JP3424004B2 - Wet exhaust gas purifier with reduced liquid loss - Google Patents

Wet exhaust gas purifier with reduced liquid loss

Info

Publication number
JP3424004B2
JP3424004B2 JP04837497A JP4837497A JP3424004B2 JP 3424004 B2 JP3424004 B2 JP 3424004B2 JP 04837497 A JP04837497 A JP 04837497A JP 4837497 A JP4837497 A JP 4837497A JP 3424004 B2 JP3424004 B2 JP 3424004B2
Authority
JP
Japan
Prior art keywords
exhaust gas
reaction tank
liquid
purifying
replenisher
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 - Fee Related
Application number
JP04837497A
Other languages
Japanese (ja)
Other versions
JPH10212930A (en
Inventor
功 加藤
Original Assignee
功 加藤
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 功 加藤 filed Critical 功 加藤
Priority to JP04837497A priority Critical patent/JP3424004B2/en
Publication of JPH10212930A publication Critical patent/JPH10212930A/en
Application granted granted Critical
Publication of JP3424004B2 publication Critical patent/JP3424004B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • 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】 【0001】 【発明の属する技術分野】本発明は排気ガスを浄化する
ための浄化液の外部流失を少なくした湿式の排気ガス浄
化装置の製造方法に関する。 【0002】 【従来の技術】従来の湿式排気ガス浄化装置はスクラバ
ーとも呼ばれ、一般的に極めて大型であり、そのため通
常の陸上運送機関等には搭載され得るものはなかった。 【0003】 【発明が解決しようとする課題】従来の湿式排気ガス浄
化装置にあっては必然的に飛沫が発生し、この飛沫は連
続して且つ大量に発生し、排気ガスと共に装置の外部に
飛散するという、いわゆる飛沫同伴の現象が生じる。そ
してこの飛沫同伴を防止しようとすると装置は複雑で大
型となり、一般の陸土交通機関などには事実上搭載不可
能という問題点があった。 【0004】本発明はエンジンを高速回転で運転して
も、外部へ流出する液体量を極めて限定化したものに
し、装置を小型化する事により、一般の陸上交通機関に
も搭載可能な湿式排気ガス浄化装置を提供することを目
的としている。 【0005】 【課題を解決するための手段】上記目的を達成するため
に、本発明の湿式排気ガス浄化装置に於いては、浄化用
溶液を入れる反応タンクはできる限り少容量とし、しか
もこの反応タンク中には液体保持能力が大きくしかも不
燃性である繊維状物質を適当量充填し、なおかつ、この
装置内の各所に飛沫を除去するため、複数の邪魔板を取
り付けたものである。 【0006】上記不燃性の繊維上物質としてはガラス繊
維又はステンレス製スチールウール等が良く、その充填
量は見掛けの容積で反応タンク容量の10%以上が望ま
しい。 【0007】上記浄化液を入れる反応タンクの容量はエ
ンジンの排気量に比例するが、エンジンの排気量以下に
することが望ましい。 【0008】ディーゼルエンジンの排気ガスは高圧であ
るためエンジンを高速回転にした時は浄化液の一部は外
部に流失する。しかし、その流出量は反応タンクの容量
自体が小容量であるから、その容積以上には流出しない
し、流出する時間も極めて短時間に限定される。 【0009】そして又、この際反応タンク内に充填して
ある繊維状物質の保水作用により、反応タンク内の液体
が短時間内に枯渇することを防止する。 【0010】充填材として用いられる繊維状物質は液体
の保水能力が大きいだけでなく、単位体積当たりの表面
積が極めて大きいから、排気ガスと浄化用溶液との気液
接触効率を高め、そのため化学反応が極めて効率的とな
るほか、黒煙の如き浮遊粒子状物質の捕捉効果を高める
事にもなる。 【0011】浄化用溶液を入れる反応タンクの内壁およ
び装置内のガス通路には発生した飛沫をできる限り元の
反応タンクに戻すため複数の邪魔板を取り付ける。 【0012】ディーゼルエンジンの排気ガスは高温であ
り一定少量の浄化液は外部から液を補充しない限りごく
短時間内に蒸発乾涸こしてしまう。そこで此を防ぐた
め、運転中は蒸発量に相当する分だけの補充液を常に添
加補充する。 【0013】従って,補充液量が蒸発によって失われる
量を上回らない限り,浄化用溶液が連続して外部へ放出
することはない。 【0014】これと逆に補充液量が蒸発によって失われ
る量以下である場合は,化学反応の効率は低下するが,
補充を行っている限り反応タンク内の充填物は湿潤状態
を保ち,浄化作用を行う事ができる。 【0015】 【発明の実施の形態】発明の実施の形態を実施例にもと
づき図面を参照して説明する。図1において,浄化用水
溶液をいれる反応タンク1の内部には保水性のあるガラ
ス繊維3を充填する.反応タンク1の底部に近い位置に
外部から排気ガスを導き入れるためのパイプの出口5を
設ける。この排気ガスの出口5は液体の内部であるよう
にする。 【0016】反応タンク1の内壁、および排気ガス通路
には複数の邪魔板4を設け、排気ガスの噴出によって発
生した飛沫を再び元の液面に戻すように配置する。 【0017】補充液用の細いパイプ7は反応タンクの下
部近くに接続する。そしてこの補充液は別個の補充液タ
ンク10から小型の補充ポンプ11、或いはエジェクタ
ーの作用等によって補充する。 【0018】補充液の液量は高温の排気ガスによって蒸
発する量と釣り合いを取るため、ピンチコック12を補
充液回路中に設けて、液量を適当に調節する 【0019】浄化液を入れる反応タンクに隣接して補助
タンク2を設ける。 【0020】この補助タンク2は反応タンクから噴出し
た飛沫が外部に直接飛散する量を少なくするためのもの
でダムの役目をする。 【0021】補助タンク2にはオーバーフローの出口1
4を設ける。この位置は浄化済み排気ガスの出口6より
も下部の位置にあり、補助タンク2の中程とする。 【0022】このオーバーフローの役目は液の補充バラ
ンスが崩れ、補充液量が蒸発損失量よりも多くなって、
補助タンク2が液で充満してしまうのを防止する。 【0023】浄化液を入れる反応タンク1の底部には廃
液バルブ8を設け、必要に応じて汚濁した廃液を装置の
外部へ排出するために使う。 【0024】反応タンク1の液面を常に一定位置に保つ
ため、補充液を自動的に作動、停止するためのセンサー
13を反応タンク1の壁面又は液面計に取付ける。 【0025】 【発明の効果】本発明は以上説明したように構成されて
いるので以下に記載されるような効果を奏する。 【0026】浄化用水溶液を入れる反応タンクの容積が
極めて小型なので、たとえ一時的に液の噴出があっても
その量は極めて限定されたものであって少なく、更にま
た噴出している時間もごく短時間である。 【0027】浄化装置全体が小型であるため、従来は不
可能であった多くの陸上交通機関にも搭載可能であり、
その収納位置は車体の底面下部にすることができる。そ
の為,搭乗人員数,積載貨物量等が制約を受ける事が無
い。 【0028】反応タンク内のガラス繊維は保水能力が大
きく且不燃性であるため、エンジンを高出力で回転して
も反応タンク内の液体の全量を一挙に噴出してしまう事
もなく、仮に補充経路が故障して、液が枯渇しても浄化
装置が使用不能になる事もなく、火災の危険性もない。 【0029】反応タンク中に充填材として使用するガラ
ス繊維は耐薬品性も大きく各種の薬品水溶液に長期間浸
漬して使用しても変質せず価格も廉価である。 【0030】ディーゼルエンジンの排気ガスは極めて高
温で300℃以上にも達するが、この高温の排気ガスに
よって水溶液は常に気化蒸発して失われる。しかし、こ
の事によって大量の有害な熱エネルギーを気化熱によっ
て相殺し、環境の改善に役立てる事ができる。このよう
にして浄化装置から排出される浄化済みのガス温度は通
常50℃以内である。この効果はエンジンが閉鎖区域に
於いて使用される時に威力を発揮する。 【0031】浄化用に使用する溶液の溶媒は水であり、
極めて普遍的な物質である。そのため全国どこでも入手
でき、更に飲料用の上水道水である必要もない。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for manufacturing a wet type exhaust gas purifying apparatus in which a purifying liquid for purifying exhaust gas is less likely to flow outside. 2. Description of the Related Art A conventional wet exhaust gas purifying apparatus, also called a scrubber, is generally very large, and therefore cannot be mounted on an ordinary land transportation engine or the like. [0003] In the conventional wet exhaust gas purifying device, droplets are inevitably generated, and these droplets are continuously generated in large amounts, and are discharged together with the exhaust gas to the outside of the device. The phenomenon of so-called entrainment of scattering occurs. In order to prevent the entrainment, the device becomes complicated and large, and there is a problem that it cannot be mounted on general land transportation. According to the present invention, even when the engine is operated at a high speed, the amount of liquid flowing out is extremely limited, and the size of the apparatus is reduced so that the wet exhaust can be mounted on general land transportation. It is intended to provide a gas purification device. [0005] In order to achieve the above object, in the wet exhaust gas purifying apparatus of the present invention, the reaction tank for containing the purifying solution is made as small as possible. The tank is filled with an appropriate amount of a fibrous substance which has a large liquid holding capacity and is nonflammable, and a plurality of baffles are attached at various places in the apparatus in order to remove splashes. [0006] The non-combustible material on fiber is preferably glass fiber or stainless steel wool, and its filling amount is desirably 10% or more of the apparent capacity of the reaction tank. [0007] The capacity of the reaction tank for storing the purifying liquid is proportional to the displacement of the engine, but is desirably smaller than the displacement of the engine. [0008] Since the exhaust gas of a diesel engine has a high pressure, a part of the purifying liquid flows out to the outside when the engine is rotated at a high speed. However, since the volume of the outflow is small due to the small capacity of the reaction tank, the volume of the outflow does not exceed the volume, and the time of the outflow is limited to a very short time. Also, at this time, the liquid in the reaction tank is prevented from being depleted in a short time due to the water retaining action of the fibrous substance filled in the reaction tank. [0010] The fibrous substance used as the filler has not only a large water retention capacity of liquid but also a very large surface area per unit volume, so that the gas-liquid contact efficiency between the exhaust gas and the purifying solution is increased, and therefore the chemical reaction Is extremely efficient and also enhances the trapping effect of suspended particulate matter such as black smoke. [0011] A plurality of baffles are attached to the inner wall of the reaction tank containing the purifying solution and the gas passage in the apparatus in order to return the generated droplets to the original reaction tank as much as possible. The exhaust gas of a diesel engine is hot and a certain small amount of the purifying liquid evaporates to dryness in a very short time unless the liquid is replenished from the outside. Therefore, in order to prevent this, during the operation, a replenisher equivalent to the amount of evaporation is always added and replenished. Therefore, unless the amount of replenisher exceeds the amount lost by evaporation, the purifying solution will not be continuously discharged to the outside. Conversely, if the amount of replenisher is less than the amount lost by evaporation, the efficiency of the chemical reaction decreases, but
As long as replenishment is being performed, the filling in the reaction tank is kept wet and can perform a purifying action. Embodiments of the present invention will be described with reference to the drawings based on embodiments. In FIG. 1, the inside of a reaction tank 1 containing an aqueous solution for purification is filled with glass fibers 3 having water retention. A pipe outlet 5 for introducing exhaust gas from the outside is provided at a position near the bottom of the reaction tank 1. The exhaust gas outlet 5 is located inside the liquid. A plurality of baffles 4 are provided on the inner wall of the reaction tank 1 and the exhaust gas passage, and are arranged so that the droplets generated by the ejection of the exhaust gas return to the original liquid level. A thin pipe 7 for the replenisher is connected near the lower part of the reaction tank. The replenisher is replenished from a separate replenisher tank 10 by the action of a small refill pump 11, an ejector, or the like. In order to balance the amount of replenisher with the amount evaporated by high-temperature exhaust gas, a pinch cock 12 is provided in the replenisher circuit to adjust the amount of the replenisher appropriately. An auxiliary tank 2 is provided adjacent to the tank. The auxiliary tank 2 serves to reduce the amount of splashes directly ejected from the reaction tank to the outside, and serves as a dam. The auxiliary tank 2 has an overflow outlet 1
4 is provided. This position is located below the outlet 6 of the purified exhaust gas, and is located in the middle of the auxiliary tank 2. The role of this overflow is that the replenishment balance of the liquid is lost, and the replenisher amount becomes larger than the evaporation loss amount.
This prevents the auxiliary tank 2 from being filled with liquid. A waste liquid valve 8 is provided at the bottom of the reaction tank 1 for storing the purifying liquid, and is used to discharge polluted waste liquid to the outside of the apparatus as required. In order to keep the liquid level in the reaction tank 1 constant, a sensor 13 for automatically operating and stopping the replenisher is attached to the wall surface of the reaction tank 1 or a liquid level gauge. The present invention is configured as described above, and has the following effects. Since the volume of the reaction tank containing the purifying aqueous solution is extremely small, even if there is a temporary ejection of the solution, the amount is very limited and small, and the time during which the solution is ejected is extremely short. It's short. Since the entire purification device is small, it can be mounted on many land transportations that were not possible before.
The storage position can be at the bottom of the bottom of the vehicle body. Therefore, there are no restrictions on the number of passengers and the amount of cargo on board. Since the glass fiber in the reaction tank has a large water retention capacity and is nonflammable, even if the engine is rotated at a high output, the entire amount of the liquid in the reaction tank is not spouted at once, and is temporarily refilled. Even if the route is broken and the liquid is depleted, the purifying device is not disabled and there is no danger of fire. Glass fiber used as a filler in a reaction tank has high chemical resistance and does not deteriorate even when used by being immersed in various chemical aqueous solutions for a long period of time, and is inexpensive. The exhaust gas of a diesel engine has a very high temperature of 300 ° C. or higher, and the aqueous solution is constantly evaporated and lost by the high-temperature exhaust gas. However, this can offset a large amount of harmful thermal energy by the heat of vaporization, which can help improve the environment. The temperature of the purified gas discharged from the purification device in this way is usually within 50 ° C. This effect works when the engine is used in a closed area. The solvent of the solution used for purification is water,
It is a very universal substance. Therefore, it can be obtained anywhere in the country, and it is not necessary to use tap water for drinking.

【図面の簡単な説明】 【図1】液の流失を少なくした湿式排気ガス浄化装置の
縦断面図である。 【図2】液の流失を少なくした湿式排気ガス浄化装置用
の補充液タンクと補充装置の略図である。 【符号の説明】 1 小型反応タンク 2 補助タンク 3 充填物 4 邪魔板 5 排気ガス取り入れ口 6 浄化済み排気ガス出口 7 補充液入り口 8 廃液排出口 9 噴出液逆送用流し板 10 補充液タンク 11 補充用ポンプ 12 補充液量調整用ピンチコック 13 液面制御用センサー 14 オーバーフロー液出口 15 浄化液注入口
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a vertical cross-sectional view of a wet exhaust gas purifying apparatus in which the flow of a liquid is reduced. FIG. 2 is a schematic view of a replenisher tank and a replenisher for a wet exhaust gas purifying apparatus with reduced liquid loss. [Description of Signs] 1 Small reaction tank 2 Auxiliary tank 3 Filling material 4 Baffle plate 5 Exhaust gas intake port 6 Purified exhaust gas outlet 7 Replenisher inlet 8 Waste liquid outlet 9 Sink plate for backflow of ejected liquid 10 Replenisher tank 11 Refill pump 12 Pinch cock 13 for adjusting the amount of replenisher Liquid level sensor 14 Overflow liquid outlet 15 Purification liquid inlet

Claims (1)

(57)【特許請求の範囲】 【請求項1】陸上交通機関に搭載可能な排気ガス浄化装
置であって、浄化用水溶液をいれる反応タンクの内部に
は、保水性のあるガラス繊維を充填して排気ガスを導き
入れる為のパイプの出口を設け、反応タンクの下部近く
に補充液用の細いパイプを接続し、反応タンクの内壁及
び排気ガス通路には複数の邪魔板を設けて排気ガス噴出
によって発生した飛沫を元に戻すように配置し、反応タ
ンクに隣接して浄化済み排気ガス出口を備えた補助タン
クを設けてなることを特徴とする排気ガス浄化装置。
(57) [Claims 1] An exhaust gas purifying device mountable on land transportation, wherein a reaction tank containing a purifying aqueous solution is filled with water-retaining glass fiber. The outlet of a pipe for introducing exhaust gas is provided, a thin pipe for replenisher is connected near the lower part of the reaction tank, and multiple baffles are provided on the inner wall of the reaction tank and the exhaust gas passage to eject exhaust gas. Exhaust gas purifying apparatus, wherein an auxiliary tank provided with a purified exhaust gas outlet is provided adjacent to the reaction tank so as to return droplets generated by the exhaust gas to its original state.
JP04837497A 1997-01-27 1997-01-27 Wet exhaust gas purifier with reduced liquid loss Expired - Fee Related JP3424004B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP04837497A JP3424004B2 (en) 1997-01-27 1997-01-27 Wet exhaust gas purifier with reduced liquid loss

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP04837497A JP3424004B2 (en) 1997-01-27 1997-01-27 Wet exhaust gas purifier with reduced liquid loss

Publications (2)

Publication Number Publication Date
JPH10212930A JPH10212930A (en) 1998-08-11
JP3424004B2 true JP3424004B2 (en) 2003-07-07

Family

ID=12801562

Family Applications (1)

Application Number Title Priority Date Filing Date
JP04837497A Expired - Fee Related JP3424004B2 (en) 1997-01-27 1997-01-27 Wet exhaust gas purifier with reduced liquid loss

Country Status (1)

Country Link
JP (1) JP3424004B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5802341B2 (en) * 2012-12-28 2015-10-28 川崎重工業株式会社 EGR unit and marine engine system

Also Published As

Publication number Publication date
JPH10212930A (en) 1998-08-11

Similar Documents

Publication Publication Date Title
KR101127626B1 (en) Wet Scrubbing System
JP3424004B2 (en) Wet exhaust gas purifier with reduced liquid loss
CN212594923U (en) Waste incineration flue gas sprays deacidification tower
JP2001141309A (en) Drain storage container
JP2001276546A (en) Dust removing device
CN111151113A (en) Waste incineration flue gas sprays deacidification tower
JP3232219U (en) Exhaust gas purification system
JP6737957B2 (en) Nuclear power plant with containment venting system with filter
CN104163459B (en) Household water filter
JP2001239130A (en) Ammonia detoxifying apparatus
JP3678254B2 (en) Combustion equipment
RU2758899C2 (en) Nuclear plant with ventilation system
JP3732887B2 (en) Drain neutralizer
JPH09287725A (en) Drain neutralising device
JPS6026806Y2 (en) air separator for water heating equipment
JP3129409B2 (en) Inboard bilge water treatment equipment
JPH0824510A (en) Defoaming method and device therefor
JPS6246079Y2 (en)
CN211612181U (en) Falling film absorption tower
RU2078047C1 (en) Deaerator
SU1183778A1 (en) Thermal deaerator
JP3732886B2 (en) Drain neutralizer
JPH10267210A (en) Steam generator
SU1280263A1 (en) Thermal deaerator
KR100458317B1 (en) System for exhausting volatile air in sewage and waste water

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100502

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100502

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100502

Year of fee payment: 7

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130502

Year of fee payment: 10

LAPS Cancellation because of no payment of annual fees