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JP3600522B2 - Reducing agent supply device for internal combustion engine - Google Patents
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JP3600522B2 - Reducing agent supply device for internal combustion engine - Google Patents

Reducing agent supply device for internal combustion engine Download PDF

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Publication number
JP3600522B2
JP3600522B2 JP2000353057A JP2000353057A JP3600522B2 JP 3600522 B2 JP3600522 B2 JP 3600522B2 JP 2000353057 A JP2000353057 A JP 2000353057A JP 2000353057 A JP2000353057 A JP 2000353057A JP 3600522 B2 JP3600522 B2 JP 3600522B2
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Prior art keywords
reducing agent
pressure
agent storage
reducing
internal combustion
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JP2002155732A (en
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和浩 伊藤
重樹 大道
尚久 大山
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Toyota Motor Corp
Soken Inc
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Nippon Soken Inc
Toyota Motor Corp
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Priority to JP2000353057A priority Critical patent/JP3600522B2/en
Priority to FR0114945A priority patent/FR2816986B1/en
Priority to DE10156714A priority patent/DE10156714B4/en
Publication of JP2002155732A publication Critical patent/JP2002155732A/en
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Publication of JP3600522B2 publication Critical patent/JP3600522B2/en
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    • 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
    • F01N9/00Electrical control of exhaust gas treating apparatus
    • 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
    • F01N3/206Adding periodically or continuously substances to exhaust gases for promoting purification, e.g. catalytic material in liquid form, NOx reducing agents
    • 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
    • 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
    • F01N2560/00Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
    • F01N2560/02Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor
    • F01N2560/026Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being an exhaust gas sensor for measuring or detecting NOx
    • 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
    • F01N2560/00Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
    • F01N2560/06Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being a temperature sensor
    • 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
    • F01N2560/00Exhaust systems with means for detecting or measuring exhaust gas components or characteristics
    • F01N2560/08Exhaust systems with means for detecting or measuring exhaust gas components or characteristics the means being a pressure sensor
    • 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
    • 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
    • F01N2610/06Adding substances to exhaust gases the substance being in the gaseous form
    • 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
    • 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
    • F01N2610/1453Sprayers or atomisers; Arrangement thereof in the exhaust apparatus
    • 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
    • F01N2610/1453Sprayers or atomisers; Arrangement thereof in the exhaust apparatus
    • F01N2610/146Control thereof, e.g. control of injectors or injection valves
    • 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
    • F01N2900/00Details of electrical control or of the monitoring of the exhaust gas treating apparatus
    • F01N2900/06Parameters used for exhaust control or diagnosing
    • F01N2900/18Parameters used for exhaust control or diagnosing said parameters being related to the system for adding a substance into the exhaust
    • F01N2900/1806Properties of reducing agent or dosing system
    • F01N2900/1808Pressure
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A50/00TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
    • Y02A50/20Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
    • 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
    • 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
    • Y02T10/40Engine management systems

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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)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

【0001】
【発明の属する技術分野】
本発明は、内燃機関の還元剤供給装置に関し、より詳細には、内燃機関より排出される窒素酸化物(NOx )を浄化するNOx 触媒に、還元剤を供給する還元剤供給装置に関する。
【0002】
【従来の技術】
内燃機関の排気系に設けられ該内燃機関より排出される窒素酸化物(以下、単にNOx と称す )を浄化するNOx 触媒に、還元剤を供給する還元剤供給装置として、例えば、特開平5−272331号公報に開示される還元剤供給装置を例示できる。
【0003】
この特開平5−272331号公報に開示される還元剤供給装置では、低温においても高い浄化率でNOx を還元し得る尿素CO(NHを還元剤に採用し、該尿素をNOx 触媒に供給して排気中に含まれるNOx の浄化を促している。
【0004】
より詳しくは、エンジンコントロール用電子制御ユニット(以下、単にECUと称す)からの還元剤供給命令を受けて、収容タンクに収容された固体状の尿素を炉筒内にて加熱ガス化させた後、該ガス化された尿素を機関排気通路におけるNOx 触媒上流側に供給してNOx の浄化を促している。
【0005】
ところで、固体状の還元剤は、気体状の還元剤および液体状の還元剤に比べて体積が小さく車両搭載性に優れるものの、そのままの状態では粒子が大きくNOx 触媒に供給できない。そこで、上記した還元剤供給装置のように固体状の還元剤を炉筒内にて加熱ガス化して、NOx 触媒に供給できる状態(変態)にする必要がある。
【0006】
【発明が解決しようとする課題】
しかしながら、従来の還元剤供給装置では、ECUからの還元剤供給命令を受けた後、還元剤をガス化してNOx 触媒に供給するため、還元剤供給命令に遅れて還元剤の供給がなされることもあった。
【0007】
とりわけ、固体状尿素を主成分とする還元剤は、ガス化に時間がかかるばかりか、適宜のタイミングを外してNOx 触媒に供給されると、NOx と反応せずに大気に放出され異臭を放つ虞もある。このため還元剤供給命令に対して即座に対応できる還元剤供給装置の開発が急がれている。
【0008】
また、要求される還元剤の供給量が、炉筒内にて生成される還元ガス(還元剤)の生成量を凌ぐ場合には還元ガスの供給が追いつかず、適量の還元剤をNOx 触媒に供給できなかった。従って、NOx 触媒におけるNOx の浄化率が大幅に低下することになり排気エミッションの低下を招く虞もある。
【0009】
また、従来の還元剤供給装置では、炉筒内にて生成された還元ガスを直に排気通路に供給するため還元剤の供給圧力が安定せず、要求された供給量に見合う適量の還元剤をNOx 触媒に供給できなかった。
【0010】
よって本発明は、還元剤の供給命令に対して、遅延することなく即座に所定量の還元剤を供給し得る内燃機関の還元剤供給装置を提供することを課題とする。
【0011】
【課題を解決するための手段】
上記した技術的課題を解決するため、本発明では、以下の手段を採用した。すなわち、
内燃機関の排気系に設けられ該内燃機関より排出される窒素酸化物を浄化するNOx 触媒に、還元剤を供給する還元剤供給装置であって、
固体状の還元剤を貯蔵する主還元剤貯蔵手段と、
前記主還元剤貯蔵手段に貯蔵された固体状の還元剤をガス化することにより該還元剤を流動化させる還元剤流動化手段と、
前記還元剤流動化手段によって流動化された還元剤を一時期貯蔵する副還元剤貯蔵手段と、
機関本体の運転状態に基づき前記NOx 触媒に供給する還元剤の供給量を算出する還元剤供給量算出手段と、
前記副還元剤貯蔵手段に貯蔵される還元剤を、前記還元剤供給量算出手によって算出された供給量に基づき前記内燃機関の排気系におけるNOx 触媒上流に添加する還元剤添加手段と、
を有し、
前記副還元剤貯蔵手段は、該副還元剤貯蔵手段に貯蔵されている還元剤の残量を算出する残量算出手段と、前記流動化された還元剤を一時期貯蔵する副還元剤貯蔵室と、この副還元剤貯蔵室内の圧力を検知する圧力検知手段と、を備え、
前記還元剤流動化手段は、前記残量算出手段によって算出される残量が所定値未満になったことを受けて、前記主還元剤貯蔵手段に貯蔵される固体状の還元剤を流動化して前記副還元剤貯蔵手段に補給し、
前記残量算出手段は、前記圧力検知手段によって検知される圧力が高いとき、還元剤の残量を多いと判断し、前記圧力検知手段によって検知される圧力が低いとき、還元剤の残量を少ないと判断することを特徴とする。
【0012】
このような手段を採用する本発明によれば、還元剤流動化手段によって添加可能に流動性を持たされた還元剤を、副還元剤貯蔵手段に予め準備、貯蔵しているため、還元剤の供給命令に対して即座に還元剤を供給できる。また、副還元剤貯蔵タンク40内に還元ガスを常時貯蔵しているため、大量の還元剤を要する場合においても安定した還元剤の供給を行える。尚、還元剤の流動化とは、還元剤添加手段による還元剤の添加時に、該添加された還元剤の拡散を容易にするための行為である。すなわち、本発明で流動化とは、ガス化、液化、ゲル化、粉体化などの行為を総称して流動化と称している。
【0013】
なお、還元剤流動化手段は、固体状の還元剤をガス化して該還元剤に流動性を持たせる。すなわち、固体状の還元剤をガス化して、還元剤添加手段による添加時に、該添加された還元剤の拡散を良好にしている。
【0014】
また、前記副還元剤貯蔵手段は、該副還元剤貯蔵手段に貯蔵されている還元剤の残量を算出する残量算出手段を備え、前記還元剤流動化手段は、前記残量算出手段によって算出される残量が所定値未満になったことを受けて、前記主還元剤貯蔵手段に貯蔵される固体状の還元剤を流動化して副還元剤貯蔵手段に補給する。
【0015】
すなわち、この手段では、副還元剤貯蔵手段に貯蔵される還元剤の残量が少なくなったとき、固体状の還元剤を新たに流動化させて副還元剤貯蔵手段に補給している。よって、固体状の還元剤を不必要に流動化させることなく、常に、副還元剤貯蔵手段に還元剤を確保できる。なお、固体状の還元剤は、通常、ガス化、液化などに伴い体積が増加する。従って、固体状の還元剤を不必要に流動化させると、その分、装置内における還元剤の貯蔵手段の容量を増やす必要があり、装置の大型化につながる。このため上記したように必要量のみを流動化させることによって、装置の大型化を最小限にとどめることができる。尚、所定値とは、ゼロを除く数値であり、経験則などに基づき任意に設定可能な値である。
【0016】
また、前記副還元剤貯蔵手段は、前記流動化された還元剤を一時期貯蔵する副還元剤貯蔵室と、この副還元剤貯蔵室内の圧力を検知する圧力検知手段と、を備え、前記残量算出手段は、前記圧力検知手段によって検知される圧力が高いとき、還元剤の残量を多いと判断し、前記圧力検知手段によって検知される圧力が低いとき、還元剤の残量を少ないと判断する。すなわち、副還元剤貯蔵室内の圧力変化に基づいて、副還元剤貯蔵室内に貯蔵される還元剤の残量を把握するようにしている。
【0017】
また、前記還元剤添加手段は、前記NOx 触媒上流の排気系に設けられ開弁時に前記副還元剤貯蔵室に貯蔵される還元剤を前記NOx 触媒上流に添加する還元剤添加弁と、前記圧力検知手段によって検知される圧力に基づいて前記還元剤添加弁の開弁時間を制御する添加弁制御手段と、を有する構成としてもよい。
【0018】
すなわち、この手段では、副還元剤貯蔵室内の圧力を圧力検知手段によって検知することにより、還元剤添加弁に作用する還元剤の供給圧力を把握している。そして、還元剤添加弁からNOx 触媒に供給される還元剤の供給量を常に目標値になるように制御している。したがって、副還元剤貯蔵室内の圧力が変動しても、要求された供給量に見合う還元剤をNOx 触媒に供給できる。
【0019】
なお、前記添加弁制御手段は、前記副還元剤貯蔵室内の圧力が高いとき、前記還元剤添加弁の開弁時間を短くし、前記副還元剤貯蔵内の圧力が低いとき、前記還元剤添加弁の開弁時間を長くするようにしてもよい。
【0020】
即ち、副還元剤貯蔵室内の圧力が高いときには、単位時間当たりにおける還元剤の供給量が増加するため開弁時間を短くし、逆に、副還元剤貯蔵室内の圧力が低いときには、単位時間当たりにおける還元剤の供給量が減少するため開弁時間を長くして、還元剤添加弁より添加される還元剤の供給量を目標値となるように維持している。
【0021】
また、前記NOx 触媒は、還元剤の存在下で、窒素酸化物を分解又は還元せしめる選択還元型NOx 触媒とするのが望ましい。また、固体状の還元剤は、前記還元剤流動化手段によるガス化時に、アンモニアを基調とする還元ガスを生成する還元剤とするのが望ましい。
【0022】
【発明の実施の形態】
以下、本発明の還元剤供給装置に係わる好適な実施の形態について図面を参照して説明する。なお、以下に説明する実施の形態は、本発明の還元剤供給装置を車両用ディーゼルエンジンに適用した形態である。
【0023】
<内燃機関の概要>
初めに、本発明の還元剤供給装置を説明するに先立ち、この還元剤供給装置が装備されるディーゼルエンジンについて図1を参照して説明する。
【0024】
ディーゼルエンジン1(以下、単にエンジンと称す)は、ピストン3、シリンダ4、シリンダヘッド5などにて構成される燃焼室2と、該燃焼室2に機関燃料を供給する燃料噴射弁6と、を有する。また、燃焼室2には、空気吸入量を測定するエアフローメータ7を備えた吸気管8が接続されて、燃焼室2内では、該吸気管8を経て導入された空気と、燃料噴射弁6により供給される機関燃料と、が混合されて自己着火による機関燃焼が行われている。
【0025】
一方、燃焼室2内での機関燃焼に伴い生成される排気ガスは、燃焼室2に接続され経路途中に選択還元型NOx 触媒9、および消音器(図示せず)を備える排気管10を経て大気に排気される。なお、以下の説明では、選択還元型NOx 触媒を単にNOx 触媒と称することもある。
【0026】
排気管10に設けられる選択還元型NOx 触媒9は、主として排気中の窒素酸化物(以下、単にNOxと称す )を効果的に浄化せしめる触媒であり、還元剤の存在下で、NOx を還元または分解して浄化する触媒である。
【0027】
なお、選択還元型NOx 触媒9としては、ゼオライトにCu等の遷移金属をイオン交換にて担持させてなる触媒、ゼオライト又はアルミナに貴金属を担持させてなる触媒、チタニウムにバナジウムを担持させてなる触媒、等を例示できる。
【0028】
また、排気管10におけるNOx 触媒9上流側には、NOx センサ11、入りガス圧センサ12、排気温度センサ13等が設けられ、また、NOx 触媒9下流側には、還元剤センサ14が設けられている。NOx センサ11は、排気ガス中のNOx 濃度を測定するセンサである。入りガス圧センサ12は、排気管10内の管内圧力(排圧)を測定するセンサである。また、排気温度センサ13は、NOx 触媒9に流入する排気ガスの温度を測定するセンサである。還元剤センサ14は、排気ガス中における還元剤の濃度を測定するセンサである。そして、各種センサは、後述するエンジンコントロール用電子制御ユニット15の入力ポートに接続されている。
【0029】
また、エンジン1は、エンジンコントロール用電子制御ユニット15(以下、単にECU15と称する)によって、運転状態に見合った制御がなされている。ECU15は、双方向性バスによって相互に接続されたROM(リード・オンリ・メモリ)、RAM(ランダム・アクセス・メモリ)、CPU(セントラルプロセッサユニット)、入力ポート、出力ポート、A/Dコンバータ等を有してなり、入力ポートに入力される各種センサからの出力信号に基づき、ROM上に展開された各種制御マップを参照して、例えば、燃料噴射弁5における燃料噴射制御などを行っている。また、本発明では、還元剤供給装置16の制御をも同時に行っている。
【0030】
そして、本発明では、エンジン1の機関燃焼に伴い排出される排気ガス中のNOx をNOx 触媒9にて浄化せしめるために、該NOx 触媒9に対して還元剤たるアンモニアガス(NH3 )を供給する還元剤供給装置16を設けている。
以下、本発明の主旨となる還元剤添加装置16について、図2を参照して詳細に説明する。
【0031】
<還元剤供給装置の構造>
まず初めに、還元剤供給装置16の構造について説明する。
還元剤供給装置16は、固体状の還元剤を内部に貯蔵する主還元剤貯蔵タンク20(主還元剤貯蔵手段)と、この主還元剤貯蔵タンク20に貯蔵された固体状の還元剤を加熱して還元ガスを生成する還元ガス生成部30(還元剤流動化手段)と、還元ガス生成部30によって生成された還元ガスを一時期貯蔵する副還元剤貯蔵タンク40(副還元剤貯蔵手段)と、副還元剤貯蔵タンク40に貯蔵された還元ガスをECU15からの還元剤供給命令に応じてNOx 触媒9に添加する還元剤添加弁50(還元剤添加手段)と、を有してなる。
【0032】
主還元剤貯蔵タンク20は、還元剤たる固体状のカルバミン酸アンモニウムを内部に収容するタンク本体21と、タンク本体21を取り囲むように設けられた断熱部材22と、を有してなり、後述する還元ガス生成部30に対して着脱自在に設けられている。
【0033】
なお、カルバミン酸アンモニウムは、アンモニアを基調とする還元剤の一種であり、常温で固体状をなし摂氏40度前後でガス化する特性を有している。また、従来から使用されている炭化水素(HC)や一酸化炭素(CO)などの還元剤に比べて遙かに強い還元作用を有するため、比較的低温度でもNOx を高い浄化効率で浄化できるといった利点を備えている。
【0034】
なお、主還元剤貯蔵タンク20を還元ガス生成部30に対して着脱自在に設ける理由としては、内部に貯蔵されるカルバミン酸アンモニウムを使い尽くしたとき、新規カルバミン酸アンモニウムを貯蔵した新品の主還元剤貯蔵タンク20と使用後の空の主還元剤貯蔵タンクとを容易に交換できるようにするためである。即ち、主還元剤貯蔵タンク20は、カートリッジ式になっている。
【0035】
還元ガス生成部30は、主還元剤貯蔵タンク20に連結し主還元剤貯蔵タンク20内に貯蔵される還元剤のガス化を促す加熱室31と、該加熱室31を取り囲むように設けられた外壁32と、を有する。また、加熱室31と外壁32との間には、機関冷却水の循環経路となるウォータジャケット(図示せず)に通じた空間33が形成され、機関燃焼により暖められた機関冷却水がこの空間33内に流れ込むことにより、加熱室31内の室内温度が昇温する仕組みとなっている。
【0036】
また、ウォータジャケットと還元ガス生成部30(空間33)との間には、該還元ガス生成部30に対する機関冷却水の流れ込みを規制する機関冷却水制御弁34が設けられている(図1参照)。そして、この機関冷却水制御弁34の開閉動作をECU15にて制御することにより、加熱室31内に流れ込む機関冷却水の流量を制御して加熱室31内の室内温度を任意に調節できるようにしている。
【0037】
そして、機関冷却水制御弁34を開弁して、機関燃焼により暖められた機関冷却水を還元ガス生成部30(空間33)に導くと、該加熱室31内の室内温度が昇温するため加熱室31に連通した主還元剤貯蔵タンク20内のカルバミン酸アンモニウムがガス化する。なお、以下の説明では、ガス化されたカルバミン酸アンモニウムを単に還元ガスと称することもある。
【0038】
副還元剤貯蔵タンク40は、還元剤たるガス状のカルバミン酸アンモニウムを貯蔵するタンク本体41と、該タンク本体41を取り囲むように設けられた断熱部材42と、タンク本体41内の圧力を検知する圧力センサ43(圧力検知手段)と、を有し、タンク本体41と上記した還元ガス生成部30とは、連結管60を介して互いに連結されている。したがって、還元ガス生成部30でガス化されたカルバミン酸アンモニウムは、連結管60を経て副還元剤貯蔵タンク40に流れ込み、副還元剤貯蔵タンク40に一旦貯蔵される。
【0039】
還元剤添加弁50は、NOx 触媒9上流側の排気管10に設けられ、ECU15からの還元剤供給命令を受けて、前記副還元剤貯蔵タンク40に貯蔵された還元ガスを、NOx 触媒9上流側の排気管10に添加する。
【0040】
還元剤添加弁50は、弁体51、及び弁体51を支持するガイド52などにて構成されるノズル部53と、該ノズル部53に設けられる弁体51の開閉を行うソレノイド54と、前記連結管60に接続し副還元剤貯蔵タンク40に貯蔵される還元ガスをノズル部53に導く導入通路55と、を有してなり、副還元剤貯蔵タンク40に貯蔵される還元ガスは、導入通路55を流下してノズル部53に導かれる。そして、還元ガスは、ソレノイド54による弁体51の開閉制御によって、適切量且つ適宜のタイミングにて排気管10に添加される仕組みとなっている。
【0041】
また、弁体51を開閉させるソレノイド54は、ECU15によってデューティ比制御され、開弁電圧の印可時に弁体51を開弁させて副還元剤貯蔵タンク40内の還元ガスを排気管10に添加するようにしている。なお、副還元剤貯蔵タンク40の内部圧力は、常時、排気管10内の排圧に比べて高く維持されており、還元ガスの添加時には、この圧力差を利用して還元ガスの添加をなし得るようにしている。副還元剤貯蔵タンク40の圧力調節に関しては、次の還元剤供給制御の説明において詳述する。
【0042】
<還元剤供給装置の制御>
以下、上記した還元剤供給装置に係る還元剤供給制御について説明する。
エンジン1の運転開始(機関燃焼の開始)に伴い機関冷却水の温度が摂氏40度前後に達すると、ECU15では、主還元剤貯蔵タンク20に貯蔵される還元剤のガス化を図るために、まず、機関冷却水制御弁34を開弁して還元ガス生成部30に機関冷却水を導き入れる。
【0043】
そして、機関冷却水によって加熱室31内の空間温度が、摂氏40度前後に達すると還元ガス生成部30に連通した主還元剤貯蔵タンク20内のカルバミン酸アンモニウムが一部ガス化して、連結路60を経て副還元剤貯蔵タンク40に充填される。
【0044】
また、このときECU15では、副還元剤貯蔵タンク40に充填された還元ガスの充填量を圧力センサ43の出力値を基づき把握しており、圧力センサ43にて検出される副還元剤貯蔵タンク40内の圧力が所定値に達したとき、還元ガスの充填量が規定量に達したとみなし、前記機関冷却水制御弁34を閉弁して、カルバミン酸アンモニウムのガス化を一時中断するようにしている。
【0045】
ここで所定値とは、各種予備実験により求められた値であり、例えば、副還元剤貯蔵タンク40の最大許容圧力、排気管10内の平均排圧、単位時間当たりにおける還元ガスの消費量等を考慮して任意に設定される値である。
【0046】
またなお、ECU15では、圧力センサ43にて検出される副還元剤貯蔵タンク40の圧力が、所定時間経過した後においても上昇しないときに主還元剤貯蔵タンク20内に貯蔵されているカルバミン酸アンモニウムが尽きたとして、車内に設けられるインジケータパネル18に警告ランプ19を点灯させ、運転者にその旨を伝える。
【0047】
また、ECU15では、NOx の浄化を促すべく還元剤の供給制御を行うために、機関負荷、機関回転数、NOx 濃度、触媒温度、還元ガスの充填圧力、などに基づいて還元剤の目標供給量を算出し、該算出された目標供給量に見合う還元剤を適宜のタイミングにてNOx 触媒9に添加するように還元剤添加弁50におけるソレノイド54の制御を行っている。
【0048】
還元剤添加弁50の制御について詳述すると、ECU15には、上記の如くエアフロメータ7からの出力信号、及びNOx センサ11からの出力信号が入力ポート及びA/D変換器を介して入力されている。そして、ECU15では、エアフロメータ7にて検出される空気吸入量と、NOx センサ11にて検出されるNOx 濃度から、単位時間当たりに排出されるNOx の排出量を演算して、該演算されたNOx 排出量に見合う還元剤の目標供給量を設定している(還元剤供給量算出手段)。
【0049】
また、ECU15には、副還元剤貯蔵タンク40に設けられた圧力センサ43からの出力信号、および排気管10に設けられた入りガス圧センサ12からの出力信号が入力されている。圧力センサ43は、副還元剤貯蔵タンク40の内部圧力に比例した出力電圧を出力し、入りガス圧センサ12は、排気管10内の排圧に比例した出力電圧を出力する。そして、ECU15では、これら各圧力センサ43,12からの出力値に基づいて、副還元剤貯蔵タンク40の圧力と、排気管10内の圧力(排圧)と、の間における圧力差を求めて、排気管10に対する還元ガスの供給圧力を算出している。
【0050】
また、ECU15では、この算出された還元ガスの供給圧力を考慮して、単位時間当たりにおける還元ガスの供給量が目標供給量となるように還元剤添加弁50における弁体51のデューティ比を演算し、該算出されたデューティ比に基づく還元剤添加弁50のデューティ比制御を行う(添加弁制御手段)。尚、ここでデューティ比とは、単位時間当たりにおける弁体51の開閉回数を意味している。したがって、デューティ比制御では、単位時間当たりにおける弁体51の開閉回数を増加させるほど、より多くの還元ガスが排気管10に供給されることとなる。
【0051】
すなわち、還元ガスの供給圧力が高いときには、単位時間当たりにおける還元ガスの供給量が必然的に増加するためデューティ比を小さく設定し、逆に還元ガスの供給圧力が低いときには、単位時間当たりにおける還元ガスの供給量が減少するためデューティ比を大きく設定している。
【0052】
また、ECU15には、排気温度センサ13からの出力信号が入力されている。排気温度センサ13は、排気ガスの温度に比例した出力電圧を出力し、NOx 触媒9の触媒温度の把握に用いられる。そして、ECU15では、排気温度センサ13にて把握される触媒温度が、NOx を浄化し得る活性化温度に達したことを受けて、算出された目標供給量に見合う還元剤添加弁50のデューティ制御を行い還元ガスをNOx 触媒9に添加する。
【0053】
また、ECU15には、還元剤センサ14からの出力信号が入力されている。そして、ECU15では、還元剤供給装置16の故障などにより大量の還元剤が不本意に供給された場合、その還元剤を還元剤センサ14にて感知して還元剤の供給を直ちに強制的に停止させる制御を行う。
【0054】
一方、副還元剤貯蔵タンク40に貯蔵される還元ガスは、還元剤添加弁50からの添加によって消費され、時間の経過と共にその残量は減少していく。そこでECU15では、副還元剤貯蔵タンク40に貯蔵される還元ガスを切らさないように、副還元剤貯蔵タンク40内における還元ガスの残量を常時把握して、その残量が少なくなった時には、副還元剤貯蔵タンク40に還元ガスを補給する還元ガス補給制御を行っている。
【0055】
ECU15にて還元ガスの残量を把握するには、上記した圧力センサ43の出力信号を利用して残量を把握している。すなわち、副還元剤貯蔵タンク40内の還元ガスが消費されると、副還元剤貯蔵タンク40の内部圧力も低下する。したがって、圧力センサ43の出力値を監視することにより副還元剤貯蔵タンク40内の残量を把握できる(残量検出手段)。
【0056】
そして、ECU15では、圧力センサ43にて検知される副還元剤貯蔵タンク40内の圧力(還元ガスの充填圧力)が所定値未満になったことを受けて、前記機関冷却水制御弁34を開弁して加熱室31を加熱し、主還元剤貯蔵タンク20に貯蔵されるカルバミン酸アンモニウムを新たにガス化させる。その結果、新たにガス化されたカルバミン酸アンモニウムが副還元剤貯蔵タンク40内に流れ込み副還元剤貯蔵タンク40内に還元ガスが補給されることになる。
【0057】
なお、ここで所定値とは任意に設定可能な値であるが、好ましくは、排圧に対して十分に大きい値とするのが望ましい。即ち、還元ガスの充填圧力を高くしておくことにより、排気管10に対する還元ガスの拡散が良好になる他、排圧の変化に対する単位時間当たりの供給量も安定する。
【0058】
なお、副還元剤貯蔵タンク40の内部圧力が所定値以上になった場合には、上記したように機関冷却水制御弁34を閉弁して、カルバミン酸アンモニウムのガス化を停止させる。
【0059】
このように本発明の還元剤供給装置16では、還元剤添加弁50からの添加をなし得るように固体状の還元剤をガス化して副還元剤貯蔵タンク40に予め貯蔵・準備しておき、ECU15からの還元剤添加命令に対して即座に対応できるようにしている。
【0060】
なお、上記した各説明は、あくまでも本発明の一実施形態にすぎず、詳細は任意に変更可能である。例えば、ECU15にてNOx の排出量を算出する場合には、ECU15にNOx 排出量マップを準備しておき、該マップを利用してNOx 排出量の算出を行わせてもよい。
【0061】
なお、NOx 排出量マップは、機関負荷と機関回転数とをパラメータとして、これらパラメータと各種予備実験により求められた単位時間当たりにおけるNOx 排出量との関係をマップ化したものである。従って、図示しないアクセル開度センサの出力信号、及びクランク角センサからの出力信号をECU15に入力してNOx 排出量マップに照らし合わせると、単位時間当たりにおけるNOx 排出量を算出できる。
【0062】
尚、アクセル開度センサは、アクセル開度に比例した出力電圧をECU15に出力し、その出力電圧は機関負荷の演算に用いられる。一方、クランク角センサは、エンジン1の図示しないクランクシャフトが一定角度回転する毎に出力パルスをECU15に出力し、その出力パルスは機関回転数の演算に用いられている。
【0063】
また、上記した例では、還元剤添加弁50に作用する還元剤の供給圧力を、入りガス圧センサ12の出力値と圧力センサ43の出力値とによって求めているが、排気管10内の圧力は、機関負荷及び機関回転数をパラメータとして作成した排圧マップにより推測できる。従って、圧力センサ43の出力値と排圧マップ上で算出された排圧とによって、還元剤の供給圧力を算出するようにしてもよい。
【0064】
また、上記した例では、入りガス圧センサ12の出力値と圧力センサ43の出力値とを考慮して、還元剤添加弁50におけるデューティ比制御を行っているが、副還元剤貯蔵タンク40に対する還元ガスの貯蔵圧力を排気管10内の圧力に対して十分に大きくすると、排圧の影響による単位時間当たりの還元剤供給量の変動を相対的に小さくできる。即ち、副還元剤貯蔵タンク40に対する還元ガスの貯蔵圧力を十分に大きく設定した場合には、副還元剤貯蔵タンク40の圧力のみを考慮して還元剤添加弁50のデューティ比制御を行ってもよい。
【0065】
また、上記した例では、ガス化された還元剤をそのままの形態で副還元剤貯蔵タンク40内に貯蔵しているが、生成された還元剤を圧縮及び冷却して体積を減少させ副還元剤貯蔵タンク40に貯蔵しても構わない。すなわち、還元ガスを圧縮して副還元剤貯蔵タンク40に貯蔵することにより、さらなる装置の小型化を図れる。例えばこの場合、副還元剤貯蔵タンク40の容積を機械的に減少させて還元ガスの圧縮を行い、還元剤貯蔵タンク40の周囲に冷却フィンなどを設けて還元ガスの冷却を図るなどの方法を例示できる。
【0066】
また、副還元剤貯蔵タンク40内にアンモニア吸蔵合金を収容しておき、該アンモニア吸蔵合金に還元ガスを吸蔵させた状態で、副還元剤貯蔵タンク40内に還元ガスを貯蔵してもよい。なお、アンモニア吸蔵合金は、還元ガスと結合して還元ガスを貯蔵するため、副還元剤貯蔵タンク40内に、より高密度に還元ガスを貯蔵できる。
【0067】
また、上記した例では固体状の還元剤をガス化させ副還元剤貯蔵タンク40に貯蔵しているが、還元ガス発生部30の温度を還元剤の液化に抑える程度まで低下せしめ、固体状の還元剤を液化した状態にて副還元剤貯蔵タンク40内に貯蔵するようにしてもよい。すなわち、副還元剤貯蔵タンク40に貯蔵される還元剤の形態は、還元剤添加弁50より即座に添加可能な形態であればよい。
【0068】
また、上記した例では、固体状の還元剤としてカルバミン酸アンモニウムを適用したが、勿論、尿素CO(NHなどの他の物質を還元剤として採用してもよい。なお、尿素など比較的高温にてガス化する還元剤を採用した場合には、還元ガス発生部30を電気ヒータなどにて構成して、還元剤のガス化を行ってもよい。また、機関潤滑油の熱を利用して加熱してもよい。
【0069】
次に、このような構成の還元剤供給装置を採用したエンジンの作用効果について述べる。
前述したように、ECU15は、NOx の排出量に応じた還元剤添加弁50のデューティ比制御を行い、目標供給量に見合った還元剤を適宜のタイミングにてNOx 触媒9に添加する。このとき本発明の還元剤供給装置16では、固体状のカルバミン酸アンモニウムを還元ガス発生部30にて加熱ガス化して、予め副還元剤貯蔵タンク40内に貯蔵・準備しているため、還元剤の添加命令に即座に対応できる。また、副還元剤貯蔵タンク40内に還元ガスを常時貯蔵しているため、大量の還元剤を要する場合においても、安定した還元剤の供給を行える。
【0070】
また、還元剤添加弁50におけるデューティ比制御は、還元剤の供給圧力を考慮して制御されている。しかも、ガス化された還元剤は、副還元剤貯蔵タンク40内に一時期貯蔵された後に添加されるため、還元剤添加弁50に対する還元ガスの供給圧力は常に安定している。従って、ECU15では、還元剤添加弁50におけるデューティ比制御を容易になしえ、目標供給量に見合った還元剤を確実にNOx 触媒9に供給できる。
【0071】
また、還元ガスの残量は、副還元剤貯蔵タンク40内の圧力変化を利用してECU15にて把握されている。このためECU15では、還元ガスの残量に基づいて固体状還元剤のガス化を制御でき、必要以上に還元剤をガス化させることもない。従って、還元剤供給装置16内に大きな容積を確保せずとも安定した還元剤の供給をなし得る。
【0072】
このように本発明の還元剤供給装置16を採用したエンジンでは、適切量、且つ適宜のタイミングにて還元剤の供給がなされるため、NOx 触媒9におけるNOx の浄化効率を飛躍的に高めることができる。また、還元剤供給装置16内に大きな容積を確保せずとも安定した還元剤の添加をなし得るため、装置本体を小型化に製作でき車両への搭載性を大幅に向上させることができる。
【0073】
なお、上記したエンジン1では、NOx を浄化する触媒として、選択還元型NOx 触媒を適用しているが、本発明の還元剤供給装置16は、勿論、吸蔵還元型NOx 触媒にも有用である。なお、吸蔵還元型NOx 触媒とは、酸素過剰雰囲気下でNOx を吸蔵し、酸素濃度が低下したときに吸蔵したNOx を放出して還元浄化せしめる触媒である。
【0074】
また、上記した実施の形態では、ディーゼルエンジンを例として説明したが、本発明の還元剤供給装置16は、ディーゼルエンジンのみならず、希薄燃焼可能なリーンバーンガソリンエンジンなどにおいても、極めて有用である。
【0075】
【発明の効果】
以上のように本発明によれば、還元剤の供給命令に対して、遅延することなく即座に所定量の還元剤を供給し得る内燃機関の還元剤供給装置を提供できる。
【図面の簡単な説明】
【図1】本実施の形態に係る還元剤供給装置を採用したディーゼルエンジンの概略構成図である。
【図2】本実施の形態に係る還元剤供給装置の概略構成図。
【符号の説明】
1 ディーゼルエンジン(エンジン)
2 燃焼室
3 ピストン
4 シリンダ
5 シリンダヘッド
6 燃料噴射弁
7 エアフローメータ
8 吸気管
9 選択還元型NOx 触媒(NOx 触媒)
10 排気管
11 NOx センサ
12 入りガス圧センサ
13 排気温度センサ
14 還元剤センサ
15 エンジンコントロール用電子制御ユニット(ECU)
16 還元剤供給装置
18 インジケータパネル
19 警告ランプ
20 主還元剤貯蔵タンク
21 タンク本体
22 断熱部材
30 還元ガス生成部
31 加熱室
32 外壁
33 空間
34 機関冷却水制御弁
40 副還元剤貯蔵タンク
41 タンク本体
42 断熱部材
43 圧力センサ
50 還元剤添加弁
51 弁体
52 ガイド
53 ノズル部
54 ソレノイド
55 導入通路
60 連結管
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a reducing agent supply device for an internal combustion engine, and more particularly to a reducing agent supply device for supplying a reducing agent to a NOx catalyst that purifies nitrogen oxides (NOx) discharged from the internal combustion engine.
[0002]
[Prior art]
As a reducing agent supply device that is provided in an exhaust system of an internal combustion engine and supplies a reducing agent to a NOx catalyst that purifies nitrogen oxides (hereinafter, simply referred to as NOx) discharged from the internal combustion engine, for example, Japanese Unexamined Patent Application Publication No. The reducing agent supply device disclosed in Japanese Patent No. 272331 can be exemplified.
[0003]
In the reducing agent supply device disclosed in Japanese Patent Application Laid-Open No. Hei 5-272331, urea CO (NH) capable of reducing NOx at a high purification rate even at low temperatures2  )2Is used as a reducing agent, and the urea is supplied to a NOx catalyst to promote purification of NOx contained in exhaust gas.
[0004]
More specifically, after receiving a reducing agent supply command from an electronic control unit for engine control (hereinafter simply referred to as an ECU), the solid urea stored in the storage tank is heated and gasified in a furnace tube. The gasified urea is supplied upstream of the NOx catalyst in the engine exhaust passage to promote NOx purification.
[0005]
By the way, the solid reducing agent has a smaller volume than the gaseous reducing agent and the liquid reducing agent and is excellent in mountability on a vehicle, but cannot be supplied to the NOx catalyst because the particles are large as they are. Therefore, it is necessary to heat and gasify the solid reducing agent in the furnace tube as in the above-described reducing agent supply device, so that the NOx catalyst can be supplied to the NOx catalyst (transformation).
[0006]
[Problems to be solved by the invention]
However, in the conventional reducing agent supply device, the reducing agent is gasified and supplied to the NOx catalyst after receiving the reducing agent supply instruction from the ECU. There was also.
[0007]
In particular, the reducing agent containing solid urea as a main component not only takes a long time to gasify, but also is released to the atmosphere without reacting with NOx and emits an offensive odor when supplied to the NOx catalyst at an appropriate timing. There is a fear. Therefore, the development of a reducing agent supply device that can immediately respond to a reducing agent supply instruction is urgently required.
[0008]
If the required supply amount of the reducing agent exceeds the amount of the reducing gas (reducing agent) generated in the furnace cylinder, the supply of the reducing gas cannot catch up, and an appropriate amount of the reducing agent is supplied to the NOx catalyst. Could not supply. Therefore, the purification rate of NOx in the NOx catalyst is greatly reduced, which may lead to a reduction in exhaust emission.
[0009]
Further, in the conventional reducing agent supply device, since the reducing gas generated in the furnace tube is directly supplied to the exhaust passage, the supply pressure of the reducing agent is not stable, and an appropriate amount of the reducing agent corresponding to the required supply amount is used. Could not be supplied to the NOx catalyst.
[0010]
Therefore, an object of the present invention is to provide a reducing agent supply device for an internal combustion engine that can supply a predetermined amount of reducing agent immediately without delay in response to a reducing agent supply command.
[0011]
[Means for Solving the Problems]
In order to solve the above technical problems, the present invention employs the following solutions. That is,
A reducing agent supply device for supplying a reducing agent to a NOx catalyst provided in an exhaust system of an internal combustion engine for purifying nitrogen oxides discharged from the internal combustion engine,
Main reducing agent storage means for storing a solid reducing agent,
The solid reducing agent stored in the main reducing agent storage means isBy gasification, the reducing agentFluidizing means for fluidizing a reducing agent,
Secondary reducing agent storage means for temporarily storing the reducing agent fluidized by the reducing agent fluidizing means,
Reducing agent supply amount calculating means for calculating a supply amount of the reducing agent to be supplied to the NOx catalyst based on an operation state of the engine body;
The reducing agent stored in the sub-reducing agent storage means is used as the reducing agent supply amount calculating means.StepReducing agent adding means for adding upstream of the NOx catalyst in the exhaust system of the internal combustion engine based on the supply amount calculated by
WithAnd
The sub-reducing agent storage unit includes a remaining amount calculating unit that calculates a remaining amount of the reducing agent stored in the sub-reducing agent storage unit, and a sub-reducing agent storage chamber that temporarily stores the fluidized reducing agent. Pressure detecting means for detecting the pressure in the secondary reducing agent storage chamber,
The reducing agent fluidizing unit fluidizes the solid reducing agent stored in the main reducing agent storage unit in response to the remaining amount calculated by the remaining amount calculating unit being less than a predetermined value. Replenish the auxiliary reducing agent storage means,
The remaining amount calculating unit determines that the remaining amount of the reducing agent is large when the pressure detected by the pressure detecting unit is high, and determines the remaining amount of the reducing agent when the pressure detected by the pressure detecting unit is low. Judge it is lessIt is characterized by the following.
[0012]
According to the present invention employing such a means, the reducing agent having fluidity so that it can be added by the reducing agent fluidizing means is prepared and stored in advance in the sub-reducing agent storage means. The reducing agent can be supplied immediately in response to the supply command. Further, since the reducing gas is always stored in the auxiliary reducing agent storage tank 40, a stable supply of the reducing agent can be performed even when a large amount of the reducing agent is required. The fluidization of the reducing agent is an action for facilitating diffusion of the added reducing agent when the reducing agent is added by the reducing agent adding unit. That is, in the present invention, fluidization generally refers to actions such as gasification, liquefaction, gelation, and powderization as fluidization.
[0013]
The reducing agent fluidizing means gasifies the solid reducing agent to give the reducing agent fluidity.You.That is, the solid reducing agent is gasified to improve the diffusion of the added reducing agent when added by the reducing agent adding means.
[0014]
Further, the sub-reducing agent storing means includes a remaining amount calculating means for calculating a remaining amount of the reducing agent stored in the sub-reducing agent storing means, and the reducing agent fluidizing means is provided by the remaining amount calculating means. When the calculated remaining amount becomes less than the predetermined value, the solid reducing agent stored in the main reducing agent storage unit is fluidized and supplied to the auxiliary reducing agent storage unit.You.
[0015]
That is, in this means, when the remaining amount of the reducing agent stored in the sub-reducing agent storage unit becomes small, the solid reducing agent is newly fluidized and supplied to the sub-reducing agent storage unit. Therefore, the reducing agent can always be secured in the auxiliary reducing agent storage unit without unnecessarily fluidizing the solid reducing agent. The volume of the solid reducing agent generally increases with gasification and liquefaction. Therefore, if the solid reducing agent is fluidized unnecessarily, it is necessary to increase the capacity of the reducing agent storage means in the device, which leads to an increase in the size of the device. Therefore, by fluidizing only the required amount as described above, the size of the apparatus can be minimized. Here, the predetermined value is a numerical value excluding zero, and is a value that can be arbitrarily set based on an empirical rule or the like.
[0016]
Further, the sub-reducing agent storage means includes a sub-reducing agent storage chamber for temporarily storing the fluidized reducing agent, and pressure detection means for detecting a pressure in the sub-reducing agent storage chamber, The calculating means determines that the remaining amount of the reducing agent is large when the pressure detected by the pressure detecting means is high, and determines that the remaining amount of the reducing agent is small when the pressure detected by the pressure detecting means is low. YouYou.That is, the remaining amount of the reducing agent stored in the sub-reducing agent storage chamber is determined based on the pressure change in the sub-reducing agent storage chamber.
[0017]
Further, the reducing agent adding means,A reducing agent addition valve that is provided in the exhaust system upstream of the NOx catalyst and that adds the reducing agent stored in the sub-reducing agent storage chamber to the upstream of the NOx catalyst when the valve is opened; and a pressure detected by the pressure detection means. And an addition valve control means for controlling a valve opening time of the reducing agent addition valve.
[0018]
That is, in this means, the supply pressure of the reducing agent acting on the reducing agent addition valve is grasped by detecting the pressure in the auxiliary reducing agent storage chamber by the pressure detecting means. Then, the supply amount of the reducing agent supplied from the reducing agent addition valve to the NOx catalyst is controlled so as to always reach the target value. Therefore, even if the pressure in the secondary reducing agent storage chamber fluctuates, the reducing agent that matches the required supply amount can be supplied to the NOx catalyst.
[0019]
Note that the addition valve control means reduces the valve opening time of the reducing agent addition valve when the pressure in the auxiliary reducing agent storage chamber is high, and reduces the addition of the reducing agent when the pressure in the auxiliary reducing agent storage is low. The valve opening time of the valve may be lengthened.
[0020]
That is, when the pressure in the sub-reducing agent storage chamber is high, the supply amount of the reducing agent per unit time is increased, so that the valve opening time is shortened. The supply time of the reducing agent supplied from the reducing agent addition valve is maintained at a target value by lengthening the valve opening time because the supply amount of the reducing agent in (1) decreases.
[0021]
The NOx catalyst is preferably a selective reduction type NOx catalyst that decomposes or reduces nitrogen oxides in the presence of a reducing agent. The solid reducing agent is preferably a reducing agent that generates a reducing gas based on ammonia when gasified by the reducing agent fluidizing means.
[0022]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, preferred embodiments of a reducing agent supply device according to the present invention will be described with reference to the drawings. The embodiments described below are embodiments in which the reducing agent supply device of the present invention is applied to a vehicle diesel engine.
[0023]
<Overview of internal combustion engine>
Before describing the reducing agent supply device of the present invention, a diesel engine equipped with the reducing agent supply device will be described with reference to FIG.
[0024]
A diesel engine 1 (hereinafter, simply referred to as an engine) includes a combustion chamber 2 including a piston 3, a cylinder 4, a cylinder head 5, and the like, and a fuel injection valve 6 that supplies engine fuel to the combustion chamber 2. Have. Further, an intake pipe 8 having an air flow meter 7 for measuring an air intake amount is connected to the combustion chamber 2. In the combustion chamber 2, air introduced through the intake pipe 8 and a fuel injection valve 6 are provided. And the engine fuel supplied by the engine is mixed to perform engine combustion by self-ignition.
[0025]
On the other hand, exhaust gas generated due to engine combustion in the combustion chamber 2 passes through an exhaust pipe 10 which is connected to the combustion chamber 2 and includes a selective reduction type NOx catalyst 9 and a muffler (not shown) in the middle of the path. Exhausted to the atmosphere. In the following description, the selective reduction type NOx catalyst may be simply referred to as a NOx catalyst.
[0026]
The selective reduction type NOx catalyst 9 provided in the exhaust pipe 10 is a catalyst mainly for effectively purifying nitrogen oxides (hereinafter simply referred to as NOx) in exhaust gas, and reduces or reduces NOx in the presence of a reducing agent. It is a catalyst that decomposes and purifies.
[0027]
Examples of the selective reduction type NOx catalyst 9 include a catalyst in which a transition metal such as Cu is supported on zeolite by ion exchange, a catalyst in which a noble metal is supported on zeolite or alumina, and a catalyst in which vanadium is supported on titanium. , Etc. can be exemplified.
[0028]
A NOx sensor 11, an incoming gas pressure sensor 12, an exhaust gas temperature sensor 13 and the like are provided on the exhaust pipe 10 on the upstream side of the NOx catalyst 9, and a reducing agent sensor 14 is provided on the downstream side of the NOx catalyst 9. ing. The NOx sensor 11 is a sensor that measures the NOx concentration in the exhaust gas. The incoming gas pressure sensor 12 is a sensor that measures a pipe pressure (exhaust pressure) in the exhaust pipe 10. Further, the exhaust gas temperature sensor 13 is a sensor that measures the temperature of the exhaust gas flowing into the NOx catalyst 9. The reducing agent sensor 14 is a sensor that measures the concentration of the reducing agent in the exhaust gas. The various sensors are connected to input ports of an engine control electronic control unit 15 described later.
[0029]
The engine 1 is controlled by an engine control electronic control unit 15 (hereinafter simply referred to as ECU 15) in accordance with the operating state. The ECU 15 includes a ROM (Read Only Memory), a RAM (Random Access Memory), a CPU (Central Processor Unit), an input port, an output port, an A / D converter, etc., which are interconnected by a bidirectional bus. For example, based on output signals from various sensors input to the input port and referring to various control maps developed on the ROM, for example, fuel injection control in the fuel injection valve 5 is performed. In the present invention, the control of the reducing agent supply device 16 is also performed at the same time.
[0030]
In the present invention, in order that the NOx catalyst 9 purifies NOx in the exhaust gas discharged with the engine combustion of the engine 1, ammonia gas (NH 3) as a reducing agent is supplied to the NOx catalyst 9. ) Is provided.
Hereinafter, the reducing agent addition device 16 which is the gist of the present invention will be described in detail with reference to FIG.
[0031]
<Structure of reducing agent supply device>
First, the structure of the reducing agent supply device 16 will be described.
The reducing agent supply device 16 heats a main reducing agent storage tank 20 (main reducing agent storing means) for storing a solid reducing agent therein and a solid reducing agent stored in the main reducing agent storage tank 20. A reducing gas generating unit 30 (reducing agent fluidizing means) for generating a reducing gas, and a sub-reducing agent storage tank 40 (sub-reducing agent storing means) for temporarily storing the reducing gas generated by the reducing gas generating unit 30; And a reducing agent addition valve 50 (reducing agent adding means) for adding the reducing gas stored in the auxiliary reducing agent storage tank 40 to the NOx catalyst 9 according to a reducing agent supply command from the ECU 15.
[0032]
The main reducing agent storage tank 20 has a tank main body 21 that contains therein solid ammonium carbamate as a reducing agent, and a heat insulating member 22 provided so as to surround the tank main body 21, which will be described later. It is provided detachably with respect to the reducing gas generator 30.
[0033]
Note that ammonium carbamate is a kind of reducing agent based on ammonia, and has a property of being solid at room temperature and gasifying at around 40 degrees Celsius. Also, since it has a much stronger reducing action than the conventionally used reducing agents such as hydrocarbon (HC) and carbon monoxide (CO), NOx can be purified with a high purification efficiency even at a relatively low temperature. It has such advantages.
[0034]
The reason why the main reducing agent storage tank 20 is detachably provided to the reducing gas generator 30 is that when the ammonium carbamate stored inside is exhausted, a new main reducing agent storing new ammonium carbamate is used. This is because the agent storage tank 20 and the empty main reducing agent storage tank after use can be easily replaced. That is, the main reducing agent storage tank 20 is of a cartridge type.
[0035]
The reducing gas generation unit 30 is connected to the main reducing agent storage tank 20 and is provided to surround the heating chamber 31 with a heating chamber 31 for promoting gasification of the reducing agent stored in the main reducing agent storage tank 20. And an outer wall 32. A space 33 is formed between the heating chamber 31 and the outer wall 32 and communicates with a water jacket (not shown) that serves as a circulation path for the engine cooling water, and the engine cooling water warmed by engine combustion is provided in this space. The inside of the heating chamber 31 is heated by flowing into the inside of the heating chamber 31.
[0036]
Further, between the water jacket and the reducing gas generator 30 (space 33), an engine cooling water control valve 34 for regulating the flow of the engine cooling water into the reducing gas generator 30 is provided (see FIG. 1). ). The opening and closing operation of the engine cooling water control valve 34 is controlled by the ECU 15 so that the flow rate of the engine cooling water flowing into the heating chamber 31 is controlled so that the room temperature in the heating chamber 31 can be arbitrarily adjusted. ing.
[0037]
Then, when the engine cooling water control valve 34 is opened to guide the engine cooling water warmed by the engine combustion to the reducing gas generation unit 30 (space 33), the room temperature in the heating chamber 31 increases. Ammonium carbamate in the main reducing agent storage tank 20 communicating with the heating chamber 31 is gasified. In the following description, the gasified ammonium carbamate may be simply referred to as a reducing gas.
[0038]
The auxiliary reducing agent storage tank 40 detects a tank body 41 for storing gaseous ammonium carbamate as a reducing agent, a heat insulating member 42 provided to surround the tank body 41, and a pressure in the tank body 41. A pressure sensor 43 (pressure detecting means) is provided, and the tank body 41 and the above-described reducing gas generator 30 are connected to each other via a connection pipe 60. Therefore, the ammonium carbamate gasified in the reducing gas generator 30 flows into the secondary reducing agent storage tank 40 via the connecting pipe 60 and is temporarily stored in the secondary reducing agent storage tank 40.
[0039]
The reducing agent addition valve 50 is provided in the exhaust pipe 10 on the upstream side of the NOx catalyst 9, and upon receiving a reducing agent supply command from the ECU 15, converts the reducing gas stored in the sub-reducing agent storage tank 40 into the upstream of the NOx catalyst 9. To the side exhaust pipe 10.
[0040]
The reducing agent addition valve 50 includes a nozzle part 53 including a valve body 51 and a guide 52 supporting the valve body 51, a solenoid 54 for opening and closing the valve body 51 provided in the nozzle part 53, An introduction passage 55 connected to the connecting pipe 60 for guiding the reducing gas stored in the sub-reducing agent storage tank 40 to the nozzle portion 53; The gas flows down the passage 55 and is guided to the nozzle 53. The reducing gas is added to the exhaust pipe 10 at an appropriate amount and at an appropriate timing by controlling the opening and closing of the valve element 51 by the solenoid 54.
[0041]
The duty ratio of the solenoid 54 that opens and closes the valve element 51 is controlled by the ECU 15, and the valve element 51 is opened when a valve opening voltage is applied to add the reducing gas in the auxiliary reducing agent storage tank 40 to the exhaust pipe 10. Like that. The internal pressure of the sub-reducing agent storage tank 40 is always maintained higher than the exhaust pressure in the exhaust pipe 10, and when the reducing gas is added, the pressure difference is used to add the reducing gas. I'm trying to get. The pressure adjustment of the auxiliary reducing agent storage tank 40 will be described in detail in the following description of the reducing agent supply control.
[0042]
<Control of reducing agent supply device>
Hereinafter, the reducing agent supply control according to the above-described reducing agent supply device will be described.
When the temperature of the engine coolant reaches about 40 degrees Celsius with the start of operation of the engine 1 (start of engine combustion), the ECU 15 performs gasification of the reducing agent stored in the main reducing agent storage tank 20 in order to gasify the reducing agent. First, the engine cooling water control valve 34 is opened to introduce the engine cooling water into the reducing gas generator 30.
[0043]
When the space temperature in the heating chamber 31 reaches about 40 degrees Celsius due to the engine cooling water, part of the ammonium carbamate in the main reducing agent storage tank 20 communicating with the reducing gas generator 30 is gasified, and the connection path After 60, the secondary reducing agent storage tank 40 is filled.
[0044]
At this time, the ECU 15 knows the amount of the reducing gas filled in the sub-reducing agent storage tank 40 based on the output value of the pressure sensor 43, and detects the sub-reducing agent storage tank 40 detected by the pressure sensor 43. When the internal pressure reaches a predetermined value, it is considered that the charging amount of the reducing gas has reached the specified amount, and the engine cooling water control valve 34 is closed to temporarily suspend the gasification of ammonium carbamate. ing.
[0045]
Here, the predetermined value is a value obtained by various preliminary experiments, for example, a maximum allowable pressure of the auxiliary reducing agent storage tank 40, an average exhaust pressure in the exhaust pipe 10, a consumption amount of the reducing gas per unit time, and the like. Is a value arbitrarily set in consideration of
[0046]
In the ECU 15, when the pressure of the sub-reducing agent storage tank 40 detected by the pressure sensor 43 does not increase even after the lapse of a predetermined time, the ammonium carbamate stored in the main reducing agent storage tank 20 does not increase. Is exhausted, a warning lamp 19 is lit on an indicator panel 18 provided in the vehicle to notify the driver of the fact.
[0047]
In addition, the ECU 15 controls the target supply amount of the reducing agent based on the engine load, the engine speed, the NOx concentration, the catalyst temperature, the charging pressure of the reducing gas, and the like in order to control the supply of the reducing agent to promote the purification of NOx. Is controlled, and the solenoid 54 in the reducing agent addition valve 50 is controlled so that a reducing agent corresponding to the calculated target supply amount is added to the NOx catalyst 9 at an appropriate timing.
[0048]
The control of the reducing agent addition valve 50 will be described in detail. The output signal from the air flow meter 7 and the output signal from the NOx sensor 11 are input to the ECU 15 through the input port and the A / D converter as described above. I have. The ECU 15 calculates the amount of NOx discharged per unit time from the air intake amount detected by the air flow meter 7 and the NOx concentration detected by the NOx sensor 11, and calculates the calculated amount. A target supply amount of the reducing agent corresponding to the NOx emission amount is set (reducing agent supply amount calculating means).
[0049]
Further, an output signal from the pressure sensor 43 provided in the sub-reducing agent storage tank 40 and an output signal from the incoming gas pressure sensor 12 provided in the exhaust pipe 10 are input to the ECU 15. The pressure sensor 43 outputs an output voltage proportional to the internal pressure of the auxiliary reducing agent storage tank 40, and the incoming gas pressure sensor 12 outputs an output voltage proportional to the exhaust pressure in the exhaust pipe 10. Then, the ECU 15 obtains a pressure difference between the pressure of the auxiliary reducing agent storage tank 40 and the pressure in the exhaust pipe 10 (discharge pressure) based on the output values from the pressure sensors 43 and 12. The supply pressure of the reducing gas to the exhaust pipe 10 is calculated.
[0050]
Also, the ECU 15 calculates the duty ratio of the valve element 51 of the reducing agent addition valve 50 in consideration of the calculated supply pressure of the reducing gas so that the supply amount of the reducing gas per unit time becomes the target supply amount. Then, duty ratio control of the reducing agent addition valve 50 is performed based on the calculated duty ratio (addition valve control means). Here, the duty ratio means the number of times the valve body 51 is opened and closed per unit time. Therefore, in the duty ratio control, as the number of times of opening and closing of the valve element 51 per unit time increases, more reducing gas is supplied to the exhaust pipe 10.
[0051]
That is, when the supply pressure of the reducing gas is high, the duty ratio is set small because the supply amount of the reducing gas per unit time is inevitably increased. Conversely, when the supply pressure of the reducing gas is low, the reduction per unit time is performed. The duty ratio is set large because the supply amount of gas decreases.
[0052]
An output signal from the exhaust temperature sensor 13 is input to the ECU 15. The exhaust temperature sensor 13 outputs an output voltage proportional to the temperature of the exhaust gas, and is used for grasping the catalyst temperature of the NOx catalyst 9. In response to the fact that the catalyst temperature detected by the exhaust gas temperature sensor 13 has reached the activation temperature at which NOx can be purified, the ECU 15 controls the duty of the reducing agent addition valve 50 to match the calculated target supply amount. And the reducing gas is added to the NOx catalyst 9.
[0053]
Further, an output signal from the reducing agent sensor 14 is input to the ECU 15. When a large amount of the reducing agent is unintentionally supplied due to a failure of the reducing agent supply device 16 or the like, the ECU 15 senses the reducing agent with the reducing agent sensor 14 and immediately stops the supply of the reducing agent. Is performed.
[0054]
On the other hand, the reducing gas stored in the sub-reducing agent storage tank 40 is consumed by the addition from the reducing agent addition valve 50, and the remaining amount thereof decreases with time. Therefore, the ECU 15 always grasps the remaining amount of the reducing gas in the sub-reducing agent storage tank 40 so as not to run out of the reducing gas stored in the sub-reducing agent storage tank 40, and when the remaining amount decreases, Reducing gas replenishment control for replenishing the auxiliary reducing agent storage tank 40 with reducing gas is performed.
[0055]
In order to grasp the remaining amount of the reducing gas by the ECU 15, the remaining amount is grasped by using the output signal of the pressure sensor 43 described above. That is, when the reducing gas in the auxiliary reducing agent storage tank 40 is consumed, the internal pressure of the auxiliary reducing agent storage tank 40 also decreases. Therefore, by monitoring the output value of the pressure sensor 43, the remaining amount in the auxiliary reducing agent storage tank 40 can be grasped (remaining amount detecting means).
[0056]
The ECU 15 opens the engine cooling water control valve 34 in response to the fact that the pressure in the auxiliary reducing agent storage tank 40 (the filling pressure of the reducing gas) detected by the pressure sensor 43 has become less than a predetermined value. The valve is heated to heat the heating chamber 31, and the ammonium carbamate stored in the main reducing agent storage tank 20 is newly gasified. As a result, the newly gasified ammonium carbamate flows into the sub-reducing agent storage tank 40 and replenishes the sub-reducing agent storage tank 40 with the reducing gas.
[0057]
Here, the predetermined value is a value that can be arbitrarily set, but is preferably a value that is sufficiently large with respect to the exhaust pressure. That is, by increasing the filling pressure of the reducing gas, the diffusion of the reducing gas into the exhaust pipe 10 is improved, and the supply amount per unit time with respect to the change in the exhaust pressure is also stabilized.
[0058]
When the internal pressure of the sub-reducing agent storage tank 40 becomes equal to or higher than a predetermined value, the engine cooling water control valve 34 is closed as described above to stop the gasification of ammonium carbamate.
[0059]
As described above, in the reducing agent supply device 16 of the present invention, the solid reducing agent is gasified and stored and prepared in the auxiliary reducing agent storage tank 40 in advance so that addition from the reducing agent addition valve 50 can be performed. It is possible to immediately respond to a reducing agent addition command from the ECU 15.
[0060]
The above description is merely one embodiment of the present invention, and details can be arbitrarily changed. For example, when the ECU 15 calculates the NOx emission amount, the ECU 15 may prepare a NOx emission amount map and use the map to calculate the NOx emission amount.
[0061]
The NOx emission map maps the relationship between these parameters and the NOx emission per unit time obtained by various preliminary experiments, using the engine load and the engine speed as parameters. Therefore, when the output signal of the accelerator opening sensor (not shown) and the output signal of the crank angle sensor are input to the ECU 15 and compared with the NOx emission map, the NOx emission per unit time can be calculated.
[0062]
The accelerator opening sensor outputs an output voltage proportional to the accelerator opening to the ECU 15, and the output voltage is used for calculating the engine load. On the other hand, the crank angle sensor outputs an output pulse to the ECU 15 every time a crankshaft (not shown) of the engine 1 rotates by a predetermined angle, and the output pulse is used for calculating the engine speed.
[0063]
In the above-described example, the supply pressure of the reducing agent acting on the reducing agent addition valve 50 is obtained from the output value of the incoming gas pressure sensor 12 and the output value of the pressure sensor 43. Can be estimated from an exhaust pressure map created using the engine load and the engine speed as parameters. Therefore, the supply pressure of the reducing agent may be calculated based on the output value of the pressure sensor 43 and the exhaust pressure calculated on the exhaust pressure map.
[0064]
In the above-described example, the duty ratio control in the reducing agent addition valve 50 is performed in consideration of the output value of the incoming gas pressure sensor 12 and the output value of the pressure sensor 43. If the storage pressure of the reducing gas is sufficiently increased with respect to the pressure in the exhaust pipe 10, the fluctuation of the supply amount of the reducing agent per unit time due to the influence of the exhaust pressure can be relatively reduced. That is, if the storage pressure of the reducing gas in the sub-reducing agent storage tank 40 is set to a sufficiently large value, the duty ratio control of the reducing agent addition valve 50 may be performed by considering only the pressure in the sub-reducing agent storage tank 40. Good.
[0065]
In the above-described example, the gasified reducing agent is stored in the form of the sub-reducing agent storage tank 40 as it is. However, the generated reducing agent is compressed and cooled to reduce the volume to reduce the volume of the reducing agent. It may be stored in the storage tank 40. That is, by compressing the reducing gas and storing it in the auxiliary reducing agent storage tank 40, the size of the apparatus can be further reduced. For example, in this case, a method of mechanically reducing the volume of the auxiliary reducing agent storage tank 40 to compress the reducing gas, and providing a cooling fin or the like around the reducing agent storage tank 40 to cool the reducing gas is used. Can be illustrated.
[0066]
Alternatively, the reducing gas may be stored in the auxiliary reducing agent storage tank 40 in a state where the ammonia storing alloy is stored in the auxiliary reducing agent storage tank 40 and the reducing gas is stored in the ammonia storing alloy. Since the ammonia storage alloy stores the reducing gas in combination with the reducing gas, the reducing gas can be stored in the auxiliary reducing agent storage tank 40 at a higher density.
[0067]
In the above-described example, the solid reducing agent is gasified and stored in the sub-reducing agent storage tank 40. The reducing agent may be stored in the auxiliary reducing agent storage tank 40 in a liquefied state. That is, the form of the reducing agent stored in the sub-reducing agent storage tank 40 may be any form that can be added immediately by the reducing agent addition valve 50.
[0068]
Further, in the above example, ammonium carbamate was applied as a solid reducing agent, but of course, urea CO (NH2  )2Other substances may be employed as the reducing agent. When a reducing agent that gasifies at a relatively high temperature such as urea is employed, the reducing gas generating unit 30 may be configured with an electric heater or the like to gasify the reducing agent. Further, heating may be performed using heat of the engine lubricating oil.
[0069]
Next, the operation and effect of the engine employing the reducing agent supply device having such a configuration will be described.
As described above, the ECU 15 controls the duty ratio of the reducing agent addition valve 50 according to the NOx emission amount, and adds the reducing agent corresponding to the target supply amount to the NOx catalyst 9 at an appropriate timing. At this time, in the reducing agent supply device 16 of the present invention, solid ammonium carbamate is heated and gasified in the reducing gas generating section 30 and stored and prepared in advance in the sub-reducing agent storage tank 40. Can immediately respond to the addition order. Further, since the reducing gas is always stored in the auxiliary reducing agent storage tank 40, even when a large amount of reducing agent is required, a stable supply of the reducing agent can be performed.
[0070]
Further, the duty ratio control in the reducing agent addition valve 50 is controlled in consideration of the supply pressure of the reducing agent. Moreover, since the gasified reducing agent is added after being temporarily stored in the auxiliary reducing agent storage tank 40, the supply pressure of the reducing gas to the reducing agent addition valve 50 is always stable. Therefore, the ECU 15 can easily control the duty ratio in the reducing agent addition valve 50, and can surely supply the NOx catalyst 9 with the reducing agent corresponding to the target supply amount.
[0071]
Further, the remaining amount of the reducing gas is grasped by the ECU 15 using the pressure change in the auxiliary reducing agent storage tank 40. Therefore, the ECU 15 can control the gasification of the solid reducing agent based on the remaining amount of the reducing gas, and does not unnecessarily gasify the reducing agent. Therefore, a stable supply of the reducing agent can be achieved without securing a large volume in the reducing agent supply device 16.
[0072]
As described above, in the engine employing the reducing agent supply device 16 of the present invention, the reducing agent is supplied at an appropriate amount and at an appropriate timing. it can. Further, since a stable addition of the reducing agent can be performed without securing a large volume in the reducing agent supply device 16, the device main body can be manufactured in a small size, and the mountability to a vehicle can be greatly improved.
[0073]
In the engine 1 described above, a selective reduction type NOx catalyst is applied as a catalyst for purifying NOx. However, the reducing agent supply device 16 of the present invention is, of course, also useful for a storage reduction type NOx catalyst. The storage-reduction type NOx catalyst is a catalyst that stores NOx in an oxygen-excess atmosphere and releases the stored NOx when the oxygen concentration decreases to purify the NOx.
[0074]
In the above-described embodiment, a diesel engine has been described as an example. However, the reducing agent supply device 16 of the present invention is extremely useful not only in a diesel engine but also in a lean burn gasoline engine capable of lean burn. .
[0075]
【The invention's effect】
As described above, according to the present invention, it is possible to provide a reducing agent supply device for an internal combustion engine that can immediately supply a predetermined amount of reducing agent without delay in response to a reducing agent supply command.
[Brief description of the drawings]
FIG. 1 is a schematic configuration diagram of a diesel engine employing a reducing agent supply device according to the present embodiment.
FIG. 2 is a schematic configuration diagram of a reducing agent supply device according to the present embodiment.
[Explanation of symbols]
1 Diesel engine (engine)
2 Combustion chamber
3 piston
4 cylinder
5 Cylinder head
6 Fuel injection valve
7 Air flow meter
8 Intake pipe
9. Selective reduction type NOx catalyst (NOx catalyst)
10 Exhaust pipe
11 NOx sensor
12 gas pressure sensor
13 Exhaust gas temperature sensor
14 Reducing agent sensor
15 Electronic control unit (ECU) for engine control
16 Reducing agent supply device
18 Indicator panel
19 Warning lamp
20 Main reducing agent storage tank
21 Tank body
22 Thermal insulation material
30 Reducing gas generator
31 heating room
32 Outer wall
33 Space
34 Engine cooling water control valve
40 Sub-reducing agent storage tank
41 Tank body
42 Insulation member
43 Pressure sensor
50 Reducing agent addition valve
51 valve body
52 Guide
53 Nozzle
54 solenoid
55 Introductory passage
60 Connecting pipe

Claims (5)

内燃機関の排気系に設けられ該内燃機関より排出される窒素酸化物を浄化するNOx 触媒に、還元剤を供給する還元剤供給装置であって、
固体状の還元剤を貯蔵する主還元剤貯蔵手段と、
前記主還元剤貯蔵手段に貯蔵された固体状の還元剤をガス化することにより該還元剤を流動化させる還元剤流動化手段と、
前記還元剤流動化手段によって流動化された還元剤を一時期貯蔵する副還元剤貯蔵手段と、
機関本体の運転状態に基づき前記NOx 触媒に供給する還元剤の供給量を算出する還元剤供給量算出手段と、
前記副還元剤貯蔵手段に貯蔵される還元剤を、前記還元剤供給量算出手によって算出された供給量に基づき前記内燃機関の排気系におけるNOx 触媒上流に添加する還元剤添加手段と、
を有し、
前記副還元剤貯蔵手段は、該副還元剤貯蔵手段に貯蔵されている還元剤の残量を算出する残量算出手段と、前記流動化された還元剤を一時期貯蔵する副還元剤貯蔵室と、この副還元剤貯蔵室内の圧力を検知する圧力検知手段と、を備え、
前記還元剤流動化手段は、前記残量算出手段によって算出される残量が所定値未満になったことを受けて、前記主還元剤貯蔵手段に貯蔵される固体状の還元剤を流動化して前記副還元剤貯蔵手段に補給し、
前記残量算出手段は、前記圧力検知手段によって検知される圧力が高いとき、還元剤の残量を多いと判断し、前記圧力検知手段によって検知される圧力が低いとき、還元剤の残量を少ないと判断することを特徴とする内燃機関の還元剤供給装置。
A reducing agent supply device for supplying a reducing agent to a NOx catalyst provided in an exhaust system of an internal combustion engine for purifying nitrogen oxides discharged from the internal combustion engine,
Main reducing agent storage means for storing a solid reducing agent,
Reducing agent fluidizing means for fluidizing the reducing agent by gasifying a solid reducing agent stored in the main reducing agent storage means,
Auxiliary reducing agent storage means for temporarily storing the reducing agent fluidized by the reducing agent fluidizing means,
Reducing agent supply amount calculating means for calculating a supply amount of the reducing agent to be supplied to the NOx catalyst based on an operation state of the engine body;
The reducing agent is stored in the auxiliary reducing agent storage unit, and a reducing agent addition means for adding the NOx catalyst upstream in the exhaust system of the internal combustion engine based on the supply amount calculated by the reducing agent supply amount calculating hand stage,
Have a,
The sub-reducing agent storage unit includes a remaining amount calculating unit that calculates a remaining amount of the reducing agent stored in the sub-reducing agent storage unit, and a sub-reducing agent storage chamber that temporarily stores the fluidized reducing agent. Pressure detecting means for detecting the pressure in the secondary reducing agent storage chamber,
The reducing agent fluidizing unit fluidizes the solid reducing agent stored in the main reducing agent storage unit in response to the remaining amount calculated by the remaining amount calculating unit being less than a predetermined value. Replenish the auxiliary reducing agent storage means,
The remaining amount calculating unit determines that the remaining amount of the reducing agent is large when the pressure detected by the pressure detecting unit is high, and determines the remaining amount of the reducing agent when the pressure detected by the pressure detecting unit is low. A reducing agent supply device for an internal combustion engine, which determines that the amount is small .
前記還元剤添加手段は、前記NO  The reducing agent adding means includes the NO. x x 触媒上流の排気系に設けられ開弁時に前記副還元剤貯蔵室に貯蔵される還元剤を前記NOThe reducing agent provided in the exhaust system upstream of the catalyst and stored in the sub-reducing agent storage chamber when the valve is opened is the NO. x x 触媒上流に添加する還元剤添加弁と、前記圧力検知手段によって検知される圧力に基づいて前記還元剤添加弁の開弁時間を制御する添加弁制御手段と、を有することを特徴とする請求項1に記載の内燃機関の還元剤供給装置。A reductant addition valve added upstream of a catalyst, and addition valve control means for controlling a valve opening time of the reductant addition valve based on a pressure detected by the pressure detection means, wherein: 2. The reducing agent supply device for an internal combustion engine according to 1. 前記添加弁制御手段は、前記副還元剤貯蔵室内の圧力が高いとき、前記還元剤添加弁の開弁時間を短くし、前記副還元剤貯蔵内の圧力が低いとき、前記還元剤添加弁の開弁時間を長くすることを特徴とする請求項2に記載の内燃機関の還元剤供給装置。  The addition valve control means, when the pressure in the secondary reducing agent storage chamber is high, shortens the opening time of the reducing agent addition valve, and when the pressure in the secondary reducing agent storage is low, The reducing agent supply device for an internal combustion engine according to claim 2, wherein the valve opening time is lengthened. 前記NO  NO x x 触媒は、還元剤の存在下で、窒素酸化物を分解又は還元せしめる選択還元型NOThe catalyst is a selective reduction type NO that decomposes or reduces nitrogen oxides in the presence of a reducing agent. x x 触媒であることを特徴とする請求項1から3の何れかに記載の内燃機関の還元剤供給装置。4. The reducing agent supply device for an internal combustion engine according to claim 1, wherein the device is a catalyst. 前記固体状の還元剤は、前記還元剤流動化手段によるガス化時に、アンモニアを基調とする還元ガスを生成することを特徴とする請求項1から4の何れかに記載の内燃機関の還元剤供給装置。  The reducing agent for an internal combustion engine according to any one of claims 1 to 4, wherein the solid reducing agent generates a reducing gas based on ammonia when gasified by the reducing agent fluidizing means. Feeding device.
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DE10156714A1 (en) 2002-06-27
FR2816986A1 (en) 2002-05-24

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