JPH045419A - Exhaust gas treating device - Google Patents
Exhaust gas treating deviceInfo
- Publication number
- JPH045419A JPH045419A JP10509490A JP10509490A JPH045419A JP H045419 A JPH045419 A JP H045419A JP 10509490 A JP10509490 A JP 10509490A JP 10509490 A JP10509490 A JP 10509490A JP H045419 A JPH045419 A JP H045419A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- magnetite
- oxygen
- gas
- exhaust
- 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
Links
- 239000007789 gas Substances 0.000 claims abstract description 82
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims abstract description 45
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 35
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 17
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 16
- 125000004430 oxygen atom Chemical group O* 0.000 claims abstract description 4
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 4
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 claims description 31
- 238000012958 reprocessing Methods 0.000 claims description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 7
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052799 carbon Inorganic materials 0.000 abstract description 5
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 20
- 239000001301 oxygen Substances 0.000 description 20
- 229910052760 oxygen Inorganic materials 0.000 description 20
- 239000001257 hydrogen Substances 0.000 description 13
- 229910052739 hydrogen Inorganic materials 0.000 description 13
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 10
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 230000002950 deficient Effects 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 238000002485 combustion reaction Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- 239000003054 catalyst Substances 0.000 description 2
- 150000001768 cations Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 229910002090 carbon oxide Inorganic materials 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- PXXKQOPKNFECSZ-UHFFFAOYSA-N platinum rhodium Chemical compound [Rh].[Pt] PXXKQOPKNFECSZ-UHFFFAOYSA-N 0.000 description 1
- ICTAZHZJEOVXOW-UHFFFAOYSA-N platinum vanadium Chemical compound [V].[Pt].[Pt].[Pt] ICTAZHZJEOVXOW-UHFFFAOYSA-N 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 229910000859 α-Fe Inorganic materials 0.000 description 1
Landscapes
- Exhaust Gas After Treatment (AREA)
Abstract
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
し、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.
この種の従来技術としては、特開昭63−113112
号公報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べて一酸化
炭素を酸化して炭酸ガスにしたり、窒素酸化物NOx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 publication, multiple catalysts such as platinum vanadium and platinum rhodium are arranged in series in the exhaust gas passage to oxidize carbon monoxide to carbon dioxide gas and convert nitrogen oxides NOx to nitrogen gas N2 for exhaust gas treatment. There is a device.
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下してそれだ
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's output is reduced and more fuel is required, which in turn generates more exhaust gases. The problem was that it did not purify the exhaust gas.
前記の課題を解決するために、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、処理した排気ガスを再度処理すべく流路上手側に戻
す流路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。In order to solve the above-mentioned problems, the present invention is an exhaust gas treatment device that decomposes carbon dioxide or nitrogen oxides in exhaust gas using magnetite activated by removing oxygen atoms, and processes the treated exhaust gas again. This exhaust gas treatment device is characterized in that a flow path is provided for returning the exhaust gas to the upstream side of the flow path.
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(Fe” )1個と3個保有した3価の鉄(
Fe”)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(0”)4個と結び付いて
Fe10.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2
50℃〜300℃)で水素(H7)と反応して酸素(0
2)が水(H20>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(ドe、04−x)と
呼ぶが、この活性化されたマグネタイトは250℃〜6
00℃(gt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 is composed of one divalent iron (Fe), which has two cations, and trivalent iron (Fe”), which has three cations.
There are two Fe"), resulting in a total of eight positive charges, which combine with four oxygen (0") containing anions to form Fe10. This magnetite is stable at 250℃ to 600℃ (the optimum temperature is 2
50℃~300℃) reacts with hydrogen (H7) to form oxygen (0
2) escapes as water (H20>), and oxygen-deficient active magnetite is obtained.In other words, active magnetite is hereinafter referred to as oxygen-deficient magnetite (de, 04-x), but this activation magnetite is heated to 250℃~6
It is in a state where chemical reactions requiring oxygen molecules can occur at 00°C (the temperature suitable for GT is 250°C to 300°C).
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、F e x 04 +y H2→Fe
、 04− x 十y H> 0)’ eqo4−x
+1/2yCO,→ 1/2:yc+Fe、O。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 formula, F e x 04 +y H2→Fe
, 04-x 1y H>0)' eqo4-x
+1/2yCO, → 1/2:yc+Fe,O.
である。It is.
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.
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 designates a switching valve that transfers 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 the exhaust gas processing units 7 and 8, which will be described later. It is a two-way selection type valve that selectively allows the water to flow into either direction.
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、
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=f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・1
5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 are exhaust gas processing units provided separately in flow paths 10 and 11 leading to the two outlet ports of the switching valve 6,
Cells 15 and 1 are filled with magnetite 14 (sintered and formed in a shape with a large number of holes 14a for ventilation) 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】7a・18aが電
動モータ17b・18bによって回転され、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6
10a・llaは戻し流路であって、排気ガス処理部7
・8にて処理した排気ガスの一部を再び流路10・11
に戻して再処理するべく設けられている。尚、10b・
llbは吸引ファンであって、強制的に処理済みの排気
ガスの一部を再び流路10・11に戻すべく設けられて
いる。17 and 18 are exhaust gas stirring devices provided in the exhaust pipes 12 and 13, respectively, and stirring blades 7a and 18a are rotated by electric motors 17b and 18b to stir the exhaust gas throughout the magnetite 14 and 14. 6 10a and lla are return flow paths provided to
・A part of the exhaust gas treated in step 8 is returned to flow paths 10 and 11.
It is designed to be returned to the factory for reprocessing. Furthermore, 10b・
A suction fan llb is provided to forcibly return a portion of the treated exhaust gas to the flow paths 10 and 11.
19はマフラーであって、排気筒12・13からの排量
をその開放口20より大気中に排出する。Reference numeral 19 denotes a muffler, which discharges the exhaust gas from the exhaust pipes 12 and 13 into the atmosphere 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l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19と共に着脱す
るボルトである。21... are bolts for attaching and detaching the exhaust manifold 2 to the diesel engine l, and 22... are bolts for attaching and detaching the cover portion 2b of the exhaust manifold 2 together with the muffler 19.
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酸素分離装置3・・・内に流れ、
各酸素分離装置3・・・内で酸素○アが大低中に放出さ
れ炭酸ガスC○2・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 oxygen separation device 3...
In each oxygen separator 3..., oxygen ○a is released into the air, producing carbon dioxide gas C○2 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H2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Fe、、0.−xに変身しているから
、炭酸ガスCO2の1!!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。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 H2 in 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 Fe, 0. - Since it is transformed into x, 1 of carbon dioxide gas CO2! ! The oxygen-deficient magnetite takes in the oxygen OX of element 02 or 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.
良好に上記の排気ガスの分解がおこなわれる。The above exhaust gas is decomposed well.
一方、水素H2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、0.に排気ガス撹拌装置1
7にて撹拌された水素H,が働き、この水素H2がマグ
ネタイト中の酸素02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 hydrogen H2 is sent,
Inert magnetite Fe, 0. Exhaust gas stirring device 1
The hydrogen H, stirred in step 7 acts, and this hydrogen H2 drives out the oxygen 02 in the magnetite, resulting in oxygen-deficient magnetite.
即ち、排気ガス処理部7側では、
ト′ e104+XH2−)F e、CL−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
、
)”e、04−x+C○2 → C+ F e 、
、 04あるいは、
Fe、04−x+2NOx−+N2+ )’e、+oa
の化学反応がおこる。That is, on the exhaust gas treatment section 7 side,
, 0 chemical reaction takes place, and on the exhaust gas treatment section 8 side, )"e, 04-x+C○2 → C+ Fe,
, 04 or Fe, 04-x+2NOx-+N2+ )'e, +oa
A 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C○2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。Regarding nitrogen oxides (NOx), the reaction is extremely fast and purification of nitrogen oxides is carried out fairly quickly, but for carbon dioxide gas (C○2), the reaction is slow and it is necessary to pressurize the exhaust gas treatment section. is desirable.
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.
上記排気ガスの浄化過程において、排気ガス処理部7・
8にて処理した排気ガスの一部を戻し流路10a・ll
aにて再び流路10・11に戻して再処理するようにし
ているので、排気ガスの浄化が的確である。In the exhaust gas purification process, the exhaust gas treatment section 7.
A part of the exhaust gas treated in step 8 is returned to the flow path 10a/ll.
Since the exhaust gas is returned to the flow paths 10 and 11 at step a for reprocessing, the exhaust gas can be purified accurately.
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 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(0−2)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2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。また、戻し流路1
0a・llaに吸引ファン10b・11bを用いた例を
示したが、排気ガスを戻す手段としては如何なる手段を
用いてもよい。更に、」−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. -2) Any means may be used, such as expelling the The larger the area, the better the decomposition efficiency, so it is better to make the contact area as wide as possible. In addition, the return flow path 1
Although an example is shown in which suction fans 10b and 11b are used for 0a and lla, any means may be used to return the exhaust gas. Furthermore, although a diesel engine is shown as an example of the internal combustion engine in the embodiment described above, any other internal combustion engine such as a gasoline engine, a gas engine, or a thermal power generator may be used.
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、処理した排気ガスを再度
処理すべく流路上手側に戻す流路を設けた排気ガス処理
装置としたから、排気ガスの炭酸ガスや窒素酸化物を分
解して炭素や窒素にする処理が的確におこなえ、前述の
従来の課題を良好に解消することができる。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 the treated exhaust gas is returned to the upstream side of the flow path for further treatment. Since the exhaust gas treatment device is equipped with a flow path, it is possible to accurately decompose carbon dioxide and nitrogen oxides in the exhaust gas into carbon and nitrogen, and successfully solve the above-mentioned conventional problems. .
図は、この発明の一実施例であって、第1図は全体の概
略平面図、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、10a・11aは戻し流路、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 channel, 10a and 11a are return channels, 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)
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、処理した排気ガスを再度処理す
べく流路上手側に戻す流路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, the flow that returns the treated exhaust gas to the upstream side for reprocessing. An exhaust gas treatment device characterized by having a passage.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10509490A JPH045419A (en) | 1990-04-19 | 1990-04-19 | Exhaust gas treating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP10509490A JPH045419A (en) | 1990-04-19 | 1990-04-19 | Exhaust gas treating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH045419A true JPH045419A (en) | 1992-01-09 |
Family
ID=14398326
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP10509490A Pending JPH045419A (en) | 1990-04-19 | 1990-04-19 | Exhaust gas treating device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH045419A (en) |
-
1990
- 1990-04-19 JP JP10509490A patent/JPH045419A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105003326B (en) | Marine exhaust denitrating system | |
KR101290022B1 (en) | Electrochemical-catalytic converter for exhaust emission control | |
JPH04243525A (en) | Apparatus for purifying exhaust gas of internal combustion engine | |
JPH0747233A (en) | Device for reducing nitrogen oxide in combustion exhaust gas | |
AU2421001A (en) | Nox-reducing catalyst with temperature regulation of exhaust gases | |
US4867949A (en) | Heat recuperative combustion device | |
US7399451B1 (en) | Pollution control | |
JP2011185261A (en) | Electrochemical and catalyst converter for controlling discharge of exhaust gas | |
JPH045419A (en) | Exhaust gas treating device | |
CN102485326A (en) | Electrochemical catalyst converter | |
JPH044020A (en) | Exhaust gas treating device | |
JPH045420A (en) | Internal combustion engine | |
JPH045421A (en) | Internal combustion engine | |
KR200361923Y1 (en) | Catalytic Integrated Multistage Corona Reactor | |
JP2662911B2 (en) | Exhaust gas purification device | |
JPH0559933A (en) | Reducing agent reforming reactor and exhaust gas purifying device | |
CN103861453B (en) | Method for manufacturing exhaust gas purification reactor | |
JP2004195367A (en) | Catalytic unit, and apparatus and system for treating toxic exhaust gas by using the same | |
JP2986830B2 (en) | Engine exhaust gas treatment device | |
CN102335552A (en) | Electrochemical-catalytic converter controlling exhaust emission and generating electricity | |
CN112746885A (en) | Tail gas purification system and purification method for oil-fired train | |
US20060042235A1 (en) | Rotary NOx trap | |
KR101060370B1 (en) | EBR equipment and engine system including the same | |
JPH045417A (en) | Exhaust gas treating device for engine | |
CN213348304U (en) | VOCs exhaust purification device |