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JP4166655B2 - Engine exhaust purification system - Google Patents

Engine exhaust purification system Download PDF

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Publication number
JP4166655B2
JP4166655B2 JP2003339246A JP2003339246A JP4166655B2 JP 4166655 B2 JP4166655 B2 JP 4166655B2 JP 2003339246 A JP2003339246 A JP 2003339246A JP 2003339246 A JP2003339246 A JP 2003339246A JP 4166655 B2 JP4166655 B2 JP 4166655B2
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exhaust
ammonia
temperature
oxidation catalyst
storage tank
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JP2005105914A (en
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剛司 増田
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UD Trucks Corp
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UD Trucks Corp
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Priority to JP2003339246A priority Critical patent/JP4166655B2/en
Priority to US10/572,558 priority patent/US7849674B2/en
Priority to EP04787623A priority patent/EP1669567B1/en
Priority to EP11191519.5A priority patent/EP2426328B1/en
Priority to PCT/JP2004/012743 priority patent/WO2005028826A1/en
Priority to EP11191521.1A priority patent/EP2426329B1/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
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2066Selective catalytic reduction [SCR]
    • F01N3/208Control of selective catalytic reduction [SCR], e.g. dosing of reducing agent
    • 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
    • F01N2610/14Arrangements 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
    • F01N2900/00Details of electrical control or of the monitoring of the exhaust gas treating apparatus
    • F01N2900/06Parameters used for exhaust control or diagnosing
    • F01N2900/16Parameters used for exhaust control or diagnosing said parameters being related to the exhaust apparatus, e.g. particulate filter or catalyst
    • F01N2900/1602Temperature of exhaust gas apparatus
    • 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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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)

Description

本発明は、尿素水溶液を用いて排気中の窒素酸化物(NOx)を還元除去するエンジンの排気浄化装置(以下「排気浄化装置」という)に関し、特に、尿素水溶液を貯蔵する貯蔵タンクの開閉時に発生する悪臭を低減する技術に関する。 TECHNICAL FIELD The present invention relates to an engine exhaust purification device (hereinafter referred to as “exhaust purification device”) that reduces and removes nitrogen oxide (NOx) in exhaust using an aqueous urea solution , and in particular, when a storage tank that stores an aqueous urea solution is opened and closed. The present invention relates to a technique for reducing generated bad odor.

エンジンの排気に含まれるNOxを除去する触媒浄化システムとして、特開2000−27627号公報(特許文献1)に開示された排気浄化装置が提案されている。
かかる排気浄化装置は、エンジンの排気系に還元触媒を配設し、還元触媒の排気上流に還元剤を噴射供給することにより、排気中のNOxと還元剤とを触媒還元反応させて、NOxを無害成分に浄化処理するものである。還元剤は、常温において液体状態で貯蔵タンクに貯蔵され、エンジン運転状態に対応した必要量が噴射ノズルから噴射供給される。また、還元反応は、NOxと反応性が良好なアンモニアを用いるもので、還元剤としては、排気熱及び排気中の水蒸気により加水分解してアンモニアを容易に発生する尿素水溶液が用いられる。
特開2000−27627号公報
As a catalyst purification system for removing NOx contained in engine exhaust, an exhaust purification device disclosed in Japanese Patent Laid-Open No. 2000-27627 (Patent Document 1) has been proposed.
Such an exhaust purification device has a reduction catalyst disposed in an exhaust system of an engine, and injects and supplies a reducing agent upstream of the exhaust of the reduction catalyst to cause a catalytic reduction reaction between NOx in the exhaust and the reducing agent, thereby reducing NOx. It purifies to harmless components. The reducing agent is stored in a storage tank in a liquid state at room temperature, and a necessary amount corresponding to the engine operating state is injected and supplied from the injection nozzle. The reduction reaction uses ammonia having good reactivity with NOx, and as the reducing agent, an aqueous urea solution that is easily hydrolyzed by exhaust heat and water vapor in the exhaust to generate ammonia is used.
JP 2000-27627 A

ところで、上記従来の排気浄化装置によると、周囲温度の変化などに伴って貯蔵タンクが高温になると、その内部に貯蔵される尿素水溶液が化学反応を起こしてアンモニア系ガスとなり、貯蔵タンクの上部空間に充満してしまう。そして、尿素水溶液を補充するときなど、作業者が貯蔵タンクの注入キャップを取り外すと、充満したアンモニア系ガスが外部に漏れ出し、悪臭が発生してしまうおそれがあった。 By the way, according to the above-described conventional exhaust purification device, when the storage tank becomes hot as the ambient temperature changes or the like, the urea aqueous solution stored in the storage tank causes a chemical reaction to become ammonia-based gas, and the upper space of the storage tank. Will be full. When an operator removes the injection cap of the storage tank, for example, when replenishing the urea aqueous solution, the filled ammonia-based gas leaks to the outside, and there is a possibility that a bad odor may be generated .

そこで、本発明は以上のような従来の問題点に鑑み、貯蔵タンクの上部空間内のアンモニア系ガスを吸気系又は排気系に戻すことで、貯蔵タンクの開閉時に発生する悪臭を抑制したエンジンの排気浄化装置を提供することを目的とする。 Therefore, in view of the conventional problems as described above, the present invention is an engine that suppresses malodors that occur when the storage tank is opened and closed by returning the ammonia-based gas in the upper space of the storage tank to the intake system or the exhaust system. An object is to provide an exhaust emission control device.

このため、請求項1記載の発明では、エンジン排気系に配設され、窒素酸化物をアンモニアにより還元浄化する還元触媒と、該還元触媒の排気下流に配設され、前記還元触媒を通過したアンモニアを酸化させるアンモニア酸化触媒と、前記還元触媒の排気上流に配設された噴射ノズルと、前記アンモニアへと転化する尿素水溶液を貯蔵する貯蔵タンクと、該貯蔵タンクに貯蔵された尿素水溶液を前記噴射ノズルに供給する還元剤供給装置と、前記貯蔵タンクの上部空間内のアンモニア系ガスを、前記アンモニア酸化触媒の上流にあたる吸気系又は排気系に強制的に排出する強制排出手段と、前記アンモニア酸化触媒の温度を検出する温度検出手段と、該温度検出手段により検出された温度が前記アンモニア酸化触媒の活性温度以上となったときに、前記強制排出手段を作動させる制御手段と、を含んでエンジンの排気浄化装置を構成したことを特徴とする。 Therefore, according to the first aspect of the present invention, the reduction catalyst that is disposed in the engine exhaust system and reduces and purifies nitrogen oxides with ammonia , and the ammonia that is disposed downstream of the reduction catalyst and passes through the reduction catalyst. and ammonia oxidation catalyst for oxidizing the an injection nozzle disposed in the exhaust upstream of the reduction catalyst, a storage tank for storing urea aqueous solution converted to the ammonia, the injected urea aqueous solution stored in said storage tank A reducing agent supply device for supplying to the nozzle , a forced discharge means for forcibly discharging the ammonia gas in the upper space of the storage tank to an intake system or an exhaust system upstream of the ammonia oxidation catalyst , and the ammonia oxidation catalyst a temperature detecting means for detecting the temperature of the temperature detected by the temperature detecting means is equal to or higher than the activation temperature of the ammonia oxidation catalyst In, and characterized in that an exhaust gas purifying apparatus for an engine including a control means for actuating said forced discharge means.

請求項2記載の発明では、前記制御手段は、前記強制排出手段を所定時間作動させることを特徴とする。
請求項3記載の発明では、前記強制排出手段は、前記貯蔵タンクの上部空間と前記アンモニア酸化触媒の上流にあたる吸気系又は排気系とを連通接続する配管に介装された電動ファンであることを特徴とする。
The invention according to claim 2 is characterized in that the control means operates the forced discharge means for a predetermined time.
According to a third aspect of the present invention, the forcible discharge means is an electric fan interposed in a pipe connecting the upper space of the storage tank and an intake system or an exhaust system upstream of the ammonia oxidation catalyst. Features.

請求項4記載の発明では、前記配管には、前記貯蔵タンクの上部空間内のアンモニア系ガスを吸気系又は排気系に排出する方向にのみ開弁する逆止弁が介装されたことを特徴とする。
請求項5記載の発明では、前記強制排出手段は、前記アンモニア酸化触媒の上流にあたる吸気系又は排気系に設けられたベンチュリと、前記貯蔵タンクの上部空間と前記吸気系又は排気系とを連通接続する配管に介装された開閉弁と、を含んで構成されると共に、前記制御手段は、前記温度検出手段により検出された温度が前記アンモニア酸化触媒の活性温度以上となったときに、前記開閉弁を開弁させることを特徴とする。
According to a fourth aspect of the present invention, the pipe is provided with a check valve that opens only in a direction of discharging the ammonia-based gas in the upper space of the storage tank to the intake system or the exhaust system. And
According to a fifth aspect of the present invention, the forced exhaust means communicates a venturi provided in an intake system or exhaust system upstream of the ammonia oxidation catalyst , and an upper space of the storage tank and the intake system or exhaust system. And an opening / closing valve interposed in a pipe that performs the opening / closing operation when the temperature detected by the temperature detection means is equal to or higher than the activation temperature of the ammonia oxidation catalyst. The valve is opened.

請求項6記載の発明では、前記温度検出手段は、前記アンモニア酸化触媒の上流側の排気温度を介して、該アンモニア酸化触媒の温度を間接的に検出することを特徴とする。 In the invention of claim 6, wherein said temperature detecting means, through the upstream side of the exhaust temperature of the ammonia oxidation catalyst, characterized in that to indirectly detect the temperature of the ammonia oxidation catalyst.

請求項1記載の発明によれば、エンジンの排気中に含まれる窒素酸化物は、貯蔵タンクに貯蔵された尿素水溶液を加水分解して得られるアンモニアを用いて、還元触媒において還元浄化される。また、還元触媒を通過したアンモニアは、その下流に配設されたアンモニア酸化触媒により酸化され、無害な物質に転化された後、大気中に排出される。
一方、周囲温度の変化などに伴って貯蔵タンク内の温度が上昇すると、尿素水溶液の一部が化学反応又は気化してアンモニア系ガスとなり、貯蔵タンクの上部空間に充満する。そして、エンジン運転状態が変化して排気温度が上昇した結果、アンモニア酸化触媒の温度がその活性温度以上になると、貯蔵タンクの上部空間内のアンモニア系ガスが、アンモニア酸化触媒の上流にあたる吸気系又は排気系に強制的に排出される。吸気系又は排気系に排出されたアンモニア系ガスは、還元触媒における還元浄化反応に寄与すると共に、アンモニア酸化触媒において酸化されて無害な物質に転化された後、大気中に排出される。このため、貯蔵タンクの上部空間内のアンモニア濃度が大幅に低下し、貯蔵タンクに尿素水溶液を充填しようとして注入キャップを取り外しても、作業者がアンモニアの臭いを感じ難くなり、貯蔵タンクの開閉時に発生する悪臭を低減することができる。
According to the first aspect of the present invention, nitrogen oxides contained in the exhaust of the engine are reduced and purified by the reduction catalyst using ammonia obtained by hydrolyzing the urea aqueous solution stored in the storage tank . Further, the ammonia that has passed through the reduction catalyst is oxidized by an ammonia oxidation catalyst disposed downstream thereof, converted into a harmless substance, and then discharged into the atmosphere.
On the other hand, when the temperature in the storage tank rises with a change in ambient temperature or the like, a part of the urea aqueous solution chemically reacts or vaporizes to become ammonia-based gas and fills the upper space of the storage tank. Then, as a result of the engine operating state changing and the exhaust temperature rising, when the temperature of the ammonia oxidation catalyst becomes equal to or higher than its activation temperature, the ammonia-based gas in the upper space of the storage tank is changed to the intake system upstream of the ammonia oxidation catalyst or It is forcibly discharged into the exhaust system. The ammonia-based gas discharged to the intake system or the exhaust system contributes to the reduction and purification reaction in the reduction catalyst , is oxidized in the ammonia oxidation catalyst and converted into a harmless substance, and then discharged into the atmosphere. For this reason, the ammonia concentration in the upper space of the storage tank is greatly reduced, and even if the injection cap is removed to fill the storage tank with the urea aqueous solution , it becomes difficult for the operator to feel the smell of ammonia. The malodor which generate | occur | produces can be reduced.

請求項2記載の発明によれば、貯蔵タンクの上部空間内のアンモニア系ガスは、アンモニア酸化触媒の温度がその活性温度以上になったときに、所定時間だけ吸気系又は排気系に強制的に排出される。このため、貯蔵タンクの上部空間内のアンモニア系ガスを吸気系又は排気系に強制排出するために、駆動エネルギが必要な電動ファンなどを用いていても、所定時間を適切に設定することで、本発明の効果を確保しつつ、バッテリ消耗などを抑制することができる。 According to the second aspect of the present invention, the ammonia-based gas in the upper space of the storage tank is forced to the intake system or the exhaust system for a predetermined time when the temperature of the ammonia oxidation catalyst becomes equal to or higher than its activation temperature. Discharged. For this reason, in order to forcibly discharge the ammonia-based gas in the upper space of the storage tank to the intake system or the exhaust system, even if an electric fan or the like that requires driving energy is used, by setting the predetermined time appropriately, While ensuring the effects of the present invention, battery consumption and the like can be suppressed.

請求項3記載の発明によれば、貯蔵タンクの上部空間内のアンモニア系ガスは、電動ファンにより、吸気系又は排気系に強制的に排出される。このため、複雑な機構を備えなくとも、電動ファンの作動を制御するのみで、本発明の効果を享受することができる。
請求項4記載の発明によれば、貯蔵タンクの上部空間と吸気系又は排気系とを連通接続する配管には、貯蔵タンクの上部空間内のアンモニア系ガスを排出する方向にのみ開弁する逆止弁が介装されているため、電動ファンの非作動時であっても、吸気系又は排気系を流れる流体が逆流することを防止できる。
According to the third aspect of the present invention, the ammonia gas in the upper space of the storage tank is forcibly discharged to the intake system or the exhaust system by the electric fan. For this reason, even if it does not have a complicated mechanism, the effect of the present invention can be enjoyed only by controlling the operation of the electric fan.
According to the fourth aspect of the present invention, the pipe connecting the upper space of the storage tank and the intake system or the exhaust system is reversely opened only in the direction of discharging the ammonia-based gas in the upper space of the storage tank. Since the stop valve is interposed, it is possible to prevent the fluid flowing through the intake system or the exhaust system from flowing backward even when the electric fan is not operating.

請求項5記載の発明によれば、アンモニア酸化触媒の温度がその活性温度以上になると、貯蔵タンクの上部空間と吸気系又は排気系とを連通接続する配管が開通し、ベンチュリを通過して負圧となって吸気又は排気により、貯蔵タンクの上部空間内のアンモニア系ガスが吸気系又は排気系に強制的に排出される。このため、アンモニア系ガスを強制排出するための電動ファンなどを駆動するエネルギが不要となり、バッテリ消耗などを抑制することができる。 According to the fifth aspect of the present invention, when the temperature of the ammonia oxidation catalyst becomes equal to or higher than the activation temperature, the piping that connects the upper space of the storage tank and the intake system or the exhaust system is opened and passes through the venturi to be negative. The ammonia-based gas in the upper space of the storage tank is forcibly discharged to the intake system or the exhaust system by the intake air or the exhaust gas under pressure. For this reason, energy for driving an electric fan or the like for forcibly discharging ammonia-based gas becomes unnecessary, and battery consumption and the like can be suppressed.

請求項6記載の発明によれば、アンモニア酸化触媒の温度を直接検出する代わりに、その温度と密接な関連がある上流側の排気温度を介して、アンモニア酸化触媒の温度を間接的に検出することができる。このため、熱的に不利な位置での温度検出を行う必要がなく、温度センサなどの熱的障害を低減することができる。 According to the sixth aspect of the present invention, instead of detecting the temperature of the ammonia oxidation catalyst directly, via the exhaust gas temperature on the upstream side with its temperature and closely related, to indirectly detect the temperature of the ammonia oxidation catalyst be able to. For this reason, it is not necessary to perform temperature detection at a thermally disadvantageous position, and thermal obstacles such as a temperature sensor can be reduced.

以下、添付された図面を参照して本発明を詳述する。
図1は、本発明を具現化した排気浄化装置の構成を示す。
エンジン10の排気は、排気マニフォールド12からその下流に向けて、酸化触媒14,NOx還元触媒16及びスリップ式アンモニア酸化触媒18(アンモニア酸化触媒)が夫々配設された排気管20を通過して大気中に排出される。また、NOx還元触媒16の排気上流には、貯蔵タンク22に貯蔵される尿素水溶液が、還元剤供給装置24及び噴射ノズル26を経由して、空気と共に噴射供給される。
Hereinafter, the present invention will be described in detail with reference to the accompanying drawings.
FIG. 1 shows the configuration of an exhaust emission control device embodying the present invention.
The exhaust of the engine 10 passes from the exhaust manifold 12 toward the downstream through an exhaust pipe 20 in which an oxidation catalyst 14, a NOx reduction catalyst 16, and a slip-type ammonia oxidation catalyst 18 ( ammonia oxidation catalyst ) are respectively disposed. Discharged inside. Further, the urea aqueous solution stored in the storage tank 22 is injected and supplied together with air to the upstream side of the exhaust of the NOx reduction catalyst 16 via the reducing agent supply device 24 and the injection nozzle 26 .

また、貯蔵タンク22の天壁には、その上部空間内の気体(アンモニア系ガス)を強制的に排出する電動ファン28が取り付けられると共に、尿素水溶液を補充するための注入キャップ30が着脱可能に取り付けられる。そして、電動ファン28の吐出口は、貯蔵タンク22から排出される方向にのみ開弁する逆止弁32が介装された配管34を介して、酸化触媒14とNOx還元触媒16との間に位置する排気管20に連通接続される。   In addition, an electric fan 28 for forcibly discharging the gas (ammonia-based gas) in the upper space is attached to the top wall of the storage tank 22 and an injection cap 30 for replenishing the urea aqueous solution is detachable. It is attached. The discharge port of the electric fan 28 is interposed between the oxidation catalyst 14 and the NOx reduction catalyst 16 via a pipe 34 provided with a check valve 32 that opens only in the direction of discharging from the storage tank 22. The exhaust pipe 20 is connected in communication.

一方、還元剤供給装置24及び電動ファン28の制御系として、酸化触媒14とNOx還元触媒16との間の排気管20であって、貯蔵タンク22からの配管34が接続される位置より排気上流側に、スリップ式アンモニア酸化触媒18の温度を間接的に検出すべく、排気温度を検出するための温度センサ36(温度検出手段)が取り付けられる。なお、温度センサ36の耐熱性が十分であれば、スリップ式アンモニア酸化触媒18の温度を直接検出するようにしてもよい。そして、温度センサ36からの排気温度信号は、コンピュータを内蔵した制御装置38に入力され、排気温度がスリップ式アンモニア酸化触媒18の活性温度(例えば200℃)以上になったときに、電動ファン28を所定時間作動させる。また、制御装置38は、エンジン回転速度及び燃料噴射量などのエンジン運転状態に応じて、還元剤供給装置24を制御する。   On the other hand, as a control system for the reducing agent supply device 24 and the electric fan 28, the exhaust pipe 20 between the oxidation catalyst 14 and the NOx reduction catalyst 16 and upstream of the position where the pipe 34 from the storage tank 22 is connected. On the side, a temperature sensor 36 (temperature detection means) for detecting the exhaust temperature is attached to indirectly detect the temperature of the slip type ammonia oxidation catalyst 18. If the temperature sensor 36 has sufficient heat resistance, the temperature of the slip type ammonia oxidation catalyst 18 may be directly detected. The exhaust temperature signal from the temperature sensor 36 is input to a control device 38 having a built-in computer, and when the exhaust temperature becomes equal to or higher than the activation temperature (for example, 200 ° C.) of the slip type ammonia oxidation catalyst 18, the electric fan 28. Is operated for a predetermined time. Further, the control device 38 controls the reducing agent supply device 24 in accordance with the engine operating state such as the engine rotation speed and the fuel injection amount.

なお、制御装置38では、そのROM(Read Only Memory)に記憶された制御プログラムにより、制御手段が実現される。また、電動ファン28及び配管34を含んで強制排出手段が構成される。
次に、かかる構成からなる排気浄化装置の作用について説明する。
エンジン10からの排気は、排気マニフォールド12及び排気管20を通って酸化触媒14へと導かれる。酸化触媒14では、その下流に位置するNOx還元触媒16でのNOx浄化効率を向上させるべく、排気中の一部の一酸化窒素(NO)を酸化して、二酸化窒素(NO2)に転化させる。酸化触媒14にてNOとNO2との構成比率が改善された排気は、排気管20を通ってNOx還元触媒16へと導かれる。一方、NOx還元触媒16の排気上流に位置する噴射ノズル26から、エンジン運転状態に応じた尿素水溶液が空気と共に噴射供給され、排気熱及び排気中の水蒸気により加水分解してアンモニアとなりつつ、排気と共にNOx還元触媒16へと供給される。そして、NOx還元触媒16では、アンモニアを用いた還元反応により、排気中のNOxを水及び無害なガスに転化して、NOx浄化が行われる。また、NOx還元触媒16を通過したアンモニアは、NOx還元触媒16の排気下流に位置するスリップ式アンモニア酸化触媒18により、大気中に放出しても無害な物質に転化される。
In the control device 38, control means is realized by a control program stored in a ROM (Read Only Memory). Further, a forced discharge means is configured including the electric fan 28 and the pipe 34.
Next, the operation of the exhaust emission control device having such a configuration will be described.
Exhaust gas from the engine 10 is guided to the oxidation catalyst 14 through the exhaust manifold 12 and the exhaust pipe 20. The oxidation catalyst 14 oxidizes a portion of the nitrogen monoxide (NO) in the exhaust gas to convert it into nitrogen dioxide (NO 2 ) in order to improve the NOx purification efficiency in the NOx reduction catalyst 16 located downstream thereof. . Exhaust gas in which the composition ratio of NO and NO 2 is improved by the oxidation catalyst 14 is guided to the NOx reduction catalyst 16 through the exhaust pipe 20. On the other hand, urea aqueous solution corresponding to the engine operating state is injected and supplied from the injection nozzle 26 located upstream of the NOx reduction catalyst 16 together with air, and is hydrolyzed by the exhaust heat and water vapor in the exhaust to become ammonia, together with the exhaust. It is supplied to the NOx reduction catalyst 16. In the NOx reduction catalyst 16, NOx purification is performed by converting NOx in the exhaust into water and harmless gas by a reduction reaction using ammonia. Further, the ammonia that has passed through the NOx reduction catalyst 16 is converted into a harmless substance even if released into the atmosphere by the slip ammonia oxidation catalyst 18 located downstream of the NOx reduction catalyst 16.

一方、周囲温度の変化などに伴って貯蔵タンク22内の温度が上昇すると、尿素水溶液が化学変化を起こしてアンモニア系ガスとなり、貯蔵タンク22の上部空間にアンモニア系ガスが充満する。そして、エンジン運転状態が変化して、排気温度がスリップ式アンモニア酸化触媒18の活性温度以上になると、電動ファン28が所定時間作動する。このため、貯蔵タンク22の上部空間内のアンモニア系ガスは、電動ファン28により強制的に排出され、配管34を通ってNOx還元触媒16の排気上流へと排出される。NOx還元触媒16の排気上流へと排出されたアンモニア系ガスは、NOx還元触媒16において還元反応に寄与すると共に、その下流に位置するスリップ式アンモニア酸化触媒18において酸化される。なお、電動ファン28と排気管20とを連通接続する配管34には逆止弁32が介装されているため、電動ファン28の非作動時であっても、排気管20を流れる排気が貯蔵タンク22へと逆流することが防止できる。   On the other hand, when the temperature in the storage tank 22 rises due to a change in ambient temperature or the like, the aqueous urea solution undergoes a chemical change to become ammonia-based gas, and the upper space of the storage tank 22 is filled with ammonia-based gas. When the engine operating state changes and the exhaust temperature becomes equal to or higher than the activation temperature of the slip type ammonia oxidation catalyst 18, the electric fan 28 operates for a predetermined time. For this reason, the ammonia-based gas in the upper space of the storage tank 22 is forcibly discharged by the electric fan 28 and discharged to the exhaust upstream of the NOx reduction catalyst 16 through the pipe 34. The ammonia-based gas discharged upstream of the NOx reduction catalyst 16 contributes to the reduction reaction in the NOx reduction catalyst 16 and is oxidized in the slip-type ammonia oxidation catalyst 18 located downstream thereof. Since the check valve 32 is interposed in the pipe 34 that connects the electric fan 28 and the exhaust pipe 20 in communication, the exhaust flowing through the exhaust pipe 20 is stored even when the electric fan 28 is not operating. Backflow to the tank 22 can be prevented.

従って、スリップ式アンモニア酸化触媒18が活性温度以上になるたびに、貯蔵タンク22の上部空間内のアンモニア系ガスがNOx還元触媒16の上流側に強制的に排出されるので、そこに残留するアンモニア濃度が大幅に低下する。このため、尿素水溶液を補充しようとして注入キャップ30を取り外しても、アンモニア濃度が低いことから、作業者がアンモニア臭を感じ難くなり、貯蔵タンク22の開閉時に発生する悪臭を低減することができる。   Therefore, every time the slip type ammonia oxidation catalyst 18 becomes higher than the activation temperature, the ammonia gas in the upper space of the storage tank 22 is forcibly discharged to the upstream side of the NOx reduction catalyst 16, so that the ammonia remaining there Concentration is greatly reduced. For this reason, even if the injection cap 30 is removed in order to replenish the urea aqueous solution, the ammonia concentration is low, so that it is difficult for the operator to feel the ammonia odor, and the bad odor generated when the storage tank 22 is opened and closed can be reduced.

なお、上記実施形態における電動ファン28に代えて、図2に示すように、NOx還元触媒16の上流側の排気管20にベンチュリ40を設け、ここに貯蔵タンク22の上部空間内のアンモニア系ガスを排出するようにしてもよい。この場合には、配管34に常閉式の電磁開閉弁42を介装し、電動ファン28を作動させるタイミングで電磁開閉弁42を開弁させるようにすればよい。このようにすれば、ベンチュリ40を通過して負圧となった排気により、貯蔵タンク22の上部空間内のアンモニア系ガスが強制的に排出されるので、電動ファン28を駆動するためのエネルギが不要となり、バッテリ消耗などを抑制することができる。   Instead of the electric fan 28 in the above embodiment, as shown in FIG. 2, a venturi 40 is provided in the exhaust pipe 20 upstream of the NOx reduction catalyst 16, and the ammonia gas in the upper space of the storage tank 22 is provided here. May be discharged. In this case, a normally closed electromagnetic opening / closing valve 42 may be interposed in the pipe 34 so that the electromagnetic opening / closing valve 42 is opened at the timing when the electric fan 28 is operated. In this way, the ammonia gas in the upper space of the storage tank 22 is forcibly discharged by the exhaust gas that has passed through the venturi 40 and has a negative pressure, so that energy for driving the electric fan 28 is increased. This eliminates the need for battery consumption.

また、上記実施形態においては、貯蔵タンク22の上部空間内のアンモニア系ガスをNOx還元触媒16の排気上流に排出する構成を採用したが、スリップ式アンモニア触媒18の上流であれば、吸気系及び排気系の任意の場所にアンモニア系ガスを排出するようにしてもよい。   Further, in the above embodiment, the configuration in which the ammonia-based gas in the upper space of the storage tank 22 is discharged upstream of the NOx reduction catalyst 16 is adopted, but if it is upstream of the slip type ammonia catalyst 18, the intake system and You may make it discharge | emit ammonia-type gas to the arbitrary places of an exhaust system.

本発明を具現化した排気浄化装置の第1実施形態の構成図1 is a configuration diagram of a first embodiment of an exhaust emission control device embodying the present invention. 本発明を具現化した排気浄化装置の第2実施形態の構成図The block diagram of 2nd Embodiment of the exhaust gas purification device which actualized this invention

符号の説明Explanation of symbols

10 エンジン
16 NOx還元触媒
18 スリップ式アンモニア酸化触媒
20 排気管
22 貯蔵タンク
24 還元剤供給装置
26 噴射ノズル
28 電動ファン
32 逆止弁
34 配管
36 温度センサ
38 制御装置
40 ベンチュリ
42 電磁開閉弁
DESCRIPTION OF SYMBOLS 10 Engine 16 NOx reduction catalyst 18 Slip-type ammonia oxidation catalyst 20 Exhaust pipe 22 Storage tank 24 Reducing agent supply apparatus
26 Injection nozzle 28 Electric fan 32 Check valve 34 Piping 36 Temperature sensor 38 Control device 40 Venturi 42 Electromagnetic on-off valve

Claims (6)

エンジン排気系に配設され、窒素酸化物をアンモニアにより還元浄化する還元触媒と、
該還元触媒の排気下流に配設され、前記還元触媒を通過したアンモニアを酸化させるアンモニア酸化触媒と、
前記還元触媒の排気上流に配設された噴射ノズルと、
前記アンモニアへと転化する尿素水溶液を貯蔵する貯蔵タンクと、
該貯蔵タンクに貯蔵された尿素水溶液を前記噴射ノズルに供給する還元剤供給装置と、
前記貯蔵タンクの上部空間内のアンモニア系ガスを、前記アンモニア酸化触媒の上流にあたる吸気系又は排気系に強制的に排出する強制排出手段と、
前記アンモニア酸化触媒の温度を検出する温度検出手段と、
該温度検出手段により検出された温度が前記アンモニア酸化触媒の活性温度以上となったときに、前記強制排出手段を作動させる制御手段と、
を含んで構成されたことを特徴とするエンジンの排気浄化装置。
A reduction catalyst disposed in the engine exhaust system for reducing and purifying nitrogen oxides with ammonia ;
An ammonia oxidation catalyst disposed downstream of the reduction catalyst and oxidizing the ammonia that has passed through the reduction catalyst;
An injection nozzle disposed upstream of the exhaust of the reduction catalyst;
A storage tank for storing an aqueous urea solution that is converted to ammonia ;
A reducing agent supply device for supplying an aqueous urea solution stored in the storage tank to the injection nozzle ;
Forcibly discharging means for forcibly discharging the ammonia gas in the upper space of the storage tank to an intake system or an exhaust system upstream of the ammonia oxidation catalyst ;
Temperature detecting means for detecting the temperature of the ammonia oxidation catalyst ;
Control means for operating the forced discharge means when the temperature detected by the temperature detection means is equal to or higher than the activation temperature of the ammonia oxidation catalyst ;
An exhaust emission control device for an engine characterized by comprising:
前記制御手段は、前記強制排出手段を所定時間作動させることを特徴とする請求項1記載のエンジンの排気浄化装置。   2. The engine exhaust gas purification apparatus according to claim 1, wherein the control means operates the forced exhaust means for a predetermined time. 前記強制排出手段は、前記貯蔵タンクの上部空間と前記アンモニア酸化触媒の上流にあたる吸気系又は排気系とを連通接続する配管に介装された電動ファンであることを特徴とする請求項1又は請求項2に記載のエンジンの排気浄化装置。 The said forced discharge means is an electric fan interposed in a pipe connecting the upper space of the storage tank and an intake system or an exhaust system upstream of the ammonia oxidation catalyst. Item 3. An exhaust emission control device for an engine according to Item 2. 前記配管には、前記貯蔵タンクの上部空間内のアンモニア系ガスを吸気系又は排気系に排出する方向にのみ開弁する逆止弁が介装されたことを特徴とする請求項3記載のエンジンの排気浄化装置。 4. The engine according to claim 3, wherein the pipe is provided with a check valve that opens only in a direction in which ammonia-based gas in the upper space of the storage tank is discharged to an intake system or an exhaust system. Exhaust purification equipment. 前記強制排出手段は、前記アンモニア酸化触媒の上流にあたる吸気系又は排気系に設けられたベンチュリと、前記貯蔵タンクの上部空間と前記吸気系又は排気系とを連通接続する配管に介装された開閉弁と、を含んで構成されると共に、
前記制御手段は、前記温度検出手段により検出された温度が前記アンモニア酸化触媒の活性温度以上となったときに、前記開閉弁を開弁させることを特徴とする請求項1又は請求項2に記載のエンジンの排気浄化装置。
The forced exhaust means is an open / close unit interposed in a pipe connecting the venturi provided in the intake system or exhaust system upstream of the ammonia oxidation catalyst and the upper space of the storage tank and the intake system or exhaust system. And a valve,
The said control means opens the said on-off valve when the temperature detected by the said temperature detection means becomes more than the activation temperature of the said ammonia oxidation catalyst , The open / close valve is characterized by the above-mentioned. Engine exhaust purification system.
前記温度検出手段は、前記アンモニア酸化触媒の上流側の排気温度を介して、該アンモニア酸化触媒の温度を間接的に検出することを特徴とする請求項1〜請求項5のいずれか1つに記載のエンジンの排気浄化装置。 Said temperature detecting means, through the upstream side of the exhaust temperature of the ammonia oxidation catalyst, any one of claims 1 to 5, characterized in that to indirectly detect the temperature of the ammonia oxidation catalyst The engine exhaust gas purification apparatus as described.
JP2003339246A 2003-09-19 2003-09-30 Engine exhaust purification system Expired - Fee Related JP4166655B2 (en)

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JP2003339246A JP4166655B2 (en) 2003-09-30 2003-09-30 Engine exhaust purification system
US10/572,558 US7849674B2 (en) 2003-09-19 2004-09-02 Exhaust emission purifying apparatus for engine
EP04787623A EP1669567B1 (en) 2003-09-19 2004-09-02 Exhaust gas purification device of engine
EP11191519.5A EP2426328B1 (en) 2003-09-19 2004-09-02 Exhaust gas purification device of engine
PCT/JP2004/012743 WO2005028826A1 (en) 2003-09-19 2004-09-02 Exhaust gas purification device of engine
EP11191521.1A EP2426329B1 (en) 2003-09-19 2004-09-02 Exhaust gas purification device of engine

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