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JP2881684B2 - Method for cooling and purifying combustion exhaust gas, device therefor and filter - Google Patents
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JP2881684B2 - Method for cooling and purifying combustion exhaust gas, device therefor and filter - Google Patents

Method for cooling and purifying combustion exhaust gas, device therefor and filter

Info

Publication number
JP2881684B2
JP2881684B2 JP7211332A JP21133295A JP2881684B2 JP 2881684 B2 JP2881684 B2 JP 2881684B2 JP 7211332 A JP7211332 A JP 7211332A JP 21133295 A JP21133295 A JP 21133295A JP 2881684 B2 JP2881684 B2 JP 2881684B2
Authority
JP
Japan
Prior art keywords
exhaust gas
water
filter
temperature
cooling
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
JP7211332A
Other languages
Japanese (ja)
Other versions
JPH0938448A (en
Inventor
米原  隆
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.)
TOKYO KOPARU KAGAKU KK
Original Assignee
TOKYO KOPARU KAGAKU KK
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 TOKYO KOPARU KAGAKU KK filed Critical TOKYO KOPARU KAGAKU KK
Priority to JP7211332A priority Critical patent/JP2881684B2/en
Publication of JPH0938448A publication Critical patent/JPH0938448A/en
Application granted granted Critical
Publication of JP2881684B2 publication Critical patent/JP2881684B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/04Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust using liquids
    • 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
    • F01N3/02Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
    • F01N3/021Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
    • 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)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Exhaust Gas After Treatment (AREA)
  • Processes For Solid Components From Exhaust (AREA)
  • Treating Waste Gases (AREA)

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】この発明は、エンジンやその
他適宜の高温の燃焼排気ガスの冷却、浄化方法及びその
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 method and an apparatus for cooling and purifying an engine and other appropriate high-temperature combustion exhaust gas.

【0002】[0002]

【従来の技術】従来、エンジンの排気ガスには、すすの
成分であるカーボン粒子や、窒素酸化物が多く含まれて
いる。そこでこれらの排気ガスをエンジンの外で、触媒
を用いて再燃焼させ、カーボン又はCOを炭酸ガスにし
たり、NOxはN2にして放出する方法や、高圧放電に
よって帯電した流動性粘着物質に付着させて除去する方
法等が採られている。
2. Description of the Related Art Conventionally, exhaust gas of an engine contains a large amount of carbon particles and nitrogen oxides as soot components. Therefore these exhaust gases outside the engine deposits, the catalyst is re-burned with, or carbon or CO to carbon dioxide, NOx is a method of releasing in the N 2, the flowable adhesive material charged by the high-pressure discharge The removal method is adopted.

【0003】[0003]

【発明が解決しようとする課題】しかしながら前者の方
法だと触媒の耐久性にも問題があり、また空気を加熱し
なければならず、設備等にコストがかかり、また維持等
にも手間がかかる。また後者の方法では流動性粘着物質
に付着したカーボンが凝集して大きくなり、燃焼しにく
くなるため再利用がしにくい。従ってこれらの流動性粘
着物質の廃棄が問題と成る。
However, in the former method, there is a problem in the durability of the catalyst, and the air must be heated, so that the equipment is costly and the maintenance is troublesome. . Also, in the latter method, the carbon adhered to the fluid adhesive substance is aggregated and becomes large, making it difficult to burn, so that it is difficult to reuse. Therefore, disposal of these fluid adhesives poses a problem.

【0004】この発明はこれらの点に鑑みてなされたも
のであり、燃焼系の中で最も多く発生しており、ガス状
態で発生する水の特性に注目し、その状態変化を活用し
たむだの少ない実用性の極めて高い燃焼排気ガスの冷
却、浄化方法及びその装置を提供し上記課題を解決しよ
うとするものである。
[0004] The present invention has been made in view of the above points, is the most generated in the combustion system, paying attention to the characteristics of water generated in the gas state, and utilizing the state change. An object of the present invention is to provide a method of cooling and purifying combustion exhaust gas which is less practical and extremely high, and a device therefor to solve the above problems.

【0005】[0005]

【課題を解決するための手段】そこで請求項1項の発明
は高温の排気ガスを外気に排出する経路において、適宜
の密閉したチャンバー内で当該排気ガスを循環使用する
水に接触させて、その熱で当該水が気化し、この気化熱
によって排気ガスの温度が下がることにより、当該排気
ガスを冷却させるとともに排気ガス中のカーボン粉末等
の固形微粒子及び一酸化炭素等の有害ガスを分解、吸着
させる燃焼排気ガスの冷却及び浄化方法とした。
SUMMARY OF THE INVENTION Accordingly, the invention of claim 1 provides a method for discharging hot exhaust gas to the outside air by contacting the exhaust gas with water for circulating use in an appropriate closed chamber. The heat evaporates the water, and the heat of vaporization lowers the temperature of the exhaust gas, thereby cooling the exhaust gas and decomposing and adsorbing solid particulates such as carbon powder and harmful gases such as carbon monoxide in the exhaust gas. And a method of cooling and purifying the combustion exhaust gas to be cooled.

【0006】請求項2項の発明は高温の排気ガスを外気
に排出する経路において、適宜の密閉したチャンバー内
で当該排気ガスを界面活性剤等の分散剤及び消泡剤を少
量添加した循環する水に接触させて、その熱で当該水が
気化し、この気化熱によって排気ガスの温度が下がるこ
とにより、当該排気ガスを冷却させるとともに、排気ガ
ス中のカーボン粉末等の固形微粒子及び一酸化炭素等の
有害ガスを分解、吸着させる燃焼排気ガスの冷却及び浄
化方法とした。
According to a second aspect of the present invention, in a path for discharging high-temperature exhaust gas to the outside air, the exhaust gas is circulated in a suitable closed chamber to which a small amount of a dispersant such as a surfactant and a defoaming agent are added. When the water is brought into contact with water and the heat evaporates the water, and the heat of vaporization lowers the temperature of the exhaust gas, the exhaust gas is cooled, and solid fine particles such as carbon powder and carbon monoxide in the exhaust gas are cooled. And a method for cooling and purifying combustion exhaust gas that decomposes and adsorbs harmful gases such as.

【0007】請求項3項の発明は高温の排気ガスを外気
に排出する経路において、適宜の密閉したチャンバー内
に複数個のフィルターを連設し、これらの各フィルター
に排気ガスを通し、これらの各フィルターに界面活性剤
等の分散剤及び消泡剤を少量添加した循環水を注ぎ、当
該フィルターを通過する排気ガスをこれらの水に触れさ
せて、その熱で当該水が気化し、この気化熱によって排
気ガスの温度が下がることにより、当該排気ガスを冷却
させるとともに、排気ガス中のカーボン粉末等の固形微
粒子及び一酸化炭素等の有害ガスを分解し上記水に吸着
させることを特徴とする、燃焼排気ガスの冷却及び浄化
方法とした。
In a third aspect of the present invention, a plurality of filters are connected in an appropriate closed chamber in a path for discharging high-temperature exhaust gas to the outside air, and the exhaust gas is passed through each of these filters. Pour circulating water to which a small amount of a dispersant such as a surfactant and an antifoaming agent are added to each filter.The exhaust gas passing through the filter is brought into contact with the water, and the heat evaporates the water. The heat reduces the temperature of the exhaust gas, thereby cooling the exhaust gas, decomposing solid particulates such as carbon powder in the exhaust gas and harmful gases such as carbon monoxide and adsorbing the water on the water. And a method of cooling and purifying combustion exhaust gas.

【0008】また請求項4項の発明は、高温の排気ガス
を外気に排出する経路において、適宜の密閉したチャン
バー内に複数個のフィルターを連設し、これらの各フィ
ルターに排気ガスを通し、これらの各フィルターに排気
ガスを通す前に界面活性剤等の分散剤及び消泡剤を少量
添加した循環水を排気ガスに接触させて、その熱で当該
水が気化し、この気化熱によって排気ガスの温度が下が
ることにより、当該排気ガスを冷却するとともに、当該
各フィルターにおいて排気ガス中のカーボン粉末等の固
形微粒子及び一酸化炭素等の有害ガスを分解し、上記水
に吸着させ、これらの冷却、分離の工程を繰り返すこと
により排気ガスを冷却、及び浄化する方法とした。
According to a fourth aspect of the present invention, a plurality of filters are connected in an appropriate closed chamber in a path for discharging high-temperature exhaust gas to the outside air, and the exhaust gas is passed through each of these filters. Before passing the exhaust gas through each of these filters, circulating water containing a small amount of a dispersant such as a surfactant and a defoaming agent is brought into contact with the exhaust gas, and the heat evaporates the water. By lowering the temperature of the gas, the exhaust gas is cooled, and at the respective filters, solid particulates such as carbon powder and the like in the exhaust gas and harmful gases such as carbon monoxide are decomposed and adsorbed on the water. A method of cooling and purifying exhaust gas by repeating steps of cooling and separation was adopted.

【0009】また請求項5項の発明は、高温の排気ガス
を外気に排出する経路において、適宜の密閉したチャン
バー内に複数個のフィルターを連設し、少なくとも最前
のフィルターに導入する前に界面活性剤等の分散剤及び
消泡剤を少量添加した水に上記排気ガスを通すか又は接
触させる構成とし、上記各フイルターの下方に上記水の
水面が位置するようにタンクを設け、このタンク内の水
を上記各接触箇所に導くポンプを設け、上記各フィルタ
ーは排気ガスを間に通す複数の板体を略平行に設け、こ
れらの板体の間隙を二層流が生じる巾とした燃焼排気ガ
スの冷却及び浄化装置とした。
According to a fifth aspect of the present invention, a plurality of filters are connected in an appropriate closed chamber in a path for discharging high-temperature exhaust gas to the outside air, and at least an interface is provided before the filter is introduced into the foremost filter. The exhaust gas is passed or brought into contact with water to which a small amount of a dispersant such as an activator and an antifoaming agent has been added, and a tank is provided so that the water surface of the water is located below each of the filters. A pump that guides the water to each of the contact points, each of the filters is provided with a plurality of plates that allow exhaust gas to pass therethrough in a substantially parallel manner, and the gap between these plates has a width that generates a two-layer flow. A gas cooling and purifying device was used.

【0010】また請求項6項の発明は、高温の排気ガス
を外気に排出する経路に設けたフィルターにおいて、排
気ガスを間に通す複数の板体を略平行に設け、これらの
板体の間隙を二層流が生じる巾にしたものである。
According to a sixth aspect of the present invention, there is provided a filter provided in a path for discharging high-temperature exhaust gas to the outside air, wherein a plurality of plates for passing the exhaust gas are provided substantially in parallel, and a gap between these plates is provided. Is the width at which a two-layer flow occurs.

【0011】また請求項7項の発明は、高温の排気ガス
を外気に排出する経路に設けたフィルターにおいて、排
気ガスを間に通す複数の板体を略平行に設け、これらの
板体の間隙を二層流が生じる巾とし、これらの板体は弾
性体からなり、排気ガスの流動方向の前端部を支持し、
後端部を自由端とし、排気ガスの流れの勢いによって各
板体の間隔が変動する構成としたものである。
According to a seventh aspect of the present invention, there is provided a filter provided in a path for discharging high-temperature exhaust gas to the outside air, wherein a plurality of plates for passing the exhaust gas are provided substantially in parallel, and a gap between these plates is provided. Is the width at which a two-layer flow occurs, and these plates are made of an elastic material and support the front end in the flow direction of the exhaust gas,
The rear end is a free end, and the interval between the plates fluctuates according to the flow of exhaust gas.

【0012】上記請求項1項の発明では、この装置を自
動車のエンジンに適用した場合、エンジンからの排気ガ
スの温度は70度乃至150度C(ガスタービンの排気
ガス等は300度C乃至500度Cの場合もある)に達
する。この排気ガスを適宜のチャンバー内で水に接触さ
せることにより、その熱で当該水が気化し、この気化熱
によって排気ガス自体の温度が下がる。一方当該排気ガ
スの中に含まれているガス状の水分は排気ガス自体の温
度の降下により凝集し、液化する。この液化により体積
を減少させ、減圧する。また排気ガス中のカーボン粉末
等の固形微粒子を分解させて水に吸着させ、これにより
固形微粒子を排気ガスから分離させる。またこれに使用
する水は循環式とした。
According to the first aspect of the present invention, when this apparatus is applied to an automobile engine, the temperature of the exhaust gas from the engine is 70 to 150 ° C. (the exhaust gas of the gas turbine is 300 to 500 ° C.). Degree C). By bringing this exhaust gas into contact with water in an appropriate chamber, the water vaporizes due to the heat, and the heat of vaporization lowers the temperature of the exhaust gas itself. On the other hand, the gaseous moisture contained in the exhaust gas agglomerates and liquefies due to a decrease in the temperature of the exhaust gas itself. This liquefaction reduces the volume and reduces the pressure. In addition, solid fine particles such as carbon powder in the exhaust gas are decomposed and adsorbed on water, thereby separating the solid fine particles from the exhaust gas. The water used for this was of a circulation type.

【0013】上記エンジンからの500度Cの排気ガス
中の水分は約360度C以上であるため、ガス体であ
り、1g分子当たり22.4リットル以上の体積を持っ
ているが、これが冷却されて水滴になると18ミリリッ
トルに縮小する。このため計算上は一種の吸引ポンプと
なり、エンジンからの排気ガスの排出を容易にする。こ
の減圧分は22400分の18で約1200分の1にな
る。この様な減圧がエンジンの吸気を促し、エンジンは
完全燃焼に近くなり、必要以上の温度に上昇しないた
め、一酸化炭素や窒素酸化物等の発生が極度に押さえら
れる。またNOxはO2と化合して硝酸となり、水の中
に溶ける。そして次ぎにくる排気ガスのCOをCO2
する酸化剤として働く。また排気ガス中の油分は分散粒
子となり、上記窒素酸化物を吸着する働きがある。
Since the moisture in the exhaust gas at 500 ° C. from the engine is about 360 ° C. or more, it is a gaseous substance and has a volume of 22.4 liters or more per gram molecule. When it becomes water droplets, it is reduced to 18 ml. Therefore, it becomes a kind of suction pump in calculation, and discharge of exhaust gas from the engine is facilitated. This reduced pressure is 18/22400, which is approximately 1/1200. Such decompression promotes the intake of the engine, and the engine approaches complete combustion, and does not rise to a temperature higher than necessary, so that generation of carbon monoxide, nitrogen oxides, and the like is extremely suppressed. NOx combines with O 2 to form nitric acid, which dissolves in water. Then, it functions as an oxidizing agent for converting CO of the next exhaust gas into CO 2 . The oil component in the exhaust gas becomes dispersed particles and has a function of adsorbing the nitrogen oxides.

【0014】上記請求項2項の発明では、上記作用に加
え、排気ガスと接触させる水に界面活性剤等の分散剤及
び消泡剤を少量添加したことにより排気ガス中のカーボ
ン粉末等の固形微粒子を上記分散剤の分散作用によりバ
ラバラにし、より小さなクラスターとし、次ぎにくる排
気ガスの中の微粒子、その他の活性のあるガス体(例え
ば一酸化炭素、窒素酸化物等)、重金属等を素早く吸着
する核になって排気ガスからこれらの微粒子等を分離す
る。
According to the second aspect of the present invention, in addition to the above functions, a small amount of a dispersant such as a surfactant and a defoaming agent are added to water to be brought into contact with the exhaust gas, so that solids such as carbon powder in the exhaust gas are added. The fine particles are separated by the dispersing action of the above dispersing agent to form smaller clusters, and the fine particles, other active gas bodies (eg, carbon monoxide, nitrogen oxides, etc.), heavy metals, etc. in the next exhaust gas can be quickly removed. These fine particles and the like are separated from exhaust gas as nuclei to be adsorbed.

【0015】上記請求項3項の発明では、上記請求項1
項及び2項における作用に加え、複数個のフィルターの
少なくとも最前のフィルターに界面活性剤等の分散剤及
び消泡剤を少量添加した水を注ぎ、排気ガスの水との接
触及び排気ガス中の固形微粒子の分解、水への吸着、分
離をフィルターを通して行うようにしている。またタン
クの水をポンプで注出口に導き、水を循環させている。
According to the third aspect of the present invention, the first aspect of the present invention is provided.
In addition to the functions described in paragraphs 2 and 3, pour water with a small amount of a dispersant such as a surfactant and a defoaming agent added to at least the foremost filter of the plurality of filters. The decomposition of solid particles, adsorption to water, and separation are performed through a filter. The water in the tank is guided to the spout by a pump to circulate the water.

【0016】また上記請求項4項の発明は、上記請求項
3項の発明とほぼ同様な作用をするが、各フィルターを
通過する前の排気ガスに水を接触させて当該排気ガスを
冷却し、接触した水は水蒸気となって各フィルターに付
着し、排気ガスはこれらの水に接して排気ガスの中の微
粒子、その他の活性のあるガス体、重金属等を素早く吸
着して分離する。しかもこれらの排気ガスの冷却と固形
微粒子の分離を繰り返す。
The fourth aspect of the present invention has substantially the same effect as the third aspect of the invention, except that water is brought into contact with the exhaust gas before passing through each filter to cool the exhaust gas. The contacted water becomes water vapor and adheres to each filter, and the exhaust gas comes into contact with the water and quickly adsorbs and separates fine particles, other active gas bodies, heavy metals and the like in the exhaust gas. In addition, the cooling of the exhaust gas and the separation of the solid fine particles are repeated.

【0017】上記請求項5項の発明では、上記請求項3
項及び4項の発明の作用と略同様であるが、各フィルタ
ーにおいて、複数の板体の間隔を極めて小さくし、これ
らの各板体の間を排気ガスを通すことにより、二層流の
働きにより、各板体表面の粘着性の高い固定層の間に流
動層が形成され、上記排気ガスはこの流動層内を移動す
るが、この中の固形微粒子は両側の各固定層に接触して
減速し、落下して下方の水に吸着される。これにより排
気ガス中の固形微粒子が当該排気ガスから分離される。
According to the fifth aspect of the present invention, the third aspect of the present invention is provided.
The operation of the present invention is substantially the same as that of the invention described in the paragraphs 4 and 5, except that in each filter, the interval between the plurality of plate members is made extremely small, and the exhaust gas is passed between these plate members so that the two-layer flow works. Thereby, a fluidized bed is formed between the highly sticky fixed layers on the surface of each plate body, and the exhaust gas moves in the fluidized bed, but the solid fine particles therein contact the respective fixed layers on both sides. It slows down, falls and is absorbed by the water below. Thereby, the solid fine particles in the exhaust gas are separated from the exhaust gas.

【0018】上記請求項6項の発明では、複数の板体の
間隔を極めて小さくし、これらの各板体の間を排気ガス
を通すことにより、二層流の働きにより、各板体表面の
粘着性の高い固定層の間に流動層が形成され、上記排気
ガスはこの流動層内を移動するが、この中の固形微粒子
は両側の各固定層に接触して減速し、落下する。これに
より排気ガス中の固形微粒子が当該排気ガスから分離さ
れる。また請求項7項の発明は、この請求項6項の発明
と同じ作用をなすが、各板体が弾性体で構成され、かつ
前端部のみが支持されているため、排気カズの流れの勢
いが強ければ各板体の間隔は拡がり、勢いが弱ければ板
体の間隔が小さくなる。
[0018] In the invention according to claim 6, the interval between the plurality of plate members is made extremely small, and exhaust gas is passed between these plate members, whereby the surface of each plate member is formed by the action of the two-layer flow. A fluidized bed is formed between the fixed beds having high adhesiveness, and the exhaust gas moves in the fluidized bed. The solid fine particles in the bed contact the fixed beds on both sides, decelerate, and fall. Thereby, the solid fine particles in the exhaust gas are separated from the exhaust gas. The invention according to claim 7 has the same effect as the invention according to claim 6, but since each plate is formed of an elastic body and only the front end is supported, the flow of exhaust gas is increased. When the distance is strong, the distance between the plates increases, and when the momentum is low, the distance between the plates decreases.

【0019】[0019]

【発明の実施の形態】以下この発明の実施の形態例を図
に基づいて説明する。図1及び図2はこの発明の第1の
実施の形態例の概略構成を示すもので、エンジンからの
排気ガスはまず放熱器1に送られる構成となっている。
そしてこの放熱器1の後にフィルターボックス2を通過
し、さらにサイクロン3を経て排気される。上記フィル
ターボックス2内にはさらに二つの区画2aに分かれ、
これらの各区画2a内に夫々対のフィルター4、4が夫
々設けられている。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below with reference to the drawings. FIGS. 1 and 2 show a schematic configuration of a first embodiment of the present invention, in which exhaust gas from an engine is first sent to a radiator 1.
After the radiator 1, the gas passes through the filter box 2 and is further exhausted through the cyclone 3. The filter box 2 is further divided into two sections 2a,
A pair of filters 4, 4 is provided in each of these sections 2a.

【0020】これらの各フィルター4は図2に示すごと
く、枠体4aの相対する辺に繊維等からなるフィラメン
ト4bを巻き付け、各繊維相互の間に小さな間隔を設け
たもので、各区画2a内の対のフィルター4は「ハ」の
字型に設けてこれらの外側にセラミック、金属、プラス
チック等の小片5を多数充填している。またこのフィル
ターボックス2の下方にはタンク6が設けられ、上記フ
ィルターボックス2及び上記サイクロン3と連絡してい
る。このタンク6内には、界面活性剤等の分散及び乳化
作用のあるものを0.01〜3%と消泡剤を極少量添加
した水が入っている。
As shown in FIG. 2, each of these filters 4 is formed by winding filaments 4b made of fibers or the like around opposite sides of a frame 4a and providing a small space between the fibers. The filter 4 is provided in the shape of a letter "C" and the outside thereof is filled with a large number of small pieces 5 of ceramic, metal, plastic or the like. A tank 6 is provided below the filter box 2 and communicates with the filter box 2 and the cyclone 3. The tank 6 contains water containing 0.01 to 3% of a substance having a dispersing and emulsifying action such as a surfactant and a very small amount of an antifoaming agent.

【0021】またこのタンク6の上記水をポンプ7を介
して噴霧する噴出口8を上記フィルターボックス2の一
方の区画2a、即ち放熱器1に続く区画2aのフィルタ
ー4、4の上に設けている。また上記タンク6に予備タ
ンク9を連結している。さらに上記サイクロン3から排
気パイプ10が導出されている。
A jet port 8 for spraying the water of the tank 6 through a pump 7 is provided on one of the sections 2a of the filter box 2, that is, on the filters 4 and 4 of the section 2a following the radiator 1. I have. A spare tank 9 is connected to the tank 6. Further, an exhaust pipe 10 is led out of the cyclone 3.

【0022】この場合、エンジンから排気した排気ガス
は約70〜160度Cに達している。しかしこの排気ガ
スを上記放熱器1に通すと、60度〜100度Cに下が
る。そしてこれを上記フィルターボックス2内に導く。
これと同時に上記ポンプ7を作動させてタンク6内の水
を一方の区画2aのフィルター4の上の噴出口8から噴
霧する。これにより水は徐々にセラミック等の小片5に
当たってフィルター4の下方に落下していくが、この間
にこれらの小片5の間及びフィルター4を排気ガスが通
り、これらの水に接触する。従ってこれらの小片5は当
該排気ガスが水に接触する面積を大きくするために設け
られたものである。
In this case, the exhaust gas discharged from the engine has reached about 70 to 160 ° C. However, when this exhaust gas is passed through the radiator 1, the temperature is lowered to 60 to 100 degrees C. This is guided into the filter box 2.
At the same time, the pump 7 is operated to spray water in the tank 6 from the jet port 8 above the filter 4 in one section 2a. As a result, the water gradually hits the small pieces 5 such as ceramics and falls below the filter 4. During this time, the exhaust gas passes between the small pieces 5 and the filter 4, and comes into contact with the water. Therefore, these small pieces 5 are provided to increase the area where the exhaust gas contacts water.

【0023】そこで排気ガスに触れた水は気化し、当該
気化熱によって排気ガスの温度が下がる。また排気の中
に含まれる水分(蒸気)は凝集し、液化する。そしてこ
の水はフィルターボックス2内の下部の孔を通ってタン
ク6内に入る。また上記排気ガスが水に接触すると、排
気ガス内のカーボン粉末等の固形微粒子は当該水内の分
散剤の分散作用によりバラバラとなり、より小さなクラ
スターとなる。そして次ぎにくる排気ガスの中の微粒
子、その他の活性のあるガス体(例えば一酸化炭素、窒
素酸化物等)、重金属等を素早く吸着する。そこでこれ
らの微粒子を含んだ水は上述の如くタンク6に入ってい
く。これにより排気ガスから微粒子等が分離される。
Then, the water that has come into contact with the exhaust gas is vaporized, and the heat of vaporization lowers the temperature of the exhaust gas. In addition, the moisture (vapor) contained in the exhaust gas aggregates and liquefies. Then, the water enters the tank 6 through the lower hole in the filter box 2. Further, when the exhaust gas comes into contact with water, solid fine particles such as carbon powder in the exhaust gas fall apart due to the dispersing action of the dispersant in the water, forming smaller clusters. Then, it quickly adsorbs fine particles, other active gas bodies (for example, carbon monoxide, nitrogen oxides, etc.), heavy metals and the like in the next exhaust gas. Then, the water containing these fine particles enters the tank 6 as described above. Thereby, fine particles and the like are separated from the exhaust gas.

【0024】この様にして二つの区画2aをへてサイク
ロン3に達し、当該サイクロン3の排気パイプ10から
外部に排出される。この状態の排気ガスは外気温とあま
り変わらず、夏の暑い時(34度C)でも38〜40度
C以下であり、冬の寒いとき(5度C)では10数度に
なる。しかも上述の如く排気ガスが冷却されて、排気ガ
ス中のガス状の水分が水滴になると体積が縮小し、その
分減圧されてエンジンからの排気ガスの排出を容易にす
る。そこでこの様な減圧がエンジンの吸気を促し、エン
ジンは完全燃焼に近くなり、必要以上の温度に上昇しな
いため、一酸化炭素や窒素酸化物等の発生が極度に押さ
えられる。
In this way, the gas reaches the cyclone 3 through the two sections 2a, and is discharged from the exhaust pipe 10 of the cyclone 3 to the outside. The exhaust gas in this state is not much different from the outside air temperature, is 38 to 40 ° C. or less even in a hot summer (34 ° C.), and becomes several tens of degrees in a cold winter (5 ° C.). In addition, as described above, the exhaust gas is cooled, and when the gaseous moisture in the exhaust gas becomes water droplets, the volume of the exhaust gas is reduced, and the pressure is reduced by that amount, thereby facilitating discharge of the exhaust gas from the engine. Thus, such a pressure reduction promotes the intake of the engine, and the engine approaches the complete combustion, and does not rise to a temperature higher than necessary. Therefore, the generation of carbon monoxide, nitrogen oxide, and the like is extremely suppressed.

【0025】図3乃至図5はこの発明の第2の実施の形
態例を示し、この例では第1密閉室11、第2密閉室1
2、第3密閉室13、第4密閉室14を連設し、これら
の各密閉室に排気ガスを通す。第1密閉室11は隔壁1
5により二つに区切られており、一方は排気ガスを下方
のタンク16の水中内に導入する導入パイプ17が設け
られた通路18となり、他方にはセラミックの球、筒、
繊維、金属板等の小片が充填されたカラム室11aとな
っている。
FIGS. 3 to 5 show a second embodiment of the present invention. In this embodiment, a first closed chamber 11 and a second closed chamber 1 are shown.
2, a third closed chamber 13 and a fourth closed chamber 14 are connected in series, and exhaust gas is passed through each of these closed chambers. The first closed chamber 11 is a partition 1
5, one is a passage 18 provided with an introduction pipe 17 for introducing exhaust gas into the water of the lower tank 16, and the other is a ceramic ball, cylinder,
The column chamber 11a is filled with small pieces such as fibers and metal plates.

【0026】また第2密閉室12以下は上記の第1密閉
室11と同様に邪魔板15により二つに区切られ、一方
は排気ガスの通路18、他方はセラミックの球、筒、繊
維、金属板等の小片が充填されたカラム室12a、13
a、14aとなっている。そしてこれらの第1密閉室1
1乃至第4密閉室14の下方には各密閉室と連絡した上
記タンク16を構成するタンク小室16a16b、16
c、16dとなり、これらのタンク小室16a、16
b、16c、16dは相互に連絡されている。またこれ
らの各密閉室11、12、13、14の各通路18及び
タンク16には空冷又は水冷の冷却パイプ19が通って
いる。
Similarly to the above-mentioned first closed chamber 11, the second closed chamber 12 and below are divided into two by a baffle plate 15, one of which is an exhaust gas passage 18, and the other is a ceramic sphere, cylinder, fiber, metal or the like. Column chambers 12a and 13 filled with small pieces such as plates
a and 14a. And these first closed chambers 1
Below the first to fourth sealed chambers 14, tank small chambers 16a16b, 16 constituting the tank 16 connected to the respective sealed chambers.
c, 16d, and these tank chambers 16a, 16
b, 16c, 16d are interconnected. An air-cooled or water-cooled cooling pipe 19 passes through each of the passages 18 and the tank 16 of each of the closed chambers 11, 12, 13, and 14.

【0027】そして第4密閉室14の後方に排気通路2
0を設けて排気ガスを外部に導出している。また上記タ
ンク16には補助タンク21を有する液面調節器22を
設けている。さらに上記第2密閉室12及び第3密閉室
13の各カラム室12a、13aの上方には水注出口2
3が夫々設けられ、上記タンク16からこれらの各水注
出口23にポンプ24により水を供給する。
The exhaust passage 2 is located behind the fourth closed chamber 14.
0 is provided to exhaust gas to the outside. The tank 16 is provided with a liquid level controller 22 having an auxiliary tank 21. Further, a water injection port 2 is provided above each of the column chambers 12a and 13a of the second closed chamber 12 and the third closed chamber 13.
3 are provided, and water is supplied from the tank 16 to the respective water outlets 23 by a pump 24.

【0028】この実施の形態例の場合上記タンク16に
は予め0.005乃至3%の界面活性剤を添加した水を
入れておく。そしてエンジンからの排気ガスは上記導入
パイプ17から第1密閉室11のタンク16の水中に排
気される。当該排気ガスは上述の如く高温高圧で排気さ
れるので当該液の中で冷却されて可溶分は溶解する。そ
の際界面活性剤含有の気泡がアワとなってカラム室11
aで液化し、当該カラム室11aの下方のタンク16a
に落ちる。これと同時にタンク16aの水に入った不溶
ガスはアワとなって次ぎの第2密閉室12の通路18を
通ってカラム室12aに送られる。この時アワだけでな
く、蒸気も多量に発生するが、水注出口23から注出し
た水がカラム室12a内に付着し、蒸気はこれらの水と
接触して冷却され、温度は急激に低下する。しかも当該
水中で上述と同様に固形微粒子や有害ガスは水に吸着さ
れて分離される。このようにして第3密閉室13におい
ても上記第2密閉室12と同様に排気ガスは冷却され、
かつ固定微粒子や有害ガスが分離されていく。
In the case of this embodiment, the tank 16 is previously filled with water to which 0.005 to 3% of a surfactant has been added. The exhaust gas from the engine is exhausted from the introduction pipe 17 into the water in the tank 16 of the first closed chamber 11. Since the exhaust gas is exhausted at a high temperature and a high pressure as described above, the exhaust gas is cooled in the liquid to dissolve the soluble matter. At this time, bubbles containing the surfactant become millet, and the column chamber 11
a, and the tank 16a below the column chamber 11a
fall into. At the same time, the insoluble gas that has entered the water in the tank 16a becomes millet and is sent to the column chamber 12a through the passage 18 in the next second sealed chamber 12. At this time, not only millet but also a large amount of steam is generated, but the water discharged from the water injection port 23 adheres to the inside of the column chamber 12a, and the steam comes into contact with the water and is cooled, so that the temperature drops rapidly. I do. In addition, solid fine particles and harmful gases are adsorbed and separated in the water in the same manner as described above. In this manner, the exhaust gas is also cooled in the third closed chamber 13 as in the second closed chamber 12, and
In addition, fixed fine particles and harmful gases are separated.

【0029】各カラム室11、12、13、14での排
気ガスの温度は図4の通りであり、またその時の一酸化
炭素や窒素酸化物の含有量は図5の通りである。この様
にして排気ガスの急激な温度低下により排気ガスの体積
が急に減少して減圧となり、排気ガスをエンジンから吸
引する力となり、エンジン内での燃焼効率は非常によく
なる。それ故エンジンの燃焼も高温化が進まず、NOx
の発生量が減少する。また排気ガス中の微粒子が水中に
分散し、これが後続の排気ガス中の一酸化炭素やNOx
をとらえ、排気ガスから分離させる。従って排気通路2
0から出てくる排気ガスの温度は外気温との差があまり
なく、クリーンな状態で出てくる。
The temperature of the exhaust gas in each of the column chambers 11, 12, 13, and 14 is as shown in FIG. 4, and the contents of carbon monoxide and nitrogen oxide at that time are as shown in FIG. In this way, the volume of the exhaust gas suddenly decreases due to the rapid temperature decrease of the exhaust gas, and the pressure of the exhaust gas is reduced. This becomes a force for sucking the exhaust gas from the engine, and the combustion efficiency in the engine becomes very good. As a result, engine combustion does not increase in temperature, and NOx
The amount of generation decreases. In addition, fine particles in the exhaust gas are dispersed in the water, and this causes the carbon monoxide and NOx in the subsequent exhaust gas to be dispersed.
And separate it from the exhaust gas. Therefore, the exhaust passage 2
The temperature of the exhaust gas coming out from 0 does not greatly differ from the outside air temperature and comes out in a clean state.

【0030】図6乃至図9はこの発明の第3の実施の形
態例を示す。この第3の実施の形態例は上記の第1及び
第2の実施の形態例とほぼ同様であるが、フィルターの
構成が異なる。即ち、この実施の形態例でもエンジンか
らの排気ガスは箱型本体25の一端の導入パイプ26か
らガイド板27にガイドされて箱型本体25の下部に形
成されたタンク28内に入る。このタンク28内には予
め0.005乃至3%の界面活性剤を添加した水を入れ
ておく。またタンク28は適宜の孔により各フィルター
30と連絡している。そしてこのタンク28の液内に入
った排気ガスは急激に冷却され、アワとなって通路29
に抜け出る。そして箱型本体25内に間隔を開けて設け
た複数個のフィルター30を順次通って他方の排気パイ
プ31から外部に排出される。
FIGS. 6 to 9 show a third embodiment of the present invention. The third embodiment is substantially the same as the first and second embodiments, except for the configuration of the filter. That is, also in this embodiment, the exhaust gas from the engine is guided by the guide plate 27 from the introduction pipe 26 at one end of the box-shaped main body 25 and enters the tank 28 formed at the lower part of the box-shaped main body 25. The tank 28 is filled with water to which 0.005 to 3% of a surfactant is added in advance. The tank 28 communicates with each filter 30 through an appropriate hole. The exhaust gas that has entered the liquid in the tank 28 is rapidly cooled, becomes a millet, and passes through the passage 29.
Get out. Then, the air is discharged to the outside from the other exhaust pipe 31 through a plurality of filters 30 provided in the box-shaped main body 25 at intervals.

【0031】これらのフィルター30の構成は図7に示
すごとく、排気ガスの流れと平行な多数の薄板30aを
間隔を開けて並べ、これらの各隣接する薄板30aの間
隔を極めて小さくし、二層流の生じる間隔とする。これ
らの薄板30aの間に排気ガスを流すと、図8に示すご
とく、排気ガスの流れの中に各薄板30aの表面に沿っ
て固定層32が生じ、これらの間に流動層33ができ
る。そこでこの固定層32は粘着度が高く、流動層33
内の固形微粒子はこれらの固定層32に当たって減速さ
れる。
As shown in FIG. 7, the structure of these filters 30 is such that a large number of thin plates 30a parallel to the flow of exhaust gas are arranged at intervals, the interval between these adjacent thin plates 30a is made extremely small, and two layers are formed. The interval at which the flow occurs. When the exhaust gas flows between the thin plates 30a, as shown in FIG. 8, a fixed layer 32 is formed along the surface of each thin plate 30a in the flow of the exhaust gas, and a fluidized layer 33 is formed therebetween. Therefore, the fixed layer 32 has a high adhesiveness and the fluidized bed 33
The solid fine particles in the interior strike these fixed layers 32 and are decelerated.

【0032】これにより各フィルター30を排気ガスが
通ると、排気ガス中の固形微粒子の一部は上記固定層3
2に接触して減速し、図9に示すごとく下方に落下して
いく。そして順次各フィルター30を通過するに従って
排気ガス中の固形微粒子は液のタンク28内に落下して
行き、排気ガスから分離され、上記排気パイプ31から
出てきた排気ガスは上記の実施の形態例と同様に温度が
下がり、かつクリーンな排気ガスとなっている。
As a result, when the exhaust gas passes through each filter 30, some of the solid fine particles in the exhaust gas
2, the vehicle decelerates and falls downward as shown in FIG. Then, the solid particulates in the exhaust gas fall into the liquid tank 28 as they pass through the filters 30 sequentially, are separated from the exhaust gas, and the exhaust gas coming out of the exhaust pipe 31 is the above-described embodiment. Similarly, the temperature is lowered and the exhaust gas is clean.

【0033】図10乃至図11はこの発明の第4の実施
の形態例を示す。この第4の実施の形態例は上記の第3
の実施の形態例とほぼ同様であるが、エンジンからの排
気ガスは箱型本体34の一端の導入パイプ35から第1
密閉室36、第2密閉室37、第3密閉室38及び第4
密閉室39に至り、邪魔板室40を通って排気パイプ4
1から外部に排気される。またこれらの各密閉室の下方
には予め0.005乃至3%の界面活性剤を添加した水
を入れたタンク42が設けられ、このタンク42は各密
閉室36乃至39と適宜の孔で連絡されている。また上
記各密閉室36乃至39は水が噴霧されるノズル43a
を有する噴霧区画43とフィルター区画44とから構成
されている。これらの各フィルター区画44は図11に
示すごとく、多数の湾曲した薄板状のフィルター板44
aを平行して並べ、各フィルター板44aの間隔を狭く
し、上記第3の実施の形態例と同様に二層流現象が生じ
る間隔としている。そして各密閉室の噴霧区画43に入
った排気ガスは各ノズル42により噴霧された水と接触
して冷却され、さらに各フィルター区画44で排気ガス
内のカーボン粉末等の固形微粒子や有害ガスを分離する
構成となっている。
FIGS. 10 and 11 show a fourth embodiment of the present invention. The fourth embodiment is similar to the third embodiment.
In this embodiment, the exhaust gas from the engine is supplied from the introduction pipe 35 at one end of the box-shaped main body 34 to the first position.
The closed chamber 36, the second closed chamber 37, the third closed chamber 38, and the fourth
The exhaust pipe 4 reaches the closed chamber 39 and passes through the baffle chamber 40.
Exhaust from 1 to the outside. Below each of these closed chambers, there is provided a tank 42 containing water to which 0.005 to 3% of a surfactant has been added in advance, and this tank 42 is connected to each of the closed chambers 36 to 39 through appropriate holes. Have been. Each of the closed chambers 36 to 39 is provided with a nozzle 43a to which water is sprayed.
, And a filter section 44. As shown in FIG. 11, each of these filter sections 44 has a large number of curved thin plate-like filter plates 44.
a are arranged in parallel, and the interval between the filter plates 44a is narrowed so that the two-layer flow phenomenon occurs as in the case of the third embodiment. The exhaust gas entering the spray section 43 of each closed chamber is cooled by contacting the water sprayed by each nozzle 42, and further separates solid particulates such as carbon powder and harmful gas in the exhaust gas by each filter section 44. Configuration.

【0034】これを具体的に説明すると、上記実施の形
態例と同様に排気ガスと接触した水は気化し、この気化
熱で排気ガスの温度が下がり、一方排気ガス中の水分
(蒸気)は凝集し、液化する。そしてこの液化した水は
下方のタンク42内に落下して入る。また上記排気ガス
が水に接触すると、排気ガス内のカーボン粉末等の固形
微粒子や有害ガスは当該水内の分散剤の分散作用により
バラバラとなり、より小さなクラスターとなる。そして
次ぎにくる排気ガスの中の微粒子、その他の活性のある
ガス体(例えば一酸化炭素、窒素酸化物等)、重金属等
を素早く吸着する。またこの排気ガスはフィルター区画
44に入り、各フィルター板44aの間を通り、二層流
現象によって固形微粒子は失速し、下方のタンク42に
落下していき、排気ガスから分離される。
More specifically, the water in contact with the exhaust gas is vaporized as in the above embodiment, and the heat of vaporization lowers the temperature of the exhaust gas, while the water (vapor) in the exhaust gas is reduced. Agglomerates and liquefies. Then, the liquefied water falls into the lower tank 42 and enters. Further, when the exhaust gas comes into contact with water, solid fine particles such as carbon powder and harmful gas in the exhaust gas are separated by the dispersing action of the dispersant in the water and become smaller clusters. Then, it quickly adsorbs fine particles, other active gas bodies (for example, carbon monoxide, nitrogen oxides, etc.), heavy metals and the like in the next exhaust gas. Further, the exhaust gas enters the filter section 44, passes between the filter plates 44a, and the solid fine particles are stalled by the two-layer flow phenomenon, fall into the lower tank 42, and are separated from the exhaust gas.

【0035】この様に排気ガスは第1密閉室36から順
に第4密閉室39まで上記工程を繰返し、次第に冷却さ
れ、外気温と略同じ温度となり、また窒素酸化物等の固
形微粒子や有害ガスのほとんどが分離、除去されて邪魔
板室40を経て排気パイプ41から外部に排気される。
As described above, the exhaust gas is sequentially cooled from the first closed chamber 36 to the fourth closed chamber 39 and gradually cooled to a temperature substantially equal to the outside air temperature. Are separated and removed, and are exhausted to the outside from the exhaust pipe 41 through the baffle plate chamber 40.

【0036】次ぎに図12及び図13は上記第3及び第
4の実施の形態におけるフィルター30及びフィルター
区画44の二層流を生じさせるフィルターの他の実施の
形態例を示す。図12のフィルター45は排気ガスの流
れる方向に略平行な二つ折りの弾性板体45aを複数並
べ、各フィルター45は支持軸46にその折り返し端を
軸支され、排気ガスの流れが速いと、各フィルター45
の二つ折りの両側の弾性板体45aが相互に狭まり、従
って隣接するフィルター45の間の間隔は拡がる。また
流れが遅いと、各フィルター45の二つ折りの両側の弾
性板体45aが相互に離れ、従って隣接するフィルター
45の間の間隔は拡がらないようになっている。また図
13に示すごとく、各フィルター45の弾性板体45a
に多数の突起又は小孔45bを設けても良い。これは上
記第3及び第4の実施の形態におけるフィルター30及
びフィルター区画44の二層流を生じさせるフィルター
板の側面に多数の突起又は小孔を設け、固形微粒子の分
離をより確実にする構成としたものである。
Next, FIGS. 12 and 13 show another embodiment of the filter for generating a two-layer flow of the filter 30 and the filter section 44 in the third and fourth embodiments. The filter 45 in FIG. 12 includes a plurality of bi-folded elastic plates 45a that are substantially parallel to the direction in which the exhaust gas flows, and each filter 45 has its folded end supported by a support shaft 46, and when the flow of the exhaust gas is fast, Each filter 45
The elastic plates 45a on both sides of the two folds become narrower with each other, so that the interval between the adjacent filters 45 increases. When the flow is slow, the elastic plates 45a on both sides of the two folds of each filter 45 are separated from each other, so that the interval between the adjacent filters 45 is not widened. Further, as shown in FIG. 13, the elastic plate 45a of each filter 45 is provided.
May be provided with a number of projections or small holes 45b. This is a configuration in which a large number of projections or small holes are provided on the side surface of the filter plate that generates a two-layer flow of the filter 30 and the filter section 44 in the third and fourth embodiments to more reliably separate solid fine particles. It is what it was.

【0037】また上記実施例では各フィルターの下方に
設けたタンクの水をポンプにより汲み上げて各フィルタ
ーの上方等から噴射させているが、これらのポンプはモ
ータ等の動力を用いても良く、また図14に示すごとく
排気ガスの通路47にプロペラ48を回転自在に設け、
排気ガスの圧力によりプロペラ48を回し、この回転を
ポンプ49に伝えてポンプ49を回転させても良い。さ
らに排気ガスに最初に水を接触させる際、図15に示す
ごとく排気ガスの通路50にオリフィス弁51を設け、
このオリフィス弁51箇所にタンクからの水のパイプ5
2の先端開口部を設けて、上記オリフィス弁51により
水を通路50内に噴霧させることもできる。
In the above embodiment, the water in the tank provided below each filter is pumped up by a pump and jetted from above each filter. However, these pumps may use the power of a motor or the like. As shown in FIG. 14, a propeller 48 is rotatably provided in an exhaust gas passage 47,
The propeller 48 may be rotated by the pressure of the exhaust gas, and the rotation may be transmitted to the pump 49 to rotate the pump 49. Further, when water is first brought into contact with the exhaust gas, an orifice valve 51 is provided in the exhaust gas passage 50 as shown in FIG.
A water pipe 5 from the tank is provided at the 51 orifice valve.
By providing two tip openings, water can be sprayed into the passage 50 by the orifice valve 51.

【0038】また上記各実施の形態例では排気ガスを接
触させる水に0.005乃至3%の界面活性剤やごく少
量の消泡剤を添加しているが、これらのものは発明の必
須要件ではない。これらのものを添加しなくとも排気ガ
スに水を接触させるとNOxの一部はO2と化合して亜
硝酸又は硝酸となり、水の中に溶け、次ぎにくる排気ガ
スのCOをCO2にする酸化剤として働く。また排気ガ
ス中の油分は分散粒子となり、上記窒素酸化物を吸着す
る働きがある。
In each of the above embodiments, 0.005 to 3% of a surfactant and a very small amount of an antifoaming agent are added to water with which exhaust gas is brought into contact. is not. If water is brought into contact with the exhaust gas without adding any of these, some of the NOx will combine with O 2 to become nitrous acid or nitric acid, dissolve in the water, and turn the next exhaust gas CO into CO 2 . Works as an oxidizing agent. The oil component in the exhaust gas becomes dispersed particles and has a function of adsorbing the nitrogen oxides.

【0039】この発明は上記実施例では自動車のエンジ
ンの排気ガスにつき説明したが、この発明の高圧の燃焼
排気ガスにはディーゼルエンジン、ガソリンエンジン、
2サイクルエンジンの排気ガス、ヘリコブター等の航空
機の排気ガス、船舶のエンジンの排気ガス、ガスタービ
ンの排気ガス、発電機用エンジンの排気ガス、工場内の
ボイラー等の燃焼排気ガス、レストランや一般家庭の厨
房の排気ガス等が含まれる。従ってこの発明はこれらの
排気ガスに適用できるものである。
Although the present invention has been described with reference to the exhaust gas of an automobile engine in the above embodiment, the high-pressure combustion exhaust gas of the present invention may be a diesel engine, a gasoline engine, or the like.
Exhaust gas from a two-cycle engine, aircraft exhaust gas such as a helicopter, ship engine exhaust gas, gas turbine exhaust gas, generator engine exhaust gas, combustion exhaust gas from boilers in factories, restaurants and households Kitchen exhaust gas. Therefore, the present invention is applicable to these exhaust gases.

【0040】[0040]

【発明の効果】請求項1項の発明では、高温の燃焼排気
ガスを適宜のチャンバー内で水に接触させることによ
り、その熱で当該水が気化し、この気化熱によって排気
ガス自体の温度が下がる。この原理により排気ガスを外
気温に近い温度まで冷却処理することができる。従って
従来これらの高温の燃焼排気ガスをそのまま外気に排出
させているため、地球の温暖化が進んでいるが、この発
明の処理によりこれを阻止することができる。しかもま
たこれらの排気ガスの冷却により、排気口からの遠赤外
線分の検出が難しくなり、標的等から守ることもでき
る。
According to the first aspect of the present invention, by contacting hot combustion exhaust gas with water in an appropriate chamber, the heat vaporizes the water, and the heat of vaporization lowers the temperature of the exhaust gas itself. Go down. By this principle, the exhaust gas can be cooled to a temperature close to the outside air temperature. Therefore, conventionally, these high-temperature combustion exhaust gases are directly discharged to the outside air, so that global warming is progressing. However, this can be prevented by the treatment of the present invention. Moreover, the cooling of these exhaust gases makes it difficult to detect far-infrared rays from the exhaust port, and can protect them from targets and the like.

【0041】また上述の如く水に接触させることによ
り、排気ガス中のカーボン粉末等の固形微粒子や有害ガ
スを分解させて当該水に吸着させ、これにより固形微粒
子や有害ガスを排気ガスから分離させることができる。
また上述の如く水に接触させることにより排気ガス中の
ガス状の水分が、排気ガス自体の温度の降下により凝集
し、液化する。この液化により体積を減少させ、減圧す
る。この様な減圧が燃焼の吸気を促し、燃焼は完全燃焼
に近くなり、必要以上の温度に上昇しないため、一酸化
炭素や窒素酸化物等の発生が極度に押さえられる。従っ
て排気ガスをクリーンな状態にして外気に放出すること
ができる。
Further, by contacting with water as described above, solid fine particles such as carbon powder and harmful gas in the exhaust gas are decomposed and adsorbed on the water, thereby separating the solid fine particles and the harmful gas from the exhaust gas. be able to.
Further, by contact with water as described above, the gaseous moisture in the exhaust gas aggregates and liquefies due to a decrease in the temperature of the exhaust gas itself. This liquefaction reduces the volume and reduces the pressure. Such reduced pressure promotes the intake of the combustion, and the combustion approaches the complete combustion, and does not rise to a temperature higher than necessary. Therefore, the generation of carbon monoxide, nitrogen oxide, and the like is extremely suppressed. Therefore, the exhaust gas can be released to the outside air in a clean state.

【0042】請求項2項の発明では、上記請求項1項の
効果に加え、排気ガスと接触させる水に界面活性剤等の
分散剤及び消泡剤を少量添加することにより排気ガス中
のカーボン粉末等の固形微粒子や有害ガスの吸着、分離
をより確実なものにできる。
According to the second aspect of the present invention, in addition to the effects of the first aspect, a small amount of a dispersant such as a surfactant and a defoaming agent are added to water to be brought into contact with the exhaust gas, thereby reducing carbon in the exhaust gas. Adsorption and separation of solid fine particles such as powders and harmful gases can be made more reliable.

【0043】請求項3項の発明では、上記請求項1項及
び2項における効果に加え、複数個のフィルターの少な
くとも最前のフィルターに界面活性剤等の分散剤及び消
泡剤を少量添加した水を注ぐため、フィルターに水が付
着し、排気ガスの水との接触面積を増やし、排気ガスの
冷却を確実なものにするとともに、排気ガス中の固形微
粒子や有害ガスの分解、水への吸着、分離をフィルター
を通して確実なものにしている。また上記請求項4項の
発明は上記請求項3項の発明とほぼ同様な効果を有する
が、さらに各フィルターを通過する前の排気ガスに水を
接触させて当該排気ガスを冷却し、接触した水は水蒸気
となって各フィルターに付着し、排気ガスはこれらの水
に接して排気ガスの中の微粒子、その他の活性のあるガ
ス体、重金属等を素早く吸着する。そしてこれらの工程
を数回繰り返すことにより、徐々に温度を下げかつ固形
微粒子等を分離していく。従って外気に排気される時は
外気温とほぼ同じ温度となり、かつカーボン等の固形微
粒子はほとんど無くなる。
According to a third aspect of the present invention, in addition to the effects of the first and second aspects, a water containing a small amount of a dispersant such as a surfactant and an antifoaming agent added to at least the foremost filter of the plurality of filters. Water is attached to the filter to increase the contact area of the exhaust gas with water, ensuring the cooling of the exhaust gas, decomposing solid particulates and harmful gases in the exhaust gas, and adsorbing to water , Ensuring separation through filters. The fourth aspect of the invention has substantially the same effect as the third aspect of the invention, but further cools the exhaust gas by contacting water with the exhaust gas before passing through each filter, and contacts the exhaust gas. Water becomes water vapor and adheres to each filter, and the exhaust gas comes into contact with the water and quickly adsorbs fine particles, other active gas bodies, heavy metals, and the like in the exhaust gas. By repeating these steps several times, the temperature is gradually lowered and solid fine particles and the like are separated. Therefore, when the air is exhausted to the outside air, the temperature becomes almost the same as the outside air temperature, and solid fine particles such as carbon hardly exist.

【0044】上記請求項5項の発明では、上記請求項3
項及び4項の発明の効果に加え、各フィルターの構成が
多数枚の薄板を並べただけの極めて簡単な構造であり、
目づまりもほとんどなく、固形微粒子を確実に分離する
ことができる。
According to the fifth aspect of the present invention, the third aspect of the present invention is provided.
In addition to the effects of the inventions of the items and 4, the configuration of each filter is a very simple structure in which a number of thin plates are arranged,
There is almost no clogging, and solid fine particles can be reliably separated.

【0045】さらに上記請求項6項及び請求項7項の発
明においては、各フィルターの構成が多数枚の薄板を並
べただけの極めて簡単な構造であり、目づまりもほとん
どなく、固形微粒子を確実に分離することができる。ま
た請求項7項の発明は、排気ガスの流れの勢いに応じて
各板体の間隔が変化し、排気ガスの流れを当該箇所で止
めることなく、スムーズに通過させることができ、かつ
固形微粒子を排気ガスからより確実に分離することがで
きる。
Further, according to the inventions of claims 6 and 7, each filter has a very simple structure in which a large number of thin plates are arranged, and there is almost no clogging and solid fine particles can be reliably obtained. Can be separated. Further, according to the invention of claim 7, the interval between the respective plates changes in accordance with the momentum of the flow of the exhaust gas, so that the flow of the exhaust gas can be smoothly passed without stopping at the position, and Can be more reliably separated from the exhaust gas.

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

【図1】この発明の第1の実施の形態例における概略構
成図である。
FIG. 1 is a schematic configuration diagram according to a first embodiment of the present invention.

【図2】この発明の第1の実施の形態例におけるフィル
ターを示す構成図である。
FIG. 2 is a configuration diagram showing a filter according to the first embodiment of the present invention.

【図3】この発明の第2の実施の形態例における概略構
成図である。
FIG. 3 is a schematic configuration diagram according to a second embodiment of the present invention.

【図4】この発明の第2の実施の形態例における各カラ
ム室での排気ガスの温度を示すグラフ図である。
FIG. 4 is a graph showing the temperature of exhaust gas in each column chamber in a second embodiment of the present invention.

【図5】この発明の第2の実施の形態例における各カラ
ム室での排気ガスに含有する窒素酸化物等の含有量を示
すグラフ図である。
FIG. 5 is a graph showing the content of nitrogen oxides and the like contained in exhaust gas in each column chamber in the second embodiment of the present invention.

【図6】この発明の第3の実施の形態例における概略構
成図である。
FIG. 6 is a schematic configuration diagram according to a third embodiment of the present invention.

【図7】この発明の第3の実施の形態例におけるフィル
ターの説明斜視図である。
FIG. 7 is an explanatory perspective view of a filter according to a third embodiment of the present invention.

【図8】この発明の第3の実施の形態例におけるフィル
ターの原理説明図である。
FIG. 8 is a diagram illustrating the principle of a filter according to a third embodiment of the present invention.

【図9】この発明の第3の実施の形態例における排気ガ
スの流れを示す説明概略図である。
FIG. 9 is an explanatory schematic diagram showing a flow of exhaust gas in a third embodiment of the present invention.

【図10】この発明の第4の実施の形態例における概略
構成図である。
FIG. 10 is a schematic configuration diagram in a fourth embodiment of the present invention.

【図11】この発明の第4の実施の形態例における第1
密閉室の概略構成断面図である。
FIG. 11 shows a first embodiment of the fourth embodiment of the present invention.
It is a schematic structure sectional view of a closed room.

【図12】この発明の第3及び第4の実施の形態例にお
けるフィルターの他の例を示す斜視図である。
FIG. 12 is a perspective view showing another example of the filter according to the third and fourth embodiments of the present invention.

【図13】この発明の第3及び第4の実施の形態例にお
けるフィルターのさらに他の例を示す斜視図である。
FIG. 13 is a perspective view showing still another example of the filter according to the third and fourth embodiments of the present invention.

【図14】この発明のポンプの駆動源の一例を示す概略
説明図である。
FIG. 14 is a schematic explanatory view showing an example of a drive source of the pump of the present invention.

【図15】この発明の排気ガスの通路に水を噴霧する他
の例を示す概略説明図である。
FIG. 15 is a schematic explanatory view showing another example of spraying water into the exhaust gas passage of the present invention.

【符号の説明】[Explanation of symbols]

1 放熱器 2 フィルターボッ
クス 3 サイクロン 4 フィルター 5 小片 6 タンク 7 ポンプ 8 噴出口 10 排気パイプ 11 第1密閉室 12 第2密閉室 13 第3密閉室 14 第4密閉室 11a カラム室 12a カラム室 13a カラム室 14a カラム室 15 隔壁 16 タンク 17 導入パイプ 18 通路 19 冷却パイプ 20 排気通路 23 水注出口 24 ポンプ 25 箱型本体 26 導入パイプ 27 ガイド板 28 タンク 29 通路 30 フィルター 30a 薄板 31 排気パイプ 32 固定層 33 流動層 34 箱型本体 35 導入パイプ 36 第1密閉室 37 第2密閉室 38 第3密閉室 39 第4密閉室 40 邪魔板室 41 排気パイプ 42 タンク 43 噴霧区画 43a ノズル 44 フィルター区画 45 フィルター 45a 弾性板体 45b 突起又は小孔 46 支持軸 47 プロペラ 48 通路 49 オリフィス弁 50 パイプ
REFERENCE SIGNS LIST 1 radiator 2 filter box 3 cyclone 4 filter 5 small piece 6 tank 7 pump 8 jet port 10 exhaust pipe 11 first closed chamber 12 second closed chamber 13 third closed chamber 14 fourth closed chamber 11a column chamber 12a column chamber 13a column Chamber 14a Column chamber 15 Partition wall 16 Tank 17 Introducing pipe 18 Passage 19 Cooling pipe 20 Exhaust passage 23 Water outlet 24 Pump 25 Box-shaped main body 26 Introducing pipe 27 Guide plate 28 Tank 29 Passage 30 Filter 30a Thin plate 31 Exhaust pipe 32 Fixed layer 33 Fluidized bed 34 Box-shaped main body 35 Introducing pipe 36 First sealed chamber 37 Second sealed chamber 38 Third sealed chamber 39 Fourth sealed chamber 40 Baffle plate chamber 41 Exhaust pipe 42 Tank 43 Spray section 43a Nozzle 44 Filter section 45 Filter 45a Elastic plate Body 4 b projections or small hole 46 support shaft 47 propeller 48 passage 49 orifice valve 50 pipe

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI F01N 3/02 B01D 53/34 135A 301 3/04 (58)調査した分野(Int.Cl.6,DB名) B01D 53/34 B01D 53/62 B01D 53/77 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification symbol FI F01N 3/02 B01D 53/34 135A 301 3/04 (58) Investigated field (Int.Cl. 6 , DB name) B01D 53 / 34 B01D 53/62 B01D 53/77

Claims (7)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 高温の排気ガスを外気に排出する経路に
おいて、適宜の密閉したチャンバー内で当該排気ガス
を、循環使用する水に接触させて、その熱で当該水が気
化し、この気化熱によって排気ガスの温度が下がること
により、当該排気ガスを冷却させるとともに排気ガス中
のカーボン粉末等の固形微粒子及び一酸化炭素等の有害
ガスを分解、吸着させることを特徴とする、燃焼排気ガ
スの冷却及び浄化方法。
In a path for discharging high-temperature exhaust gas to the outside air, the exhaust gas is brought into contact with water for circulating use in an appropriately closed chamber, and the heat evaporates the water. By lowering the temperature of the exhaust gas, the exhaust gas is cooled, and solid particulates such as carbon powder in the exhaust gas and harmful gases such as carbon monoxide are decomposed and adsorbed. Cooling and purification methods.
【請求項2】 高温の排気ガスを外気に排出する経路に
おいて、適宜の密閉したチャンバー内で当該排気ガスを
界面活性剤等の分散剤及び消泡剤を少量添加した循環す
る水に接触させて、その熱で当該水が気化し、この気化
熱によって排気ガスの温度が下がることにより、当該排
気ガスを冷却させるとともに、排気ガス中のカーボン粉
末等の固形微粒子及び一酸化炭素等の有害ガスを分解、
吸着させることを特徴とする、燃焼排気ガスの冷却及び
浄化方法。
2. In a path for discharging high-temperature exhaust gas to the outside air, the exhaust gas is brought into contact with circulating water to which a small amount of a dispersant such as a surfactant and a defoaming agent have been added in a suitable closed chamber. The heat evaporates the water, and the heat of vaporization lowers the temperature of the exhaust gas, thereby cooling the exhaust gas and removing solid particulates such as carbon powder and harmful gas such as carbon monoxide in the exhaust gas. Disassembly,
A method for cooling and purifying combustion exhaust gas, which is characterized in that it is adsorbed.
【請求項3】 高温の排気ガスを外気に排出する経路に
おいて、適宜の密閉したチャンバー内に複数個のフィル
ターを連設し、これらの各フィルターに排気ガスを通
し、これらの各フィルターに界面活性剤等の分散剤及び
消泡剤を少量添加した循環水を注ぎ、当該フィルターを
通過する排気ガスをこれらの水に触れさせて、その熱で
当該水が気化し、この気化熱によって排気ガスの温度が
下がることにより、当該排気ガスを冷却させるととも
に、排気ガス中のカーボン粉末等の固形微粒子及び一酸
化炭素等の有害ガスを分解し上記水に吸着させることを
特徴とする、燃焼排気ガスの冷却及び浄化方法。
3. A plurality of filters are connected in an appropriate closed chamber in a path for discharging high-temperature exhaust gas to the outside air, and the exhaust gas is passed through each of these filters. Circulating water to which a small amount of a dispersing agent such as a dispersant and an antifoaming agent is added, and the exhaust gas passing through the filter is brought into contact with the water, and the heat evaporates the water. By lowering the temperature, the exhaust gas is cooled, and solid particulates such as carbon powder and the like in the exhaust gas and harmful gas such as carbon monoxide are decomposed and adsorbed to the water. Cooling and purification methods.
【請求項4】 高温の排気ガスを外気に排出する経路に
おいて、適宜の密閉したチャンバー内に複数個のフィル
ターを連設し、これらの各フィルターに排気ガスを通
し、これらの各フィルターに排気ガスを通す前に界面活
性剤等の分散剤及び消泡剤を少量添加した循環水を排気
ガスに接触させて、その熱で当該水が気化し、この気化
熱によって排気ガスの温度が下がることにより、当該排
気ガスを冷却させるとともに、当該各フィルターにおい
て排気ガス中のカーボン粉末等の固形微粒子及び一酸化
炭素等の有害ガスを分解し、上記水に吸着させ、これら
の冷却、分離の工程を繰り返すことを特徴とする、燃焼
排気ガスの冷却及び浄化方法。
4. A plurality of filters are connected in an appropriate closed chamber in a path for discharging high-temperature exhaust gas to the outside air, exhaust gas is passed through each of these filters, and exhaust gas is passed through each of these filters. Before passing through, circulating water to which a small amount of a dispersant such as a surfactant and a defoaming agent is added is brought into contact with the exhaust gas, and the heat vaporizes the water, and the heat of vaporization lowers the temperature of the exhaust gas. While cooling the exhaust gas, each filter decomposes solid particulates such as carbon powder and the like in the exhaust gas and harmful gases such as carbon monoxide, adsorbs the above water, and repeats the cooling and separating steps. A method for cooling and purifying combustion exhaust gas, characterized in that:
【請求項5】 高温の排気ガスを外気に排出する経路に
おいて、適宜の密閉したチャンバー内に複数個のフィル
ターを連設し、少なくとも最前のフィルターに導入する
前に界面活性剤等の分散剤及び消泡剤を少量添加した水
に上記排気ガスを通すか又は接触させる構成とし、上記
各フイルターの下方に上記水の水面が位置するようにタ
ンクを設け、このタンク内の水を上記各接触箇所に導く
ポンプを設け、上記各フィルターは排気ガスを間に通す
複数の板体を略平行に設け、これらの板体の間隙を二層
流が生じる巾としたことを特徴とする、燃焼排気ガスの
冷却及び浄化装置。
5. A route for discharging high-temperature exhaust gas to the outside air, in which a plurality of filters are connected in an appropriate closed chamber, and at least before being introduced into the foremost filter, a dispersant such as a surfactant is added. The exhaust gas is passed or contacted with water to which a small amount of an antifoaming agent has been added, and a tank is provided so that the water surface of the water is located below each of the filters. A plurality of plates for passing the exhaust gas therebetween are provided substantially in parallel, and the gap between these plates is set to a width at which a two-layer flow is generated. Cooling and purification equipment.
【請求項6】 高温の排気ガスを外気に排出する経路に
設けたフィルターにおいて、排気ガスを間に通す複数の
板体を略平行に設け、これらの板体の間隙を二層流が生
じる巾としたことを特徴とする、フィルター。
6. A filter provided in a path for discharging high-temperature exhaust gas to the outside air, wherein a plurality of plate members for passing the exhaust gas therebetween are provided substantially in parallel, and a gap between these plate members is formed so that a two-layer flow is generated. A filter, characterized in that:
【請求項7】 高温の排気ガスを外気に排出する経路に
設けたフィルターにおいて、排気ガスを間に通す複数の
板体を略平行に設け、これらの板体の間隙を二層流が生
じる巾とし、これらの板体は弾性体からなり、排気ガス
の流動方向の前端部を支持し、後端部を自由端とし、排
気ガスの流れの勢いによって各板体の間隔が変動する構
成としたことを特徴とする、フィルター。
7. A filter provided in a path for discharging high-temperature exhaust gas to the outside air, wherein a plurality of plates for passing the exhaust gas therebetween are provided substantially in parallel, and the gap between these plates is a width at which a two-layer flow is generated. These plates are made of an elastic body, support the front end in the flow direction of the exhaust gas, make the rear end a free end, and have a configuration in which the interval between the respective plates fluctuates due to the momentum of the flow of the exhaust gas. A filter, characterized in that:
JP7211332A 1995-07-28 1995-07-28 Method for cooling and purifying combustion exhaust gas, device therefor and filter Expired - Lifetime JP2881684B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7211332A JP2881684B2 (en) 1995-07-28 1995-07-28 Method for cooling and purifying combustion exhaust gas, device therefor and filter

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7211332A JP2881684B2 (en) 1995-07-28 1995-07-28 Method for cooling and purifying combustion exhaust gas, device therefor and filter

Publications (2)

Publication Number Publication Date
JPH0938448A JPH0938448A (en) 1997-02-10
JP2881684B2 true JP2881684B2 (en) 1999-04-12

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ID=16604206

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Country Status (1)

Country Link
JP (1) JP2881684B2 (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITPR20050013A1 (en) * 2005-03-31 2006-10-01 Antonio Petrolini PARTICULATE HOLDERS.
JP2007051626A (en) * 2005-08-12 2007-03-01 Hideo Kuwabara Apparatus for reducing gas concentration and collecting dust in exhaust gas from automobile, marine vessel and moving vehicle
KR101784883B1 (en) * 2013-03-18 2017-11-06 카와사키 주코교 카부시키 카이샤 Cleaning/cooling device, egr unit and engine system

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4734024U (en) * 1971-05-19 1972-12-15
JP3318340B2 (en) * 1992-03-19 2002-08-26 日立電子エンジニアリング株式会社 Scrubber

Also Published As

Publication number Publication date
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