JPH1077831A - Exhaust emission control device for engine - Google Patents

Exhaust emission control device for engine

Info

Publication number
JPH1077831A
JPH1077831A JP8271278A JP27127896A JPH1077831A JP H1077831 A JPH1077831 A JP H1077831A JP 8271278 A JP8271278 A JP 8271278A JP 27127896 A JP27127896 A JP 27127896A JP H1077831 A JPH1077831 A JP H1077831A
Authority
JP
Japan
Prior art keywords
water
exhaust gas
moisture
branch passage
engine
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP8271278A
Other languages
Japanese (ja)
Other versions
JP3767040B2 (en
Inventor
Reiko Domeki
礼子 百目木
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Motors Corp
Original Assignee
Mitsubishi Motors Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Mitsubishi Motors Corp filed Critical Mitsubishi Motors Corp
Priority to JP27127896A priority Critical patent/JP3767040B2/en
Publication of JPH1077831A publication Critical patent/JPH1077831A/en
Application granted granted Critical
Publication of JP3767040B2 publication Critical patent/JP3767040B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2086Activating the catalyst by light, photo-catalysts
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N13/00Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00
    • F01N13/009Exhaust or silencing apparatus characterised by constructional features ; Exhaust or silencing apparatus, or parts thereof, having pertinent characteristics not provided for in, or of interest apart from, groups F01N1/00 - F01N5/00, F01N9/00, F01N11/00 having two or more separate purifying devices arranged in series
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F01MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
    • F01NGAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
    • F01N3/00Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
    • F01N3/08Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
    • F01N3/10Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
    • F01N3/18Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control
    • F01N3/20Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by methods of operation; Control specially adapted for catalytic conversion ; Methods of operation or control of catalytic converters
    • F01N3/2053By-passing catalytic reactors, e.g. to prevent overheating
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Toxicology (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Abstract

PROBLEM TO BE SOLVED: To combine the decrease of moisture in exhaust gas and the presence of a reducing agent such as CO, HC by providing a moisture decomposing means for decomposing moisture, released from a moisture eliminating means, to generate reducing hydrogen. SOLUTION: Until a moisture storage body 46b in a moisture eliminating means 42b in a branch passage 22b is saturated, a photocatalyst 50b is deactivated and does not act. When a moisture eliminating means 42a is energized, on the other hand, moisture stored in a moisture storage body 46a is released, brought into contact with the photocatalyst 50a and decomposed so as to generate reducing hydrogen H and OH. When the moisture absorbing capacity of the moisture storage body 45b is lowered, exhaust gas of an engine 10 flows to a branch passage 22a. At the same time, the moisture storage body 46a starts storing moisture in exhaust gas, and the photocatalyst 50a is deactivated. Exhaust gas passes the photocatalyst 50a without stopping and is fed to a catalytic converter 18. On the other hand, the release of moisture stored in the moisture storage body 46b is started. At the same time, the photocatalyst 50b is activated.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、エンジン、特に車
両用エンジンから排出される排ガスの浄化装置に関する
ものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for purifying exhaust gas discharged from an engine, especially a vehicle engine.

【0002】[0002]

【従来の技術】エンジン、特に自動車等車両用エンジン
から排出される排ガス中の有害成分である窒素酸化物
(NO)、一酸化炭素(CO)及び炭化水素(HC)
を同時に効率的に浄化する触媒として、コージェライト
等の耐熱多孔質担体に、白金(Pt)、パラジウム(P
d)、ロジウム(Rh)等の貴金属の一種又は二種をベ
ースとし、必要に応じニッケル(Ni)、コバルト(C
o)等の酸化物を添加したものを触媒成分として担持さ
せた三元触媒が広く使用されている。
2. Description of the Related Art Nitrogen oxides (NO x ), carbon monoxide (CO) and hydrocarbons (HC), which are harmful components in exhaust gas discharged from engines, particularly engines for vehicles such as automobiles.
Platinum (Pt), palladium (P) on a heat-resistant porous carrier such as cordierite
d), one or two noble metals such as rhodium (Rh), and nickel (Ni), cobalt (C
A three-way catalyst in which an oxide such as o) is supported as a catalyst component is widely used.

【0003】しかしながら、上記三元触媒は、排ガス中
の酸素濃度が略1%以下の所謂理論空燃比付近の運転領
域では、効率的に有害成分の浄化を行なうことができる
が、排ガス中の酸素濃度が数%以上の場合、即ちオット
ーサイクルエンジンのリーン燃焼領域及び本質的に酸素
過剰状態で運転されるディーゼルエンジンから排出され
る排ガスでは、有害成分の浄化効率が著しく低い欠点が
ある。
However, the three-way catalyst can efficiently purify harmful components in an operating region near the so-called stoichiometric air-fuel ratio where the oxygen concentration in the exhaust gas is approximately 1% or less. When the concentration is several% or more, that is, in the exhaust gas discharged from the lean combustion region of the Otto cycle engine and the diesel engine operated in an essentially oxygen-excess state, there is a disadvantage that the purification efficiency of harmful components is extremely low.

【0004】そこで、各種の天然ゼオライト又は合成ゼ
オライト等の分子篩構造を有する物質に、遷移金属を担
持させることによって、排ガス中の酸素濃度が高い上記
リーン燃焼領域でも、NO及びHCを浄化することが
できるようにした触媒、例えば一般にゼオライト触媒と
呼ばれている触媒が開発されている。この種の分子篩構
造の物質に遷移金属を担持させた触媒(以下この種の触
媒を、場合により分子篩構造触媒という)は、排ガス中
に含まれているCOやHCを還元剤とする反応によっ
て、効果的にNOを除去することができるものであ
る。
[0004] Therefore, the substance having a molecular sieve structure, such as various natural zeolite or synthetic zeolite, by supporting the transition metal, even at high concentration of oxygen in the exhaust gas the lean combustion region, to purify NO x and HC For example, a catalyst which is generally known as a zeolite catalyst has been developed. A catalyst in which a transition metal is supported on a substance having a molecular sieve structure of this type (hereinafter, this type of catalyst is sometimes referred to as a molecular sieve structure catalyst) is produced by a reaction using CO or HC contained in exhaust gas as a reducing agent. effectively it is capable of removing NO x.

【0005】しかしながら、上記分子篩構造触媒は、少
量の水分の存在によって結晶構造に変化が生じ、排ガス
中のNOの除去性能が著しく低減することが知られて
おり、従って、排ガス中の水分を少くとも5%以下、好
ましくは1%以下に低減する手段を設けることなく、分
子篩構造触媒を単独で排ガス通路内に配置しても、優れ
たNO低減効果を期待することはできない。
[0005] However, it is known that the molecular sieve structure catalyst changes its crystal structure due to the presence of a small amount of water, and significantly reduces the NO x removal performance in the exhaust gas. at least 5%, preferably without providing a means for reducing the 1% or less, be located within the exhaust gas passage molecular sieve structure catalyst alone can not be expected excellent nO x reduction effect.

【0006】上記問題点を解決するために、分子篩構造
触媒、例えばゼオライト触媒の上流側における排ガス通
路内に、水性ガス反応触媒を配置したものが、特開平4
−300631号公開公報に開示されている。しかしな
がら、この既提案の排ガス浄化装置では、水性ガス反応
触媒により水分を除去する際に、排ガス中のCO及びH
Cが還元剤として用いられるので、下流側の分子篩構造
触媒が、NO除去機能を発揮するために必要な排ガス
中の還元成分の量が不足し、十分なNO除去効果が得
られなくなる不都合がある。
In order to solve the above-mentioned problems, a catalyst having a water gas reaction catalyst disposed in an exhaust gas passage on the upstream side of a catalyst having a molecular sieve structure, for example, a zeolite catalyst has been disclosed in Japanese Unexamined Patent Publication No. Hei.
-300631. However, in the proposed exhaust gas purifying apparatus, when water is removed by the water gas reaction catalyst, CO and H in the exhaust gas are removed.
Since C is used as the reducing agent, the downstream side of the molecular sieve structure catalyst, insufficient amount of reducing components in the exhaust gas necessary to exert NO x removal function, not sufficient NO x removal effect can be obtained inconvenience There is.

【0007】[0007]

【発明が解決しようとする課題】本発明は、上記事情に
鑑み創案されたもので、分子篩構造触媒が効果的にNO
を除去するために必要な条件である、排ガス中の水分
の低減と、十分な量のCO、HC等還元剤の存在とを、
両立させることができるようにしたエンジンの排ガス浄
化装置を提供することを目的とするものである。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above circumstances, and a catalyst having a molecular sieve structure can effectively reduce NO.
x , which is a condition necessary for removing x , that is, reduction of water in exhaust gas and the presence of a sufficient amount of a reducing agent such as CO and HC,
It is an object of the present invention to provide an exhaust gas purifying device for an engine that can achieve both.

【0008】[0008]

【課題を解決するための手段】上記目的を達成するた
め、本発明は、エンジンの排気通路内に配置され分子篩
構造を有する物質に遷移金属を担持させた触媒と、同触
媒の上流側における排気通路内に配置され、排ガス中の
水分を吸蔵する水分除去手段と同水分除去手段から放出
された水分を分解して還元性水素を生成する水分分解手
段とからなる水分処理装置とを設けたことを特徴とする
エンジンの排ガス浄化装置を提案するものである。
In order to achieve the above object, the present invention provides a catalyst in which a transition metal is supported on a substance having a molecular sieve structure and disposed in an exhaust passage of an engine, and an exhaust gas upstream of the catalyst. A water treatment device that is disposed in the passage and includes a water removal unit that stores moisture in exhaust gas and a water decomposition unit that decomposes water released from the water removal unit and generates reductive hydrogen. The present invention proposes an engine exhaust gas purifying apparatus characterized by the following.

【0009】本発明において、上記触媒の上流側におけ
る排気通路に配設され切換弁によって選択的に排ガスが
供給される二つの分岐通路と、上記分岐通路内に夫々配
設された水分処理装置と、排ガスが供給されている一方
の分岐通路内の水分処理装置における水分除去手段の水
分吸蔵飽和が検知されたとき、上記切換弁を作動させて
他方の分岐通路に排ガスを供給するコントロールユニッ
トとを具え、上記切換弁により排ガスの供給が停止され
た上記一方の分岐通路内の水分除去手段では吸蔵された
水分が放出されると共に水分分解手段により還元性水素
が生成され、かつ排ガスが供給される上記他方の分岐通
路内の水分除去手段では排ガス中の水分が吸蔵されるよ
うに構成されることが好ましく、また上記水分分解手段
は、紫外線の照射により水を分解して還元性水素を生成
する光触媒であることが好ましい。
In the present invention, there are provided two branch passages which are disposed in an exhaust passage upstream of the catalyst and to which exhaust gas is selectively supplied by a switching valve, and a water treatment device which is disposed in each of the branch passages. A control unit that operates the switching valve to supply the exhaust gas to the other branch passage when the moisture occlusion saturation of the moisture removing unit in the moisture treatment device in the one branch passage to which the exhaust gas is supplied is detected. The water removing means in the one branch passage, in which the supply of the exhaust gas is stopped by the switching valve, releases the occluded water, generates the reducing hydrogen by the water decomposing means, and supplies the exhaust gas. It is preferable that the water removing means in the other branch passage is configured to occlude water in the exhaust gas. It is preferably a photocatalyst that generates reducing hydrogen by decomposing more water.

【0010】[0010]

【発明の実施の形態】以下本発明の好ましい実施形態を
添付図面について具体的に説明する。図中符号10は概
念的に示したエンジン、例えば自動車等車両用のエンジ
ンであって、同エンジン10は、図示しないエアクリー
ナを介して外気を取入れる吸気マニホールド12、及び
同エンジン10内で発生した燃焼ガスを外気に排出する
排気マニホールド14を具え、同排気マニホールド14
はその排出端に連結された排気管と共に、エンジン10
の排気通路16を形成する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the present invention will be specifically described below with reference to the accompanying drawings. In the figure, reference numeral 10 denotes an engine conceptually shown, for example, an engine for a vehicle such as an automobile. The engine 10 is generated in an intake manifold 12 that takes in outside air via an air cleaner (not shown) and in the engine 10. An exhaust manifold for discharging the combustion gas to the outside air;
Together with the exhaust pipe connected to the discharge end of the engine 10
Is formed.

【0011】上記排気通路16の下流側に総括的に符号
18で示した触媒コンバータが介装され、同触媒コンバ
ータ18の内部には分子篩構造触媒20が収容されてい
る。上記排気マニホールド14の下流側における排気通
路16と上記触媒コンバータ18の上流側における排気
通路16との間に、二つの分岐通路22a及び22bが
設けられている。分岐通路22a及び22bの上流合流
部24に切換弁26が設けられ、同切換弁26の弁軸2
8に弁制御レバー30が固着されている。
A catalytic converter indicated generally by reference numeral 18 is interposed downstream of the exhaust passage 16, and a catalyst 20 having a molecular sieve structure is accommodated inside the catalytic converter 18. Two branch passages 22 a and 22 b are provided between the exhaust passage 16 on the downstream side of the exhaust manifold 14 and the exhaust passage 16 on the upstream side of the catalytic converter 18. A switching valve 26 is provided at an upstream junction 24 of the branch passages 22a and 22b, and a valve shaft 2 of the switching valve 26 is provided.
A valve control lever 30 is fixed to 8.

【0012】上記弁制御レバー30にはアクチュエータ
32によって駆動される作動ロッド34の出力端が枢着
されている。同アクチュエータ32には、電磁式アクチ
ュエータ、圧縮空気作動のエアシリンダ装置、電動モー
タによって駆動されるピニオン及び同ピニオンと噛合す
るラック棒等からなる電気−機械式アクチュエータ等任
意のアクチュエータを採用することができる。また、上
記分岐通路22a及び22bの下流側合流部分と上記触
媒コンバータ18との間の排気通路16に、排ガス中に
含まれている水分を検知する水分センサ36が設けら
れ、同水分センサ36により検知された排ガス中の水分
含有率Ewを示す信号又は情報は、上記アクチュエータ
32を制御するコントロールユニット38に供給され
る。
An output end of an operating rod 34 driven by an actuator 32 is pivotally connected to the valve control lever 30. The actuator 32 may be an arbitrary actuator such as an electromagnetic actuator, an air cylinder device operated by compressed air, a pinion driven by an electric motor, and an electro-mechanical actuator including a rack bar meshing with the pinion. it can. Further, a moisture sensor 36 for detecting moisture contained in the exhaust gas is provided in the exhaust passage 16 between the downstream merging portion of the branch passages 22a and 22b and the catalytic converter 18. A signal or information indicating the detected water content Ew in the exhaust gas is supplied to a control unit 38 for controlling the actuator 32.

【0013】上記分岐通路22a及び22b内に、夫々
総括的に符号40a及び40bで示された水分処理装置
が設けられ、同水分処理装置40aは、排ガス中の水分
を吸収して貯蔵する水分除去手段42aと、その下流側
に配置された水分分解手段44aとを具えている。同様
に、上記水分処理装置40bは、排ガス中の水分を吸蔵
する水分除去手段42bとその下流側に配置された水分
分解手段44bとを具えている。上記水分除去手段42
a及び42bは実質的に同一の構造を有し、また上記水
分分解手段44a及び44bも実質的に同一の構造を有
する。
In the branch passages 22a and 22b, there are provided water treatment devices indicated generally by reference numerals 40a and 40b, respectively. The water treatment device 40a absorbs and stores moisture in exhaust gas. Means 42a and a water decomposing means 44a disposed downstream thereof. Similarly, the water treatment device 40b includes a water removing unit 42b that stores moisture in the exhaust gas and a water decomposing unit 44b that is disposed downstream thereof. The water removing means 42
a and 42b have substantially the same structure, and the water decomposing means 44a and 44b also have substantially the same structure.

【0014】上記水分除去手段42a及び42bは、高
温の排ガスに耐えることができ、かつ耐食性及び化学的
安定性が優れたアルミナ(Al)、シリカ(Si
)、ジルコニア(ZrO)等セラミックス系材料
からなり、無数の微小細孔を有する多孔質の水分吸蔵体
46a、46bと、同水分吸蔵体46a、46bを加熱
することによって吸蔵された水分を放出させる加熱装置
48a、48bとを具えている。また、上記水分分解手
段44a及び44bは、各々光触媒50a、50bと、
同光触媒50a、50bに活性を生起させる紫外線照射
装置52a、52bとを具えている。
The moisture removing means 42a and 42b can withstand high-temperature exhaust gas and have excellent corrosion resistance and chemical stability, such as alumina (Al 2 O 3 ) and silica (Si).
O 2 ), zirconia (ZrO 2 ), or other ceramic-based material, having porous micro-pores 46a, 46b having innumerable micropores, and water stored by heating the micro-pores 46a, 46b. And heating devices 48a and 48b for discharging the gas. The water decomposing means 44a and 44b are provided with photocatalysts 50a and 50b, respectively.
The photocatalysts 50a and 50b are provided with ultraviolet irradiation devices 52a and 52b for generating activity.

【0015】上記分子篩構造を有する物質に遷移金属を
担持させた触媒20は、一般にゼオライトと称せられ、
主成分がシリカ及びアルミナで、Si/Al比が5〜1
00程度であり、結晶構造がX型、Y型、ZSM型等の
メタロシリケート等、及びこれらのゼオライト、メタロ
シリケートを遷移金属でイオン交換したものである。
The catalyst 20 in which a transition metal is supported on a substance having a molecular sieve structure is generally called zeolite.
Main component is silica and alumina, Si / Al ratio is 5-1
It is about 00, and has a crystal structure of a metallosilicate such as X-type, Y-type, or ZSM-type, or a zeolite or metallosilicate obtained by ion-exchange with a transition metal.

【0016】また、上記光触媒50a及び50bは、ア
ルミナ、コージェライト等からなる担体に、チタニア
(TiO)を主剤とし、必要に応じ酸化鉄(Fe
)、酸化銅(CuO)、酸化ニッケル(NiO)等
の添加剤を一種又は二種以上担持させたものを有利に採
用することができる。さらに、上記紫外線照射装置52
a及び52bは、排ガスの高温に耐え、耐衝撃性を強化
した石英ガラス製容器内に収容され、波長λが300n
m前後の紫外線を生起するランプを具えている。さら
に、上記光触媒50a及び50bの担体の具体的形状構
造及び紫外線照射装置52a及び52bの関係的配置
は、任意である。
The photocatalysts 50a and 50b are mainly composed of titania (TiO 2 ) on a carrier made of alumina, cordierite or the like, and if necessary, iron oxide (Fe 2 O).
3 ) One or two or more additives such as copper oxide (Cu 2 O) and nickel oxide (NiO) can be advantageously used. Further, the ultraviolet irradiation device 52
a and 52b are housed in a quartz glass container that withstands the high temperature of the exhaust gas and has enhanced impact resistance, and has a wavelength λ of 300 n.
It has a lamp that produces ultraviolet light of about m. Further, the specific shape and structure of the carriers of the photocatalysts 50a and 50b and the relative arrangement of the ultraviolet irradiation devices 52a and 52b are arbitrary.

【0017】図1は、切換弁26によって分岐通路22
aが閉止されると共に、分岐通路22bが開放され、エ
ンジン10の排ガスが分岐通路22bに流入している状
態を示している。排ガスは分岐通路22b内に設けられ
ている水分除去手段42bの水分吸蔵体46bを通過す
る間に、効果的に含有水分を吸収され、水分含有率が5
%以下、好ましくは1%以下の排ガスとなって休止して
いる水分分解手段44bを素通りして触媒コンバータ1
8に流れ、同コンバータ内に収蔵された分子篩構造触媒
20に接触する。排ガス中の水分が少なく、かつCO、
HC等の還元成分が途中で失なわれることもないので、
たとえ理論空燃比状態より多くの酸素が存在する過剰雰
囲気下においても、効果的にNOが除去され、同時に
CO、HCも浄化される。
FIG. 1 shows that the switching valve 26 controls the branch passage 22.
a is closed, the branch passage 22b is opened, and the exhaust gas of the engine 10 flows into the branch passage 22b. While the exhaust gas passes through the water occluding body 46b of the water removing means 42b provided in the branch passage 22b, the water content is effectively absorbed, and the water content becomes 5%.
% Or less, preferably 1% or less exhaust gas, and pass through the water decomposition means 44b which is at rest, and the catalytic converter 1
8 and contacts the molecular sieve structured catalyst 20 stored in the converter. The moisture in the exhaust gas is low and CO,
Since the reducing components such as HC are not lost on the way,
Even under excess atmosphere more oxygen than the stoichiometric air-fuel ratio condition exists, effectively NO x are removed, at the same time CO, HC also be purified.

【0018】分岐通路22b内の水分除去手段42bに
おける水分吸蔵体46bが飽和するまでの間、水分セン
サ36によって検知される排ガス中の水分含有率Ewが
設定値より低いので、コントロールユニット38の指令
により、アクチュエータ32は消勢されて切換弁26は
図中実線で示した上記切換位置に保持され、水分除去手
段42bの加熱装置48bも消勢されている。また、水
分分解手段44bの紫外線照射装置52bも消勢されて
いるので、光触媒50bは失活し作用しない。
Until the water occluding body 46b in the water removing means 42b in the branch passage 22b is saturated, the water content Ew in the exhaust gas detected by the water sensor 36 is lower than the set value. As a result, the actuator 32 is deenergized, the switching valve 26 is held at the switching position indicated by the solid line in the drawing, and the heating device 48b of the moisture removing means 42b is also deenergized. Further, since the ultraviolet irradiation device 52b of the water decomposing means 44b is also deenergized, the photocatalyst 50b is deactivated and does not operate.

【0019】一方、コントロールユニット38によっ
て、分岐通路22a内の水分除去手段42aにおける加
熱装置48aが付勢されると共に、水分分解装置44a
の紫外線照射装置52aが付勢されているので、前サイ
クルにおいて水分吸蔵体46aに吸蔵されていた水分が
加熱により放出され、活性化している光触媒50aに接
触して分解され、還元性水素H及びOHが生成する。上
記還元性水素H及びOHは、上記した分岐通路22bか
らの低水分含有率の排ガスと共に、触媒コンバータ18
に流入して、分子篩構成触媒20のNO浄化に必要な
還元性雰囲気を強化するので、NO浄化効率の一層の
向上が達成される。
On the other hand, the heating unit 48a in the water removing means 42a in the branch passage 22a is energized by the control unit 38 and the water decomposing device 44a
Is irradiated, the water occluded in the water occlusion body 46a in the previous cycle is released by heating, comes into contact with the activated photocatalyst 50a, is decomposed, and the reducing hydrogen H and OH is formed. The reducing hydrogen H and OH are mixed with the exhaust gas having a low water content from the branch passage 22b and the catalytic converter 18
To enhance the reducing atmosphere required for NO x purification of the molecular sieve-constituting catalyst 20, so that the NO x purification efficiency is further improved.

【0020】時間の経過と共に、上記分岐通路22b内
の水分吸蔵体46bが飽和し又は飽和に近い状態となっ
て水分吸収能力が或る限度まで低下すると、同分岐通路
22bを流れる排ガス中の水分が次第に増大するので、
水分センサ36の水分含有率Ewを検知した信号又は情
報に基づき、コントローラ38がアクチュエータ32を
付勢する。アクチュエータ32の付勢により、作動ロッ
ド34が図において上方に変位し、弁制御レバー30を
介して切換弁26が点線で示した位置に切換えられる。
この結果、エンジン10の排ガスは分岐通路22aに流
れ、分岐通路22bへの流入は遮断されることとなる。
As time elapses, the water absorbing body 46b in the branch passage 22b becomes saturated or nearly saturated and the water absorbing capacity decreases to a certain limit. Gradually increases,
The controller 38 energizes the actuator 32 based on a signal or information that the moisture sensor 36 has detected the moisture content Ew. By the urging of the actuator 32, the operating rod 34 is displaced upward in the figure, and the switching valve 26 is switched to the position shown by the dotted line via the valve control lever 30.
As a result, the exhaust gas of the engine 10 flows to the branch passage 22a, and the inflow to the branch passage 22b is cut off.

【0021】これと同時に、分岐通路22aの水分除去
手段42aにおける加熱装置48aが消勢されて、その
水分吸蔵体46aが排ガス中の水分の吸蔵を始め、また
水分分解手段44aの紫外線照射装置52aが消勢され
るので、光触媒50aが失活し、排ガスが同光触媒50
aを素通りして触媒コンバータ18に供給される。
At the same time, the heating device 48a in the water removing means 42a of the branch passage 22a is deenergized, and the water occluding body 46a starts occluding water in the exhaust gas, and the ultraviolet irradiation device 52a of the water decomposing means 44a. Is deactivated, the photocatalyst 50a is deactivated, and the exhaust gas is
is supplied to the catalytic converter 18 without passing through a.

【0022】一方、遮断された分岐通路22bの水分除
去手段42bにおける加熱装置48bが付勢されるの
で、水分吸蔵体46bに吸蔵された水分が放出され始め
る。それと同時に、水分分解手段44bの紫外線照射装
置52bが付勢されるので、光触媒50bが活性化さ
れ、上記水分吸蔵体46bから放出された水分が光触媒
50bに接触して分解し、還元性の水素HとOHが生成
し、触媒コンバータ18に供給される。この結果、上記
と全く同様に、排ガス中のNOの浄化が効果的に行な
われ、またCO、HCの浄化が行なわれる。
On the other hand, since the heating device 48b in the water removing means 42b of the blocked branch passage 22b is energized, the water occluded by the water occlusion body 46b starts to be released. At the same time, the ultraviolet irradiation device 52b of the water decomposing means 44b is energized, so that the photocatalyst 50b is activated, and the water released from the water occluding body 46b comes into contact with the photocatalyst 50b to be decomposed, thereby reducing hydrogen. H and OH are generated and supplied to the catalytic converter 18. Consequently, just as above, the purification of the NO x in the exhaust gas is effectively carried out, also CO, purification of HC is performed.

【0023】なお、上記実施形態では、水分処理装置4
0a及び40bを構成する水分除去手段42a、42b
と水分分解手段44a、44bとが、夫々別個の装置と
して図示されているが、共通のケーシング内に、水分除
去手段42aと水分分解手段44aとを収容し、同様
に、水分除去手段42bと水分分解手段44bとを収容
することもできる。
In the above embodiment, the water treatment device 4
Moisture removing means 42a, 42b constituting 0a and 40b
And the water decomposing means 44a and 44b are shown as separate devices, respectively. However, the water removing means 42a and the water decomposing means 44a are housed in a common casing. The disassembling means 44b can also be accommodated.

【0024】[0024]

【発明の効果】叙上のように、本発明に係るエンジンの
排ガス浄化装置は、エンジンの排気通路内に配置され分
子篩構造を有する物質に遷移金属を担持させた触媒と、
同触媒の上流側における排気通路内に配置され、排ガス
中の水分を吸蔵する水分除去手段と同水分除去手段から
放出された水分を分解して還元性水素を生成する水分分
解手段とからなる水分処理装置とを設けたことを特徴と
し、酸素過剰状態で、しかも多量の水分を含むエンジン
の排ガス中の有害成分、特に通常は除去困難なNO
効果的に浄化することができる利点がある。
As described above, the exhaust gas purifying apparatus for an engine according to the present invention includes a catalyst in which a transition metal is supported on a substance having a molecular sieve structure and disposed in an exhaust passage of the engine;
Moisture disposed in an exhaust passage on the upstream side of the catalyst and comprising water removing means for storing moisture in exhaust gas and water decomposing means for decomposing water released from the water removing means to generate reductive hydrogen. characterized by comprising a processing unit, an oxygen excess state, moreover harmful components in the exhaust gas of the engine including a large amount of water, in particular usually an advantage capable of purifying difficult NO x removal effectively .

【0025】また、本発明において、上記触媒の上流側
における排気通路に配設され切換弁によって選択的に排
ガスが供給される二つの分岐通路と、上記分岐通路内に
夫々配設された水分処理装置と、排ガスが供給されてい
る一方の分岐通路内の水分処理装置における水分除去手
段の水分吸蔵飽和が検知されたとき、上記切換弁を作動
させて他方の分岐通路に排ガスを供給するコントロール
ユニットを具え、上記切換弁により排ガスの供給が停止
された上記一方の分岐通路内の水分除去手段では吸蔵さ
れた水分が放出されると共に水分分解手段により還元性
水素が生成され、かつ排ガスが供給される上記他方の分
岐通路内の水分除去手段では排ガス中の水分が吸蔵され
るように構成されたことにより、上記水分除去手段の限
りある水分吸蔵能力にも拘わらず、エンジンの連続運転
中、常時排ガスの浄化を継続的に、かつ効果的に行ない
得る利点がある。なおまた、上記水分分解手段は、紫外
線の照射により水を分解して還元性水素を生成する光触
媒であることにより、紫外線照射に必要な僅かのエネル
ギ消費によって分子篩構造触媒のNO浄化に有効な還
元性水素を生成し、浄化効率を向上し得る利点がある。
Further, in the present invention, two branch passages disposed in the exhaust passage upstream of the catalyst and to which exhaust gas is selectively supplied by a switching valve, and a water treatment disposed in the branch passage, respectively. A control unit for operating the switching valve to supply the exhaust gas to the other branch passage when the water occlusion saturation of the moisture removing means in the moisture treatment device in the one branch passage to which the exhaust gas is supplied is detected. In the water removing means in the one branch passage in which the supply of exhaust gas is stopped by the switching valve, the occluded water is released and the reducing hydrogen is generated by the water decomposing means, and the exhaust gas is supplied. The moisture removal means in the other branch passage is configured to absorb moisture in the exhaust gas, so that the moisture removal means has a limited moisture storage capacity. Despite, during continuous operation of the engine, continuously to purify the constantly gas, and there is an advantage that can effectively perform. Note also, the water decomposition unit, by a photocatalyst to generate a reducing hydrogen by decomposing water by irradiation of ultraviolet light, effective to the NO x purification molecular sieve structure catalyzed by small energy consumption required to ultraviolet radiation There is an advantage that reductive hydrogen can be generated and purification efficiency can be improved.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の好ましい実施形態を示す概略構成図で
ある。
FIG. 1 is a schematic configuration diagram showing a preferred embodiment of the present invention.

【符号の説明】[Explanation of symbols]

10…エンジン、14…排気マニホールド、16…排気
通路、18…触媒コンバータ、20…触媒、22a及び
22b…分岐通路、26…切換弁、32…アクチュエー
タ、36…水分センサ、38…コントロールユニット、
40a及び40b…水分処理装置、42a及び42b…
水分除去手段、44a及び44b…水分分解手段、46
a及び46b…水分吸蔵体、48a及び48b…加熱装
置、50a及び50b…光触媒、52a及び52b…紫
外線照射装置。
DESCRIPTION OF SYMBOLS 10 ... Engine, 14 ... Exhaust manifold, 16 ... Exhaust passage, 18 ... Catalytic converter, 20 ... Catalyst, 22a and 22b ... Branch passage, 26 ... Switching valve, 32 ... Actuator, 36 ... Moisture sensor, 38 ... Control unit,
40a and 40b ... water treatment device, 42a and 42b ...
Water removing means, 44a and 44b ... water decomposing means, 46
a and 46b: a water occluding body, 48a and 48b: a heating device, 50a and 50b: a photocatalyst, 52a and 52b: an ultraviolet irradiation device.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 B01J 29/04 ZAB F01N 3/28 ZAB 35/02 ZAB 301C F01N 3/28 ZAB B01D 53/36 ZABJ 301 102C ──────────────────────────────────────────────────の Continuation of the front page (51) Int.Cl. 6 Identification code Agency reference number FI Technical indication location B01J 29/04 ZAB F01N 3/28 ZAB 35/02 ZAB 301C F01N 3/28 ZAB B01D 53/36 ZABJ 301 102C

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 エンジンの排気通路内に配置され分子篩
構造を有する物質に遷移金属を担持させた触媒と、同触
媒の上流側における排気通路内に配置され、排ガス中の
水分を吸蔵する水分除去手段と同水分除去手段から放出
された水分を分解して還元性水素を生成する水分分解手
段とからなる水分処理装置とを設けたことを特徴とする
エンジンの排ガス浄化装置。
1. A catalyst in which a transition metal is supported on a substance having a molecular sieve structure and which is disposed in an exhaust passage of an engine, and a water removal which is disposed in an exhaust passage upstream of the catalyst and occludes moisture in exhaust gas. An exhaust gas purifying apparatus for an engine, comprising: a water treatment device comprising: a water decomposing means for decomposing water released from the water removing means to generate reductive hydrogen.
【請求項2】 上記触媒の上流側における排気通路に配
設され切換弁によって選択的に排ガスが供給される二つ
の分岐通路と、上記分岐通路内に夫々配設された水分処
理装置と、排ガスが供給されている一方の分岐通路内の
水分処理装置における水分除去手段の水分吸蔵飽和が検
知されたとき、上記切換弁を作動させて他方の分岐通路
に排ガスを供給するコントロールユニットとを具え、上
記切換弁により排ガスの供給が停止された上記一方の分
岐通路内の水分除去手段では吸蔵された水分が放出され
ると共に水分分解手段により還元性水素が生成され、か
つ排ガスが供給される上記他方の分岐通路内の水分除去
手段では排ガス中の水分が吸蔵されるように構成された
ことを特徴とする請求項1記載のエンジンの排ガス浄化
装置。
2. A branch passage disposed in an exhaust passage upstream of the catalyst and selectively supplied with exhaust gas by a switching valve; a water treatment device disposed in each of the branch passages; And a control unit for operating the switching valve to supply exhaust gas to the other branch passage when the water occlusion saturation of the moisture removing means in the water treatment device in the one branch passage in which the water is supplied is detected. In the water removing means in the one branch passage in which the supply of the exhaust gas is stopped by the switching valve, the occluded water is released and the reducing hydrogen is generated by the water decomposing means, and the exhaust gas is supplied. 2. The exhaust gas purifying apparatus for an engine according to claim 1, wherein the moisture removing means in the branch passage is configured to occlude moisture in the exhaust gas.
【請求項3】 上記水分分解手段は、紫外線の照射によ
り水を分解して還元性水素を生成する光触媒であること
を特徴とする請求項1又は請求項2記載のエンジンの排
ガス浄化装置。
3. The exhaust gas purifying apparatus for an engine according to claim 1, wherein the water decomposing means is a photocatalyst that decomposes water by irradiation with ultraviolet rays to generate reductive hydrogen.
JP27127896A 1996-09-05 1996-09-05 Engine exhaust gas purification device Expired - Fee Related JP3767040B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27127896A JP3767040B2 (en) 1996-09-05 1996-09-05 Engine exhaust gas purification device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27127896A JP3767040B2 (en) 1996-09-05 1996-09-05 Engine exhaust gas purification device

Publications (2)

Publication Number Publication Date
JPH1077831A true JPH1077831A (en) 1998-03-24
JP3767040B2 JP3767040B2 (en) 2006-04-19

Family

ID=17497854

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27127896A Expired - Fee Related JP3767040B2 (en) 1996-09-05 1996-09-05 Engine exhaust gas purification device

Country Status (1)

Country Link
JP (1) JP3767040B2 (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1243766B1 (en) * 2001-03-21 2008-07-23 Nissan Motor Co., Ltd. Exhaust gas purification device of internal combustion engine
WO2008117829A1 (en) * 2007-03-26 2008-10-02 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification apparatus
JP2011236074A (en) * 2010-05-10 2011-11-24 Mie Univ Hydrogen producing method using nano-composite semiconductor photocatalyst material and methanol aqueous solution
JP2017137769A (en) * 2016-02-01 2017-08-10 株式会社デンソー Exhaust gas recirculation system

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1243766B1 (en) * 2001-03-21 2008-07-23 Nissan Motor Co., Ltd. Exhaust gas purification device of internal combustion engine
WO2008117829A1 (en) * 2007-03-26 2008-10-02 Toyota Jidosha Kabushiki Kaisha Exhaust gas purification apparatus
JP2008240568A (en) * 2007-03-26 2008-10-09 Toyota Motor Corp Exhaust emission control device
US8257471B2 (en) 2007-03-26 2012-09-04 Toyota Jidosha Kabushiki Kaisha Exhaust-gas converting apparatus
KR101233524B1 (en) * 2007-03-26 2013-02-14 도요타지도샤가부시키가이샤 Exhaust-gas absorbing apparatus
JP2011236074A (en) * 2010-05-10 2011-11-24 Mie Univ Hydrogen producing method using nano-composite semiconductor photocatalyst material and methanol aqueous solution
JP2017137769A (en) * 2016-02-01 2017-08-10 株式会社デンソー Exhaust gas recirculation system

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