手段と、求められた関数値を出荷
調整時のNOx規制値で乗じ,かつ運転時のNOx第1規制値
で除して運転時の関数値を求める運転時関数値算出手段
と、上記支配式に運転時の給気温度と使用燃料の比重お
よび窒素含有量を代入してその関数値が上記運転時の関
数値になり、かつ排気中の窒素酸化物濃度を上記NOx第
1規制値にせしめるような給気の絶対湿度を算出する基
準絶対湿度算出手段と、算出された基準絶対湿度と実測
または気象データとして与えられた運転時の大気の絶対
湿度との差およびディーゼル機関の出力に比例した加湿
量を算出し、算出した加湿量を表わす信号を上記加湿器
に出力する加湿量算出手段とを有する第1制御装置と、
排気中の窒素酸化物濃度を上記NOx第1規制値以下のNOx
第2規制値にするため排気に加えるべきアンモニア量を
ディーゼル機関の出力や上記加湿量に基づいて算出し、
このアンモニア量を表わす信号を上記還元装置に出力す
る第2制御装置を備えたことを特徴とする。
That is, the diesel engine according to the present invention can reduce the nitrogen oxide concentration in the exhaust gas, which increases or decreases with the dryness or humidity of the supply air due to the seasonal change in the absolute humidity of the installation environment, to a certain low level. The humidifier installed in the air supply piping system to add a predetermined amount of water to the sucked air to humidify it, and the exhaust piping system of the diesel engine, which reduces nitrogen oxides in the exhaust with ammonia and a catalyst. Reducing device, the absolute humidity of the supply air, the supply air temperature that is uniquely determined by the operating conditions of the engine, the specific gravity of the fuel used, and the governing equation for the NOx concentration defined by the function of the nitrogen content. Initial function value calculating means for substituting the above-mentioned variable values to obtain a function value, and the obtained function value is multiplied by the NOx regulation value at the time of shipment adjustment and divided by the NOx first regulation value at the time of operation Function of Substituting the operating air temperature and the specific gravity of the fuel used and the nitrogen content into the above governing equation, the function value becomes the above operating function value, and Reference absolute humidity calculating means for calculating the absolute humidity of the supply air so that the nitrogen oxide concentration becomes the NOx first regulation value, and the calculated reference absolute humidity and the atmospheric air at the time of operation given as actual measurement or meteorological data. A first controller having a humidification amount calculating means for calculating a humidification amount proportional to a difference from the absolute humidity and an output of the diesel engine, and outputting a signal representing the calculated humidification amount to the humidifier,
NOx concentration in the exhaust is less than the above NOx first regulation value
Calculate the amount of ammonia to be added to the exhaust gas to reach the second regulation value based on the output of the diesel engine and the humidification amount,
A second control device for outputting a signal representing the amount of ammonia to the reduction device is provided.

〈作用〉 第1制御装置の初期関数値算出手段は、NOx濃度の支配
式に出荷調整時における給気の絶対湿度,給気温度,使
用燃料の比重および窒素含有量の値を代入して出荷調整
時の関数値を求める。
<Operation> The initial function value calculation means of the first control device is shipped by substituting the values of absolute humidity of supply air, supply temperature, specific gravity of fuel used, and nitrogen content into the governing equation of NOx concentration during shipping adjustment. Find the function value during adjustment.

次いで、運転時関数値算出手段は、求められた関数値を
出荷調整時のNOx規制値で乗じ,かつ運転時のNOx第1規
制値で除して運転時の関数値を求める。さらに、基準絶
対湿度算出手段は、上記支配式に運転時の給気温度と使
用燃料の比重および窒素含有量を代入してその関数値が
上記運転時の関数値になり、かつ排気中の窒素酸化物濃
度を上記運転時のNOx第1規制値にせしめるような絶対
湿度を算出する。最後に、規制装置の加湿算出手段は、
算出された基準絶対湿度と運転時の大気の絶対湿度との
差およびディーゼル機関の出力に比例した加湿量を算出
し、算出した加湿量を表わす信号を加湿器に出力する。
Next, the operating-time function value calculating means multiplies the obtained function value by the NOx regulation value at the time of shipment adjustment and divides by the NOx first regulation value at the time of operation to obtain the function value at the time of operation. Furthermore, the reference absolute humidity calculating means substitutes the supply air temperature during operation, the specific gravity of the fuel used, and the nitrogen content into the governing equation, and the function value becomes the function value during operation, and the nitrogen in the exhaust gas The absolute humidity is calculated so that the oxide concentration becomes the NOx first regulation value during the above operation. Finally, the humidification calculation means of the control device
A humidification amount proportional to the difference between the calculated reference absolute humidity and the absolute humidity of the atmosphere during operation and the output of the diesel engine is calculated, and a signal representing the calculated humidification amount is output to the humidifier.

加湿器は、ディーゼル機関の給気配管系に吸い込まれた
大気に、上記信号に対応する量の水分を加えて給気を加
湿する。
The humidifier humidifies the supply air by adding the amount of water corresponding to the signal to the atmosphere sucked into the supply pipe system of the diesel engine.

こうして、運転時の大気の絶対湿度が、基準絶対湿度を
下回ると、その差および機関出力に比例した水分が給気
に加えられるので、排気中のNOx濃度は、常に季節変動
最小値以下の上記NOx第1規制値まで減少する。
In this way, when the absolute humidity of the atmosphere during operation falls below the reference absolute humidity, moisture proportional to the difference and engine output is added to the air supply, so the NOx concentration in the exhaust is always below the minimum seasonal fluctuation value. NOx 1st regulation value is reduced.

一方、アンモニア量を制御する第2制御装置は、排気中
の窒素酸化物濃度を上記NOx第1規制値以下のNOx第2規
制値にするため排気に加えるべきアンモニア量を、機関
出力や上記加湿量に基づいて算出し、このアンモニア量
を表わす信号を還元装置に出力する。
On the other hand, the second control device for controlling the amount of ammonia determines the amount of ammonia to be added to the exhaust in order to bring the concentration of nitrogen oxides in the exhaust to the NOx second regulation value which is equal to or lower than the NOx first regulation value, the engine output or the humidification. It is calculated based on the amount, and a signal representing this amount of ammonia is output to the reduction device.

上記アンモニア量は、機関出力の増加と共に僅に増加す
るものの、季節変動のない一定値であり、還元装置でこ
の量のアンモニアが加えられた排気は、上記NOx第1規
制値からさらにNOx第2規制値まで減少する。かくて、
大気に排出される排出ガス中のNOx濃度は、厳しいNOx排
出基準値に適合することになる。
Although the above-mentioned ammonia amount slightly increases as the engine output increases, it is a constant value that does not change seasonally, and the exhaust gas to which this amount of ammonia has been added by the reducing device further exceeds the NOx first regulation value and the NOx second regulation value. Reduce to the regulation value. Thus,
The NOx concentration in the exhaust gas discharged to the atmosphere will meet the strict NOx emission standard value.

〈実施例〉 以下、本発明を図示の実施例により詳細に説明する。<Examples> Hereinafter, the present invention will be described in detail with reference to illustrated examples.

第1図は本発明のディーゼル機関の一実施例を示す概略
図であり、1は給気管2と排気管3を備えたエンジン本
体、4はこのエンジン本体1の燃料ラックの変位を検出
する出力センサとしてのラック目盛センサ、5は上記給
気管2の入口に圧縮機5aを、排気管3の出口にこの圧縮
機に連結するタービン5bを夫々配置してなる過給機、6
はこの過給機5の下流側の給気管2に介設した空気冷却
器、7は流量制御弁7aを制御する第1制御装置を内蔵
し、上記空気冷却器6の上流側の給気管2に水蒸気また
は微粒化された水滴を供給して、給気を加湿する加湿器
である。
FIG. 1 is a schematic view showing an embodiment of a diesel engine of the present invention, 1 is an engine body having an air supply pipe 2 and an exhaust pipe 3, and 4 is an output for detecting a displacement of a fuel rack of the engine body 1. A rack scale sensor 5 serving as a sensor is a supercharger in which a compressor 5a is arranged at the inlet of the air supply pipe 2 and a turbine 5b connected to the compressor is arranged at the outlet of the exhaust pipe 3, 6
Is an air cooler provided in the air supply pipe 2 on the downstream side of the supercharger 5, 7 is a built-in first control device for controlling the flow control valve 7a, and the air supply pipe 2 is on the upstream side of the air cooler 6. It is a humidifier that humidifies the supply air by supplying water vapor or atomized water droplets to.

また、8は流量制御弁8aを介して排気管3にアンモニア
ガスを供給するボンベ、9は上記流量制御弁8aを制御す
る第2制御装置、10は過給機5の上流側の排気管3の
一部をなすバイパス管3aに並列に接続され、内部に充填
した触媒によりアンモニアを含む排気ガス中から窒素酸
化物(NOx)を還元する還元装置、11は還元装置10
とバイパス管3aとに分流する排気ガスの流量比を制御す
る分流弁である。
Further, 8 is a cylinder for supplying ammonia gas to the exhaust pipe 3 via the flow control valve 8a, 9 is a second control device for controlling the flow control valve 8a, and 10 is the exhaust pipe 3 on the upstream side of the supercharger 5. Is connected in parallel to a bypass pipe 3a forming a part of the exhaust gas, and a reducing device for reducing nitrogen oxides (NOx) from the exhaust gas containing ammonia by a catalyst filled therein, 11 is a reducing device 10
And a bypass valve 3a for controlling the flow rate ratio of the exhaust gas that is branched.

上記加湿器7内のコンピュータからなる第1制御装置
は、後述する初期関数値算出手段,運転時関数値算出手
段,基準絶対湿度算出手段,加湿量算出手段を有して、
図示しない絶対湿度センサが検出したあるいは予め気象
データとして与えられた大気の絶対湿度Xおよびラック
目盛センサ4が検出した機関出力Lに基づいて、排気中
の窒素酸化物濃度を、第3図に示す季節変動最小値Cmin
以下の一定レベルであるNOx第1規制値C1 *にするために
給気に加えるべき加湿量Yを算出し、この加湿量Yを表
わす信号を流量制御弁7aに出力するようになっている。
加湿量Yの算出手順を次に述べる。
The first controller composed of a computer in the humidifier 7 has an initial function value calculation means, an operation time function value calculation means, a reference absolute humidity calculation means, and a humidification amount calculation means, which will be described later.
FIG. 3 shows the nitrogen oxide concentration in the exhaust gas based on the absolute humidity X of the atmosphere detected by an absolute humidity sensor (not shown) or given in advance as meteorological data and the engine output L detected by the rack scale sensor 4. Minimum seasonal fluctuation Cmin
The humidification amount Y to be added to the supply air to calculate the NOx first regulation value C 1 * , which is a constant level below, is calculated, and a signal representing this humidification amount Y is output to the flow control valve 7a. .
The calculation procedure of the humidification amount Y will be described below.

即ち、上記コンピュータは、下記の関数で定義される排
気中のNOx濃度を支配する値Kを算出するプログラムを
有する。
That is, the computer has a program for calculating the value K that governs the NOx concentration in the exhaust gas, which is defined by the following function.

K=K(X,Tb,γ,y)…(1) 但し、X:給気の絶対湿度 Tb:機関の標準運転条件で一意的に決まる給気温度 γ:使用燃料の比重あるいは着火性を示す指標 y:燃料中の窒素含有量を表わす変数 そして、コンピュータは、初期関数値算出手段として、
機関出荷調整時の上記各変数X0,Tb0,γ,y0を(1)式
に代入して初期設定値Kを算出すると共に、運転時関
数値算出手段として、このK値とNOx還元装置なしの
出荷調整時のNOx濃度の規制値C0 *との積を、運転時の目
標値たる上記NOx第1規制値C1 *で割って運転時の目標値
Ksを算出する。次に、コンピュータは、基準絶対湿度算
出手段として、運転に先立って入力される条件値Tb,
γ,yを(1)式に代入してK(X,Tb,γ,y)が上
記目標値Ksになるような基準絶対湿度Xを算出する。
更に、加湿量算出手段として、上記基準絶対湿度X
ら運転中に絶対湿度センサが検出した(あるいは予め気
象データとして与えられた)大気の絶対湿度Xを減算し
た後、ラック目盛センサ4が検出した機関出力Lが設定
値L(第4図参照)以下か否かを判断し、L≧L
判断したとき、上記減算結果(X−X)及び機関出力
Lと比例関係にある上記加湿量Yを(Y=f(L,X))を算
出して、算出した加湿量Yを表わす信号を流量制御弁7
aに出力するのである。
K = K (X, Tb, γ, y) (1) where X: absolute humidity of supply air Tb: supply air temperature uniquely determined by standard operating conditions of engine γ: specific gravity or ignitability of fuel used Indicating y: variable indicating the nitrogen content in the fuel The computer, as an initial function value calculating means,
The above variables X 0 , Tb 0 , γ 0 , y 0 at the time of engine shipment adjustment are substituted into the equation (1) to calculate the initial setting value K 0 , and this K 0 value is used as the operation time function value calculating means. The target value during operation is divided by the product of the NOx concentration regulation value C 0 * at the time of shipment adjustment without the NOx reduction device and the above-mentioned NOx first regulation value C 1 * which is the operation target value.
Calculate Ks. Next, the computer serves as a reference absolute humidity calculating means, the condition value Tb, which is input prior to the operation,
By substituting γ, y into the equation (1), the reference absolute humidity X * is calculated so that K (X, Tb, γ, y) becomes the target value Ks.
Further, as a humidification amount calculating means, after subtracting the absolute humidity X of the atmosphere detected by the absolute humidity sensor during operation (or given in advance as meteorological data) from the reference absolute humidity X * , the rack scale sensor 4 detects it. When the engine output L is equal to or less than the set value L 0 (see FIG. 4), and when L ≧ L 0 , it is proportional to the subtraction result (X * −X) and the engine output L. The humidification amount Y is calculated as (Y = f (L, X)), and a signal representing the calculated humidification amount Y is output.
It is output to a.

こうして、算出された加湿量Yは、第4図の直線Aで示
す冬期の最大値から直線Bで示す夏期の最小値の間の機
関出力Lに比例する一定勾配の直線として得られ、機関
出力LがL以上になると加湿が開始される。そして、
給気管2内の給気に上記加湿量Yの水蒸気等が加えられ
ると排気中のNOx濃度は、第3図の季節的変動を示す曲
線Cから目標値たる一定レベルであるNOx第1規制値C1 *
まで減少することになる。
In this way, the calculated humidification amount Y is obtained as a straight line having a constant slope proportional to the engine output L between the maximum value in winter indicated by the straight line A in FIG. 4 and the minimum value in the summer indicated by the straight line B. Humidification is started when L becomes L 0 or more. And
When the humidification amount Y of water vapor or the like is added to the air supply pipe 2, the NOx concentration in the exhaust gas is a constant level, which is a target value from the curve C showing the seasonal variation in FIG. C 1 *
Will be reduced to.

一方、アンモニアガス量を制御する第2制御装置9は、
ラック目盛センサ4が検出した機関出力Lに基づいて、
排気中のNOx濃度を上記NOx第1規制値C1 *以下のNOx第2
規制値C2 *にするため排気に加えるべきアンモニア量Z
(Z=g(Y,L))を算出し、このアンモニア量Zを表わす
信号を流量制御弁8aに出力するようになっている。上記
アンモニア量Zは、機関出力Lの増加と共に僅かに増加
するものの、季節的変動のない一定値であり、排気管3
内の排気にこの量Zのアンモニアが加えられて還元装置
10を通過すると、排気中のNOx濃度は、第3図の直線C
1 *からさらに一定許容レベルC2 *まで減少することにな
る。
On the other hand, the second controller 9 that controls the amount of ammonia gas is
Based on the engine output L detected by the rack scale sensor 4,
The NOx concentration in the exhaust gas is the NOx second regulation value below the NOx first regulation value C 1 * .
Ammonia amount Z to be added to the exhaust gas to reach the regulation value C 2 *
(Z = g (Y, L)) is calculated and a signal representing this ammonia amount Z is output to the flow rate control valve 8a. Although the ammonia amount Z slightly increases as the engine output L increases, it is a constant value without seasonal fluctuations, and the exhaust pipe 3
When this amount Z of ammonia is added to the exhaust gas inside and passes through the reduction device 10, the NOx concentration in the exhaust gas is the straight line C in FIG.
It will be further reduced from 1 * to a certain allowable level C 2 * .

第2図は、上記実施例におけるNOx低減技術の複合化の
基本概念を示している。排気中のNOx濃度と燃料消費率b
eの関係は、図中の曲線Dで示すように噴射時期が矢印
E方向に遅延する程、即ちbeが増加する程減少する。そ
こで、燃料消費率beが悪化しない適当に低いNOx濃度の
点Pを選び、燃焼マッチングや高圧縮比の採用で機関
の燃焼改善を行なってbeを点Pまで向上させる。次
に、加湿器7で給気を上述の如く加湿することによりNO
x濃度を一定レベルの点C1 *まで低減し、さらに制御装置
9で排気にアンモニアを供給し、還元装置10で選択還
元アンモニア脱硝を行なうことによりNOx濃度を一定許
容レベルの点C2 *まで低減して、厳しいNOx排出基準値を
達成せんとするのである。
FIG. 2 shows the basic concept of compounding NOx reduction technology in the above embodiment. NOx concentration in exhaust gas and fuel consumption rate b
The relationship of e decreases as the injection timing is delayed in the direction of arrow E, that is, as be increases, as indicated by the curve D in the figure. Therefore, a point P 1 with an appropriately low NOx concentration that does not deteriorate the fuel consumption rate be is selected, and combustion is improved in the engine by adopting combustion matching or a high compression ratio to increase be to the point P 2 . Next, the humidifier 7 humidifies the supply air as described above to obtain NO.
The NOx concentration is reduced to a certain allowable level point C 2 * by reducing the x concentration to a certain level point C 1 * , further supplying ammonia to the exhaust by the control device 9, and performing selective reduction ammonia denitration by the reducing device 10. We will try to reduce it and achieve the strict NOx emission standard value.

上記構成のディーゼル機関の脱硝動作について、第5図
のフローチャートを参照しつつ次に述べる。
The denitration operation of the diesel engine having the above configuration will be described below with reference to the flowchart of FIG.

ステップS1において、ラック目盛センサ4により検出
されたエンジン本体1の機関出力信号Lが、加湿器7内
の第1制御装置たるコンピュータと第2制御装置9に入
力されるとともに、絶対湿度センサまたは気象データに
よるその時期(季節)の大気の絶対湿度信号Xが、上記
コンピュータに入力される。上記コンピュータは、ステ
ップS2で機関出力信号Lと絶対湿度信号Xに基づい
て、排気中のNOx濃度を季節変動最小値Cmin以下のNOx第
1規制値C1 *(第3図参照)にするために給気に加える
べき加湿量Yを算出し、機関出力がLを超えたとき算
出した加湿量Yになるように流量制御弁7aを制御して、
給気管2内の給気を加湿する。次に、第2制御装置9
は、ステップS3で機関出力信号Lに基づいて、排気中
のNOx濃度をNOx第2規制値C2 *(第3図参照)にするた
めに排気に加えるべきNH量Zを算出し、機関出力が
を超えたとき、算出したNH量Zになるように流
量制御弁8aを制御して、排気管3内の排気にNHを供
給する。還元装置10を通過することにより、排気ガス
中のNOxは供給されたNH量に応じてNに還元さ
れ、ステップS2の加湿により一定レベルC1 *まで低減
している排気中のNOx濃度は、さらに一定許容レベルC2 *
まで低減せしめられる。こうして、過給機5のタービン
5bを経て大気に排出される排気ガス中のNOx濃度は、厳
しいNOx排出基準値C2 *に適合することになる。
In step S1, the engine output signal L of the engine body 1 detected by the rack scale sensor 4 is input to the computer and the second control device 9 which are the first control device in the humidifier 7, and the absolute humidity sensor or the weather condition is measured. The absolute humidity signal X of the atmosphere at that time (season) based on the data is input to the computer. The computer is based on the engine output signal L and the absolute humidity signal X at step S2, to the NOx concentration in the exhaust gas to the seasonal variation minimum value Cmin following NOx first regulating value C 1 * (see FIG. 3) The humidification amount Y to be added to the intake air is calculated, and the flow control valve 7a is controlled so that the humidification amount Y calculated when the engine output exceeds L 0 is obtained.
The supply air in the supply pipe 2 is humidified. Next, the second control device 9
Calculates the NH 3 amount Z to be added to the exhaust in order to set the NOx concentration in the exhaust to the NOx second regulation value C 2 * (see FIG. 3) based on the engine output signal L in step S3. When the output exceeds L 0 , the flow rate control valve 8a is controlled so that the calculated NH 3 amount Z is obtained, and NH 3 is supplied to the exhaust gas in the exhaust pipe 3. By passing through the reduction device 10, NOx in the exhaust gas is reduced to N 2 according to the supplied NH 3 amount, and the NOx concentration in the exhaust gas is reduced to a certain level C 1 * by the humidification in step S2. Is a more constant tolerance level C 2 *
Can be reduced to Thus, the turbine of the supercharger 5
The NOx concentration in the exhaust gas discharged to the atmosphere via 5b will meet the strict NOx emission standard value C 2 * .

本発明では、加湿器7によりNOx濃度を季節変動最小値C
min以下の一定レベルC1 *まで低減しているので、還元装
置10を小型化して過給機5の上流側に設けることがで
きるうえ、NH注入量を年間に亘って一定にして注入
量制御を簡素化でき、しかも厳しい排出基準への規制を
正確かつ容易に行なえるという利点がある。また、上記
実施例では、還元装置10を過給機5の上流側に設けて
いるので、高温の排気ガスにより機関の中低負荷時には
予熱装置がなくとも触媒反応の活性化が図れて、脱硝効
率が大幅に向上し、運転負荷範囲を拡大することができ
る。なお、機関が低負荷で排気中のNOx濃度が低い場合
や媒の多い場合は、流量制御弁8aを止めてNHの注入
を停止し、分流弁11を調整して排気ガスをバイパス管
3aに導くことにより、還元装置10内の触媒の耐用年数
を延ばすことができる。
In the present invention, the humidifier 7 is used to reduce the NOx concentration to the minimum seasonal fluctuation value C.
Since it is reduced to a constant level C 1 * of min or less, the reducing device 10 can be miniaturized and installed upstream of the supercharger 5, and the NH 3 injection amount can be made constant over the year. There is an advantage that the control can be simplified and the regulation to the strict emission standard can be performed accurately and easily. Further, in the above-described embodiment, since the reducing device 10 is provided on the upstream side of the supercharger 5, the catalyst reaction can be activated by the high temperature exhaust gas even when there is no preheating device at the time of medium and low load of the engine, and the denitration can be performed. The efficiency is greatly improved and the operating load range can be expanded. When the engine has a low load and the NOx concentration in the exhaust is low or there is a large amount of medium, the flow control valve 8a is stopped to stop the injection of NH 3 , and the shunt valve 11 is adjusted to exhaust gas bypass pipe.
By leading to 3a, the useful life of the catalyst in the reduction device 10 can be extended.

第6図は、本発明のディーゼル機関の他の実施例を示し
ている。この実施例は、第1の実施例の還元装置10を
過給機5の下流側に移し、還元装置10にボンベ8から
流量制御弁8aを経て直接NHを注入するとともに、加
湿器7からの加湿量Yを表わす信号を受ける制御装置9
で上記流量制御弁8aを制御するようにした点を除いて、
第1図の実施例と同じであり、同じ部材には同一番号を
付している。
FIG. 6 shows another embodiment of the diesel engine of the present invention. In this embodiment, the reducing device 10 of the first embodiment is moved to the downstream side of the supercharger 5, NH 3 is directly injected into the reducing device 10 from the cylinder 8 through the flow rate control valve 8a, and the humidifier 7 is also used. Control device 9 for receiving a signal indicating the humidification amount Y of
Except that the flow control valve 8a is controlled by
This is the same as the embodiment of FIG. 1, and the same members are given the same numbers.

この実施例は、加湿器7をNOx低減の主たる手段として
用いて、これによりNOx濃度を第3図のレベルC1 *以下の
一定レベルにまで下げ、第1図に比べて下流側ゆえ脱硝
効率の劣る還元装置10を補助手段として用いて、第3
図の一定許容レベルC2 *を達成するもので、各部材の動
作は前述の実施例と基本的には同じである。従って、還
元装置10の脱硝効率の大幅向上はないが、その分過給
機5の効率が向上するとともに、前述と同様、還元装置
10の小型化とNH注入量制御の簡素化と正確化が図
れ、加湿器7と還元装置10による脱硝負荷の分担で運
転負荷範囲を拡大することができる。
In this embodiment, the humidifier 7 is used as a main means for reducing NOx, whereby the NOx concentration is lowered to a certain level below the level C 1 * in FIG. 3, and the denitration efficiency is lower than that in FIG. 1 because of the downstream side. Using the inferior reducing device 10 as an auxiliary means,
In order to achieve the constant allowable level C 2 * in the figure, the operation of each member is basically the same as that of the above-described embodiment. Therefore, although the denitrification efficiency of the reduction device 10 is not significantly improved, the efficiency of the supercharger 5 is improved by that amount, and the reduction device 10 is downsized and the NH 3 injection amount control is simplified and accurate, as described above. Therefore, the operating load range can be expanded by sharing the denitration load by the humidifier 7 and the reducing device 10.

なお、本発明が実施例に限られないのはいうまでもな
い。
Needless to say, the present invention is not limited to the embodiments.

〈発明の効果〉 以上の説明で明らかなように、本発明のディーゼル機関
は、設置環境の絶対湿度の季節変化に伴って乾湿する大
気を吸入する給気管系に、給気を加湿する加湿器を設け
る一方、排気管系に排気中の窒素酸化物をアンモニアと
触媒により還元する還元装置を設けるとともに、給気の
絶対湿度と,機関の運転条件で一義的に定まる給気温度
と,使用燃料の比重および窒素含有量の関数で定義され
るNOx濃度の支配式に出荷調整時における上記諸変数値
を代入して関数値を求める初期関数値算出手段と、求め
られた関数値を出荷調整時のNOx規制値で乗じ,かつ運
転時のNOx第1規制値で除して運転時の関数値を求める
運転時関数値算出手段と、上記支配式に運転時の給気温
度と使用燃料の比重および窒素含有量を代入してその関
数値が上記運転時の関数値になり、かつ排気中の窒素酸
化物濃度を上記NOx第1規制値にせしめるような給気の
絶対湿度を算出する基準絶対湿度算出手段と、算出され
た基準絶対湿度と実測または気象データとして与えられ
た運転時の大気の絶対湿度との差およびディーゼル機関
の出力に比例した加湿量を算出し、算出した加湿量を表
わす信号を上記加湿器に出力する加湿量算出手段とを有
する第1制御装置と、排気中の窒素酸化物濃度を上記NO
x第1規制値以下のNOx第2規制値にするため排気に加え
るべきアンモニア量をディーゼル機関の出力や上記加湿
量に基づいて算出し、このアンモニア量を表わす信号を
上記還元装置に出力する第2説明装置を備えているの
で、加湿器で排気ガス中の窒素酸化物濃度の季節変動を
なくして一定の低レベルにし、これにより還元装置の小
型化と簡素かつ正確な脱硝制御を実現し、運転負荷範囲
を拡大することができ、将来の厳しい窒素酸化物排出基
準への適合が可能になる。
<Effects of the Invention> As is clear from the above description, the diesel engine of the present invention is a humidifier that humidifies the supply air to the air supply pipe system that inhales the atmosphere that dries and humidifies with the seasonal changes in the absolute humidity of the installation environment. On the other hand, the exhaust pipe system is provided with a reducing device for reducing the nitrogen oxides in the exhaust gas with ammonia and a catalyst, and the absolute humidity of the supply air, the supply air temperature uniquely determined by the operating conditions of the engine, and the fuel used. The initial function value calculating means for calculating the function value by substituting the above-mentioned various variable values at the time of shipping adjustment into the governing equation of the NOx concentration defined by the function of the specific gravity and the nitrogen content, and the calculated function value at the time of shipping adjustment. NOx regulation value of, and operating time function value calculating means for obtaining the function value at the time of operation by dividing by the NOx first regulation value at the time of operation, and the specific gravity of the supply air temperature at the time of operation and the fuel used in the above governing equation. And the nitrogen content is substituted and the function value is The reference absolute humidity calculating means for calculating the absolute humidity of the supply air that becomes the function value at the time of operation and that makes the concentration of nitrogen oxides in the exhaust the NOx first regulation value, and the calculated reference absolute humidity. A humidification amount calculation means for calculating a humidification amount proportional to the difference between the absolute humidity of the atmosphere during operation given as actual measurement or meteorological data and the output of the diesel engine, and outputting a signal representing the calculated humidification amount to the humidifier. And a NOx concentration in the exhaust gas above the NO.
x NOx that is less than or equal to the first regulation value Calculates the amount of ammonia to be added to the exhaust gas based on the output of the diesel engine and the humidification amount, and outputs a signal representing this ammonia amount to the reduction device. 2 Since it is equipped with an explanation device, the humidifier eliminates seasonal fluctuations in the nitrogen oxide concentration in the exhaust gas to a certain low level, thereby realizing downsizing of the reduction device and simple and accurate denitration control. The operating load range can be expanded, and it becomes possible to meet the severe nitrogen oxide emission standards in the future.

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

第1図は本発明のディーゼル機関の一実施例を示す概略
図、第2図は上記実施例におけるNOx低減技術の複合化
の基本概念を示す図、第3図は排気ガス中のNOx濃度の
季節変化を示す図、第4図は機関出力と加湿量の関係を
示す図、第5図は上記実施例の脱硝動作を示すフローチ
ャート、第6図は本発明の他の実施例を示す概略図、第
7図は従来の脱硝装置へのNH注入量の季節変動を示
す図である。 1…エンジン本体、2…給気管、3…排気管、4…ラッ
ク目盛センサ、5…過給機、7…加湿器、7a,8a…流量
制御弁、8…タンク、 9…制御装置、10…還元装置。
FIG. 1 is a schematic diagram showing an embodiment of the diesel engine of the present invention, FIG. 2 is a diagram showing the basic concept of compounding NOx reduction technology in the above embodiment, and FIG. 3 is a graph showing NOx concentration in exhaust gas. FIG. 4 is a diagram showing a seasonal change, FIG. 4 is a diagram showing a relationship between an engine output and a humidification amount, FIG. 5 is a flow chart showing a denitration operation of the above embodiment, and FIG. 6 is a schematic diagram showing another embodiment of the present invention. FIG. 7 is a diagram showing seasonal variation of the NH 3 injection amount into the conventional denitration device. 1 ... Engine main body, 2 ... Air supply pipe, 3 ... Exhaust pipe, 4 ... Rack scale sensor, 5 ... Supercharger, 7 ... Humidifier, 7a, 8a ... Flow control valve, 8 ... Tank, 9 ... Control device, 10 ... return device.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】設置環境における大気の絶対湿度の季節変
化による給気の乾湿に伴って増減する排気中の窒素酸化
物濃度を一定の低レベルまで減少できるディーゼル機関
において、 上記ディーゼル機関の給気配管系に設けられ、吸い込ま
れた大気に所定量の水分を加えて加湿する加湿器と、 上記ディーゼル機関の排気配管系に設けられ、排気中の
窒素酸化物をアンモニアと触媒により還元する還元装置
と、 給気の絶対湿度と,機関の運転条件で一義的に定まる給
気温度と,使用燃料の比重および窒素含有量の関数で定
義されるNOx濃度の支配式に出荷調整時における上記諸
変数値を代入して関数値を求める初期関数値算出手段
と、求められた関数値を出荷調整時のNOx規制値で乗
じ,かつ運転時のNOx第1規制値で除して運転時の関数
値を求める運転時関数値算出手段と、上記支配式に運転
時の給気温度と使用燃料の比重および窒素含有量を代入
してその関数値が上記運転時の関数値になり、かつ排気
中の窒素酸化物濃度を上記NOx第1規制値にせしめるよ
うな給気の絶対湿度を算出する基準絶対湿度算出手段
と、算出された基準絶対湿度と実測または気象データと
して与えられた運転時の大気の絶対湿度との差およびデ
ィーゼル機関の出力に比例した加湿量を算出し、算出し
た加湿量を表わす信号を上記加湿器に出力する加湿量算
出手段とを有する第1制御装置と、 排気中の窒素酸化物濃度を上記NOx第1規制値以下のNOx
第2規制値にするため排気に加えるべきアンモニア量を
ディーゼル機関の出力や上記加湿量に基づいて算出し、
このアンモニア量を表わす信号を上記還元装置に出力す
る第2制御装置を備えたことを特徴とするディーゼル機
関。
1. A diesel engine capable of reducing the concentration of nitrogen oxides in the exhaust gas, which increases and decreases with the dryness of the supply air due to seasonal changes in the absolute humidity of the installation environment, to a certain low level. A humidifier installed in the piping system to add a predetermined amount of moisture to the sucked air to humidify it, and a reducing device installed in the exhaust piping system of the diesel engine to reduce nitrogen oxides in the exhaust with ammonia and a catalyst. , The absolute humidity of the supply air, the supply air temperature that is uniquely determined by the operating conditions of the engine, the specific gravity of the fuel used, and the NOx concentration defined by the functions of the nitrogen content. An initial function value calculating means for substituting a value to obtain a function value, and the calculated function value is multiplied by the NOx regulation value at the time of shipment adjustment, and divided by the NOx first regulation value at the time of operation, and the function value at the time of operation Seeking luck Substituting the operating temperature supply air temperature, the specific gravity of the fuel used and the nitrogen content into the above governing equation, the function value becomes the above operating function value, and the nitrogen oxides in the exhaust gas Reference absolute humidity calculating means for calculating the absolute humidity of the supply air so that the concentration becomes the NOx first regulation value, and the calculated reference absolute humidity and the absolute humidity of the atmosphere at the time of operation given as actual measurement or meteorological data. Difference and a humidification amount proportional to the output of the diesel engine, and a first controller having a humidification amount calculation means for outputting a signal representing the calculated humidification amount to the humidifier, and a nitrogen oxide concentration in the exhaust gas. NOx below the above NOx first regulation value
Calculate the amount of ammonia to be added to the exhaust gas to reach the second regulation value based on the output of the diesel engine and the humidification amount,
A diesel engine comprising a second control device for outputting a signal representing the amount of ammonia to the reduction device.
JP2061898A 1990-03-13 1990-03-13 Diesel engine Expired - Fee Related JPH0658058B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2061898A JPH0658058B2 (en) 1990-03-13 1990-03-13 Diesel engine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2061898A JPH0658058B2 (en) 1990-03-13 1990-03-13 Diesel engine

Publications (2)

Publication Number Publication Date
JPH03264732A JPH03264732A (en) 1991-11-26
JPH0658058B2 true JPH0658058B2 (en) 1994-08-03

Family

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JP (1) JPH0658058B2 (en)

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FI112526B (en) * 1999-07-21 2003-12-15 Waertsilae Finland Oy Procedure for reducing nitric oxide emissions (NOx) from a turbocharged four-stroke piston engine
DE19938292A1 (en) * 1999-08-12 2001-02-15 Munters Euroform Gmbh Carl Device for humidifying the intake air of internal combustion engines with a turbocharger
DE10053904C2 (en) * 2000-10-31 2003-05-22 Emitec Emissionstechnologie Small volume NO¶x¶ adsorber
FI112692B (en) * 2000-11-03 2003-12-31 Waertsilae Finland Oy Method and arrangement for reducing nitrogen oxide (NOx) emissions from supercharged piston engines
JP2003343272A (en) * 2002-05-21 2003-12-03 Man B & W Diesel As Large internal combustion engine with supercharger
DE102009046120A1 (en) * 2009-10-28 2011-05-12 Ford Global Technologies, LLC, Dearborn Method for humidifying intake air of combustion engine, particularly diesel engine, involves determining humidity of intake air, where liquid is injected into intake air depending on humidity of intake air
JP5709100B2 (en) * 2010-08-11 2015-04-30 独立行政法人海上技術安全研究所 Denitration device for internal combustion engine and ship
JP5878860B2 (en) * 2011-12-08 2016-03-08 エムエーエヌ・ディーゼル・アンド・ターボ・フィリアル・アフ・エムエーエヌ・ディーゼル・アンド・ターボ・エスイー・ティスクランド Turbocharged large two-stroke diesel engine with exhaust gas purification function
CN103953470B (en) * 2014-03-21 2016-06-29 哈尔滨工程大学 A kind of supercharged diesel engine air intake duct humidifying device
CN106194507B (en) * 2016-07-08 2018-06-12 哈尔滨工程大学 Supercharged diesel engine emulsifying combustion is realized based on jet pump and reduces NOXThe device of discharge
CN115450772B (en) * 2022-09-27 2023-10-10 东风商用车有限公司 Strategy for controlling engine NOx emissions

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58117344A (en) * 1981-12-28 1983-07-12 Mazda Motor Corp Controller for humidity of suction for engine
JPS6344924A (en) * 1986-08-11 1988-02-25 Takuma Co Ltd Denitration treatment of exhaust gas

Also Published As

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