JP4344684B2 - Exhaust gas purification device for internal combustion engine - Google Patents

Exhaust gas purification device for internal combustion engine Download PDF

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JP4344684B2
JP4344684B2 JP2004355910A JP2004355910A JP4344684B2 JP 4344684 B2 JP4344684 B2 JP 4344684B2 JP 2004355910 A JP2004355910 A JP 2004355910A JP 2004355910 A JP2004355910 A JP 2004355910A JP 4344684 B2 JP4344684 B2 JP 4344684B2
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exhaust gas
internal combustion
combustion engine
reaction chamber
ammonia
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JP2006161728A (en
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英明 牧田
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英明 牧田
牧田 浩幸
牧田 富美子
牧田 裕子
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Description

本発明は、自動車用ディーゼルエンジン等の内燃機関の排気ガス中に含まれる窒素酸化物(NOX )、炭化水素(HC)、一酸化炭素(CO)、微小粉塵粒子(PM)等の有害物質を効果的に低減する排気ガス浄化装置に関する。 The present invention relates to harmful substances such as nitrogen oxides (NO x ), hydrocarbons (HC), carbon monoxide (CO), and fine dust particles (PM) contained in the exhaust gas of internal combustion engines such as automobile diesel engines. The present invention relates to an exhaust gas purification device that effectively reduces the above.

大気及び環境汚染の大きな要因である自動車の排気ガス対策として、普通乗用車や軽乗用車では触媒機構や燃焼機構によって有害物質を低減する浄化方式が進展している。しかるに、トラックやバス等のディーゼル機関を利用する大型自動車の排気ガスについては、窒素酸化物、炭化水素、一酸化炭素等の有害化学物質に加え、排気を黒煙状にする大量の微小粉塵粒子を含むにも関わらず、充分に有効な浄化方式が見出されておらず、その対策が急務になっている。   As a countermeasure for automobile exhaust gas, which is a major cause of air and environmental pollution, a purification system for reducing harmful substances by a catalyst mechanism and a combustion mechanism has been developed for ordinary passenger cars and light passenger cars. However, for exhaust gas from large vehicles that use diesel engines such as trucks and buses, in addition to harmful chemical substances such as nitrogen oxides, hydrocarbons, and carbon monoxide, a large amount of fine dust particles that make the exhaust blackish However, a sufficiently effective purification method has not been found, and countermeasures are urgently needed.

そこで、本発明らは先に、内燃機関等の有害排ガス低減装置として、燃料油供給経路に介在させた筒状ケーシング内に、多数の強磁石を軸方向所定間隔置きに配設した構造(特許文献1,2)、遠赤外線セラミック片を充填した構造(特許文献3)、中央部に強磁石を配設して両端部に遠赤外線セラミックを充填した構造(特許文献4,5)とし、燃料油がこれら強磁石や遠赤外線セラミックあるいは両者に接触して通過するようにしたものをそれぞれ提案している。更に、本発明者らは、内燃機関等の排気ガス浄化装置として、排気ガス通路に介在させた筒状ケーシング内に、パンチングプレートからなる筒の外周に金属製ネットを巻回した構造の筒状金属ネットフィルターを設け、この筒状金属ネットフィルターの内側に遠赤外線セラミック球体を充填した構造(特許文献6)、同様の筒状金属ネットフィルターからなる内外筒間に遠赤外線セラミック球体を充填すると共に、この充填層中にヒーターを挿入した構造(特許文献7)とし、排気ガスが筒状金属ネットフィルター及び遠赤外線セラミック球体充填層を通過するようにしたものもそれぞれ提案している。
登録実用新案第3023699号公報 特開平9−209850号公開 登録実用新案第3027705号公報 登録実用新案第3012857号公報 登録実用新案第3025486号公報 特開2003−20927公報 特開2003−20934公報
Therefore, the present inventors have previously described a structure in which a large number of strong magnets are arranged at predetermined intervals in the axial direction in a cylindrical casing interposed in a fuel oil supply path as a harmful exhaust gas reduction device for an internal combustion engine or the like (patented) Documents 1 and 2), a structure filled with a far-infrared ceramic piece (Patent Document 3), a structure in which a strong magnet is arranged at the center and a far-infrared ceramic is filled at both ends (Patent Documents 4 and 5), fuel Proposals have been made for oil to pass through these strong magnets, far-infrared ceramics, or both. Furthermore, the present inventors, as an exhaust gas purifying device for an internal combustion engine or the like, have a cylindrical structure in which a metal net is wound around the outer periphery of a cylinder made of a punching plate in a cylindrical casing interposed in an exhaust gas passage. A structure in which a metal net filter is provided, and a far-infrared ceramic sphere is filled inside the cylindrical metal net filter (Patent Document 6), and a far-infrared ceramic sphere is filled between inner and outer cylinders made of the same cylindrical metal net filter. A structure in which a heater is inserted in the packed bed (Patent Document 7) and exhaust gas passes through a cylindrical metal net filter and a far-infrared ceramic sphere packed bed is also proposed.
Registered Utility Model No. 3023699 Published Japanese Patent Laid-Open No. 9-209850 Registered Utility Model No. 30277705 Registered Utility Model No. 3012857 Registered Utility Model No. 3025486 JP 2003-20927 A JP 2003-20934 A

しかして、前記提案の有害排ガス低減装置では、燃料油が強磁石や遠赤外線セラミックと接触することにより、磁気や遠赤外線の作用で燃料油分子が活性化し、内燃機関における燃焼効率が向上し、もって排気ガス中の有害物質が大幅に低減することが確認されている。一方、前記提案の排気ガス浄化装置では、筒状金属ネットフィルターによって排気ガス中の微小粉塵粒子が効率よく除去されると共に、遠赤外線セラミックから放射される遠赤外線によって有害化学物質の分解が進むことが判明している。   Thus, in the proposed harmful exhaust gas reduction device, the fuel oil comes into contact with the strong magnet or the far-infrared ceramic so that the fuel oil molecules are activated by the action of magnetism or far-infrared radiation, and the combustion efficiency in the internal combustion engine is improved. Thus, it has been confirmed that harmful substances in exhaust gas are greatly reduced. On the other hand, in the proposed exhaust gas purification device, the dust particles in the exhaust gas are efficiently removed by the cylindrical metal net filter, and the decomposition of harmful chemical substances proceeds by the far infrared rays emitted from the far infrared ceramics. Is known.

本発明の目的は、前記提案の種々の浄化方式から更に発展して、内燃機関の排気ガス中の有害物質をより大幅に低減でき、近年及び将来的な自動車排ガスの厳しい排出規制にも性能と経済性の両面で充分に対応し得る排気ガス浄化装置を提供することにある。   The object of the present invention is further developed from the various purification methods proposed above, and can significantly reduce harmful substances in the exhaust gas of an internal combustion engine. An object of the present invention is to provide an exhaust gas purifying apparatus that can sufficiently cope with both economical aspects.

上記目的を達成するための手段を図面の参照符号を付して示せば、請求項1の発明は、内燃機関(ディーゼルエンジン1)の排気ガス通路2に、ベローズ構造の周壁3aを有する横型筒状の排ガス反応室3を介装し、この排ガス反応室3に流入する排気ガス中にアンモニア及び水蒸気を注入する注入手段(アンモニア注入装置5)を設けてなる内燃機関の排気ガス浄化装置にある。 If means for achieving the above object is shown with reference numerals in the drawings, the invention of claim 1 is a horizontal cylinder having a bellows structure peripheral wall 3a in an exhaust gas passage 2 of an internal combustion engine (diesel engine 1). interposed the Jo exhaust gas reaction chamber 3, in an exhaust gas purification device of the injection means (ammonia injection unit 5) an internal combustion engine comprising providing a for injecting the ammonia and water vapor in the exhaust gas flowing into the exhaust gas reaction chamber 3 .

また、請求項2の発明は、前記請求項1の排気ガス浄化装置において、前記注入手段が、排ガス反応室3の上流側で排気ガス中にアンモニア水を霧状にして注入するアンモニヤ注入装置5からなるものとしている。   According to a second aspect of the present invention, there is provided an ammonia injection device 5 according to the first aspect, wherein the injection means injects ammonia water into the exhaust gas in the form of a mist upstream of the exhaust gas reaction chamber 3. It is supposed to consist of

請求項3の発明は、前記請求項2の排気ガス浄化装置において、前記アンモニア水の濃度が8%以上で10%未満である構成としている。   According to a third aspect of the present invention, in the exhaust gas purifying apparatus of the second aspect, the ammonia water concentration is 8% or more and less than 10%.

請求項の発明は、前記請求項1〜3のいずれかの排気ガス浄化装置において、前記ベローズ構造の周壁3aを有する筒状の排ガス反応室3の両側端板3b,3b間に、複数本の曲がり防止用長ボルト4が当該排ガス反応室3を外側から挟むように配設されてなる請求項3記載の内燃機関の排気ガス浄化装置。 According to a fourth aspect of the present invention, there is provided an exhaust gas purifying apparatus according to any one of the first to third aspects, wherein a plurality of exhaust gas purification apparatuses are provided between the side end plates 3b, 3b of the cylindrical exhaust gas reaction chamber 3 having the peripheral wall 3a of the bellows structure. 4. An exhaust gas purifying device for an internal combustion engine according to claim 3, wherein the long bolt 4 for preventing the bending is disposed so as to sandwich the exhaust gas reaction chamber 3 from the outside.

請求項の発明は、前記請求項1〜のいずれかの排気ガス浄化装置において、前記排ガス反応室3の排ガス導入口31及び排ガス導出口32が、当該排ガス反応室3内に中心線方向に沿って突入する短筒状に形成され、その周壁31a,32aが多孔状をなすと共に、内端31b,32bが閉塞してなる構成としている。
ガス浄化装置。
According to a fifth aspect of the present invention, in the exhaust gas purifying apparatus according to any one of the first to fourth aspects, the exhaust gas inlet 31 and the exhaust gas outlet 32 of the exhaust gas reaction chamber 3 are arranged in the center line direction in the exhaust gas reaction chamber 3. The peripheral walls 31a and 32a are porous, and the inner ends 31b and 32b are closed.
Gas purification device.

請求項の発明は、前記請求項1〜のいずれかの排気ガス浄化装置において、内燃機関がディーゼルエンジン1であり、前記アンモニア及び水蒸気の注入部よりも上流側の排気ガス通路2にディーゼル微粒子フィルター6が介装されてなる構成としている。 According to a sixth aspect of the present invention, in the exhaust gas purifying apparatus according to any one of the first to fifth aspects, the internal combustion engine is the diesel engine 1, and the diesel is disposed in the exhaust gas passage 2 upstream of the ammonia and water vapor injection portion. The configuration is such that a particulate filter 6 is interposed.

請求項の発明は、前記請求項の排気ガス浄化装置において、前記ディーゼル微粒子フィルター6が酸化触媒を担持したハニカムセラミック層からなるものとしている。 The invention of claim 7 is the exhaust gas purification device of claim 6, wherein the diesel particulate filter 6 is consisted of honeycomb ceramic layer carrying an oxidation catalyst.

請求項の発明は、前記請求項1〜のいずれかの排気ガス浄化装置において、燃料タンク12と内燃機関1とを繋ぐ燃料油供給経路13に、筒状ケーシング14a内に複数の強磁石14b…が配置し、燃料油をこれら強磁石14b…に接触して通過させる燃料油活性化装置14を介装してなる構成としている。 The invention of claim 8 is the exhaust gas purifying apparatus according to any one of claims 1 to 7 , wherein a plurality of strong magnets are provided in the cylindrical casing 14a in the fuel oil supply path 13 connecting the fuel tank 12 and the internal combustion engine 1. 14b... Is arranged, and a fuel oil activation device 14 that allows fuel oil to contact and pass through these strong magnets 14b.

請求項1の発明に係る内燃機関の排気ガス浄化装置によれば、排ガス反応室に流入する排気ガス中にアンモニア及び水蒸気が注入されるから、該排ガス反応室内において、アンモニアの触媒作用によって排気ガス中に含まれる窒素酸化物(NOX )の窒素ガス(N2 )と水(H2 O)への分解が進むことになる。しかして、排ガス反応室内が周壁のベローズ構造による大きな流れ抵抗によって激しい擾乱状態となるため、窒素酸化物の分解反応がより効率よく進行し、最終的に放出される排気ガス中の窒素酸化物が著しく低減される。しかも、温度低下時には周壁下部側で該ベローズ構造の溝部が液溜めとなり、凝縮水分及び余剰のアンモニア水の外部への流出が防止される。また、内燃機関の稼働状況による排気ガスの圧力変動に対応してベローズ構造の周壁が拡縮変形すると共に、熱変動に伴う膨張・収縮の寸法変化もベローズ構造の周壁で吸収されるため、排ガス反応室の器壁や取付部の損傷が回避され、更に該周壁による振動の吸収効果も得られ、もって排気ガス浄化装置の耐久性が向上する。 According to the exhaust gas purifying apparatus for an internal combustion engine according to the invention of claim 1, since ammonia and water vapor in the exhaust gas flowing into the exhaust gas reaction chamber is injected, the exhaust gas reaction chamber, the exhaust by the catalytic action of the ammonia gas The decomposition of nitrogen oxide (NO x ) contained therein into nitrogen gas (N 2 ) and water (H 2 O) proceeds. Therefore, since the exhaust gas reaction chamber is in a severely disturbed state due to the large flow resistance due to the bellows structure of the peripheral wall, the decomposition reaction of nitrogen oxide proceeds more efficiently , and the nitrogen oxide in the exhaust gas finally released is reduced. Remarkably reduced. In addition, when the temperature is lowered, the groove portion of the bellows structure becomes a liquid reservoir on the lower side of the peripheral wall, and the outflow of condensed water and excess ammonia water to the outside is prevented. In addition, the bellows structure peripheral wall expands and contracts in response to exhaust gas pressure fluctuations depending on the operating status of the internal combustion engine, and expansion and contraction dimensional changes due to thermal fluctuations are also absorbed by the bellows structure peripheral wall. Damage to the chamber wall and the mounting portion of the chamber can be avoided, and further, an effect of absorbing vibration by the peripheral wall can be obtained, thereby improving the durability of the exhaust gas purification device.

請求項2の発明によれば、排ガス反応室の上流側で注入された霧状のアンモニア水が高温の排気ガスと均一に混じり合って気化し、アンモニアガスと水蒸気になり、排ガス反応室内で前記の窒素酸化物の分解がより効率よく進行する。   According to the invention of claim 2, the mist-like ammonia water injected on the upstream side of the exhaust gas reaction chamber is uniformly mixed with the high-temperature exhaust gas and vaporized to become ammonia gas and water vapor. Decomposition of nitrogen oxide proceeds more efficiently.

請求項3の発明によれば、前記アンモニア水の濃度が国連、危険物取扱い規則、消防法、劇毒法等の適用対象外となる低濃度であるため、取扱い上の危険性がなく、万一漏れた場合でも健康及び環境面で深刻な事態に至る懸念はない。   According to the invention of claim 3, since the concentration of the ammonia water is a low concentration that is outside the scope of application of the UN, dangerous goods handling regulations, firefighting law, dramatic poisoning law, etc., there is no danger in handling. If leaked, there is no concern about serious health and environmental problems.

請求項の発明によれば、前記ベローズ構造の周壁を有する排ガス反応室は、内圧変動や熱変動による拡縮変形を生じても、外周囲に配置した長ボルトによって全体の曲がり変形が阻止されるため、該曲がり変形による破裂や亀裂等の損傷を生じず優れた耐久性が得られる。 According to the invention of claim 4, the exhaust gas reaction chamber having the peripheral wall of the bellows structure is prevented from being bent entirely by the long bolts arranged on the outer periphery even if expansion / contraction deformation occurs due to internal pressure fluctuation or thermal fluctuation. Therefore, excellent durability can be obtained without causing damage such as rupture and cracking due to the bending deformation.

請求項の発明によれば、排ガス反応室の入口側では排気ガスが中心部の筒状の排ガス導入口から該反応室の周辺に向けて放射状に放出される一方、排ガス反応室の出口側では周辺から中心部の筒状の排ガス導出口へ向かう流れとなるため、排ガス反応室内での排気ガスの擾乱度合が激しくなり、それだけ窒素酸化物の分解反応が効率よく進行する。 According to the invention of claim 5 , while exhaust gas is discharged radially from the cylindrical exhaust gas inlet at the center toward the periphery of the reaction chamber on the inlet side of the exhaust gas reaction chamber, In this case, since the flow is directed from the periphery to the cylindrical exhaust gas outlet, the degree of disturbance of the exhaust gas in the exhaust gas reaction chamber becomes intense, and the decomposition reaction of nitrogen oxide proceeds efficiently.

請求項の発明によれば、ディーゼルエンジンの排気ガスを対象として、前記アンモニア及び水蒸気の注入部よりも上流側に介装されたディーゼル微粒子フィルターにより、排気ガス中の微小粉塵粒子(PM)が除去される。 According to the invention of claim 6 , for the exhaust gas of a diesel engine, the diesel particulate filter interposed upstream of the ammonia and water vapor injection portion allows fine dust particles (PM) in the exhaust gas to be emitted. Removed.

請求項の発明によれば、前記のディーゼル微粒子フィルターが酸化触媒を担持したハニカムセラミック層からなるため、フィルター作用に加えて、触媒活性によってカーボンや炭化水素の酸化分解ならびに一酸化炭素(CO)の酸化が行われ、もって排気ガス中の微小粉塵粒子(PM)が更に低減されると共に、炭化水素や一酸化炭素も著しく低減される。 According to the invention of claim 7 , since the diesel particulate filter is composed of a honeycomb ceramic layer carrying an oxidation catalyst, in addition to the filter action, oxidative decomposition of carbon and hydrocarbons and carbon monoxide (CO) by catalytic activity. As a result, the fine dust particles (PM) in the exhaust gas are further reduced, and the hydrocarbons and carbon monoxide are also significantly reduced.

請求項の発明によれば、内燃機関へ送る燃料油が磁気によって活性化され、該内燃機関での燃焼効率が向上することから、内燃機関から出た段階での排気ガス中の有害物質が減り、それだけ最終的に排出される排気ガスの有害物質量が少なくなる。 According to the invention of claim 8, since the fuel oil sent to the internal combustion engine is activated by magnetism and the combustion efficiency in the internal combustion engine is improved, harmful substances in the exhaust gas at the stage of leaving the internal combustion engine The amount of harmful substances in the exhaust gas that is finally exhausted is reduced accordingly.

以下、本発明の排気ガス浄化装置をトラック用ディーゼルエンジンの排気ガス浄化に適用した実施形態について、図面を参照して具体的に説明する。   Hereinafter, an embodiment in which an exhaust gas purification apparatus of the present invention is applied to exhaust gas purification of a truck diesel engine will be described in detail with reference to the drawings.

図1及び図2において、EはトラックTのディーゼルエンジン、1は該エンジンEからの排気ガス通路、2は排気ガス通路1の上流側に介装されたディーゼル微粒子フィルター(以下、DPFという)、3は排気ガス通路1の下流側に介装された排ガス反応室、4はDPF2と排ガス反応室3との間に介装された蛇腹管、5はDPF2と蛇腹管4との間において排気ガス通路1内にアンモニア水を霧状にして注入するアンモニヤ注入装置、6は燃料タンク、7は燃料タンク6とディーゼルエンジンEとを繋ぐ燃料油供給経路、8は燃料油供給経路7に介装された燃料油活性化装置である。また、図2中、Aはアクセルペダル、Cはアンモニヤ注入用コントローラー、Pはアンモニヤ注入用ポンプである。   1 and 2, E is a diesel engine of the truck T, 1 is an exhaust gas passage from the engine E, 2 is a diesel particulate filter (hereinafter referred to as DPF) interposed upstream of the exhaust gas passage 1, 3 is an exhaust gas reaction chamber interposed downstream of the exhaust gas passage 1, 4 is a bellows tube interposed between the DPF 2 and the exhaust gas reaction chamber 3, and 5 is an exhaust gas between the DPF 2 and the bellows tube 4. An ammonia injection device for injecting ammonia water into the passage 1 in the form of a mist, 6 is a fuel tank, 7 is a fuel oil supply path connecting the fuel tank 6 and the diesel engine E, and 8 is interposed in the fuel oil supply path 7. A fuel oil activation device. In FIG. 2, A is an accelerator pedal, C is an ammonia injection controller, and P is an ammonia injection pump.

DPF2は、マフラー(消音器)形態の筒状ケーシング20内に、白金(Pt)の如き酸化触媒を担持したハニカムセラミック層21が装填されたものからなる。そのハニカムセラミック層21はハニカムの気孔が交互に逆側を片側遮断された形で配列している。   The DPF 2 is formed by loading a honeycomb ceramic layer 21 carrying an oxidation catalyst such as platinum (Pt) in a cylindrical casing 20 in the form of a muffler (silencer). The honeycomb ceramic layers 21 are arranged such that the pores of the honeycomb are alternately cut off on the opposite side.

排ガス反応室3は、ステンレス鋼製であり、図3(A)(B)で詳細に示すように、ベローズ構造の周壁3aを備えた横型円筒状になっている。また、この排ガス反応室3の排気ガス通路1に連通する排ガス導入口31及び排ガス導出口32は、当該排ガス反応室3内に中心線方向に沿って突入する短筒状に構成され、周壁31a,32aがパンチングメタルにて多孔状をなすと共に、先端31b,32bが閉塞している。そして、この排ガス反応室3の両側端板3b,3cには、周方向3箇所に等配して突片30が形成されており、両側端板3b,3cの各々対向する突片30,30間に、排ガス反応室3の外周を三方から挟むように、長ボルト33がナット34…を介して止着されている。   The exhaust gas reaction chamber 3 is made of stainless steel and, as shown in detail in FIGS. 3A and 3B, has a horizontal cylindrical shape with a peripheral wall 3a having a bellows structure. Further, the exhaust gas inlet 31 and the exhaust gas outlet 32 communicating with the exhaust gas passage 1 of the exhaust gas reaction chamber 3 are configured in a short cylinder shape that enters the exhaust gas reaction chamber 3 along the direction of the center line, and the peripheral wall 31a. , 32a is made of a perforated metal and the tips 31b, 32b are closed. Further, on both side end plates 3b, 3c of the exhaust gas reaction chamber 3, projecting pieces 30 are formed equally at three places in the circumferential direction, and the projecting pieces 30, 30 opposed to the both side end plates 3b, 3c, respectively. In the middle, long bolts 33 are fastened via nuts 34 so as to sandwich the outer periphery of the exhaust gas reaction chamber 3 from three directions.

アンモニヤ注入装置5は、タンク51に収容したアンモニア水をポンプPを介してノズル52へ送り、DPF2と蛇腹管4との間の排気ガス管路11内へ該ノズル52より霧状にして注入するようになっている。しかして、アンモニヤ注入用コントローラーCは、ディーゼルエンジンEの回転数に対応してポンプPの吐出量を増減すると共に、アクセルペダルAの踏み込み量がゼロ又は所定値以下になった際にポンプPの吐出を停止又は絞るようになっている。また、タンク51内のアンモニア水量が規定値まで減ったとき、これが液面レベルセンサ53にて検知され、その検知信号によって運転席に設けた報知器54が作動し、ブザーや音声又は発光によって運転者に知らせるようになっている。   The ammonia injection device 5 sends the ammonia water stored in the tank 51 to the nozzle 52 through the pump P, and injects it into the exhaust gas pipe 11 between the DPF 2 and the bellows tube 4 in the form of a mist from the nozzle 52. It is like that. Thus, the ammonia injection controller C increases or decreases the discharge amount of the pump P according to the rotational speed of the diesel engine E, and when the depression amount of the accelerator pedal A becomes zero or a predetermined value or less, The discharge is stopped or throttled. Further, when the amount of ammonia water in the tank 51 decreases to a specified value, this is detected by the liquid level sensor 53, and the alarm 54 provided in the driver's seat is activated by the detection signal, and the operation is performed by a buzzer, sound or light emission. To inform the person.

上記構成の排気ガス浄化装置によれば、ディーゼルエンジンEから排気ガス通路1に排出される排気ガスは、まずDPF2を通る過程で一次浄化されたのち、アンモニヤ注入装置5から供給されるアンモニア水の気化ガス(アンモニアと水蒸気)を混入し、蛇腹管4を経て排ガス反応室3内に流入し、ここでの反応によって二次浄化された上で、排気口(図示省略)へ続く排気ガス管路12へ流入し、排気口より外部へ放出される。そして、この排気口より放出される段階では、窒素酸化物(NOx)、炭化水素(HC)、一酸化炭素(CO)等の有害ガス成分が非常に少なく、且つ微小粉塵粒子(PM)が大幅に低減されて排気煙濃度も薄い状態になっている。   According to the exhaust gas purification apparatus having the above configuration, the exhaust gas discharged from the diesel engine E to the exhaust gas passage 1 is first purified in the process of passing through the DPF 2 and then the ammonia water supplied from the ammonia injection device 5. Vaporized gas (ammonia and water vapor) is mixed, flows into the exhaust gas reaction chamber 3 through the bellows tube 4, is purified by the reaction here, and then continues to the exhaust port (not shown). 12 is discharged from the exhaust port to the outside. At the stage of being discharged from the exhaust port, harmful gas components such as nitrogen oxides (NOx), hydrocarbons (HC), and carbon monoxide (CO) are extremely small, and minute dust particles (PM) are greatly reduced. As a result, the exhaust smoke density is low.

上記のDPF2での一次浄化では、フィルター作用によるPMや煤等の固形粒子の濾過除去と、触媒活性によるPM構成成分のカーボン(C)や炭化水素(HC)の酸化分解ならびに一酸化炭素の酸化が行われる。その酸化反応を次に示す。なお、本来の微小粉塵粒子は3μm以下であるため、一般的に8μm程度までの固形粒子を除去対象とする通常のエアクリーナーでは除去できない。
(1)カーボン … C + O2 → CO2 (炭酸ガス)
(2)炭化水素 … HC + O2 → H2 O(水蒸気),CO2
(3)一酸化炭素 … 2CO + O2 → 2CO2
In the primary purification using the DPF 2 described above, filtration and removal of solid particles such as PM and soot, oxidative decomposition of carbon components (C) and hydrocarbons (HC), and oxidation of carbon monoxide by catalytic activity. Is done. The oxidation reaction is shown below. In addition, since the original fine dust particles are 3 μm or less, they cannot be removed by a normal air cleaner that generally removes solid particles up to about 8 μm.
(1) Carbon: C + O 2 → CO 2 (carbon dioxide)
(2) Hydrocarbon: HC + O 2 → H 2 O (steam), CO 2
(3) Carbon monoxide: 2CO + O 2 → 2CO 2

排ガス反応室3での二次浄化は、排気ガス中に含まれていた窒素酸化物(NOx)のアンモニアとの反応による窒素ガスと水への分解である。すなわち、アンモニアには還元作用があり、次のような反応によって排気ガス中の一酸化窒素(NO)及び二酸化窒素(NO2 )から酸素を奪って窒素ガス(N2 )と水蒸気(H2 O)を生成する。
(4) 2NO + 2NH4 OH → 2N2 + 4H2 O + H2
(5) 4NO2 + 4NH4 OH → 4N2 + 10H2 O + O2
(6) 2H2 + O2 → 2H2
The secondary purification in the exhaust gas reaction chamber 3 is decomposition of nitrogen oxide (NOx) contained in the exhaust gas into nitrogen gas and water by reaction with ammonia. That is, ammonia has a reducing action, and nitrogen gas (N 2 ) and water vapor (H 2 O) are deprived of oxygen from nitrogen monoxide (NO) and nitrogen dioxide (NO 2 ) in the exhaust gas by the following reaction. ) Is generated.
(4) 2NO + 2NH 4 OH → 2N 2 + 4H 2 O + H 2
(5) 4NO 2 + 4NH 4 OH → 4N 2 + 10H 2 O + O 2
(6) 2H 2 + O 2 → 2H 2 O

使用するアンモニア水としては、濃度が8%以上で10%未満のものが好適である。これは、10%未満という低濃度の場合、国連、危険物取扱い規則、消防法、劇毒法等の適用対象外であるように、取扱い上の危険性がなく、万一漏れた場合でも健康及び環境面で深刻な事態に至る懸念がないことによる。ただし、アンモニア水の濃度が8%未満になると後述するNOX 分解作用を充分に発揮できなくなるため、該濃度を8%以上とするが、±0.5%程度の誤差を見越して設定濃度を9%にすることが推奨される。 As the aqueous ammonia used, one having a concentration of 8% or more and less than 10% is suitable. In the case of a low concentration of less than 10%, there is no danger in handling, as it is not covered by the UN, Dangerous Goods Handling Regulations, Fire Service Law, Violent Poison Law, etc. This is because there is no concern about serious environmental problems. However, if the concentration of ammonia water is less than 8%, it will not be possible to fully exhibit the NO x decomposition action described later. Therefore, the concentration is set to 8% or more. 9% is recommended.

しかして、排ガス反応室3にあっては、ベローズ構造の周壁3aによって大きな流れ抵抗を生じることに加え、短筒状をなして突入した排ガス導入口31及び排ガス導出口32の内端が閉塞し、多孔状の周壁31a,32aよりガスが出入するから、入口側では中心から周辺に向けて放射状に排気ガスが放出され、出口側では周辺から中心部に向かう流れになり、導入口31から導出口32への直線的な流れを生じず、もって内部は激しい擾乱状態となって前記の窒素酸化物の分解反応が促進される。従って、排ガス反応室3の全長が短くとも高いNOx削減効果が得られる。   Thus, in the exhaust gas reaction chamber 3, in addition to causing a large flow resistance by the peripheral wall 3a of the bellows structure, the inner ends of the exhaust gas inlet 31 and the exhaust gas outlet 32 that have entered into a short cylinder shape are blocked. Since the gas enters and exits from the porous peripheral walls 31a and 32a, the exhaust gas is discharged radially from the center toward the periphery on the inlet side, and flows from the periphery toward the center on the outlet side. A linear flow to the outlet 32 is not generated, and the inside becomes a severely disturbed state, and the decomposition reaction of the nitrogen oxide is promoted. Therefore, even if the total length of the exhaust gas reaction chamber 3 is short, a high NOx reduction effect can be obtained.

また、この排ガス反応室3はベローズ構造の周壁3aを備えた横円筒状であるため、温度低下時には内面下部のベローズ溝部が液溜めとなり、凝縮水分及び余剰のアンモニア水は外部へ流出することなく貯留される。そして、この貯留分は次の温度上昇に伴って気化し、アンモニアは反応消費されると共に、凝縮水分は水蒸気として排気ガスに付随して排出される。   Further, since the exhaust gas reaction chamber 3 has a horizontal cylindrical shape with a peripheral wall 3a having a bellows structure, when the temperature is lowered, the bellows groove portion at the bottom of the inner surface becomes a liquid reservoir, so that condensed water and excess ammonia water do not flow out to the outside. Stored. The stored portion is vaporized as the next temperature rises, ammonia is reacted and consumed, and condensed water is discharged as water vapor along with the exhaust gas.

排気ガスの排出量はエンジン回転数に略比例して増減するが、このエンジン回転数を回転数センサー(図示省略)で検出し、その検出信号に基づいてアンモニヤ注入用コントローラーCがアンモニア水の注入量をエンジン回転数に応じて段階的又は連続的に増減するから、該排出量の変動によるアンモニア水の注入量の過不足を生じず、高いNOx効率が安定的に維持される。因みに、トラック用ディーゼルエンジンEのエンジン回転数と9%アンモニア水の好適注入量との関係を例示すれば、エンジン排気量毎の目安は次の表1のようになる。   The exhaust gas emission amount increases or decreases in proportion to the engine speed. The engine speed is detected by a speed sensor (not shown), and the ammonia injection controller C injects ammonia water based on the detection signal. Since the amount is increased or decreased stepwise or continuously in accordance with the engine speed, high and low NOx efficiency is stably maintained without causing excess or deficiency in the amount of ammonia water injected due to fluctuations in the exhaust amount. Incidentally, if the relationship between the engine speed of the truck diesel engine E and the preferred injection amount of 9% ammonia water is shown as an example, the standard for each engine displacement is as shown in Table 1 below.

Figure 0004344684
Figure 0004344684

しかして、例えば坂道での下り走行状態とか、信号待ちや渋滞中のアイドリング状態のようにエンジンEにかかる負荷が小さい状況下では、排気ガス中に含まれるNOx量も少なくなるが、かかる状況においては運転者がアクセルペダルAから足を離すか踏み込みを弛めることを利用し、該アクセルペダルAの踏み込み量がゼロ又は所定値以下になった際にアクセルスイッチ(図示省略)で検知し、その検知信号に基づいてコントローラーCがアンモニア水の注入を停止又は減少させる。従って、エンジンEにかかる負荷の小さい状況下で、アンモニア水が注入過多になって未反応状態で排気ガスに混じって放出される懸念はない。   Therefore, for example, under a situation where the load on the engine E is small, such as a downhill running state on a slope or an idling state while waiting for traffic lights or traffic jams, the amount of NOx contained in the exhaust gas is reduced. Uses the fact that the driver releases his foot from the accelerator pedal A or relaxes the depression, and when the depression amount of the accelerator pedal A is zero or below a predetermined value, it is detected by an accelerator switch (not shown), and the detection Based on the signal, the controller C stops or reduces the injection of the ammonia water. Therefore, there is no concern that ammonia water is excessively injected under the condition of a small load on the engine E and is discharged in an unreacted state and mixed with exhaust gas.

一方、ディーゼルエンジンEの稼働状況によって排気ガスの排出量が変化するため、排ガス反応室3内の圧力が大きく変動するが、本実施形態では該圧力変動に対応してベローズ構造の周壁3aが拡縮変形する。また、エンジン停止時と運転時とで排ガス反応室3内に大きな温度差を生じるが、この温度変動に伴う膨張・収縮の寸法変化もベローズ構造の周壁3aによって吸収される。しかも、このように前記圧力や温度の変動に伴って周壁3aが拡縮変形しても、外周囲に配置した長ボルト33によって排ガス反応室3全体の曲がり変形が阻止される。従って、本実施形態では、前記圧力や温度の変動による排ガス反応室3の器壁の破裂や亀裂ならびに取付部の損傷が回避され、優れた耐久性が得られる。   On the other hand, the exhaust gas emission amount varies depending on the operating condition of the diesel engine E, and thus the pressure in the exhaust gas reaction chamber 3 varies greatly. In this embodiment, the peripheral wall 3a of the bellows structure expands and contracts in response to the pressure variation. Deform. In addition, a large temperature difference is generated in the exhaust gas reaction chamber 3 when the engine is stopped and when the engine is operating. The expansion / contraction dimensional change due to the temperature fluctuation is also absorbed by the peripheral wall 3a of the bellows structure. Moreover, even if the peripheral wall 3a is expanded or contracted due to the fluctuation of the pressure or temperature in this way, the entire exhaust gas reaction chamber 3 is prevented from being bent and deformed by the long bolts 33 arranged on the outer periphery. Therefore, in this embodiment, rupture and cracking of the wall of the exhaust gas reaction chamber 3 due to fluctuations in the pressure and temperature and damage to the mounting portion are avoided, and excellent durability is obtained.

なお、排ガス反応室3の上流側に介在させた蛇腹管4は、排ガス反応室3と同様のベローズ構造の周壁の伸縮性を利用し、エンジン稼働や走行に伴う振動の吸収と、圧力及び温度の変動による排気ガス通路1全体の伸縮の吸収を担い、もって管路全体の耐久性を高めるように機能している。無論、排ガス反応室3においても、ベローズ構造の周壁3aによる振動吸収作用はある。   The bellows tube 4 interposed upstream of the exhaust gas reaction chamber 3 utilizes the elasticity of the peripheral wall of the bellows structure similar to that of the exhaust gas reaction chamber 3, and absorbs vibrations due to engine operation and running, pressure and temperature. It functions to absorb the expansion and contraction of the entire exhaust gas passage 1 due to the fluctuation of the above, and thereby to improve the durability of the entire pipeline. Of course, also in the exhaust gas reaction chamber 3, there is a vibration absorbing action by the peripheral wall 3a of the bellows structure.

ところで、上記の一次浄化と二次浄化の作用自体は処理順序が前後逆であっても支障なく発揮されるが、アンモニア水の注入によって排気ガス温度はある程度低下する一方、DPF2での触媒活性による酸化反応には高温が望ましいことから、本実施形態のようにアンモニア水の注入をDPF2の下流側で行う構成が推奨される。また、エンジンEからDPF2の出口までの排気ガス通路1は、ガラスウール等の断熱材で包み込み、その外周をアルミ箔等で被覆して保温することが好ましい。しかして、排気ガス温度は、例えばディーゼルエンジンEを出た段階で480℃程度である場合、上記保温により、DPF2の出口で350〜400℃程度、排ガス反応室3の出口で230℃程度となる。   By the way, although the primary purification and the secondary purification itself are exerted without any problem even if the processing order is reversed, the temperature of the exhaust gas is lowered to some extent by the injection of ammonia water, but due to the catalytic activity in the DPF2. Since a high temperature is desirable for the oxidation reaction, a configuration in which ammonia water is injected downstream of the DPF 2 as in this embodiment is recommended. Further, it is preferable that the exhaust gas passage 1 from the engine E to the outlet of the DPF 2 is wrapped with a heat insulating material such as glass wool and the outer periphery thereof is covered with an aluminum foil or the like to keep the temperature. Thus, for example, when the exhaust gas temperature is about 480 ° C. when leaving the diesel engine E, the temperature is about 350 to 400 ° C. at the outlet of the DPF 2 and about 230 ° C. at the outlet of the exhaust gas reaction chamber 3 due to the heat retention. .

燃料油供給経路7に介装された燃料油活性化装置8は、図4に示すように、円筒状ケース81に中心線に沿う固定軸82が貫設され、この固定軸82に異方性フェライト等よりなる多数枚の強磁石板83…が一定間隔置きに止着された構造を有している。そして、これら強磁石板83…は、各々が略正方形の角部を円弧状に切除した形状を備えており、その周方向の向きが順次少しずつ変わるようにして固定軸82に止着され、もって正方形の四辺とケース81の内周面との間に構成される流通間隙の位置がケース軸方向で順次変化するように設定している。84はケース24内の要所で固定軸25を保持する保持板で、円形の一部が流通間隙として切除された形状を備え、ケース81に一体化されている。   As shown in FIG. 4, the fuel oil activation device 8 interposed in the fuel oil supply path 7 has a fixed shaft 82 extending through the cylindrical case 81 along the center line, and the fixed shaft 82 is anisotropic. A large number of strong magnet plates 83 made of ferrite or the like are fixed at regular intervals. These strong magnet plates 83 are each provided with a shape obtained by cutting a substantially square corner portion into an arc shape, and are fixed to the fixed shaft 82 in such a manner that its circumferential direction changes little by little. Accordingly, the position of the flow gap formed between the four sides of the square and the inner peripheral surface of the case 81 is set so as to sequentially change in the case axial direction. Reference numeral 84 denotes a holding plate that holds the fixed shaft 25 at an important point in the case 24, and has a shape in which a circular part is cut off as a flow gap, and is integrated with the case 81.

しかして、この燃料油活性化装置8では、燃料タンク6より供給される軽油が、円筒状ケース81の一端に設けた入口8aより流入し、各強磁石板83とケース81の内周面との間を順次通過して出口8bに至る過程で、強磁石板83…による強い磁力作用を受けて活性化する。従って、ディーゼルエンジンEでの燃焼効率が向上し、燃費が低減すると共に、該エンジンEから出た段階での排気ガス中の有害物質が減り、それだけ最終的に排出される排気ガスの有害物質量が少なくなる。   Thus, in the fuel oil activation device 8, the light oil supplied from the fuel tank 6 flows in from the inlet 8 a provided at one end of the cylindrical case 81, and each strong magnet plate 83 and the inner peripheral surface of the case 81 In the process of sequentially passing between the two and reaching the outlet 8b, it is activated by receiving a strong magnetic force action by the strong magnet plates 83. Therefore, the combustion efficiency in the diesel engine E is improved, the fuel consumption is reduced, and the harmful substances in the exhaust gas at the stage of exiting from the engine E are reduced. Less.

本発明の排気ガス浄化装置は、実施形態で用いたような燃料油活性化装置及びDPFの一方又は両方を省略した構成を包含するが、特に微小粉塵粒子(PM)を効果的に低減する上でDPFの使用が推奨される。しかして、DPFとしては、種々の構造の市販品を使用でき、その中でも前記実施形態で用いたような触媒活性を有するものが望ましいが、フィルター機能のみでもPM削減能力が高いものであれば好適に使用できる。なお、前記実施形態で用いたDPF2のように酸化触媒をセラミックに担持させた構成では、セラミックより放射される遠赤外線効果によって触媒活性が高められるため、例えば道路の渋滞によってエンジン回転数が落ちている場合等、排気ガス温度が低下している状態でも高いPM削減率を達成できる。   The exhaust gas purifying apparatus of the present invention includes a configuration in which one or both of the fuel oil activating apparatus and the DPF as used in the embodiment are omitted. In particular, the exhaust gas purifying apparatus can effectively reduce fine dust particles (PM). The use of DPF is recommended. Thus, as the DPF, commercially available products having various structures can be used, and among them, those having catalytic activity as used in the above-described embodiment are preferable, but those having a high PM reduction ability only by the filter function are preferable. Can be used for In the configuration in which the oxidation catalyst is supported on the ceramic as in the DPF 2 used in the above embodiment, the catalytic activity is enhanced by the far-infrared effect radiated from the ceramic. For example, the engine speed decreases due to traffic congestion on the road. A high PM reduction rate can be achieved even when the exhaust gas temperature is low.

なお、前記実施形態では排ガス反応室3の上流側に伸縮及び振動吸収用の蛇腹管4を配しているが、DPF2や排ガス反応室3の据え付け状態によっては、このような蛇腹管4は省略可能である。その他、本発明の排気ガス浄化装置の細部構成については実施形態以外に種々設計変更可能である。また、前記実施形態では内燃機関として燃料に軽油を用いるディーゼルエンジンを例示したが、本発明の排気ガス浄化装置はディーゼルエンジン以外の種々の内燃機関にも同様に適用可能である。 While in the previous SL embodiment are arranged bellows tube 4 for stretching and vibration absorption on the upstream side of the exhaust gas reaction chamber 3, depending on the installation condition of DPF2 and exhaust gas reaction chamber 3, such bellows tube 4 It can be omitted. In addition, the detailed configuration of the exhaust gas purifying apparatus of the present invention can be variously modified in addition to the embodiment. Moreover, although the diesel engine which uses light oil as a fuel was illustrated as an internal combustion engine in the said embodiment, the exhaust-gas purification apparatus of this invention is applicable similarly to various internal combustion engines other than a diesel engine.

次に、本発明の排気ガス浄化装置による自動車ディーゼルエンジンの排気ガス浄化の実施例について、該排気ガス浄化装置を用いない比較例と対比して説明する。   Next, an embodiment of exhaust gas purification of an automobile diesel engine by the exhaust gas purification device of the present invention will be described in comparison with a comparative example in which the exhaust gas purification device is not used.

比較例1・実施例1
下記の自動車Aを用い、比較例1では排気ガス浄化装置を搭載せずに表2に示す13運転モードで、実施例1では図2に示す装置構成の排気ガス浄化装置を搭載して表4に示す13運転モードで、それぞれ試験を行って希釈排出ガス成分濃度(CO,HC,NOX ,CO2 )、希釈率、希釈排出ガス量、時間当たりのガス排出量、PM総排出量を測定した。その結果を比較例1は表3に、実施例1は表5に示す。なお、試験内容と浄化装置構成の詳細は次のとおりである。
Comparative Example 1 / Example 1
The following automobile A is used, and in Comparative Example 1, the exhaust gas purification device is not installed, but in the 13 operation modes shown in Table 2, and in Example 1, the exhaust gas purification device having the device configuration shown in FIG. In each of the 13 operation modes shown in Fig. 1, the test is performed to measure the diluted exhaust gas component concentration (CO, HC, NO x , CO 2 ), dilution rate, diluted exhaust gas amount, gas exhaust amount per hour, and total PM exhaust amount. did. The results are shown in Table 3 for Comparative Example 1 and Table 5 for Example 1. The details of the test contents and the configuration of the purification device are as follows.

〔自動車A〕
車名・型式 : 日野ディーゼルトラック U−FD3HLAK
走行距離数 : 490379km(比較例1)、490311km(実施例1) 車両総重量 : 5530kg
エンジン型式 : H07D(4サイクル−6気筒)
総排気量 : 7.412L
[Car A]
Car name / model: Hino Diesel Truck U-FD3HLAK
Number of mileage: 490379 km (Comparative Example 1), 490311 km (Example 1) Total vehicle weight: 5530 kg
Engine model: H07D (4 cycle-6 cylinder)
Total displacement: 7.412L

〔試験内容〕
試験機関 : 財団法人 日本車両検査協会 自動車試験所
試験期日 ; 平成15年12月2日
試験項目 :
(1)シャシダイナモメータによるディーゼル自動車13モード排出ガス試験
(2)ディーゼル排気煙濃度試験(フリーアクセルモード)
使用燃料 : 低硫黄軽油
〔contents of the test〕
Testing organization: Japan Vehicle Inspection Association Automobile Testing Laboratory Test date: December 2, 2003 Test item:
(1) Diesel vehicle 13 mode exhaust gas test with chassis dynamometer (2) Diesel exhaust smoke concentration test (free accelerator mode)
Fuel used: Low sulfur gas oil

〔浄化装置構成〕
DPF : Dinax A/S社製SOOTEX−RN41(白金担持ハニカムセ ラミック型DPF)
アンモニア注入装置 : タンク…SUS304製−容量50L、ポンプ…最大吐出 量450ml/min、使用アンモニア水濃度9%、注入量…表1を基準
排ガス反応室 : 牧田運送社製MB0001(図3の構造で全てSUS304製) 反応室…全長500mm,外径200mm
導出入口…内径77mm、反応室内突入長さ200mm、周壁に径5mmの 孔が150個(周方向15列、径方向10列)
燃料油活性化装置 : 牧田運送社製Futures
[Purification device configuration]
DPF: SONETEX-RN41 (platinum-supporting honeycomb ceramic type DPF) manufactured by Dinax A / S
Ammonia injection device: Tank ... Made of SUS304-Capacity 50L, Pump ... Maximum discharge amount 450ml / min, Ammonia water concentration 9%, Injection amount ... Based on Table 1 Exhaust gas reaction chamber: MB0001 made by Makita Transportation Co., Ltd. (with the structure of FIG. 3) All made of SUS304) Reaction chamber ... Overall length 500mm, outer diameter 200mm
Outlet inlet: inside diameter 77 mm, reaction chamber entry length 200 mm, peripheral wall with 150 holes with a diameter of 5 mm (15 rows in the circumferential direction, 10 rows in the radial direction)
Fuel oil activation device: Futures manufactured by Makita Transportation Co., Ltd.

比較例2・実施例2
下記の自動車Bを用い、比較例2では排気ガス浄化装置を搭載せずに表6に示す13運転モードで、実施例2では図2に示す装置構成の排気ガス浄化装置を搭載して表8に示す13運転モードで、それぞれ試験を行って希釈排出ガス成分濃度、希釈率、希釈排出ガス量、時間当たりのガス排出量、PM総排出量を測定した。その結果を比較例2は表7に、実施例2は表9に示す。なお、浄化装置構成の詳細は実施例1と同じである。
Comparative Example 2 and Example 2
The following automobile B was used, and in Comparative Example 2, the exhaust gas purification device was not installed, but in the 13 operation modes shown in Table 6, and in Example 2, the exhaust gas purification device having the device configuration shown in FIG. Each of the 13 operation modes shown in Fig. 1 was tested to measure the diluted exhaust gas component concentration, dilution rate, diluted exhaust gas amount, gas exhaust amount per hour, and total PM exhaust amount. The results are shown in Table 7 for Comparative Example 2 and Table 9 for Example 2. The details of the purification device configuration are the same as those in the first embodiment.

〔自動車B〕
車名・型式 : ニッサンディーゼルトラック KC−MK211HH
走行距離数 : 166275km(比較例2)、166132km(実施例2) 車両総重量 : 7990kg
エンジン型式 : FE6(4サイクル−6気筒)
総排気量 : 6.925L
[Car B]
Car name / model: Nissan Diesel Truck KC-MK211HH
Number of mileage: 166275 km (Comparative Example 2), 166132 km (Example 2) Total vehicle weight: 7990 kg
Engine model: FE6 (4 cycle-6 cylinder)
Total displacement: 6.925L

〔試験内容〕
試験機関 : 財団法人 日本車両検査協会 自動車試験所
試験期日 ; 平成15年10月16日
試験項目 :
(1)シャシダイナモメータによるディーゼル自動車13モード排出ガス試験
(2)ディーゼル排気煙濃度試験(フリーアクセルモード)
使用燃料 : 低硫黄軽油
〔contents of the test〕
Testing organization: Japan Vehicle Inspection Association Automobile Testing Laboratory Test Date: October 16, 2003 Test Items:
(1) Diesel vehicle 13 mode exhaust gas test with chassis dynamometer (2) Diesel exhaust smoke concentration test (free accelerator mode)
Fuel used: Low sulfur gas oil

実施例3
比較例2及び実施例2で用いた自動車Bについて、実施例2と同じ排気ガス浄化装置を搭載して稼働させながら、九州地区で高速道路及び一般道路を含む30,000kmの実走行耐久テストを行ったところ、走行期間中に該浄化装置の異常や取付部位の損傷は全く認められなかった。そして、この実走行耐久テスト後に、(財)日本車両検査協会 自動車試験所で比較例2及び実施例2と同様の試験を行った(試験期日…平成15年11月28日)。その13運転モードを表10に、試験結果を表11にそれぞれ示す。

Figure 0004344684
Example 3
About the automobile B used in Comparative Example 2 and Example 2, an actual running durability test of 30,000 km including a highway and a general road was performed in the Kyushu region while operating the same exhaust gas purifying device as that of Example 2 in operation. As a result, no abnormality of the purification device or damage to the attachment site was observed during the running period. Then, after this actual running durability test, a test similar to Comparative Example 2 and Example 2 was conducted at the Japan Vehicle Inspection Association Car Testing Laboratory (Test Date: November 28, 2003). Table 13 shows the 13 operation modes, and Table 11 shows the test results.
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

表12に、上記比較例1,2及び実施例1〜3の試験による排ガス成分とPMの平均排出量と本発明による削減率(%)ならびに黒煙排出量を示す。なお、平均排出量は各成分の排出量合計を仕事量の合計で割った値である。   Table 12 shows the average emissions of exhaust gas components and PM, the reduction rate (%), and the amount of black smoke emitted by the present invention in the tests of Comparative Examples 1 and 2 and Examples 1 to 3. The average emission amount is a value obtained by dividing the total emission amount of each component by the total work amount.

Figure 0004344684
Figure 0004344684

この表12に示すように、本発明の排気ガス浄化装置を用いた場合は、3万kmの実走行耐久性テスト後(実施例3)を含めて、浄化装置のない場合(比較例1,2)に比べ、排気ガス中の窒素酸化物(NOX )では80%以上、微小粉塵粒子(PM)も85%以上といった極めて高い削減率が得られており、更に一酸化炭素(CO)や黒煙では略100%、炭化水素(HC)についても50%前後と大幅に低減している。従って、本発明の排気ガス浄化装置によれば、排気ガス中の有害成分を効果的に低減できることが判る。 As shown in Table 12, when the exhaust gas purifying apparatus of the present invention is used, the case where there is no purifying apparatus (Comparative Example 1,) after the actual running durability test of 30,000 km (Example 3). Compared to 2), nitrogen oxides (NO x ) in the exhaust gas have an extremely high reduction rate of 80% or more and fine dust particles (PM) of 85% or more. Furthermore, carbon monoxide (CO) and Black smoke is about 100% and hydrocarbon (HC) is about 50%. Therefore, according to the exhaust gas purification apparatus of the present invention, it can be seen that harmful components in the exhaust gas can be effectively reduced.

実施例4
下記の自動車Cを用い、図2に示す装置構成の排気ガス浄化装置を搭載して表13に示す13運転モードで試験を行って希釈排出ガス成分濃度(CO,HC,NOX ,CO2 )、希釈率、希釈排出ガス量、時間当たりのガス排出量を測定した。その結果を表14示す。試験内容と浄化装置構成の詳細は次のとおりである。
Example 4
The following automobile C is used, and the exhaust gas purification device having the device configuration shown in FIG. 2 is mounted, and the test is performed in the 13 operation modes shown in Table 13, and the diluted exhaust gas component concentrations (CO, HC, NO x , CO 2 ) The dilution rate, the amount of diluted exhaust gas, and the amount of gas discharged per hour were measured. The results are shown in Table 14. Details of the test contents and the purification device configuration are as follows.

〔自動車C〕
車名・型式 : 三菱ディーゼルトラック P−FU415N改
走行距離数 : 813284km
車両総重量 : 19715kg
エンジン型式 : 8DC9(4サイクル−8V気筒)
総排気量 : 16.0L
[Car C]
Car name / model: Mitsubishi Diesel Truck P-FU415N modified Traveling distance: 81284 km
Total vehicle weight: 19715kg
Engine model: 8DC9 (4 cycle-8V cylinder)
Total displacement: 16.0L

〔試験内容〕
試験機関 : 財団法人 日本自動車研究所
試験期日 ; 平成16年7月5日
試験項目 : シャシダイナモメータによるディーゼル自動車13モード排出ガス 試験
使用燃料 : 低硫黄軽油
〔contents of the test〕
Test organization: Japan Automobile Research Institute Test date: July 5, 2004 Test item: Diesel vehicle 13-mode exhaust gas test with chassis dynamometer Fuel used: Low sulfur gas oil

〔浄化装置構成〕
DPF : Dinax A/S社製SOOTEX−RN43(白金担持ハニカムセ ラミック型DPF)
アンモニア注入装置 : タンク…SUS304製−容量98L、ポンプ…最大吐出 量450ml/min、使用アンモニア水濃度9%、注入量…表1を基準
排ガス反応室 : 牧田運送社製MB0004(図3の構造で全てSUS304製) 反応室…全長500mm,外径300mm
導出入口…内径77mm、反応室内突入長さ200mm、周壁に径5mmの 孔が150個(周方向15列、径方向10列)
燃料油活性化装置 : 牧田運送社製Futures
[Purification device configuration]
DPF: SONETEX-RN43 (platinum-supporting honeycomb ceramic type DPF) manufactured by Dinax A / S
Ammonia injection device: tank ... made of SUS304-capacity 98L, pump ... maximum discharge amount 450ml / min, used ammonia water concentration 9%, injection amount ... based on Table 1 Exhaust gas reaction chamber: Makita Transport Co., Ltd. MB0004 (with structure of FIG. 3) All made of SUS304) Reaction chamber ... Overall length 500mm, outer diameter 300mm
Outlet inlet: inside diameter 77 mm, reaction chamber entry length 200 mm, peripheral wall with 150 holes with a diameter of 5 mm (15 rows in the circumferential direction, 10 rows in the radial direction)
Fuel oil activation device: Futures manufactured by Makita Transportation Co., Ltd.

実施例5
下記の自動車Dを用い、図2に示す装置構成の排気ガス浄化装置を搭載して表15に示す13運転モードで試験を行って希釈排出ガス成分濃度(CO,HC,NOX ,CO2 )、希釈率、希釈排出ガス量、時間当たりのガス排出量を測定した。その結果を表16に示す。なお、期日を含む試験内容と浄化装置構成の詳細は実施例4と同じである。
Example 5
The following automobile D is used, and the exhaust gas purifying apparatus having the apparatus configuration shown in FIG. 2 is mounted and tested in the 13 operation modes shown in Table 15, and diluted exhaust gas component concentrations (CO, HC, NO x , CO 2 ) The dilution rate, the amount of diluted exhaust gas, and the amount of gas discharged per hour were measured. The results are shown in Table 16. The details of the test including the date and the details of the purification device configuration are the same as those in the fourth embodiment.

〔自動車D〕
車名・型式 : いすずディーゼルトラック P−CXM19P改
走行距離数 : 152115km
車両総重量 : 19975kg
エンジン型式 : 10PC1(4サイクル−10V気筒)
総排気量 : 15.0L
[Car D]
Car name / model: Isuzu Diesel truck P-CXM19P modified Travel distance: 152 115km
Total vehicle weight: 19975kg
Engine model: 10PC1 (4 cycle-10V cylinder)
Total displacement: 15.0L

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

Figure 0004344684
Figure 0004344684

次の表17は上記実施例4,5の試験による排ガス成分の平均排出量を示す。この表17より、車両総重量が20トン近い大型ディーゼルトラックにおいても、本発明の排気ガス浄化装置を用いることにより、排気ガス中のNOxやPMを始めとする有害成分を非常に少なくできることが判る。

Figure 0004344684
Table 17 below shows the average emission amount of exhaust gas components in the tests of Examples 4 and 5 above. From Table 17, it can be seen that even in a large diesel truck having a gross vehicle weight of nearly 20 tons, the use of the exhaust gas purification apparatus of the present invention can significantly reduce harmful components such as NOx and PM in the exhaust gas. .
Figure 0004344684

実施例6
実施例2で用いた自動車B及び実施例4で用いた自動車Dについて、実施例2及び実施例4と同じ排気ガス浄化装置を各々搭載して稼働させながら、国道2号線の芦屋−宝塚間57kmの実走行を行い、この走行全区間中を通して荷台に載った作業者が半導体製造ガス検知器(新コスモ電機社製XD303アンモニア)により、排気口から放出される排気ガス中のアンモニア濃度を継続的に測定した。しかして、この区間は標高約600mの有馬温泉を経る上り下りとカーブの多いコースであり、しかも途中での信号による停止が芦屋側で46回、宝塚側で21回もあったが、排気ガス中のアンモニア濃度はエンジンの負荷状態に関わらず、自動車Bでは終始0.1ppm以下、自動車Dでは終始0ppm(測定限度外)であった。この結果から、本発明の排気ガス浄化装置は、処理剤にアンモニア水を利用するが、エンジンEにかかる負荷の変動が大きく且つ頻繁に起こる状況下でも、アンモニア水が排気ガスに混じって放出される懸念がないことが判る。
Example 6
About the automobile B used in Example 2 and the automobile D used in Example 4, the same exhaust gas purifying device as that of Example 2 and Example 4 was mounted and operated, and the road between Ashiya and Takarazuka on National Route 2 was 57 km. The operator who was on the platform throughout the entire section of the vehicle continuously controlled the ammonia concentration in the exhaust gas discharged from the exhaust port using the semiconductor manufacturing gas detector (XD303 ammonia manufactured by New Cosmo Electric Co., Ltd.). Measured. However, this section is a course with a lot of ascending and descending through the Arima Hot Spring at an altitude of about 600m, and there were 46 stops at the Ashiya side and 21 times at the Takarazuka side in the middle, but the exhaust gas The ammonia concentration was 0.1 ppm or less throughout the vehicle B and 0 ppm throughout the vehicle D (outside the measurement limit) regardless of the engine load. From this result, the exhaust gas purifying apparatus of the present invention uses ammonia water as the treatment agent, but the ammonia water is mixed with the exhaust gas and released even under a situation in which the load on the engine E varies greatly and frequently occurs. It can be seen that there is no concern.

本発明の一実施形態に係る内燃機関の排気ガス浄化装置を取り付けたトラックの概略側面図である。1 is a schematic side view of a truck equipped with an exhaust gas purification device for an internal combustion engine according to an embodiment of the present invention. 同排気ガス浄化装置の概略構成図である。It is a schematic block diagram of the same exhaust gas purification device. 同排気ガス浄化装置の排ガス反応室を示し、(A)は正面図、(B)は(A)のB−B線の断面矢視図である。The exhaust gas reaction chamber of the exhaust gas purification apparatus is shown, (A) is a front view, and (B) is a cross-sectional view taken along line BB in (A). 同排気ガス浄化装置に用いる燃料油活性化装置の縦断側面図である。It is a vertical side view of the fuel oil activation device used for the exhaust gas purification device.

符号の説明Explanation of symbols

1 排気ガス通路
2 ディーゼル微粒子フィルター
3 排ガス反応室
3a 周壁部
31 排ガス導入口
31a 周壁
31b 内端
32 排ガス導出口
32a 周壁
32b 内端
33 長ボルト
5 アンモニア注入装置
51 アンモニア水タンク
6 燃料タンク
7 燃料油供給経路
8 燃料油活性化装置
81 筒状ケーシング
83 強磁石
A アクセルペダル
C アンモニヤ注入用コントローラー
E ディーゼルエンジン
P アンモニヤ注入用ポンプ
DESCRIPTION OF SYMBOLS 1 Exhaust gas passage 2 Diesel particulate filter 3 Exhaust gas reaction chamber 3a Circumferential wall part 31 Exhaust gas inlet 31a Perimeter wall 31b Inner end 32 Exhaust gas outlet 32a Peripheral wall 32b Inner end 33 Long bolt 5 Ammonia injection device 51 Ammonia water tank 6 Fuel tank 7 Fuel oil Supply path 8 Fuel oil activation device 81 Cylindrical casing 83 Strong magnet A Accelerator pedal C Controller for ammonia injection E Diesel engine P Pump for ammonia injection

Claims (8)

内燃機関の排気ガス通路に、ベローズ構造の周壁を有する横型筒状の排ガス反応室を介装し、この排ガス反応室に流入する排気ガス中にアンモニア及び水蒸気を注入する注入手段を設けてなる内燃機関の排気ガス浄化装置。 An internal combustion engine in which an exhaust gas passage of an internal combustion engine is provided with a horizontal cylindrical exhaust gas reaction chamber having a bellows-shaped peripheral wall, and injection means for injecting ammonia and water vapor into the exhaust gas flowing into the exhaust gas reaction chamber is provided. Engine exhaust gas purification device. 前記注入手段が、排ガス反応室の上流側で排気ガス中にアンモニア水を霧状にして注入するアンモニヤ注入装置からなる請求項1記載の内燃機関の排気ガス浄化装置。   2. An exhaust gas purification apparatus for an internal combustion engine according to claim 1, wherein said injection means comprises an ammonia injection device for injecting ammonia water into the exhaust gas in the form of a mist on the upstream side of the exhaust gas reaction chamber. 前記アンモニア水の濃度が8%以上で10%未満である請求項2に記載の内燃機関の排気ガス浄化装置。   The exhaust gas purification apparatus for an internal combustion engine according to claim 2, wherein the concentration of the ammonia water is 8% or more and less than 10%. 前記ベローズ構造の周壁を有する筒状の排ガス反応室の両側端板間に、複数本の曲がり防止用長ボルトが当該排ガス反応室を外側から挟むように配設されてなる請求項1〜3のいずれかに記載の内燃機関の排気ガス浄化装置。 A plurality of bending-preventing long bolts are disposed between both side end plates of the cylindrical exhaust gas reaction chamber having the peripheral wall of the bellows structure so as to sandwich the exhaust gas reaction chamber from the outside . The exhaust gas purification apparatus for an internal combustion engine according to any one of the above. 前記排ガス反応室の排ガス導入口及び排ガス導出口が、当該排ガス反応室内に中心線方向に沿って突入する短筒状に形成され、その周壁が多孔状をなすと共に、内端が閉塞してなる請求項1〜のいずれかに記載の内燃機関の排気ガス浄化装置。 An exhaust gas inlet and an exhaust gas outlet of the exhaust gas reaction chamber are formed in a short cylindrical shape that enters the exhaust gas reaction chamber along the center line direction, and the peripheral wall forms a porous shape and the inner end is closed. The exhaust gas purification apparatus for an internal combustion engine according to any one of claims 1 to 4 . 内燃機関がディーゼルエンジンであり、前記アンモニア及び水蒸気の注入部よりも上流側の排気ガス通路にディーゼル微粒子フィルターが介装されてなる1〜のいずれかに記載の内燃機関の排気ガス浄化装置。 The exhaust gas purifying device for an internal combustion engine according to any one of 1 to 5 , wherein the internal combustion engine is a diesel engine, and a diesel particulate filter is interposed in an exhaust gas passage upstream of the ammonia and water vapor injection portion. 前記ディーゼル微粒子フィルターが酸化触媒を担持したハニカムセラミック層からなる請求項記載の内燃機関の排気ガス浄化装置。 The exhaust gas purifying device for an internal combustion engine according to claim 6, wherein the diesel particulate filter is composed of a honeycomb ceramic layer carrying an oxidation catalyst. 燃料タンクと内燃機関とを繋ぐ燃料油供給経路に、筒状ケーシング内に複数の強磁石が配置し、燃料油をこれら強磁石に接触して通過させる燃料油活性化装置を介装してなる請求項1〜のいずれかに記載の内燃機関の排気ガス浄化装置。 A fuel oil supply path connecting the fuel tank and the internal combustion engine is provided with a plurality of strong magnets arranged in a cylindrical casing, and a fuel oil activation device for passing the fuel oil in contact with the strong magnets is interposed. The exhaust gas purification apparatus for an internal combustion engine according to any one of claims 1 to 7 .
JP2004355910A 2004-12-08 2004-12-08 Exhaust gas purification device for internal combustion engine Expired - Fee Related JP4344684B2 (en)

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