JP2007218108A - Exhaust emission control device - Google Patents

Exhaust emission control device Download PDF

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JP2007218108A
JP2007218108A JP2006036654A JP2006036654A JP2007218108A JP 2007218108 A JP2007218108 A JP 2007218108A JP 2006036654 A JP2006036654 A JP 2006036654A JP 2006036654 A JP2006036654 A JP 2006036654A JP 2007218108 A JP2007218108 A JP 2007218108A
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reduction catalyst
mist
sulfuric acid
water
exhaust
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Hiroshi Funahashi
博 舟橋
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Hino Motors Ltd
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Hino Motors Ltd
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<P>PROBLEM TO BE SOLVED: To provide an exhaust emission control device in which high concentration SO<SB>2</SB>gas is not generated in desulfurization of NOx occlusion/reduction catalyst. <P>SOLUTION: In the exhaust emission control device, the NOx occlusion/reduction catalyst 5 is disposed along an exhaust pipe 4, and fuel 8 can be added to an inlet side of the NOx occlusion/reduction catalyst 5. The exhaust emission control device comprises: a water spray means 18 disposed downstream of the NOx occlusion/reduction catalyst 5 and atomizing water 15 and spraying the water 15 into exhaust gas 3; and a mist catcher (a mist catch board 19, a rear wall part 20 of a desulfurization case 12, or a tail pipe 21) catching sulfuric acid mist downstream of the water spray means 18, and reacted with the sulfuric acid mist to form sulfide. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、NOx吸蔵還元触媒を用いた排気浄化装置に関するものである。   The present invention relates to an exhaust purification device using a NOx storage reduction catalyst.

従来より、ディーゼルエンジンにおいては、排気空燃比がリーンの時に排気ガス中のNOxを酸化して硝酸塩の状態で一時的に吸蔵し且つ排気ガス中の酸素濃度が低下した時に未燃HCやCO等の介在によりNOxを分解放出して還元浄化する性質を備えたNOx吸蔵還元触媒を排気管の途中に装備し、このNOx吸蔵還元触媒によりNOxの排出濃度を低減することが行われている。   Conventionally, in diesel engines, when the exhaust air-fuel ratio is lean, NOx in the exhaust gas is oxidized and temporarily stored in the form of nitrate, and when the oxygen concentration in the exhaust gas decreases, unburned HC, CO, etc. A NOx occlusion reduction catalyst having the property of decomposing and releasing NOx through the intervention of the catalyst to reduce and purify is provided in the middle of the exhaust pipe, and this NOx occlusion reduction catalyst is used to reduce the NOx emission concentration.

ただし、NOx吸蔵還元触媒においては、NOxの吸蔵量が増大して飽和量に達してしまうと、それ以上のNOxを吸蔵できなくなるため、定期的にNOx吸蔵還元触媒に流入する排気ガスの酸素濃度をHC等の還元剤により低下させてNOxを分解放出させる必要がある。   However, in the NOx occlusion reduction catalyst, if the occlusion amount of NOx increases and reaches the saturation amount, no more NOx can be occluded, so the oxygen concentration of the exhaust gas that periodically flows into the NOx occlusion reduction catalyst Needs to be reduced by a reducing agent such as HC to decompose and release NOx.

例えば、ガソリンエンジンに使用した場合であれば、機関の運転空燃比を低下(機関をリッチ空燃比で運転)することにより、排気ガス中の酸素濃度を低下し且つ排気ガス中の未燃HCやCO等の還元成分を増加してNOxの分解放出を促すことができるが、NOx吸蔵還元触媒をディーゼルエンジンの排気浄化装置として使用した場合には機関をリッチ空燃比で運転することが困難である。   For example, when used in a gasoline engine, by reducing the operating air-fuel ratio of the engine (operating the engine at a rich air-fuel ratio), the oxygen concentration in the exhaust gas is reduced and unburned HC in the exhaust gas is reduced. Although it is possible to promote the decomposition and release of NOx by increasing the reducing components such as CO, it is difficult to operate the engine at a rich air-fuel ratio when the NOx occlusion reduction catalyst is used as an exhaust purification device of a diesel engine. .

このため、NOx吸蔵還元触媒の上流側で排気ガス中に燃料を添加することにより、この添加燃料を還元剤としてNOx吸蔵還元触媒上で酸素と反応させることで排気ガス中の酸素濃度を低下させる必要がある(例えば、特許文献1参照)。
特開2002−81311号公報
Therefore, by adding fuel to the exhaust gas upstream of the NOx storage reduction catalyst, the added fuel is used as a reducing agent to react with oxygen on the NOx storage reduction catalyst, thereby reducing the oxygen concentration in the exhaust gas. There is a need (see, for example, Patent Document 1).
JP 2002-81111 A

しかしながら、ディーゼルエンジンの排気ガス中には、燃料の軽油中に含まれる硫黄分に由来したSO2ガス(亜硫酸ガス)が存在しているため、このSO2ガスがNOx吸蔵還元触媒上でNOxと同様に酸化して硫酸塩として吸蔵されてしまうことが避けられないが、この硫酸塩は硝酸塩と比べて安定であるため、NOx吸蔵還元触媒を再生させるべく燃料添加を実行しても、該NOx吸蔵還元触媒に吸蔵されている硫酸塩が一部しか放出されずに残留してしまう結果、NOx吸蔵還元触媒のNOx吸蔵サイトの回復割合が小さくなって吸蔵能力が低下してしまうという問題があり、この硫酸塩の残留の問題に関しては未だ具体的な実用レベルの解決策が確立されていないのが実情である。 However, in the exhaust gas of the diesel engine, SO 2 gas (sulfurous acid gas) derived from sulfur contained in the light oil of the fuel is present, so this SO 2 gas is combined with NOx on the NOx storage reduction catalyst. Similarly, it is unavoidable that it is oxidized and occluded as a sulfate, but since this sulfate is more stable than nitrate, even if fuel addition is performed to regenerate the NOx occlusion reduction catalyst, the NOx As a result of the fact that only a part of the sulfate stored in the storage reduction catalyst is released and remains, there is a problem that the recovery rate of the NOx storage site of the NOx storage reduction catalyst is reduced and the storage capacity is reduced. In reality, no practical solution has yet been established for the problem of residual sulfate.

即ち、NOx吸蔵還元触媒から硫酸塩を脱離させる手法自体は、NOx吸蔵還元触媒の触媒床温度を約600〜700℃の脱硫温度条件まで上げて酸欠状態に保つことにより、NOx吸蔵還元触媒から硫酸塩をSO2ガスとして放出させてNOx吸蔵還元触媒の脱硫処理を図り得ることが既に知られているが、その脱硫処理の際にNOx吸蔵還元触媒に時間をかけて蓄えられていたSO2ガスが一度にまとまって放出されてしまうことで高濃度のSO2ガスが発生するという問題があり、この高濃度のSO2ガスの発生がNOx吸蔵還元触媒の脱硫処理の実用化を阻む大きな要因となっていた。 That is, the method of desorbing sulfate from the NOx occlusion reduction catalyst itself involves increasing the catalyst bed temperature of the NOx occlusion reduction catalyst to a desulfurization temperature condition of about 600 to 700 ° C. It is already known that the NOx occlusion reduction catalyst can be desulfurized by releasing sulfate as SO 2 gas from the SOx, but the SOx that has been stored in the NOx occlusion reduction catalyst over time during the desulfurization treatment There is a problem that a high concentration of SO 2 gas is generated by releasing two gases at once, and the generation of this high concentration of SO 2 gas greatly hinders the practical use of the NOx storage reduction catalyst desulfurization treatment. It was a factor.

本発明は、上述の実情に鑑みてなされたものであり、NOx吸蔵還元触媒の脱硫処理時に高濃度のSO2ガスが発生しないようにした排気浄化装置を提供することを目的としている。 The present invention has been made in view of the above-described circumstances, and an object of the present invention is to provide an exhaust emission control device that prevents high-concentration SO 2 gas from being generated during the desulfurization treatment of the NOx storage reduction catalyst.

本発明は、排気管の途中にNOx吸蔵還元触媒を備えて該NOx吸蔵還元触媒の入側に燃料を添加し得るようにした排気浄化装置において、NOx吸蔵還元触媒より下流側で排気ガス中に水を霧化して散布する水噴霧手段と、該水噴霧手段の下流側で硫酸ミストを捕え且つ該硫酸ミストと反応して硫化物を成すミストキャッチャとを備えたことを特徴とするものである。   The present invention provides an exhaust gas purification apparatus provided with a NOx storage reduction catalyst in the middle of an exhaust pipe so that fuel can be added to the inlet side of the NOx storage reduction catalyst. A water spraying means for atomizing and spraying water, and a mist catcher that catches sulfuric acid mist on the downstream side of the water spraying means and reacts with the sulfuric acid mist to form a sulfide. .

而して、NOx吸蔵還元触媒に脱硫処理を施すにあたり、該NOx吸蔵還元触媒の入側に燃料を添加すると、この添加燃料がNOx吸蔵還元触媒上で酸素と反応することにより周囲の排気ガス中の酸素濃度が低下し且つその反応熱により触媒床温度が脱硫温度条件まで上げられ、NOx吸蔵還元触媒から硫酸塩がSO2ガスとして放出されることになる。 Thus, when desulfurization treatment is performed on the NOx storage reduction catalyst, if fuel is added to the inlet side of the NOx storage reduction catalyst, the added fuel reacts with oxygen on the NOx storage reduction catalyst, so that the surrounding exhaust gas As a result, the catalyst bed temperature is raised to the desulfurization temperature condition by the reaction heat, and the sulfate is released as SO 2 gas from the NOx storage reduction catalyst.

この際、NOx吸蔵還元触媒の下流側で水噴霧手段により水を霧化して散布すると、排気ガス中でSO2ガスが水と反応して硫酸(H2SO4)となることで液化し、その液化した硫酸ミストがミストキャッチャに捕えられて該ミストキャッチャと反応することで硫化物を成し、そのままミストキャッチャの一部として保持されることになるので、NOx吸蔵還元触媒の脱硫処理時にSO2ガスがまとまって車外へ放出されてしまう虞れがなくなる。 At this time, when water is atomized and sprayed by the water spraying means on the downstream side of the NOx occlusion reduction catalyst, the SO 2 gas reacts with water in the exhaust gas to become sulfuric acid (H 2 SO 4 ), and is liquefied. The liquefied sulfuric acid mist is captured by the mist catcher and reacts with the mist catcher to form a sulfide, which is retained as a part of the mist catcher. Therefore, during the desulfurization treatment of the NOx storage reduction catalyst, (2) There is no risk of gas being collected outside the vehicle.

尚、ミストキャッチャは、硫酸ミストによる硫化が進むにつれて該硫酸ミストを硫化物として取り込むことが困難になってくるため、ミストキャッチャの硫化が十分に進んで全体が硫化物となってきた頃合で新しいミストキャッチャと交換するようにすれば良い。   As the mist catcher becomes more difficult to take in the sulfuric acid mist as sulfide as the sulfidation by the sulfuric acid mist progresses, the mist catcher is new when the mist catcher is sufficiently sulfided to become a sulfide as a whole. Replace with a mist catcher.

また、本発明においては、水噴霧手段とミストキャッチャとの間に、水分を保持しながら排気ガスを通過せしめる水分保持フィルタを備えることが好ましく、このようにすれば、水噴霧手段から散布された水分が水分保持フィルタにより保持され、該水分保持フィルタを通過する排気ガス中のSO2ガスと水との接触頻度が高められるので、SO2ガスと水との反応効率が向上される。 Further, in the present invention, it is preferable to include a moisture retention filter that allows exhaust gas to pass while retaining moisture between the water spraying means and the mist catcher. Since moisture is retained by the moisture retention filter and the contact frequency between the SO 2 gas and the water in the exhaust gas passing through the moisture retention filter is increased, the reaction efficiency between the SO 2 gas and water is improved.

更に、本発明においては、硫酸ミストと反応して硫化物を成し得る金属フィルタにより水分保持フィルタを構成することが好ましく、このようにすれば、水分保持フィルタで硫酸生成の反応が起こるだけでなく、その生成された硫酸が直ちに水分保持フィルタを成す金属フィルタと反応して硫化物として保持されることになる。   Furthermore, in the present invention, it is preferable that the moisture retention filter is constituted by a metal filter that can react with the sulfuric acid mist to form a sulfide, and in this way, only the reaction of sulfuric acid generation occurs in the moisture retention filter. Instead, the generated sulfuric acid immediately reacts with the metal filter forming the moisture retaining filter and is retained as a sulfide.

上記した本発明の排気浄化装置によれば、下記の如き種々の優れた効果を奏し得る。   According to the exhaust emission control device of the present invention described above, various excellent effects as described below can be obtained.

(I)本発明の請求項1に記載の発明によれば、脱硫処理時にNOx吸蔵還元触媒から放出されるSO2ガスを水と反応させて硫酸(H2SO4)とし、その液化した硫酸ミストをミストキャッチャにより捕えて該ミストキャッチャと反応させることで硫化物とし、そのままミストキャッチャの一部として保持させて確実に処理することができるので、NOx吸蔵還元触媒の脱硫処理時に高濃度のSO2ガスが発生してしまう問題を解決することができる。 (I) According to the first aspect of the present invention, the SO 2 gas released from the NOx occlusion reduction catalyst during the desulfurization treatment is reacted with water to form sulfuric acid (H 2 SO 4 ), and the liquefied sulfuric acid Mist is captured by the mist catcher and reacted with the mist catcher to form a sulfide, which can be retained as a part of the mist catcher and processed reliably, so that a high concentration of SOx can be treated during the desulfurization treatment of the NOx storage reduction catalyst. 2 The problem of gas generation can be solved.

(II)本発明の請求項2に記載の発明によれば、水噴霧手段から散布された水分を水分保持フィルタにより保持して排気ガス中のSO2ガスと水との接触頻度を著しく高めることができるので、SO2ガスと水との反応効率を大幅に向上することができて更に確実なSO2ガスの処理を図ることができる。 (II) According to the invention described in claim 2 of the present invention, the water sprayed from the water spraying means is held by the moisture holding filter, and the contact frequency between the SO 2 gas in the exhaust gas and the water is significantly increased. Therefore, the reaction efficiency between the SO 2 gas and water can be greatly improved, and the SO 2 gas can be treated more reliably.

(III)本発明の請求項3に記載の発明によれば、水分保持フィルタで硫酸生成の反応が起こし、その生成された硫酸を直ちに水分保持フィルタを成す金属フィルタと反応させて硫化物として保持することができるので、SO2ガスから硫化物とするまでの反応を効率良く進めることができる。 (III) According to the invention described in claim 3 of the present invention, a reaction for producing sulfuric acid occurs in the moisture retention filter, and the produced sulfuric acid is immediately reacted with the metal filter constituting the moisture retention filter and retained as sulfide. Therefore, the reaction from SO 2 gas to sulfide can be efficiently advanced.

以下本発明の実施の形態を図面を参照しつつ説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図1は本発明を実施する形態の一例を示すもので、本形態例の排気浄化装置においては、ディーゼルエンジン1から排気マニホールド2を介して排出される排気ガス3が流通する排気管4の途中に、フロースルー方式のハニカム構造を有するNOx吸蔵還元触媒5が触媒ケース6に抱持されて装備されており、該触媒ケース6の入口部分には、軽油タンク7内の燃料8(軽油)を軽油ポンプ9を介し導いて噴射する燃料添加インジェクタ10が設けられている。   FIG. 1 shows an example of an embodiment for carrying out the present invention. In the exhaust purification apparatus of this embodiment, the exhaust pipe 4 through which the exhaust gas 3 discharged from the diesel engine 1 through the exhaust manifold 2 flows is shown. In addition, a NOx occlusion reduction catalyst 5 having a flow-through type honeycomb structure is mounted and mounted on a catalyst case 6, and fuel 8 (light oil) in a light oil tank 7 is placed at the inlet of the catalyst case 6. There is provided a fuel addition injector 10 which is guided through a light oil pump 9 and injected.

尚、ここに図示している例では、前記触媒ケース6内におけるNOx吸蔵還元触媒5の後段に、酸化触媒を担持して成る触媒担持型のパティキュレートフィルタ11が装備されており、前段のNOx吸蔵還元触媒5を経た排気ガス3中に含まれるパティキュレートを捕集して更なる排気浄化を図り得るようにしてある。   In the example shown here, a catalyst-carrying particulate filter 11 carrying an oxidation catalyst is mounted on the downstream side of the NOx storage-reduction catalyst 5 in the catalyst case 6, so that the NOx in the front stage is provided. Particulates contained in the exhaust gas 3 that has passed through the occlusion reduction catalyst 5 are collected so that further exhaust purification can be achieved.

更に、この触媒ケース6の直後に、脱硫ケース12が連絡配管13を介して接続されていると共に、この脱硫ケース12の入口部分には、水タンク14内の水15を水ポンプ16を介し導いて噴霧する噴射ノズル17が設けられており、これら水タンク14と水ポンプ16と噴射ノズル17とにより、排気ガス3中に水15を霧化して散布する水噴霧手段18が構成されるようになっている。   Further, immediately after the catalyst case 6, a desulfurization case 12 is connected via a connecting pipe 13, and water 15 in the water tank 14 is guided to the inlet portion of the desulfurization case 12 via a water pump 16. The water tank 14, the water pump 16, and the spray nozzle 17 constitute a water spray means 18 that atomizes and sprays the water 15 into the exhaust gas 3. It has become.

また、前記脱硫ケース12内における後段側には、後述の硫酸ミストを捕え且つ該硫酸ミストと反応して硫化物を成すミストキャッチャとして、鉄系金属から成るミストキャッチ板19が配設されており、該ミストキャッチ板19は、パンチングメタルや金属メッシュ等により構成された通気構造を成すものとなっている。   Further, a mist catch plate 19 made of an iron-based metal is disposed on the rear stage side in the desulfurization case 12 as a mist catcher that catches sulfuric acid mist, which will be described later, and reacts with the sulfuric acid mist to form a sulfide. The mist catch plate 19 has a ventilation structure made of a punching metal, a metal mesh or the like.

更に、脱硫ケース12の後壁部20や、該後壁部20の最下位置に接続されたテールパイプ21も夫々鉄系金属により製作されてミストキャッチャとしての役割を果し得るようにしてある。   Further, the rear wall portion 20 of the desulfurization case 12 and the tail pipe 21 connected to the lowermost position of the rear wall portion 20 are each made of an iron-based metal so that it can serve as a mist catcher. .

尚、これらのミストキャッチャの材質は、硫酸ミストと反応して硫化物を成す金属であれば良く、必ずしも鉄系金属で制作することに限定されるものではない。   In addition, the material of these mist catchers should just be a metal which reacts with a sulfuric acid mist and forms a sulfide, and is not necessarily limited to producing with a ferrous metal.

一方、前記脱硫ケース12内における前段側には、排気ガス3を拡散させて水分の分散を促す分散板22が設けられており、この分散板22も前述のミストキャッチ板19と同様にパンチングメタルや金属メッシュ等により構成された通気構造を成すものとなっている。   On the other hand, on the upstream side in the desulfurization case 12, a dispersion plate 22 that diffuses the exhaust gas 3 and promotes the dispersion of moisture is provided. This dispersion plate 22 is also punched metal like the mist catch plate 19 described above. And a ventilation structure composed of a metal mesh or the like.

そして、前記脱硫ケース12内における分散板22とミストキャッチ板19とに挟まれた空間には、水分を保持しながら排気ガス3を通過せしめる水分保持フィルタとして、コージェライト等から成る多孔質のセラミックフィルタ23が配置されており、このセラミックフィルタ23は、前記パティキュレートフィルタ11と略同様のハニカム構造を有し、格子状に区画された各流路の入口が交互に目封じされ、入口が目封じされていない流路については、その出口が目封じされるようになっている。   In the space between the dispersion plate 22 and the mist catch plate 19 in the desulfurization case 12, a porous ceramic made of cordierite or the like is used as a moisture retaining filter that allows the exhaust gas 3 to pass while retaining moisture. A filter 23 is disposed. The ceramic filter 23 has a honeycomb structure substantially the same as that of the particulate filter 11, and the inlets of the respective flow paths partitioned in a lattice pattern are alternately sealed, and the inlets are closed. About the flow path which is not sealed, the exit is sealed.

而して、このように構成された排気浄化装置に関し、NOx吸蔵還元触媒5に吸蔵されて残留する硫酸塩をSO2ガスとして放出させる脱硫処理を施すにあたり、NOx吸蔵還元触媒5の入側に燃料添加インジェクタ10から燃料8を添加すると、この添加した燃料8がNOx吸蔵還元触媒5上で酸素と反応することにより周囲の排気ガス3中の酸素濃度が低下し且つその反応熱により触媒床温度が脱硫温度条件まで上げられ、NOx吸蔵還元触媒5から硫酸塩がSO2ガスとして放出されることになる。 Thus, with regard to the exhaust purification apparatus configured as described above, when performing a desulfurization treatment in which the sulfate stored in the NOx occlusion reduction catalyst 5 is released as SO 2 gas, the NOx occlusion reduction catalyst 5 is placed on the inlet side. When the fuel 8 is added from the fuel addition injector 10, the added fuel 8 reacts with oxygen on the NOx occlusion reduction catalyst 5, thereby reducing the oxygen concentration in the surrounding exhaust gas 3 and the heat of reaction causes the catalyst bed temperature. Is raised to the desulfurization temperature condition, and the sulfate is released from the NOx occlusion reduction catalyst 5 as SO 2 gas.

この際、水タンク14内の水15を水ポンプ16を介し導いて噴射ノズル17により排気ガス3中に霧化して散布すると、排気ガス3中でSO2ガスが水15と反応して硫酸(H2SO4)となることで液化し、その液化した硫酸ミストがミストキャッチ板19に捕えられて該ミストキャッチ板19と反応することで硫化鉄(硫化物)となり、そのままミストキャッチ板19の一部として保持されることになるので、NOx吸蔵還元触媒5の脱硫処理時にSO2ガスがまとまって車外へ放出されてしまう虞れがなくなる。 At this time, when the water 15 in the water tank 14 is guided through the water pump 16 and atomized into the exhaust gas 3 by the spray nozzle 17, the SO 2 gas reacts with the water 15 in the exhaust gas 3 and sulfuric acid ( H 2 SO 4 ) is liquefied, and the liquefied sulfuric acid mist is captured by the mist catch plate 19 and reacts with the mist catch plate 19 to become iron sulfide (sulfide). Since it is held as a part, there is no possibility that SO 2 gas is collected and released outside the vehicle during the desulfurization treatment of the NOx storage reduction catalyst 5.

ここで、同様の反応は脱硫ケース12の後壁部20やテールパイプ21においても起こり、これら脱硫ケース12の後壁部20やテールパイプ21にも硫酸ミストが捕えられて硫化鉄(硫化物)を成し、そのまま脱硫ケース12の後壁部20やテールパイプ21の一部として保持されることになる。   Here, the same reaction also occurs in the rear wall portion 20 and the tail pipe 21 of the desulfurization case 12, and sulfuric acid mist is also captured by the rear wall portion 20 and the tail pipe 21 of the desulfurization case 12 to cause iron sulfide (sulfide). And is held as a part of the rear wall portion 20 and the tail pipe 21 as it is.

尚、ミストキャッチ板19や脱硫ケース12の後壁部20、テールパイプ21といったミストキャッチャは、硫酸ミストによる硫化が進むにつれて該硫酸ミストを硫化鉄として取り込むことが困難になってくるため、ミストキャッチ板19の硫化が十分に進んで全体が硫化鉄となってきた頃合で新しいものと交換するようにすれば良い。   The mist catcher such as the mist catch plate 19, the rear wall portion 20 of the desulfurization case 12, and the tail pipe 21 becomes difficult to take in the sulfuric acid mist as iron sulfide as the sulfidation by the sulfuric acid mist progresses. What is necessary is just to replace | exchange for the new thing at the time when the sulfidation of the board 19 fully progressed and the whole became iron sulfide.

また、特に本形態例においては、水噴霧手段18とミストキャッチ板19との間にセラミックフィルタ23を備えているので、水噴霧手段18から散布された水分がセラミックフィルタ23により保持され、該セラミックフィルタ23を通過する排気ガス3中のSO2ガスと水15との接触頻度が高められる結果、SO2ガスと水15との反応効率が向上されることになる。 In particular, in the present embodiment, the ceramic filter 23 is provided between the water spraying means 18 and the mist catch plate 19, so that the water sprayed from the water spraying means 18 is held by the ceramic filter 23, and the ceramic As a result of increasing the contact frequency between the SO 2 gas in the exhaust gas 3 passing through the filter 23 and the water 15, the reaction efficiency between the SO 2 gas and the water 15 is improved.

従って、上記によれば、脱硫処理時にNOx吸蔵還元触媒5から放出されるSO2ガスを水15と反応させて硫酸(H2SO4)とし、その液化した硫酸ミストをミストキャッチ板19や脱硫ケース12の後壁部20、テールパイプ21といったミストキャッチャにより捕えて硫化鉄として取り込み、そのままミストキャッチ板19や脱硫ケース12の後壁部20、テールパイプ21の一部として保持させて確実に処理することができるので、NOx吸蔵還元触媒5の脱硫処理時に高濃度のSO2ガスが発生してしまう問題を解決することができる。 Therefore, according to the above, the SO 2 gas released from the NOx occlusion reduction catalyst 5 during the desulfurization treatment is reacted with the water 15 to form sulfuric acid (H 2 SO 4 ), and the liquefied sulfuric acid mist is converted into the mist catch plate 19 or the desulfurization. Caught by a mist catcher such as the rear wall portion 20 of the case 12 and the tail pipe 21 and taken in as iron sulfide, and held as part of the mist catch plate 19, the rear wall portion 20 of the desulfurization case 12, and the tail pipe 21 for reliable processing. Therefore, it is possible to solve the problem that a high concentration of SO 2 gas is generated during the desulfurization treatment of the NOx storage reduction catalyst 5.

また、特に本形態例においては、水噴霧手段18から散布された水分をセラミックフィルタ23により保持して排気ガス3中のSO2ガスと水15との接触頻度を著しく高めることができるので、SO2ガスと水15との反応効率を大幅に向上することができて更に確実なSO2ガスの処理を図ることができる。 In particular, in the present embodiment, the water sprayed from the water spraying means 18 can be held by the ceramic filter 23 so that the contact frequency between the SO 2 gas in the exhaust gas 3 and the water 15 can be remarkably increased. The reaction efficiency between the two gases and the water 15 can be greatly improved, and the SO 2 gas can be treated more reliably.

図2は本発明の別の形態例を示すもので、本形態例においては、図1のセラミックフィルタ23に替えて、硫酸ミストと反応して硫化物を成し得る金属フィルタ24を水分保持フィルタとして採用したものとなっており、この種の金属フィルタ24には、ミクロンオーダーの金属繊維を積層焼結したもの、金属粉末の焼結体、金属メッシュを積層焼結したもの、金属メッシュに金属粉末を焼結させたもの等を用いることができる。   FIG. 2 shows another embodiment of the present invention. In this embodiment, instead of the ceramic filter 23 of FIG. 1, a metal filter 24 that can form sulfide by reacting with sulfuric acid mist is used as a moisture retaining filter. This type of metal filter 24 has a micron-order metal fiber laminated and sintered, a metal powder sintered body, a metal mesh laminated and sintered, a metal mesh with metal What sintered the powder etc. can be used.

而して、このようにすれば、金属フィルタ24で硫酸生成の反応が起こるだけでなく、その生成された硫酸が直ちに水分保持フィルタを成す金属フィルタ24と反応して硫化物として保持されることになるので、SO2ガスから硫化物とするまでの反応を効率良く進めることができる。 Thus, in this way, not only the reaction of sulfuric acid generation occurs in the metal filter 24, but the generated sulfuric acid immediately reacts with the metal filter 24 constituting the moisture retention filter and is held as sulfide. Therefore, the reaction from SO 2 gas to sulfide can be efficiently advanced.

尚、本発明の排気浄化装置は、上述の形態例にのみ限定されるものではなく、ミストキャッチャは、硫酸ミストを捕えて硫化物を成すものであれば良く、図示の如きミストキャッチ板や脱硫ケースの後壁部、テールパイプに限定されないこと、その他、本発明の要旨を逸脱しない範囲内において種々変更を加え得ることは勿論である。   The exhaust purification device of the present invention is not limited to the above-described embodiment. The mist catcher may be any mist catcher that captures sulfuric acid mist and forms a sulfide. Of course, the present invention is not limited to the rear wall portion of the case and the tail pipe, and various modifications can be made without departing from the scope of the present invention.

本発明を実施する形態の一例を示す概略図である。It is the schematic which shows an example of the form which implements this invention. 本発明の別の形態例を示す概略図である。It is the schematic which shows another form example of this invention.

符号の説明Explanation of symbols

3 排気ガス
4 排気管
5 NOx吸蔵還元触媒
8 燃料
15 水
18 水噴霧手段
19 ミストキャッチ板(ミストキャッチャ)
20 後壁部(ミストキャッチャ)
21 テールパイプ(ミストキャッチャ)
23 セラミックフィルタ(水分保持フィルタ)
24 金属フィルタ(水分保持フィルタ)
3 Exhaust gas 4 Exhaust pipe 5 NOx storage reduction catalyst 8 Fuel 15 Water 18 Water spray means 19 Mist catch plate (mist catcher)
20 Rear wall (mist catcher)
21 Tail pipe (mist catcher)
23 Ceramic filter (moisture retention filter)
24 Metal filter (moisture retention filter)

Claims (3)

排気管の途中にNOx吸蔵還元触媒を備えて該NOx吸蔵還元触媒の入側に燃料を添加し得るようにした排気浄化装置において、NOx吸蔵還元触媒より下流側で排気ガス中に水を霧化して散布する水噴霧手段と、該水噴霧手段の下流側で硫酸ミストを捕え且つ該硫酸ミストと反応して硫化物を成すミストキャッチャとを備えたことを特徴とする排気浄化装置。   In an exhaust gas purification apparatus provided with a NOx occlusion reduction catalyst in the middle of an exhaust pipe so that fuel can be added to the inlet side of the NOx occlusion reduction catalyst, water is atomized into the exhaust gas downstream from the NOx occlusion reduction catalyst. An exhaust purification device comprising: a water spraying means for spraying and a mist catcher that catches sulfuric acid mist on the downstream side of the water spraying means and reacts with the sulfuric acid mist to form a sulfide. 水噴霧手段とミストキャッチャとの間に、水分を保持しながら排気ガスを通過せしめる水分保持フィルタを備えたことを特徴とする請求項1に記載の排気浄化装置。   The exhaust emission control device according to claim 1, further comprising a moisture retention filter that allows exhaust gas to pass while retaining moisture between the water spray means and the mist catcher. 硫酸ミストと反応して硫化物を成し得る金属フィルタにより水分保持フィルタを構成したことを特徴とする請求項1に記載の排気浄化装置。   The exhaust gas purifying apparatus according to claim 1, wherein the moisture retention filter is formed of a metal filter that can react with sulfuric acid mist to form sulfide.
JP2006036654A 2006-02-14 2006-02-14 Exhaust emission control device Pending JP2007218108A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2012145029A (en) * 2011-01-12 2012-08-02 Hino Motors Ltd Exhaust emission control device
WO2012117566A1 (en) 2011-02-28 2012-09-07 トヨタ自動車株式会社 Exhaust gas purification device for internal combustion engine
JPWO2012090865A1 (en) * 2010-12-27 2014-06-05 Jx日鉱日石エネルギー株式会社 Desulfurization apparatus and fuel cell system
JPWO2012090864A1 (en) * 2010-12-27 2014-06-05 Jx日鉱日石エネルギー株式会社 Desulfurization apparatus and fuel cell system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPWO2012090865A1 (en) * 2010-12-27 2014-06-05 Jx日鉱日石エネルギー株式会社 Desulfurization apparatus and fuel cell system
JPWO2012090864A1 (en) * 2010-12-27 2014-06-05 Jx日鉱日石エネルギー株式会社 Desulfurization apparatus and fuel cell system
JP5738318B2 (en) * 2010-12-27 2015-06-24 Jx日鉱日石エネルギー株式会社 Desulfurization apparatus and fuel cell system
JP5738317B2 (en) * 2010-12-27 2015-06-24 Jx日鉱日石エネルギー株式会社 Desulfurization apparatus and fuel cell system
JP2012145029A (en) * 2011-01-12 2012-08-02 Hino Motors Ltd Exhaust emission control device
WO2012117566A1 (en) 2011-02-28 2012-09-07 トヨタ自動車株式会社 Exhaust gas purification device for internal combustion engine

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