JP3051493B2 - Nitrogen oxide purification method - Google Patents

Nitrogen oxide purification method

Info

Publication number
JP3051493B2
JP3051493B2 JP3112909A JP11290991A JP3051493B2 JP 3051493 B2 JP3051493 B2 JP 3051493B2 JP 3112909 A JP3112909 A JP 3112909A JP 11290991 A JP11290991 A JP 11290991A JP 3051493 B2 JP3051493 B2 JP 3051493B2
Authority
JP
Japan
Prior art keywords
exhaust gas
catalyst
residence time
temperature
nitrogen oxides
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.)
Expired - Lifetime
Application number
JP3112909A
Other languages
Japanese (ja)
Other versions
JPH04341321A (en
Inventor
野島  繁
耕三 飯田
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 Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries Ltd
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 Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP3112909A priority Critical patent/JP3051493B2/en
Publication of JPH04341321A publication Critical patent/JPH04341321A/en
Application granted granted Critical
Publication of JP3051493B2 publication Critical patent/JP3051493B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

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

【0001】[0001]

【産業上の利用分野】本発明は排ガスの浄化方法に関
し、特に排ガス中の窒素酸化物(以後、NOxと略す)
を浄化する方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for purifying exhaust gas, and in particular, to nitrogen oxides (hereinafter abbreviated as NOx) in exhaust gas.
A method of purifying water.

【0002】[0002]

【従来の技術】自動車等の排気ガス処理においては、触
媒を用いて排ガス中のNOx、炭化水素、COを浄化す
るのが一般的である。現在、用いられている触媒の中
で、Pt、Rh系の三元触媒は理論空燃比付近において
NOx、炭化水素、COを同時除去しているが、O2
度が低いため燃費が悪くなるという問題点を抱えてい
る。
2. Description of the Related Art In the treatment of exhaust gas from automobiles and the like, it is general to purify NOx, hydrocarbons and CO in exhaust gas using a catalyst. Currently, in the used catalyst, Pt, NOx Rh system of the three-way catalyst in the vicinity of the stoichiometric air-fuel ratio, hydrocarbons, although simultaneous removal of CO, that the O 2 concentration fuel consumption due to the low deteriorate I have a problem.

【0003】[0003]

【発明が解決しようとする課題】一方、燃費向上のた
め、O2 濃度1%以上においてNOxを除去できる触媒
の開発が急がれているが、未だ実用化されていないのが
現状である。また、自動車エンジンの排気ガス処理に4
00セルの1リットルクラスのハニカム触媒を用いると
排気ガスラインの圧力損失が大きくなり、エンジンの性
能低下、マフラーの破損等の問題を抱えている。そのた
め触媒を用いずに排気ガス中のNOxを除去する方法が
望まれている。
On the other hand, the development of a catalyst capable of removing NOx at an O 2 concentration of 1% or more has been urgently promoted in order to improve fuel efficiency, but it has not yet been put to practical use. In addition, 4
If a 1-liter class honeycomb catalyst of 00 cells is used, the pressure loss in the exhaust gas line becomes large, and there are problems such as deterioration of engine performance and damage of the muffler. Therefore, a method for removing NOx in exhaust gas without using a catalyst is desired.

【0004】本発明は上記技術水準に鑑み、触媒を用い
ずとも排気ガス中のNOxを除去しうる方法を提供しよ
うとするものである。
The present invention has been made in view of the above-mentioned state of the art, and aims to provide a method capable of removing NOx in exhaust gas without using a catalyst.

【0005】[0005]

【課題を解決するための手段】本発明者らは鋭意触媒を
用いずに排ガス中のNOxを除去する方法を検討した結
果、驚くべく現象を見い出した。それは、これまで盲点
であったように思われるが、排ガス中の炭化水素、とり
わけ、エチレン、プロピレンが酸素含有下で特定の温度
範囲において効率的にNOxと反応してNOxはN
2 に、炭化水素はH 2 OとCO2 に変換する現象であ
る。
Means for Solving the Problems The present inventors have eagerly prepared a catalyst.
Investigation of a method to remove NOx in exhaust gas without using
As a result, I found a surprising phenomenon. It's a blind spot so far
It seems that hydrocarbons in the exhaust gas
That is, ethylene and propylene are at a certain temperature under oxygen content.
NOx reacts efficiently with NOx in the range
TwoAnd the hydrocarbon is H TwoO and COTwoIs a phenomenon that converts to
You.

【0006】本発明は上記知見に基づいて完成されたも
のであって、本発明は窒素酸化物、一酸化炭素及び炭化
水素を含有し、かつ高O 2 濃度を有する自動車排気ガス
を浄化する方法において、排気通路を400〜700℃
の範囲で保温し、該排気ガスを上記温度域に滞留時間
0.5秒以上保持することにより排気ガス中の窒素酸化
物を還元無害化することを特徴とする窒素酸化物の浄化
方法である。
The present invention has been completed based on the above findings, and the present invention provides a method for purifying automobile exhaust gas containing nitrogen oxides, carbon monoxide and hydrocarbons and having a high O 2 concentration. At 400 to 700 ° C.
The method for purifying nitrogen oxides is characterized in that nitrogen oxides in the exhaust gas are reduced and made harmless by keeping the temperature within the range described above and maintaining the exhaust gas in the temperature range for a residence time of 0.5 seconds or more. .

【0007】[0007]

【作用】ガソリン自動車は通常エンジンからマフラーま
で約800〜200℃までの広範囲な温度分布を有する
のが常であり、排気ガス管の中の滞留時間も通常0.5
秒以下である。本発明においては排気ガス管は温度を
00〜700℃に均一に保温し、さらに排気ガスの滞留
時間も0.5秒以上になるように、排気ガス管を数回往
復させる工夫がなされるものである。
The gasoline vehicle usually has a wide temperature distribution from the engine to the muffler from about 800 to 200 ° C., and the residence time in the exhaust gas pipe is usually 0.5.
Seconds or less. In the present invention, the exhaust gas pipe has a temperature of 4
The exhaust gas pipe is reciprocated several times so that the temperature is uniformly maintained at 00 to 700 ° C. and the residence time of the exhaust gas is 0.5 seconds or more.

【0008】本発明の排ガス浄化反応式は例えば(排ガ
ス中の炭化水素をC2 4 とすると) 2NO+C2 4 +2O2 → N2 +2CO2 +2H2
O ・・・(1) で表わされ、NOが選択的に触媒を用いずにN2 に還元
される温度は400〜700℃、好ましくは450〜7
00℃、とりわけ450〜650℃である。この反応温
度以外では還元剤が活性化されなかったり、還元剤(C
2 4 等)の燃焼反応のみが生じるため脱硝は生じな
い。また上記(1)式により脱硝をスムーズに行なわせ
るには均一温度の排気管中の滞留時間は0.5秒以上、
好ましくは1秒以上であることが好ましい。
In the exhaust gas purification reaction formula of the present invention, for example (assuming that the hydrocarbon in the exhaust gas is C 2 H 4 ), 2NO + C 2 H 4 + 2O 2 → N 2 + 2CO 2 + 2H 2
The temperature at which NO is selectively reduced to N 2 without using a catalyst is 400 to 700 ° C., preferably 450 to 7
00 ° C, especially 450-650 ° C. At a temperature other than this reaction temperature, the reducing agent is not activated or the reducing agent (C
No denitration occurs because only the combustion reaction of 2 H 4 etc. occurs. In order to smoothly perform the denitration according to the above equation (1), the residence time in the exhaust pipe at a uniform temperature is 0.5 seconds or more.
Preferably it is 1 second or more.

【0009】本発明方法により、従来実現されていなか
った高O2 濃度を有するリーンバーン領域での脱硝を触
媒を用いずに可能にしたものである。
According to the method of the present invention, denitration in a lean burn region having a high O 2 concentration, which has not been realized conventionally, is made possible without using a catalyst.

【0010】[0010]

【実施例】【Example】

(例1)リーンバーンガソリンエンジン模擬排気ガス組
成として、NO:400ppm、CO:1000pp
m、C2 4 :1500ppm、CO2 :10%、H2
O:10%、O2 :8%、残N2 の原料ガスを均一に保
温した反応管の内へ所定滞留時間で供給した。各温度、
各GHSVにおける脱硝率、脱エチレン率を表1に示
す。なお、こゝで示す滞留時間とは排気ガスが均一な温
度域に滞留している時間を指す。
(Example 1) As a simulated exhaust gas composition of a lean burn gasoline engine, NO: 400 ppm, CO: 1000 pp
m, C 2 H 4: 1500ppm , CO 2: 10%, H 2
O: 10%, O 2: 8%, was fed at a predetermined residence time to within the reaction tube was uniformly kept the raw material gas remaining N 2. Each temperature,
Table 1 shows the denitration rate and ethylene removal rate in each GHSV. Note that the residence time indicated here refers to the time during which the exhaust gas remains in a uniform temperature range.

【0011】表1に示す結果より主に温度400〜70
0℃において、上記排ガス組成で充分に脱硝することが
わかり、さらに滞留時間が長くなるにつれ、脱硝率が向
上することが判明した。また、C2 4 以外の他の炭化
水素の存在下でも、ほゞ例1と同様な効果が得られた。
[0011] From the results shown in Table 1, mainly the temperature 400-70
At 0 ° C., it was found that the denitration was sufficiently performed with the above exhaust gas composition, and it was found that as the residence time was further increased, the denitration rate was improved. Further, even in the presence of a hydrocarbon other than C 2 H 4 , almost the same effect as in Example 1 was obtained.

【表1】 [Table 1]

【0012】(例2)例1の結果に基づき、実際のリー
ンバーンガソリンエンジン排気ガス管を550℃均一に
保温でき、さらに所定以上の滞留時間を保つために排気
ガスを往復運動させマフラーより系外へ排出されるよう
にした。
(Example 2) Based on the results of Example 1, the exhaust gas pipe of an actual lean-burn gasoline engine can be kept uniformly at 550 ° C and the exhaust gas is reciprocated to maintain a residence time longer than a predetermined value. It was discharged outside.

【0013】このシステムの概略図を図1に示す。滞留
時間を1秒に保つようにした結果、触媒を用いずに図2
に示すように新10モード運転(通産省認定)を実施し
た結果脱硝率30%を有した。なお入口排気ガスの平均
組成は例1に示す模擬ガス組成と同様である。
A schematic diagram of this system is shown in FIG. As a result of keeping the residence time at 1 second, the catalyst was not used, and as shown in FIG.
As a result, a new 10-mode operation (certified by the Ministry of International Trade and Industry) resulted in a denitration rate of 30%. The average composition of the inlet exhaust gas was the same as the simulated gas composition shown in Example 1.

【0014】(比較例1)従来の排気ガスラインを図3
に示す。この従来法は排気ガス管は800〜200℃を
不均一に有し、排気管内における排気ガスの滞留時間は
0.2秒であった。触媒を用いずに新10モード運転を
実施した結果脱硝率は2%であった。なお、この排気ガ
ス平均組成も例1の模擬ガスと同じである。
Comparative Example 1 A conventional exhaust gas line is shown in FIG.
Shown in In this conventional method, the exhaust gas pipe has a non-uniform temperature of 800 to 200 ° C., and the residence time of the exhaust gas in the exhaust pipe is 0.2 seconds. As a result of performing a new 10-mode operation without using a catalyst, the denitration rate was 2%. The average composition of the exhaust gas is the same as that of the simulation gas of Example 1.

【0015】[0015]

【発明の効果】実施例にて示すように窒素酸化物、炭化
水素を含む排ガスを排気温度400〜700℃にて所定
滞留時間以上(0.5秒以上)保つことにより触媒を用
いずに、脱硝することが可能であることを明らかにし
た。
As shown in the examples, by keeping exhaust gas containing nitrogen oxides and hydrocarbons at an exhaust temperature of 400 to 700 ° C. for a predetermined residence time or more (0.5 seconds or more), a catalyst can be used without using a catalyst. It has been clarified that denitration is possible.

【0016】その結果、従来のリーンバーンガソリンエ
ンジン、ディーゼルエンジンの排気ガス浄化方法とし
て、触媒を用いる方法の代替として有効であることが判
明した。
As a result, it has been found that it is effective as a method for purifying exhaust gas of a conventional lean burn gasoline engine or diesel engine as an alternative to a method using a catalyst.

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

【図1】本発明の一実施例の説明図FIG. 1 is an explanatory diagram of one embodiment of the present invention.

【図2】新10モード運転の車速の図表FIG. 2 is a chart showing vehicle speeds in a new 10-mode driving mode.

【図3】従来の窒素酸化物の浄化方法の一態様の説明図FIG. 3 is an explanatory diagram of one embodiment of a conventional nitrogen oxide purification method.

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) B01D 53/56 F01N 3/08 F01N 3/10 ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) B01D 53/56 F01N 3/08 F01N 3/10

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 窒素酸化物、一酸化炭素及び炭化水素を
含有し、かつ高O 2 濃度を有する自動車排気ガスを浄化
する方法において、排気通路を400〜700℃の範囲
で保温し、該排気ガスを上記温度域に滞留時間0.5秒
以上保持することにより排気ガス中の窒素酸化物を還元
無害化することを特徴とする窒素酸化物の浄化方法。
1. A method for purifying automobile exhaust gas containing nitrogen oxides, carbon monoxide and hydrocarbons and having a high O 2 concentration, wherein the exhaust passage is kept in a temperature range of 400 to 700 ° C. A method for purifying nitrogen oxides, comprising reducing and detoxifying nitrogen oxides in exhaust gas by maintaining the gas in the above temperature range for a residence time of 0.5 seconds or more.
JP3112909A 1991-05-17 1991-05-17 Nitrogen oxide purification method Expired - Lifetime JP3051493B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3112909A JP3051493B2 (en) 1991-05-17 1991-05-17 Nitrogen oxide purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3112909A JP3051493B2 (en) 1991-05-17 1991-05-17 Nitrogen oxide purification method

Publications (2)

Publication Number Publication Date
JPH04341321A JPH04341321A (en) 1992-11-27
JP3051493B2 true JP3051493B2 (en) 2000-06-12

Family

ID=14598529

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3112909A Expired - Lifetime JP3051493B2 (en) 1991-05-17 1991-05-17 Nitrogen oxide purification method

Country Status (1)

Country Link
JP (1) JP3051493B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP6134094B2 (en) * 2011-11-04 2017-05-24 株式会社神戸製鋼所 Nitrogen oxide removal method
JP5751245B2 (en) 2012-11-30 2015-07-22 Tdk株式会社 Chip component mounting structure and module product using the same

Also Published As

Publication number Publication date
JPH04341321A (en) 1992-11-27

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