JP2020041428A - Post-exhaust treatment device - Google Patents

Post-exhaust treatment device Download PDF

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JP2020041428A
JP2020041428A JP2018166850A JP2018166850A JP2020041428A JP 2020041428 A JP2020041428 A JP 2020041428A JP 2018166850 A JP2018166850 A JP 2018166850A JP 2018166850 A JP2018166850 A JP 2018166850A JP 2020041428 A JP2020041428 A JP 2020041428A
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exhaust
exhaust gas
urea
gas temperature
urea water
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長岡 大治
Taiji Nagaoka
大治 長岡
隆行 坂本
Takayuki Sakamoto
隆行 坂本
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Isuzu Motors Ltd
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    • 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
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Abstract

To provide a post-exhaust treatment device capable of suppressing nitrogen oxide slip right after engine start.SOLUTION: To solve the problem, the post-exhaust treatment device includes: a first urea SCR 102 installed in an exhaust pipe 112 of an engine 101, an exhaust emission control catalyst 103 arranged on the exhaust downstream side of the first urea SCR 102; a second urea SCR 105 arranged on the exhaust downstream side of the exhaust emission control catalyst 103; a first urea water injector 106 arranged on the exhaust upstream side of the first urea SCR 102; a first exhaust temperature detector 107 arranged between the first urea SCR 102 and the exhaust emission control catalyst 103; a second urea water injector 108 arranged between the exhaust emission control catalyst 103 and the second urea SCR 105; and a second exhaust temperature detector 109 arranged between the exhaust emission control catalyst 103 and the second urea SCR 105.SELECTED DRAWING: Figure 1

Description

エンジンの排気を浄化する排気後処理装置に関する。   The present invention relates to an exhaust aftertreatment device for purifying exhaust of an engine.

尿素SCR又はLNTを備える排気後処理装置が知られている。   Exhaust aftertreatment devices comprising urea SCR or LNT are known.

尿素SCRを備える排気後処理装置では、エンジンの窒素酸化物排出量を推定又は検出し、窒素酸化物排出量に応じ尿素水を尿素SCRに供給し、排気熱で尿素水をアンモニアに加水分解し、アンモニアで窒素酸化物を還元する。   The exhaust aftertreatment device provided with the urea SCR estimates or detects the nitrogen oxide emission of the engine, supplies urea water to the urea SCR according to the nitrogen oxide emission, and hydrolyzes the urea water to ammonia with the exhaust heat. To reduce nitrogen oxides with ammonia.

尿素SCRを備える排気後処理装置では、アンモニア吸蔵制御を実行する事が一般的になっている。アンモニア吸蔵制御では、アンモニアを尿素SCRに吸蔵させておく事で排気温度が低い時の窒素酸化物浄化率を上昇させる事が出来る。   In an exhaust after-treatment device provided with a urea SCR, it is common to execute ammonia storage control. In the ammonia storage control, the nitrogen oxide purification rate when the exhaust gas temperature is low can be increased by storing ammonia in the urea SCR.

LNTを備える排気後処理装置では、リーン運転時に窒素酸化物を吸蔵し、リッチ運転時に窒素酸化物を還元する。   An exhaust aftertreatment device equipped with an LNT stores nitrogen oxides during lean operation and reduces nitrogen oxides during rich operation.

特に、近年の排気規制の強化に伴い、尿素SCRとLNTとを併用する事で排気温度が高い時も低い時も窒素酸化物を浄化する事が出来る排気後処理装置が開発されている。   In particular, with the recent tightening of exhaust regulations, exhaust aftertreatment devices have been developed that can purify nitrogen oxides when the exhaust temperature is high or low by using urea SCR and LNT together.

特開2011−220115号公報JP 2011-220115 A 特開2013−117191号公報JP 2013-117191 A

然し乍ら、尿素SCRとLNTとを併用する排気後処理装置でも、エンジン始動直後は、LNTの窒素酸化物吸蔵量に限界が有り、尿素SCRが活性化温度に至る迄は窒素酸化物スリップが発生する虞が有る。   However, even in an exhaust aftertreatment device using both urea SCR and LNT, immediately after the engine is started, the amount of nitrogen oxide stored in the LNT is limited, and a nitrogen oxide slip occurs until the urea SCR reaches the activation temperature. There is a fear.

エンジン暖気制御を実行したり、電気ヒータやバーナで尿素SCRを加熱したりする事も考えられるものの、何れも燃費やコストとのトレードオフに成る。   Although it is conceivable to execute the engine warm-up control or to heat the urea SCR with an electric heater or a burner, any of these is a trade-off between fuel efficiency and cost.

以上の事情に鑑み、エンジン始動直後の窒素酸化物スリップを抑制する事が出来る排気後処理装置を提供する事を目的とする。   In view of the above circumstances, an object of the present invention is to provide an exhaust after-treatment device capable of suppressing a nitrogen oxide slip immediately after starting an engine.

エンジンの排気を浄化する排気後処理装置に於いて、前記エンジンの排気管に設置される第1の尿素SCRと、前記排気管に設置され、前記第1の尿素SCRの排気下流側に配置された排気浄化触媒と、前記排気管に設置され、前記排気浄化触媒の排気下流側に配置された第2の尿素SCRと、前記排気管に設置され、前記第1の尿素SCRの排気上流側に配置された第1の尿素水噴射器と、前記排気管に設置され、前記第1の尿素SCRと前記排気浄化触媒との間に配置された第1の排気温度検出器と、前記排気管に設置され、前記排気浄化触媒と前記第2の尿素SCRとの間に配置された第2の尿素水噴射器と、前記排気管に設置され、前記排気浄化触媒と前記第2の尿素SCRとの間に配置された第2の排気温度検出器と、を備える排気後処理装置を提供する。   In an exhaust aftertreatment device for purifying the exhaust of an engine, a first urea SCR installed in an exhaust pipe of the engine and an exhaust downstream side of the first urea SCR installed in the exhaust pipe are provided. An exhaust purification catalyst, a second urea SCR installed in the exhaust pipe and disposed downstream of the exhaust purification catalyst, and a second urea SCR installed in the exhaust pipe and exhaust upstream of the first urea SCR. A first urea water injector disposed therein, a first exhaust temperature detector disposed on the exhaust pipe, disposed between the first urea SCR and the exhaust purification catalyst, A second urea water injector disposed between the exhaust purification catalyst and the second urea SCR; and a second urea water injector disposed in the exhaust pipe, the second urea water injector being disposed between the exhaust purification catalyst and the second urea SCR. A second exhaust gas temperature sensor disposed therebetween. Providing post-processing apparatus.

前記第1の排気温度検出器で検出された排気温度が第1の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させ、前記第2の排気温度検出器で検出された排気温度が前記第1の閾値排気温度よりも高い第2の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させつつ、前記エンジンでポスト噴射を実行させ、前記第2の排気温度検出器で検出された排気温度が前記第2の閾値排気温度よりも高い第3の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させると共に、前記エンジンでポスト噴射を実行させつつ、前記第2の尿素水噴射器で尿素水を前記第2の尿素SCRに供給させる制御装置を更に備える事が望ましい。   When the exhaust gas temperature detected by the first exhaust gas temperature detector is equal to or lower than a first threshold exhaust gas temperature, the first urea water injector supplies urea water to the first urea SCR; When the exhaust gas temperature detected by the second exhaust gas temperature detector is equal to or lower than a second threshold exhaust gas temperature higher than the first threshold exhaust gas temperature, the first urea water injector supplies the first urea water injector with the first urea water. When the engine performs post-injection while supplying to the urea SCR, and the exhaust temperature detected by the second exhaust temperature detector is equal to or lower than a third threshold exhaust temperature higher than the second threshold exhaust temperature. The urea water is supplied to the first urea SCR by the first urea water injector, and the urea water is supplied to the second urea water injector by the second urea water injector while the engine performs post-injection. May be further equipped with a control device for supplying the urea SCR Masui.

前記排気管に設置され、前記第1の尿素SCRと前記排気浄化触媒との間に配置された炭化水素噴射器を更に備え、前記第1の排気温度検出器で検出された排気温度が第1の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させ、前記第2の排気温度検出器で検出された排気温度が前記第1の閾値排気温度よりも高い第2の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させつつ、前記炭化水素噴射器で炭化水素を前記排気浄化触媒に供給させ、前記第2の排気温度検出器で検出された排気温度が前記第2の閾値排気温度よりも高い第3の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させると共に、前記炭化水素噴射器で炭化水素を前記排気浄化触媒に供給させつつ、前記第2の尿素水噴射器で尿素水を前記第2の尿素SCRに供給させる制御装置を更に備える事が望ましい。   A hydrocarbon injector disposed in the exhaust pipe and disposed between the first urea SCR and the exhaust gas purification catalyst, wherein the exhaust gas temperature detected by the first exhaust gas temperature detector is equal to the first exhaust gas temperature. Urea water is supplied to the first urea SCR by the first urea water injector when the exhaust gas temperature detected by the second exhaust temperature detector is lower than the first exhaust gas temperature. When the temperature is equal to or lower than a second threshold exhaust temperature higher than the threshold exhaust temperature, the urea water is supplied to the first urea SCR by the first urea water injector, and the hydrocarbon is injected by the hydrocarbon injector into the first urea SCR. The first urea water injection is performed when the exhaust gas is supplied to an exhaust purification catalyst and the exhaust temperature detected by the second exhaust temperature detector is equal to or lower than a third threshold exhaust temperature higher than the second threshold exhaust temperature. Urea water is supplied to the first urea SCR by the While the hydrocarbons in the hydrocarbon injector is supplied to the exhaust gas purifying catalyst, it is desirable to further comprise a control device for supplying urea water to the second urea SCR in the second urea water injector.

前記第1の尿素SCRと前記第2の尿素SCRは、ゼオライトを含む事が望ましい。   It is desirable that the first urea SCR and the second urea SCR include zeolite.

前記排気浄化触媒は、酸化触媒とNOX吸蔵還元型触媒の一方又は両方を備える事が望ましい。 The exhaust gas purifying catalyst, it is desirable to provide one or both of the oxidation catalyst and the NO X storage reduction catalyst.

エンジン始動直後の窒素酸化物スリップを抑制する事が出来る排気後処理装置を提供する事が可能に成る。   It is possible to provide an exhaust after-treatment device capable of suppressing a nitrogen oxide slip immediately after starting the engine.

実施の形態に係る排気後処理装置の構造を説明する図である。It is a figure explaining the structure of the exhaust after-treatment device concerning an embodiment. 実施の形態に係る排気後処理装置の動作を説明する図である。It is a figure explaining operation of an exhaust after-treatment device concerning an embodiment. 実施の形態に係る排気後処理装置の効果を説明する図である。It is a figure explaining the effect of the exhaust aftertreatment device concerning an embodiment.

以下、実施の形態を添付図面に順って説明する。   Hereinafter, embodiments will be described with reference to the accompanying drawings.

図1に示す様に、実施の形態に係る排気後処理装置100は、エンジン(例えば、ディーゼルエンジン)101の排気を浄化する装置であって、第1のNOX選択還元型触媒(Selective Catalytic Reduction:以下「尿素SCR」という)102と、排気浄化触媒103と、微粒子捕集フィルタ(Catalyzed Soot Filter:以下「CSF」という)104と、第2の尿素SCR105と、第1の尿素水噴射器106と、第1の排気温度検出器107と、第2の尿素水噴射器108と、第2の排気温度検出器109と、炭化水素噴射器110と、制御装置111と、を備える。尚、制御装置111は、例えば、ECU(Engine Control Unit)やDCU(Dosing Control Unit)等で構成される。 As shown in FIG. 1, the exhaust post-treatment device 100 according to the embodiment, the engine (e.g., diesel engines) An apparatus for purifying the exhaust 101, the first of the NO X selective reduction catalyst (S elective C atalytic R eduction: follows) 102 of "urea SCR", and the exhaust gas purifying catalyst 103, particulate collection filter (C atalyzed S oot F ilter: follows) 104 called "CSF", and the second urea SCR105, first Urea water injector 106, a first exhaust gas temperature detector 107, a second urea water injector 108, a second exhaust gas temperature detector 109, a hydrocarbon injector 110, a control device 111, Is provided. The control unit 111 is composed of, for example, a ECU (E ngine C ontrol U nit ) and DCU (D osing C ontrol U nit ) and the like.

第1の尿素SCR102は、エンジン101の排気管112に設置される。第1の尿素SCR102は、ゼオライトを含む。ゼオライトは、水を吸着する際に発熱する(吸着熱を生成する)。従って、第1の尿素SCR102は、排気に含まれる水を利用する事で排気温度を上昇させる。第1の尿素SCR102は、水吸着効率(発熱効率)に特化され、発熱機能を主機能とする。   The first urea SCR 102 is installed in an exhaust pipe 112 of the engine 101. The first urea SCR 102 contains zeolite. The zeolite generates heat (adsorbs heat of adsorption) when adsorbing water. Therefore, the first urea SCR 102 raises the exhaust gas temperature by using the water contained in the exhaust gas. The first urea SCR 102 is specialized in water adsorption efficiency (heat generation efficiency) and has a heat generation function as a main function.

排気浄化触媒103は、排気管112に設置され、第1の尿素SCR102の排気下流側に配置される。排気浄化触媒103は、排気上流側の一部にゼオライトが担持され、第1の尿素SCR102と同様に、排気に含まれる水を利用する事で排気温度を上昇させる。排気浄化触媒103は、酸化触媒(Diesel Oxidation Catalyst:以下「DOC」という)とNOX吸蔵還元型触媒(Lean NOX Trap:以下「LNT」という)の一方を備える事も出来るし、DOCとLNTの両方を備える事も出来る。DOCとLNTの両方を備える場合は、DOCが排気上流側に配置され、LNTが排気下流側に配置される。DOCは、一酸化炭素を二酸化炭素に酸化すると共に炭化水素を二酸化炭素と水とに還元する。LNTは、リーン運転時に一酸化窒素を二酸化窒素に酸化すると共に二酸化窒素を吸蔵し、リッチ運転時に二酸化窒素を放出すると共に二酸化窒素を窒素と水と二酸化炭素とに還元する。排気浄化触媒103は、炭化水素や一酸化炭素を酸化する際に発熱する(酸化熱を生成する)。従って、炭化水素や一酸化炭素を排気浄化触媒103に供給する事で排気温度を上昇させる事が出来る。 The exhaust purification catalyst 103 is provided in the exhaust pipe 112 and is disposed downstream of the first urea SCR 102 in exhaust gas. In the exhaust gas purification catalyst 103, zeolite is carried on a part of the exhaust gas upstream side, and similarly to the first urea SCR 102, the temperature of the exhaust gas is raised by using water contained in the exhaust gas. Exhaust gas purifying catalyst 103, an oxidation catalyst (D iesel O xidation C atalyst: hereinafter "DOC") and the NO X storage reduction catalyst: also comprising one (L ean N O X T rap hereinafter referred to as "LNT") Yes, it can have both DOC and LNT. When both the DOC and the LNT are provided, the DOC is arranged on the exhaust upstream side, and the LNT is arranged on the exhaust downstream side. DOC oxidizes carbon monoxide to carbon dioxide and reduces hydrocarbons to carbon dioxide and water. The LNT oxidizes nitrogen monoxide to nitrogen dioxide and occludes nitrogen dioxide during lean operation, releases nitrogen dioxide during rich operation, and reduces nitrogen dioxide to nitrogen, water and carbon dioxide. The exhaust purification catalyst 103 generates heat when oxidizing hydrocarbons and carbon monoxide (generates heat of oxidation). Therefore, the exhaust gas temperature can be increased by supplying hydrocarbons and carbon monoxide to the exhaust gas purifying catalyst 103.

CSF104は、排気に含まれる煤を捕集する。CSF104の排気上流側にDOCを配置する事で二酸化窒素や熱量をCSF104に効率的に供給する事が出来る為、煤の燃焼を促進させる事が可能に成る。   The CSF 104 collects soot contained in the exhaust gas. By arranging the DOC upstream of the exhaust of the CSF 104, nitrogen dioxide and heat can be efficiently supplied to the CSF 104, so that the combustion of soot can be promoted.

第2の尿素SCR105は、排気管112に設置され、排気浄化触媒103の排気下流側に配置される。第2の尿素SCR105は、第1の尿素SCR102と同様に、ゼオライトを含む。第2の尿素SCR105は、第1の尿素SCR102よりも体積(容積)が大きい。第2の尿素SCR105は、アンモニアで一酸化窒素と二酸化窒素とを窒素と水とに還元する。第2の尿素SCR105は、第1の尿素SCR102と異なり、排気浄化効率に特化され、排気浄化機能を主機能とする。   The second urea SCR 105 is provided in the exhaust pipe 112 and is arranged on the exhaust gas downstream side of the exhaust purification catalyst 103. The second urea SCR 105 contains zeolite, like the first urea SCR 102. The second urea SCR 105 has a larger volume than the first urea SCR 102. The second urea SCR 105 reduces nitric oxide and nitrogen dioxide with ammonia to nitrogen and water. Unlike the first urea SCR 102, the second urea SCR 105 is specialized in exhaust purification efficiency and has an exhaust purification function as a main function.

第1の尿素水噴射器106は、排気管112に設置され、第1の尿素SCR102の排気上流側に配置される。第1の尿素水噴射器106は、尿素水を第1の尿素SCR102に供給する。第1の尿素水噴射器106は、制御装置111で制御される。   The first urea water injector 106 is installed in the exhaust pipe 112 and is arranged on the exhaust upstream side of the first urea SCR 102. The first urea water injector 106 supplies urea water to the first urea SCR 102. The first urea water injector 106 is controlled by the control device 111.

第1の排気温度検出器107は、排気管112に設置され、第1の尿素SCR102と排気浄化触媒103との間に配置される。第1の排気温度検出器107は、第1の尿素SCR102と排気浄化触媒103との間の排気温度を検出する。第1の排気温度検出器107で検出された排気温度は、制御装置111に入力される。   The first exhaust gas temperature detector 107 is installed in the exhaust pipe 112 and is disposed between the first urea SCR 102 and the exhaust gas purification catalyst 103. The first exhaust gas temperature detector 107 detects an exhaust gas temperature between the first urea SCR 102 and the exhaust gas purifying catalyst 103. The exhaust gas temperature detected by the first exhaust gas temperature detector 107 is input to the control device 111.

第2の尿素水噴射器108は、排気管112に設置され、排気浄化触媒103と第2の尿素SCR105との間に配置される。第2の尿素水噴射器108は、窒素酸化物排出量に応じ尿素水を第2の尿素SCR105に供給する。窒素酸化物排出量は、エンジン回転数や燃料供給量を基に推定されるか、又は窒素酸化物濃度検出器で検出される。第2の尿素SCR105に供給された尿素水は、排気熱でアンモニアに加水分解される。第2の尿素水噴射器108は、制御装置111で制御される。   The second urea water injector 108 is provided in the exhaust pipe 112 and is disposed between the exhaust purification catalyst 103 and the second urea SCR 105. The second urea water injector 108 supplies urea water to the second urea SCR 105 according to the amount of nitrogen oxide discharged. The nitrogen oxide emission amount is estimated based on the engine speed and the fuel supply amount, or detected by a nitrogen oxide concentration detector. The urea water supplied to the second urea SCR 105 is hydrolyzed to ammonia by exhaust heat. The second urea water injector 108 is controlled by the control device 111.

第2の排気温度検出器109は、排気管112に設置され、排気浄化触媒103と第2の尿素SCR105との間に配置される。第2の排気温度検出器109は、排気浄化触媒103と第2の尿素SCR105との間の排気温度を検出する。第2の排気温度検出器109で検出された排気温度は、制御装置111に入力される。   The second exhaust gas temperature detector 109 is installed in the exhaust pipe 112 and is disposed between the exhaust gas purifying catalyst 103 and the second urea SCR 105. The second exhaust gas temperature detector 109 detects an exhaust gas temperature between the exhaust gas purifying catalyst 103 and the second urea SCR 105. The exhaust gas temperature detected by the second exhaust gas temperature detector 109 is input to the control device 111.

炭化水素噴射器110は、排気管112に設置され、第1の尿素SCR102と排気浄化触媒103との間に配置される。炭化水素噴射器110は、炭化水素(未燃燃料)を排気浄化触媒103に供給する。炭化水素噴射器110は、制御装置111で制御される。   The hydrocarbon injector 110 is provided in the exhaust pipe 112 and is disposed between the first urea SCR 102 and the exhaust purification catalyst 103. The hydrocarbon injector 110 supplies a hydrocarbon (unburned fuel) to the exhaust purification catalyst 103. The hydrocarbon injector 110 is controlled by the control device 111.

制御装置111は、第1の排気温度検出器107で検出された排気温度が第1の閾値排気温度(例えば、150℃)以下の場合に、第1の尿素水噴射器106で尿素水を第1の尿素SCR102に供給させる。尿素水を第1の尿素SCR102に供給する事で尿素水に含まれる水を第1の尿素SCR102に吸着させる事が出来る為、排気温度を上昇させる事が可能に成る。尿素水を第1のSCR102に供給する際は、例えば、エンジン回転数や燃料供給量を基に排気に含まれる水量(第1のSCR102に吸着される水量)を推定し、該水量に応じ第1のSCR102の発熱量を推定し、該発熱量を最大にするべく、尿素水供給量を調整する。尚、エンジン回転数や燃料供給量を基に排気に含まれる標準水量を推定し、該標準水量を外気温度や外気湿度で補正する事で排気に含まれる水量を高精度に推定する事が出来る。   When the exhaust gas temperature detected by the first exhaust gas temperature detector 107 is equal to or lower than a first threshold exhaust gas temperature (for example, 150 ° C.), the control device 111 controls the first urea water injector 106 to remove urea water. One urea SCR 102 is supplied. By supplying the urea water to the first urea SCR 102, the water contained in the urea water can be adsorbed on the first urea SCR 102, so that the exhaust gas temperature can be raised. When supplying urea water to the first SCR 102, for example, the amount of water contained in the exhaust gas (the amount of water adsorbed by the first SCR 102) is estimated based on the engine speed and the amount of fuel supply, and the urea water is supplied in accordance with the amount of water. The calorific value of the first SCR 102 is estimated, and the urea water supply amount is adjusted to maximize the calorific value. In addition, the amount of water contained in the exhaust gas can be estimated with high accuracy by estimating the standard water amount contained in the exhaust gas based on the engine speed and the fuel supply amount and correcting the standard water amount with the outside air temperature and the outside air humidity. .

制御装置111は、第2の排気温度検出器109で検出された排気温度が第1の閾値排気温度よりも高い第2の閾値排気温度(例えば、180℃)以下の場合に、第1の尿素水噴射器106で尿素水を第1の尿素SCR102に供給させつつ、エンジン101(の燃料噴射器)でポスト噴射を実行させる。ポスト噴射を実行する事で炭化水素や一酸化炭素を排気浄化触媒103に供給すると共に排気浄化触媒103で炭化水素や一酸化炭素を酸化させる事が出来る為、排気温度を上昇させる事が可能に成る。   When the exhaust gas temperature detected by the second exhaust gas temperature detector 109 is equal to or lower than a second threshold exhaust gas temperature (for example, 180 ° C.) higher than the first threshold exhaust gas temperature, the controller 111 While the urea water is supplied to the first urea SCR 102 by the water injector 106, the post-injection is executed by (the fuel injector of) the engine 101. By executing the post injection, hydrocarbons and carbon monoxide can be supplied to the exhaust purification catalyst 103 and the hydrocarbons and carbon monoxide can be oxidized by the exhaust purification catalyst 103, so that the exhaust temperature can be increased. Become.

制御装置111は、第2の排気温度検出器109で検出された排気温度が第2の閾値排気温度以下の場合に、ポスト噴射に代え又は加え、炭化水素噴射器110で炭化水素を排気浄化触媒103に供給させる事が出来る。炭化水素を排気浄化触媒103に供給する事で排気浄化触媒103で炭化水素を酸化させる事が出来る為、排気温度を上昇させる事が可能に成る。炭化水素を排気浄化触媒103に供給する際は、例えば、エンジン回転数や燃料供給量を基に排気に含まれる炭化水素量(排気浄化触媒103に供給される炭化水素量)を推定し、該炭化水素量に応じ排気浄化触媒103の酸化発熱量を推定し、該酸化発熱量を最大にするべく、炭化水素供給量を調整する。   When the exhaust gas temperature detected by the second exhaust gas temperature detector 109 is equal to or lower than the second threshold exhaust gas temperature, the control device 111 replaces or adds to post-injection and uses the hydrocarbon injector 110 to remove hydrocarbons from the exhaust purification catalyst. 103 can be supplied. By supplying hydrocarbons to the exhaust purification catalyst 103, the hydrocarbons can be oxidized by the exhaust purification catalyst 103, so that the exhaust gas temperature can be raised. When supplying hydrocarbons to the exhaust purification catalyst 103, for example, the amount of hydrocarbons contained in exhaust gas (the amount of hydrocarbons supplied to the exhaust purification catalyst 103) is estimated based on the engine speed and the amount of fuel supplied, and The amount of heat generated by oxidation of the exhaust purification catalyst 103 is estimated according to the amount of hydrocarbons, and the amount of hydrocarbon supplied is adjusted so as to maximize the amount of heat generated by oxidation.

制御装置111は、第2の排気温度検出器109で検出された排気温度が第2の閾値排気温度よりも高い第3の閾値排気温度(例えば、200℃)以下の場合に、第1の尿素水噴射器106で尿素水を第1の尿素SCR102に供給させると共に、エンジン101でポスト噴射を実行させ、及び/又は炭化水素噴射器110で炭化水素を排気浄化触媒103に供給させつつ、第2の尿素水噴射器108で尿素水を第2の尿素SCR105に供給させる。第3の閾値排気温度は、第2の尿素SCR105の活性化温度を意味する。尿素水を第2の尿素SCR105に供給する事で尿素水に含まれる水を第2の尿素SCR105に吸着させる事が出来る為、排気温度を上昇させる事が可能に成る。   When the exhaust gas temperature detected by the second exhaust gas temperature detector 109 is equal to or lower than a third threshold exhaust gas temperature (for example, 200 ° C.) higher than the second threshold exhaust gas temperature, the control device 111 While the urea water is supplied to the first urea SCR 102 by the water injector 106, post injection is performed by the engine 101, and / or the hydrocarbon is supplied to the exhaust purification catalyst 103 by the hydrocarbon injector 110, The urea water is supplied to the second urea SCR 105 by the urea water injector 108. The third threshold exhaust temperature means the activation temperature of the second urea SCR 105. By supplying the urea water to the second urea SCR 105, the water contained in the urea water can be adsorbed on the second urea SCR 105, so that the exhaust gas temperature can be raised.

制御装置111は、第2の排気温度検出器109で検出された排気温度が第3の閾値排気温度超の場合に、ポスト噴射の実行や炭化水素の供給を停止し、通常の(従来の)排気浄化制御を実行する。排気浄化制御では、規定の排気浄化率が達成される様に、窒素酸化物排出量に応じ尿素水を第2の尿素SCR105に供給する。   When the exhaust gas temperature detected by the second exhaust gas temperature detector 109 is higher than the third threshold exhaust gas temperature, the control device 111 stops the execution of post-injection and the supply of hydrocarbons, and performs the normal (conventional) operation. Execute exhaust gas purification control. In the exhaust gas purification control, urea water is supplied to the second urea SCR 105 according to the nitrogen oxide emission amount so that a specified exhaust gas purification rate is achieved.

以上を纏めると、制御装置111は、エンジン始動直後に以下の制御を実行する。   In summary, the control device 111 executes the following control immediately after starting the engine.

図2に示す様に、ステップS101では、第1の排気温度検出器107で検出された排気温度T1が第1の閾値排気温度TTHRESHOLD1以下か否かを判定し、排気温度T1が第1の閾値排気温度TTHRESHOLD1以下の場合に、ステップS102に進み、排気温度T1が第1の閾値排気温度TTHRESHOLD1超の場合に、ステップS103に進む。 As shown in FIG. 2, in step S101, the exhaust temperatures T 1 detected by the first exhaust temperature sensor 107 determines whether the first threshold exhaust temperature T THRESHOLD1 less, the exhaust temperatures T 1 second when: 1 threshold exhaust temperature T THRESHOLD1, the process proceeds to step S102, if the exhaust gas temperature T 1 THRESHOLD1 than the first threshold exhaust temperature T, the processing flow advances to step S103.

ステップS102では、排気温度T1を上昇させるべく、第1の尿素水噴射器106で第1の尿素SCR102に尿素水を供給させる(第1の昇温制御)。 In step S102, urea water is supplied to the first urea SCR 102 by the first urea water injector 106 to increase the exhaust gas temperature T1 ( first temperature increase control).

ステップS103では、第2の排気温度検出器109で検出された排気温度T2が第2の閾値排気温度TTHRESHOLD2以下か否かを判定し、排気温度T2が第2の閾値排気温度TTHRESHOLD2以下の場合に、ステップS104に進み、排気温度T2が第2の閾値排気温度TTHRESHOLD2超の場合に、ステップS105に進む。 In step S103, it is determined whether the exhaust gas temperature T 2 detected by the second exhaust gas temperature detector 109 is equal to or lower than a second threshold exhaust gas temperature T THRESHOLD2 , and the exhaust gas temperature T 2 is set to the second threshold exhaust gas temperature T THRESHOLD2. in the following cases, the process proceeds to step S104, if the exhaust temperature T 2 THRESHOLD2 than the second threshold exhaust temperature T, the processing flow advances to step S105.

ステップS104では、排気温度T2を上昇させるべく、第1の尿素水噴射器106で第1の尿素SCR102に尿素水を供給させつつ、エンジン101でポスト噴射を実行させるか、及び/又は炭化水素噴射器110で排気浄化触媒103に炭化水素を供給させる(第2の昇温制御)。 In step S104, in order to raise the exhaust gas temperature T 2, while supplying the urea water in the first urea water injector 106 to the first urea SCR 102, whether to perform the post injection in the engine 101, and / or hydrocarbon Hydrocarbon is supplied to the exhaust purification catalyst 103 by the injector 110 (second temperature raising control).

ステップS105では、第2の排気温度検出器109で検出された排気温度T2が第3の閾値排気温度TTHRESHOLD3以下か否かを判定し、排気温度T2が第3の閾値排気温度TTHRESHOLD3以下の場合に、ステップS106に進み、排気温度T2が第3の閾値排気温度TTHRESHOLD3超の場合に、ステップS107に進む。 In step S105, the exhaust temperature T 2 detected by the second exhaust temperature detector 109 determines whether the third threshold exhaust temperature T THRESHOLD3 below, the exhaust temperature T 2 is the third threshold exhaust temperature T THRESHOLD3 in the following cases, the process proceeds to step S106, if the exhaust temperature T 2 of the third threshold exhaust temperature T THRESHOLD3 greater, the process proceeds to step S107.

ステップS106では、排気温度T2を上昇させるべく、第1の尿素水噴射器106で第1の尿素SCR102に尿素水を供給させると共に、エンジン101でポスト噴射を実行させ、及び/又は炭化水素噴射器110で排気浄化触媒103に炭化水素を供給させつつ、第2の尿素水噴射器108で第2の尿素SCR105に尿素水を供給させる(第3の昇温制御)。 In step S106, in order to raise the exhaust gas temperature T 2, together to supply urea water to the first urea water injector 106 first urea SCR 102, to execute the post injection in the engine 101, and / or hydrocarbon injection The urea water is supplied to the second urea SCR 105 by the second urea water injector 108 while the hydrocarbon is supplied to the exhaust purification catalyst 103 by the heater 110 (third temperature increase control).

ステップS107では、以上の昇温制御を停止し、排気浄化制御を実行する。   In step S107, the above-described temperature increase control is stopped, and the exhaust gas purification control is executed.

従って、図3に示す様に、エンジン始動後に排気温度T1,T2を速やかに上昇させ、排気温度を第2の尿素SCR105の活性化温度超にする事が出来る為、エンジン始動後の早い段階で第2の尿素SCR105で窒素酸化物の浄化を行え、エンジン始動直後の窒素酸化物スリップを抑制する事が出来る。特に、排気温度T1は、本来、図3の破線に示す様に推移するが、炭化水素を添加する事によって本来よりも早く昇温される。 Accordingly, as shown in FIG. 3, since the exhaust temperatures T 1 and T 2 can be quickly raised after the engine is started, and the exhaust temperature can be set to be higher than the activation temperature of the second urea SCR 105, it is possible to quickly start the operation after the engine is started. At this stage, nitrogen oxides can be purified by the second urea SCR 105, and nitrogen oxide slip immediately after engine start can be suppressed. In particular, the exhaust temperatures T 1 is originally but to remain as shown in broken line in FIG. 3, it is quickly heated than the original by the addition of hydrocarbons.

100 排気後処理装置
101 エンジン
102 第1の尿素SCR
103 排気浄化触媒
104 CSF
105 第2の尿素SCR
106 第1の尿素水噴射器
107 第1の排気温度検出器
108 第2の尿素水噴射器
109 第2の排気温度検出器
110 炭化水素噴射器
111 制御装置
112 排気管
Reference Signs List 100 exhaust aftertreatment device 101 engine 102 first urea SCR
103 Exhaust purification catalyst 104 CSF
105 Second urea SCR
106 first urea water injector 107 first exhaust temperature detector 108 second urea water injector 109 second exhaust temperature detector 110 hydrocarbon injector 111 controller 112 exhaust pipe

Claims (5)

エンジンの排気を浄化する排気後処理装置に於いて、
前記エンジンの排気管に設置される第1の尿素SCRと、
前記排気管に設置され、前記第1の尿素SCRの排気下流側に配置された排気浄化触媒と、
前記排気管に設置され、前記排気浄化触媒の排気下流側に配置された第2の尿素SCRと、
前記排気管に設置され、前記第1の尿素SCRの排気上流側に配置された第1の尿素水噴射器と、
前記排気管に設置され、前記第1の尿素SCRと前記排気浄化触媒との間に配置された第1の排気温度検出器と、
前記排気管に設置され、前記排気浄化触媒と前記第2の尿素SCRとの間に配置された第2の尿素水噴射器と、
前記排気管に設置され、前記排気浄化触媒と前記第2の尿素SCRとの間に配置された第2の排気温度検出器と、
を備える
事を特徴とする排気後処理装置。
In the exhaust aftertreatment device that purifies the exhaust of the engine,
A first urea SCR installed in an exhaust pipe of the engine;
An exhaust gas purification catalyst installed in the exhaust pipe and arranged on the exhaust gas downstream side of the first urea SCR;
A second urea SCR installed in the exhaust pipe and arranged on the exhaust gas downstream side of the exhaust purification catalyst;
A first urea water injector installed in the exhaust pipe and arranged on the exhaust upstream side of the first urea SCR;
A first exhaust gas temperature detector installed in the exhaust pipe and disposed between the first urea SCR and the exhaust gas purification catalyst;
A second urea water injector disposed in the exhaust pipe and disposed between the exhaust purification catalyst and the second urea SCR;
A second exhaust gas temperature sensor installed in the exhaust pipe and disposed between the exhaust gas purification catalyst and the second urea SCR;
An exhaust aftertreatment device characterized by comprising:
前記第1の排気温度検出器で検出された排気温度が第1の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させ、前記第2の排気温度検出器で検出された排気温度が前記第1の閾値排気温度よりも高い第2の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させつつ、前記エンジンでポスト噴射を実行させ、前記第2の排気温度検出器で検出された排気温度が前記第2の閾値排気温度よりも高い第3の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させると共に、前記エンジンでポスト噴射を実行させつつ、前記第2の尿素水噴射器で尿素水を前記第2の尿素SCRに供給させる制御装置を更に備える
請求項1に記載の排気後処理装置。
When the exhaust gas temperature detected by the first exhaust gas temperature detector is equal to or lower than a first threshold exhaust gas temperature, the first urea water injector supplies urea water to the first urea SCR; When the exhaust gas temperature detected by the second exhaust gas temperature detector is equal to or lower than a second threshold exhaust gas temperature higher than the first threshold exhaust gas temperature, the first urea water injector supplies the first urea water injector with the first urea water. When the engine performs post-injection while supplying to the urea SCR, and the exhaust temperature detected by the second exhaust temperature detector is equal to or lower than a third threshold exhaust temperature higher than the second threshold exhaust temperature. The urea water is supplied to the first urea SCR by the first urea water injector, and the urea water is supplied to the second urea water injector by the second urea water injector while the engine performs post-injection. And a control device for supplying the urea SCR to the urea SCR. Item 7. An exhaust aftertreatment device according to Item 1.
前記排気管に設置され、前記第1の尿素SCRと前記排気浄化触媒との間に配置された炭化水素噴射器を更に備え、
前記第1の排気温度検出器で検出された排気温度が第1の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させ、前記第2の排気温度検出器で検出された排気温度が前記第1の閾値排気温度よりも高い第2の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させつつ、前記炭化水素噴射器で炭化水素を前記排気浄化触媒に供給させ、前記第2の排気温度検出器で検出された排気温度が前記第2の閾値排気温度よりも高い第3の閾値排気温度以下の場合に、前記第1の尿素水噴射器で尿素水を前記第1の尿素SCRに供給させると共に、前記炭化水素噴射器で炭化水素を前記排気浄化触媒に供給させつつ、前記第2の尿素水噴射器で尿素水を前記第2の尿素SCRに供給させる制御装置を更に備える
請求項1に記載の排気後処理装置。
A hydrocarbon injector disposed on the exhaust pipe and disposed between the first urea SCR and the exhaust gas purification catalyst;
When the exhaust gas temperature detected by the first exhaust gas temperature detector is equal to or lower than a first threshold exhaust gas temperature, the first urea water injector supplies urea water to the first urea SCR; When the exhaust gas temperature detected by the second exhaust gas temperature detector is equal to or lower than a second threshold exhaust gas temperature higher than the first threshold exhaust gas temperature, the first urea water injector supplies the first urea water injector with the first urea water. The hydrocarbon is supplied to the exhaust gas purification catalyst by the hydrocarbon injector while the urea SCR is supplied, and the exhaust gas temperature detected by the second exhaust gas temperature detector is higher than the second threshold exhaust gas temperature. When the temperature is equal to or lower than the threshold exhaust temperature of 3, the urea water is supplied to the first urea SCR by the first urea water injector, and the hydrocarbon is supplied to the exhaust purification catalyst by the hydrocarbon injector. Urea water is supplied to the second urine using the second urea water injector. Exhaust post-treatment device according to claim 1, further comprising a control device for supplying to the SCR.
前記第1の尿素SCRと前記第2の尿素SCRは、ゼオライトを含む
請求項1乃至3の何れか一項に記載の排気後処理装置。
The exhaust aftertreatment device according to any one of claims 1 to 3, wherein the first urea SCR and the second urea SCR include zeolite.
前記排気浄化触媒は、酸化触媒とNOX吸蔵還元型触媒の一方又は両方を備える
請求項1乃至4の何れか一項に記載の排気後処理装置。
The exhaust gas purifying catalyst, an exhaust aftertreatment device according to any one of claims 1 to 4 comprising one or both of the oxidation catalyst and the NO X storage reduction catalyst.
JP2018166850A 2018-09-06 2018-09-06 Post-exhaust treatment device Pending JP2020041428A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116641779A (en) * 2023-06-21 2023-08-25 山东可兰素环保科技有限公司 Heavy truck diesel power gas assisted atomization SCR urea solution injection system

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015130212A1 (en) * 2014-02-28 2015-09-03 Scania Cv Ab Exhaust treatment system and method for treatment of an exhaust stream

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2015130212A1 (en) * 2014-02-28 2015-09-03 Scania Cv Ab Exhaust treatment system and method for treatment of an exhaust stream

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116641779A (en) * 2023-06-21 2023-08-25 山东可兰素环保科技有限公司 Heavy truck diesel power gas assisted atomization SCR urea solution injection system

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