JPH044020A - Exhaust gas treating device - Google Patents

Exhaust gas treating device

Info

Publication number
JPH044020A
JPH044020A JP2105996A JP10599690A JPH044020A JP H044020 A JPH044020 A JP H044020A JP 2105996 A JP2105996 A JP 2105996A JP 10599690 A JP10599690 A JP 10599690A JP H044020 A JPH044020 A JP H044020A
Authority
JP
Japan
Prior art keywords
exhaust gas
magnetite
oxygen
exhaust
carbon dioxide
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.)
Pending
Application number
JP2105996A
Other languages
Japanese (ja)
Inventor
Norio Shudo
首藤 矩生
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.)
Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki and Co Ltd
Iseki Agricultural Machinery Mfg Co 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 Iseki and Co Ltd, Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki and Co Ltd
Priority to JP2105996A priority Critical patent/JPH044020A/en
Publication of JPH044020A publication Critical patent/JPH044020A/en
Pending legal-status Critical Current

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Abstract

PURPOSE:To well crack carbon dioxide and NOx to carbon and nitrogen by providing an exhaust gas stirrer on the upstream of an exhaust gas flow passage than magnetite. CONSTITUTION:This exhaust gas treating device cracks the carbon dioxide and NOx in exhaust gases by the magnetite which is activated by making oxygen atoms lack. The magnetite 14 is transformed to the oxygen-lacking magnetite in an exhaust gas treating section 8 connected to the flow passage 11 where the exhaust gases flow and, therefore, the oxygen of the carbon dioxide and the oxygen of the NOx are taken by the oxygen-lacking magnetite. The exhaust gases are stirred over the entire part of the magnetite 14 by the exhaust gas stirrer 18 at this time, by which the exhaust gases are well cracked.

Description

【発明の詳細な説明】 〔産業上の利用分野〕 この発明は排気ガス中の炭酸ガスや窒素酸化物を少なく
シ、又は無くす排気ガス処理装置に関するものである。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to an exhaust gas treatment device that reduces or eliminates carbon dioxide and nitrogen oxides in exhaust gas.

〔従来技術〕[Prior art]

この種の従来技術としては、特開昭63−113112
号公翰に示すように白金バナジュウムや白金ロジュウム
等の複数の触媒を排気ガス通路に直列的に並入で一酸化
炭素を酸化して炭酸ガスにしたり、窒素酸化物N Ox
を窒素ガスN2にする排気ガス処理装置がある。
As a conventional technique of this kind, Japanese Patent Application Laid-Open No. 63-113112
As shown in the notice, multiple catalysts such as platinum vanadium and platinum rhodium are placed in series in the exhaust gas passage to oxidize carbon monoxide to carbon dioxide gas and oxidize nitrogen oxides NOx.
There is an exhaust gas treatment device that converts nitrogen gas into nitrogen gas N2.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

上記従来のものは、コストが高くなると共に、−酸化炭
素を炭酸ガスとして排気させてしまい(現在世界中で温
暖化の要因になっている炭酸ガスの放出は抑えなければ
ならないにも拘らず)、完全な浄化対策になっていない
The conventional methods mentioned above are not only expensive, but also emit carbon oxide as carbon dioxide gas (despite the fact that the emission of carbon dioxide gas, which is currently a cause of global warming around the world, must be suppressed). , it is not a complete purification measure.

更に、複数箇所の各別な触媒中を排気ガスは通過しなけ
ればならないために、エンジンの出力が低ドしてそれだ
け多くの燃料が必要になりこのために更に多くの排気ガ
スが発生して本質的な排気ガスの浄化にならないという
課題があった。
Furthermore, because the exhaust gases have to pass through different catalysts at multiple locations, the engine output is lower and more fuel is required, which in turn generates more exhaust gases. The problem was that it did not essentially purify the exhaust gas.

[課題を解決する手段〕 前記の課題を解決するために、この発明は酸素原子を欠
鎮させて活性化したマグネタイトにて排気ガス中の炭酸
ガス又は窒素酸化物を分解する排気ガス処理装置におい
て、該マグネタイトよりも排気ガス流路上手側に排気ガ
ス撹拌装置を設けたことを特徴とする排気ガス処理装置
としたものである。
[Means for Solving the Problems] In order to solve the above problems, the present invention provides an exhaust gas treatment device that decomposes carbon dioxide or nitrogen oxides in exhaust gas using magnetite activated by depleting oxygen atoms. , an exhaust gas treatment device characterized in that an exhaust gas stirring device is provided on the upstream side of the exhaust gas flow from the magnetite.

〔作用〕[Effect]

排気ガス処理装置の基本的な作用は、マグネタイト(フ
ェライト)を有効に利用したものである。
The basic function of the exhaust gas treatment device is to make effective use of magnetite (ferrite).

即ち、マグネタイトの分子構造は陽イオンを2個保有し
た2価の鉄(1’e” )1個と3個保有した3価の鉄
D’e”)2個が存在して計8価のプラス電荷になり、
これが陰イオンを保有する酸素(02)4個と結び付い
てl’e、04の安定したマグネタイトになっているが
、このマグネタイトは250℃〜600℃(最適の温度
は250℃〜300℃)で水素(H7)と反応して酸素
(O3)が水(H,O)になって逃げ、酸素が欠乏した
活性のマグネタイトが得られる。即ち、活性のマグネタ
イトは、以下、酸素欠落マグネタイト(Fe10、−x
)と呼ぶが、この活性化されたマグネタイトは250℃
〜600℃(最適の温度は250℃〜300℃)で酸素
分子を要求する化学反応可能な状態にある。
In other words, the molecular structure of magnetite consists of one divalent iron (1'e") that has two cations and two trivalent iron (D'e") that has three cations, making it a total of 8 valent iron. becomes a positive charge,
This combines with four oxygen (02) particles that contain anions to form stable magnetite l'e, 04, but this magnetite is stable at 250°C to 600°C (the optimal temperature is 250°C to 300°C). Oxygen (O3) reacts with hydrogen (H7) and escapes as water (H, O), yielding active oxygen-deficient magnetite. That is, active magnetite is hereinafter referred to as oxygen-deficient magnetite (Fe10, -x
), but this activated magnetite is heated to 250℃
At ~600°C (optimal temperature is 250°C to 300°C), it is ready for chemical reactions that require oxygen molecules.

したがって、この状態にした酸素欠落マグネタイトに炭
酸ガスを反応させると炭素と不活性状態のマグネタイト
になり、次に、水素をこの不活性マグネタイトに反応さ
せると急速に活性マグネタイトと水になる。これを化学
反応式にすると。
Therefore, when oxygen-deficient magnetite in this state is reacted with carbon dioxide gas, it becomes carbon and inactive magnetite, and then when hydrogen is reacted with this inactive magnetite, it rapidly becomes active magnetite and water. If we convert this into a chemical reaction equation.

Fe、04+yH,→Fe、○a−x + y H?○
Fe、04−x+1/2yCO,→ 1/2yC+l’
e、04である。
Fe, 04+yH, →Fe, ○a-x + yH? ○
Fe, 04-x+1/2yCO, → 1/2yC+l'
e, 04.

したがって、内燃機関の排気通路途中に設けたマグネタ
イトを上記のように酸素欠落マグネタイトにしてこれに
排気ガスを接触させて炭酸ガスの一部を炭素と水に分解
して排出し、窒素酸化物を窒素ガスにして排出する。
Therefore, the magnetite provided in the middle of the exhaust passage of an internal combustion engine is converted into oxygen-deficient magnetite as described above, and the exhaust gas is brought into contact with this to decompose part of the carbon dioxide gas into carbon and water, which are then discharged and nitrogen oxides are removed. Discharge as nitrogen gas.

〔実施例〕〔Example〕

この発明の一実施例について詳述すると、1は内燃機関
の一種である4気筒ヂーゼルエンジンで、2はその排気
マニホールドである。
Describing one embodiment of the present invention in detail, numeral 1 is a four-cylinder diesel engine, which is a type of internal combustion engine, and numeral 2 is its exhaust manifold.

3は排気マニホールド2の各気筒毎の排気通路2a内に
設けられた酸素分離装置である。
3 is an oxygen separation device provided in the exhaust passage 2a of each cylinder of the exhaust manifold 2.

4は水素又はヘリウム等の無酸素ガス(当実施例では水
素で説明する。)を入れたガスボンベである。
Reference numeral 4 denotes a gas cylinder containing an oxygen-free gas such as hydrogen or helium (hydrogen will be used in this embodiment).

5は無酸素ガスの取出し通路である。5 is an oxygen-free gas extraction passage.

6は切換弁で、各気筒毎の酸素分離装置3・を通過し集
合パイプ3aにて集合させた排気ガスとガスボンベ4か
らの無酸素ガスとを後述の排気ガス処理部7・8の何れ
かに選択的に流入させる2方向選択型の弁になっている
Reference numeral 6 denotes a switching valve, which directs the exhaust gas that has passed through the oxygen separator 3 for each cylinder and collected in the collection pipe 3a and the oxygen-free gas from the gas cylinder 4 to either of the exhaust gas processing units 7 and 8, which will be described later. It is a two-way selection valve that selectively allows water to flow into the water.

9は無酸素ガスの取出し通路5の途中に設けられた開閉
弁である。
Reference numeral 9 denotes an on-off valve provided in the middle of the oxygen-free gas extraction passage 5.

7・8は前記切換弁6の二つの出口側ポートに通ずる流
路10・11に各別に設けた排気ガス処理部であって5
各流路10・11に連結した排気筒12・13にマグネ
タイト14(通気可能に多数の穴14a・・・の開いた
形状に焼結形成されている)を充填したセル15・15
を内装させ、更に、セル15・15が内装される排気筒
12・13の外周部にヒータ16を設けてマグネタイト
14が内装された部分を250℃〜300℃の温度に保
つように構成している(尚、このヒータ16はエンジン
熱でマグネタイト14を250℃〜300℃に保つ場合
は必要でない)。
Reference numerals 7 and 8 designate exhaust gas treatment units provided separately in flow paths 10 and 11 leading to the two outlet ports of the switching valve 6, respectively.
Cells 15 and 15 filled with magnetite 14 (sintered into a shape with a large number of holes 14a for ventilation) are filled in exhaust pipes 12 and 13 connected to each flow path 10 and 11.
Further, a heater 16 is provided on the outer periphery of the exhaust pipes 12 and 13 in which the cells 15 and 15 are installed to keep the part where the magnetite 14 is installed at a temperature of 250°C to 300°C. (This heater 16 is not necessary if the magnetite 14 is kept at 250° C. to 300° C. by engine heat).

17・18は各々排気筒12・13内に設けられた排気
ガス撹拌装置であって、各々撹拌翼17a・1.8 a
が電動モータ17b・18bによって同転され、排気ガ
スをマグネタイト14・14全体に撹拌するように設け
られている。
17 and 18 are exhaust gas stirring devices provided in the exhaust pipes 12 and 13, respectively, with stirring blades 17a and 1.8a, respectively.
are rotated simultaneously by electric motors 17b and 18b, and are provided so as to stir exhaust gas throughout the magnetites 14 and 14.

19はマフラーであって、排%<、m12・13からの
排気をその開放口20より大剣中に排出する。
Reference numeral 19 is a muffler, which discharges the exhaust from m12 and m13 into the large sword through its open port 20.

尚、21・・・は排気マニホールド2をヂーゼルエンジ
ン1に着脱するためのボルトであり、22・・は排気マ
ニホールド2の蓋部2bをマフラー】9と共に着脱する
ボルトである。
In addition, 21... are bolts for attaching and detaching the exhaust manifold 2 to the diesel engine 1, and 22... are bolts for attaching and detaching the cover portion 2b of the exhaust manifold 2 together with the muffler ]9.

上側の作用について詳述すると、ヂーゼルエンジン1の
各気筒の排気ガスが各#未分離装置3・・・内に流れ、
各酸素分離装置3・・・内で酸素02が大気中に放出さ
れ炭酸ガスCO2・窒素酸化物N。
To explain the upper operation in detail, the exhaust gas from each cylinder of the diesel engine 1 flows into each # unseparated device 3...
In each oxygen separator 3..., oxygen 02 is released into the atmosphere, producing carbon dioxide gas CO2 and nitrogen oxides N.

Xの混合した排気ガスが集合パイプ3aを通って切換弁
6に向けて流出する。そして、その排気ガスは切換弁6
を経て流路11に流れ、一方ガスボンベ4の水素H7が
通路5及び開閉弁9を通って切換弁6を経て流路10に
流れる。すると、排気ガスの流れる流路11に接続され
た排気ガス処理部8では、マグネタイト14を予め水素
H2を通して活性にしておけばマグネタイト自体が酸素
欠落マグネタイトFe10.−xに変身しているから、
炭酸ガスCO2の酸素02あるいはNOxの酸素OXを
該酸素欠落マグネタイトが取り込み、炭素Cが析出した
り、あるいは窒素ガスN2になって飛び出る。このとき
、排気ガス撹拌装置18にてマグネタイト14全体に排
気ガスが撹拌されるので、良好に上記の排気ガスの分解
がおこなわれる。
The exhaust gas mixed with X flows out toward the switching valve 6 through the collecting pipe 3a. Then, the exhaust gas is transferred to the switching valve 6
On the other hand, hydrogen H7 from the gas cylinder 4 passes through the passage 5 and the on-off valve 9, and flows into the flow passage 10 via the switching valve 6. Then, in the exhaust gas processing section 8 connected to the flow path 11 through which the exhaust gas flows, if the magnetite 14 is activated by passing hydrogen H2 in advance, the magnetite itself becomes oxygen-deficient magnetite Fe10. -Because it transforms into x,
The oxygen-deficient magnetite takes in oxygen 02 of carbon dioxide gas CO2 or oxygen OX of NOx, and carbon C precipitates or escapes as nitrogen gas N2. At this time, the exhaust gas is stirred throughout the magnetite 14 by the exhaust gas stirring device 18, so that the above-mentioned exhaust gas is effectively decomposed.

一方、水素H7が送り込まれる排気ガス処理部7では、
不活性のマグネタイトFe、04に排気ガス撹拌装置1
7にて撹拌された水素H2が働き、この水素H2がマグ
ネタイト中の酸素07を追い出して酸素欠落マグネタイ
トになる。
On the other hand, in the exhaust gas treatment section 7 into which the hydrogen H7 is sent,
Inert magnetite Fe, exhaust gas stirring device 1 in 04
The hydrogen H2 stirred in step 7 acts, and this hydrogen H2 drives out oxygen 07 in the magnetite, resulting in oxygen-deficient magnetite.

即ち、排気ガス処理部7側では、 F’ e z O4+x H2→F e :l○4−X
+XH,0の化学反応がおこなわれ、排気ガス処理部8
側では、 F”e、04−x  +co、−+C+Fe、Onある
いは。
That is, on the exhaust gas treatment section 7 side, F' ez O4+x H2→F e :l○4-X
A chemical reaction of +XH,0 takes place, and the exhaust gas treatment section 8
On the side, F”e, 04-x +co, -+C+Fe, On or.

)’eioa−x+2NOx  −+ N7+Fet 
○4の化学反応がおこる。
)'eioa-x+2NOx −+ N7+Fet
○4 chemical reaction occurs.

尚、窒素酸化物NOxについては、極めて速い反応にな
り、窒素酸化物の浄化は相当速く行なわれるが、炭酸ガ
スCO7については、反応が遅く、排気ガス処理部を加
圧状態にすることが望ましい。
It should be noted that the reaction with nitrogen oxides NOx is extremely fast and the purification of nitrogen oxides is carried out fairly quickly, but the reaction with carbon dioxide CO7 is slow and it is desirable to pressurize the exhaust gas treatment section. .

そして、所定時間(1分〜3分程度が適当)第2図の状
態を続けた後、今度は切換弁6を切換えて排気ガスが流
路10に、水素H2が流路11に流れるように切換える
と、前記と同じ作用で排気ガスが浄化されることになる
After continuing the state shown in Fig. 2 for a predetermined period of time (approximately 1 to 3 minutes), the switching valve 6 is switched so that the exhaust gas flows into the flow path 10 and the hydrogen H2 flows into the flow path 11. When switched, the exhaust gas will be purified by the same effect as described above.

そして、水素H2送込み側の開閉弁9は、前記切換弁6
の切換えに連動して所定時間(10秒〜30秒程度)開
口すると閉口するようにしておけば、水素H2の無駄を
なくすることができる。
The on-off valve 9 on the hydrogen H2 feed side is the switching valve 6.
By opening the opening for a predetermined period of time (approximately 10 seconds to 30 seconds) and then closing it in conjunction with the switching, it is possible to eliminate waste of hydrogen H2.

尚、上記実施例においては、マグネタイト中の酸素を追
い出して酸素欠落マグネタイトにする手段として無酸素
ガス(水素又はヘリウム)を用いる例を示したが、他に
マグネタイトに高電圧をかけて酸素(0”)を追い出す
等如何なる手段を用いても良い。また、マグネタイトは
焼結形成したもの以外に、粉状9粒状又は板状等如何な
る形状のものを用いても良いが、排気ガスとの接触面積
が広くなる程分解効率が良くなるので、できるだけ接触
面積が広くなるようにすると良い。更に、上記実施例で
は内燃機関としてヂーゼルエンジンの例を示したが、他
にガソリンエンジン、ガスエンジン、又は火力発電機等
の如何なる内燃機関でも良い。
In the above example, an example was shown in which an oxygen-free gas (hydrogen or helium) was used as a means to expel oxygen from magnetite to form oxygen-deficient magnetite. ”) may be used. In addition, magnetite may be in any shape, such as powder, grains, or plates, in addition to sintered magnetite, but the area of contact with the exhaust gas may be The wider the area, the better the decomposition efficiency, so it is better to make the contact area as wide as possible.Furthermore, in the above embodiment, a diesel engine was used as an internal combustion engine, but other engines such as a gasoline engine, a gas engine, or a thermal engine may also be used. Any internal combustion engine such as a generator may be used.

〔作用効果〕[Effect]

この発明は、酸素原子を欠落させて活性化したマグネタ
イトにて排気ガス中の炭酸ガス又は窒素酸化物を分解す
る排気ガス処理装置において、該マグネタイトよりも排
気ガス流路上手側に排気ガス撹拌装置を設けたことを特
徴とする排気ガス処理装置としたから、撹拌装置にて排
気ガスがマグネタイト全体に撹拌され、良好に炭酸ガス
や窒素酸化物を分解して炭素や窒素にすることができ。
This invention relates to an exhaust gas treatment device that decomposes carbon dioxide or nitrogen oxides in exhaust gas using magnetite activated by removing oxygen atoms, in which an exhaust gas stirring device is provided on the upstream side of the exhaust gas flow from the magnetite. Since the exhaust gas treatment device is characterized by being equipped with a stirring device, the exhaust gas is stirred throughout the magnetite by the stirring device, and carbon dioxide gas and nitrogen oxides can be effectively decomposed into carbon and nitrogen.

前述の従来の課題を的確に解消することができる。The above-mentioned conventional problems can be accurately solved.

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

図は、この発明の一実施例であって、第1図は全体の概
略平向図、第2図はそのA−A矢視部を断面にした側面
図である。図中の記号 1はヂーゼルエンジン、2は排気マニホールド、3は酸
素分離装置、4はガスボンベ、5は取出し通路、6は切
換弁、7・8は排気ガス処理部、9は開閉弁、10・1
1は流路、12・13は排気筒、14はマグネタイト、
15はセル、16はヒータ、17・18は排気ガス撹拌
装置、19はマフラーを示す。
The drawings show an embodiment of the present invention, in which FIG. 1 is a schematic plan view of the entire device, and FIG. 2 is a side view taken along the line A--A in cross section. In the figure, symbol 1 is a diesel engine, 2 is an exhaust manifold, 3 is an oxygen separator, 4 is a gas cylinder, 5 is an extraction passage, 6 is a switching valve, 7 and 8 are exhaust gas treatment parts, 9 is an on-off valve, 10. 1
1 is a flow path, 12 and 13 are exhaust pipes, 14 is magnetite,
15 is a cell, 16 is a heater, 17 and 18 are exhaust gas stirring devices, and 19 is a muffler.

Claims (1)

【特許請求の範囲】[Claims] (1)酸素原子を欠落させて活性化したマグネタイトに
て排気ガス中の炭酸ガス又は窒素酸化物を分解する排気
ガス処理装置において、該マグネタイトよりも排気ガス
流路上手側に排気ガス撹拌装置を設けたことを特徴とす
る排気ガス処理装置。
(1) In an exhaust gas treatment device that decomposes carbon dioxide or nitrogen oxides in exhaust gas using magnetite activated by removing oxygen atoms, an exhaust gas stirring device is installed on the upstream side of the exhaust gas flow from the magnetite. An exhaust gas treatment device characterized by being provided with.
JP2105996A 1990-04-20 1990-04-20 Exhaust gas treating device Pending JPH044020A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2105996A JPH044020A (en) 1990-04-20 1990-04-20 Exhaust gas treating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2105996A JPH044020A (en) 1990-04-20 1990-04-20 Exhaust gas treating device

Publications (1)

Publication Number Publication Date
JPH044020A true JPH044020A (en) 1992-01-08

Family

ID=14422328

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2105996A Pending JPH044020A (en) 1990-04-20 1990-04-20 Exhaust gas treating device

Country Status (1)

Country Link
JP (1) JPH044020A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009172467A (en) * 2008-01-22 2009-08-06 Nippon Steel Corp Metal carrier, decomposition catalyst of carbon dioxide in gas, method of manufacturing the carrier and catalyst, and method for decomposition of carbon dioxide

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009172467A (en) * 2008-01-22 2009-08-06 Nippon Steel Corp Metal carrier, decomposition catalyst of carbon dioxide in gas, method of manufacturing the carrier and catalyst, and method for decomposition of carbon dioxide

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