JPH06146862A - Exhaust gas treatment method for internal combustion engine and device for the same - Google Patents

Exhaust gas treatment method for internal combustion engine and device for the same

Info

Publication number
JPH06146862A
JPH06146862A JP32996992A JP32996992A JPH06146862A JP H06146862 A JPH06146862 A JP H06146862A JP 32996992 A JP32996992 A JP 32996992A JP 32996992 A JP32996992 A JP 32996992A JP H06146862 A JPH06146862 A JP H06146862A
Authority
JP
Japan
Prior art keywords
exhaust gas
water
internal combustion
combustion engine
nox
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP32996992A
Other languages
Japanese (ja)
Inventor
Naohiro Morozumi
直洋 両角
Shinya Masuda
信也 増田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Yamaha Motor Co Ltd
Original Assignee
Yamaha Motor Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Yamaha Motor Co Ltd filed Critical Yamaha Motor Co Ltd
Priority to JP32996992A priority Critical patent/JPH06146862A/en
Publication of JPH06146862A publication Critical patent/JPH06146862A/en
Pending legal-status Critical Current

Links

Landscapes

  • Exhaust Gas After Treatment (AREA)

Abstract

PURPOSE:To neutralize and remove SOx, NOx, and other poisonous elements adhered to and absorbed in water by arranging a temperature lowering water adding part of exhaust gas for lowering a temperature of the exhaust gas, and sending the exhaust gas to a neutralizer which stores solid alkali. CONSTITUTION:Exhaust gas generated through combustion in an internal combustion engine is treated by a process including the steps of adding water, and making the water to be in contact with a solid alkali. SOx or NOx contained in the exhaust gas can be dissolved into water, so that capturing effect of the SOx, NOx is improved by atomizing water in the exhaust gas and increasing a contact ratio. The water absorbing SOx, NOx is stored in a neutralizer, for neutralizing through contact with the solid alkali stored in the neutralizer. Odor of the exhaust gas is eliminated accordingly, and causes for acid rain, corrosion of concrete, and photochemical smog are eliminated.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、都市ガスまたは液化石
油ガス (以下LPGという) を燃料とする内燃機関の排
気ガス処理方法およびその装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an exhaust gas treatment method and apparatus for an internal combustion engine using city gas or liquefied petroleum gas (hereinafter referred to as LPG) as a fuel.

【0002】[0002]

【従来の技術】近年、化石燃料、例えば都市ガスまたは
LPGが小型の据置型内燃機関、例えばガスヒートポン
プ(GHP)用内燃機関の燃料として多く使用されてい
る。周知のようにこれら都市ガスまたはLPGには、ガ
ス洩れを感知・確認し易いように通常有臭成分 (S含有
化合物であることが多い) によって着臭されていること
が多い。
2. Description of the Related Art In recent years, fossil fuels such as city gas or LPG have been widely used as fuels for small stationary internal combustion engines such as internal combustion engines for gas heat pumps (GHPs). As is well known, these city gases or LPGs are usually odorized by odorous components (often S-containing compounds) so that gas leaks can be easily detected and confirmed.

【0003】[0003]

【発明が解決しようとする課題】前記のような、化石燃
料を使用する機関から発生する排ガスには、CO、CH、NO
x、SOxなどが含まれており、これらが酸性雨、建築物の
腐食、光化学スモッグ等の発生要因となり、環境破壊を
引き起こし、大きな社会問題となっている。大規模な化
石燃量の消費機関である火力発電所とか大型船舶などで
は、排気ガス中に含まれるSOx ・NOx を浄化して大気中
に放出するようにされており、自動車も廃ガス規制によ
って浄化が義務付けられている。
The exhaust gas generated from an engine that uses fossil fuel as described above contains CO, CH, and NO.
x, SOx, etc. are included, which cause acid rain, corrosion of buildings, photochemical smog, etc., causing environmental damage and becoming a major social problem. Large-scale ships and thermal power plants that consume large-scale fossil fuels purify SOx and NOx contained in exhaust gas and release them into the atmosphere. Purification is mandatory.

【0004】都市ガスまたはLPGを使用した前記GH
P用内燃機関は、排気ガス中のHC、COが少ないクリーン
エンジンであるという特徴は有するが、燃料ガスと空気
を混合して燃焼させるため、NOx はどうしても発生する
ことになり、またこれら燃料ガスは水素分含有料が多い
ため、この排気には H2O (水) も多量に含まれる。さら
には着臭剤の燃焼から発生するSOx も含まれ、これらが
一体となって酸性液を生じる。ところで、このGHP用
内燃機関を含むGHPシステムは、GHP用内燃機関に
よって圧縮機を駆動して冷暖房を行うシステムであるの
で、家屋の近くやビルの屋上等の場所へ設置されること
が多い。このためGHP用内燃機関から生じた酸性液が
家屋やビルを構成する金属やコンクリート構造物の腐食
を引き起こすという不具合がある。NOxの処理は、一般
に固定装置が発生源の場合、アンモニアガスを使用した
接触還元法が採用されている。この場合、触媒として白
金(Pt) あるいは酸化チタニウム、酸化バナジウム (TiO
2-V2O5) を用い、次式のような反応によりNOxは窒素に
還元される。
Said GH using city gas or LPG
The internal combustion engine for P has the characteristic that it is a clean engine with a small amount of HC and CO in the exhaust gas, but because it mixes and burns the fuel gas and air, NOx is inevitably generated, and these fuel gases are also generated. Since this has a large hydrogen content, this exhaust gas also contains a large amount of H 2 O (water). Furthermore, SOx generated from the combustion of odorants is also included, and these together form an acidic liquid. By the way, since the GHP system including the GHP internal combustion engine is a system that drives the compressor by the GHP internal combustion engine to perform cooling and heating, it is often installed near a house or on a rooftop of a building. For this reason, there is a problem that the acidic liquid generated from the GHP internal combustion engine causes corrosion of the metal or concrete structure constituting the house or building. For the treatment of NOx, a catalytic reduction method using ammonia gas is generally used when a fixed device is the source. In this case, platinum (Pt) or titanium oxide, vanadium oxide (TiO
2- V 2 O 5 ) is used to reduce NOx to nitrogen by the following reaction.

【0005】4NO+4NH3+O2 → 4N2+6H2O NO+NO2+2NH → 2N2+3H2O また、自動車のような移動する内燃機関にはPt・Rh・Pd
系の三元触媒を使用することが多い。しかしながら、ア
ンモニアガスを使用する場合、反応装置とアンモニア貯
蔵タンクが必要となり、装置が大がかりなものとなると
共に、有害なアンモニアガスが洩れることを心配しなけ
ればならない。また、前記自動車に用いられる三元触媒
を使用した場合、使用範囲が限定される問題がある。こ
れは、自動車用燃料の場合、燃料製造段階で脱硫装置に
よりS分が除去されているので、含S燃料を用いた内燃
機関の排気ガスから、前記三元触媒を使用しての脱硫は
できない。
4NO + 4NH 3 + O 2 → 4N 2 + 6H 2 O NO + NO 2 + 2NH → 2N 2 + 3H 2 O For a moving internal combustion engine such as an automobile, Pt ・ Rh ・ Pd
Often a three-way catalyst of the system is used. However, when ammonia gas is used, a reactor and an ammonia storage tank are required, which makes the device bulky, and it is necessary to worry that harmful ammonia gas leaks. Further, when the three-way catalyst used in the automobile is used, there is a problem that the range of use is limited. This is because in the case of fuel for automobiles, since the S content is removed by the desulfurization device at the fuel production stage, it is not possible to desulfurize exhaust gas of an internal combustion engine using S-containing fuel using the above-mentioned three-way catalyst. .

【0006】本発明は前記従来技術における問題点を解
消し、小型据置型の都市ガスまたはLPGを燃料とする
内燃機関の排気ガスを浄化する処理方法およびその装置
を提供することを目的としている。
An object of the present invention is to solve the above problems in the prior art and to provide a processing method and apparatus for purifying exhaust gas of an internal combustion engine using small stationary city gas or LPG as a fuel.

【0007】[0007]

【課題を解決するための手段】前記目的を達成するた
め、本発明者らは鋭意研究を重ねた結果、内燃機関の排
気ガスを冷却することによりNOx ・SOx 等有害成分が水
に吸収 (着) され易くなることを知見し、本発明を完成
するに至った。すなわち本発明は、都市ガスまたは液化
石油ガスを燃料とする内燃機関の排気ガス排出口に、排
気ガスの温度低下用水添加部を設けて、排気ガスを所定
温度まで低下させ、引続き低温となった前記排気ガス
を、固体アルカリを収納した中和器に送通して、水に付
着・吸収されたSOx ・ NOx その他有害成分を中和除去せ
しめることを特徴とする、内燃機関の排気ガス処理方法
を要旨とするものである。
[Means for Solving the Problems] In order to achieve the above object, the inventors of the present invention have conducted extensive studies, and as a result, by cooling exhaust gas of an internal combustion engine, harmful components such as NOx and SOx are absorbed in water. ), And it came to complete the present invention. That is, according to the present invention, an exhaust gas outlet for an internal combustion engine that uses city gas or liquefied petroleum gas as a fuel is provided with a water addition unit for lowering the temperature of the exhaust gas to lower the exhaust gas to a predetermined temperature, and the temperature of the exhaust gas becomes low. The exhaust gas is passed through a neutralizer containing a solid alkali to neutralize and remove SOx, NOx and other harmful components adhering to and absorbed in water. It is a summary.

【0008】また、排気ガスへ水を添加する前にオゾン
を添加することによって排気ガスの脱臭を行うことも本
発明の要旨である。さらに本発明は、都市ガスまたは液
化石油ガスを燃料とする内燃機関の排気ガス処理装置に
おいて、排気ガス通路に、排気ガス温度低下用水添加部
と、固体アルカリを内蔵した中和器とを順次配置してな
ることを特徴とする内燃機関の排気ガス処理装置もその
要旨としている。
Further, it is also a gist of the present invention to deodorize the exhaust gas by adding ozone before adding water to the exhaust gas. Furthermore, the present invention is an exhaust gas treatment device for an internal combustion engine that uses city gas or liquefied petroleum gas as a fuel, in which an exhaust gas temperature lowering water addition section and a neutralizer containing solid alkali are sequentially arranged in the exhaust gas passage. An exhaust gas treatment device for an internal combustion engine, which is characterized in that

【0009】[0009]

【作用】本発明の構成と作用を説明する。本発明方法
は、内燃機関において燃焼した排気ガスを 水を添加する工程 前記水を固体アルカリと接触させる工程 の組合せによって処理する工程で構成されている。
The structure and operation of the present invention will be described. The method of the present invention comprises a step of treating the exhaust gas burned in the internal combustion engine with a combination of the step of adding water and the step of bringing the water into contact with a solid alkali.

【0010】排気ガス中に含有されるSOx あるいはNOx
は水に可溶であり、その水溶液は酸性を示す。しかしな
がら、このような気体が水に溶解する際には液体の温度
が低いほど多量に溶解される。また気体と接触する水の
表面積が大きいほど溶解あるいは吸収され易い。そこで
排気ガス中に水を噴霧することにより排気ガス温度を低
下させると共に水の表面積を大きくしてSOx , NOx との
接触割合を多くし補集効果を高める。水の添加量は排気
ガス温度を98℃以下にするように添加する。好ましくは
70℃以下がより効果的である。98℃を超える温度では、
SOx ・ NOx が水溶液から再び揮発して、吸収効果が上ら
ない。排気ガスに加える全体的水量は排気ガス中の有害
成分の量に応じて定められる。排気ガスの温度から予想
される水量は処理装置の構造によっても変化するが150
℃では毎時40〜20リットル、有害成分の量が400〜1500m
g/m3 では毎時4〜20リットルが好ましい水添加量であ
る。多量の水添加は不経済であると共に中和器の機能劣
化が著しく、水が不足すると充分な有害成分除去を達成
することができない。
SOx or NOx contained in exhaust gas
Is soluble in water and its aqueous solution exhibits acidity. However, when such a gas dissolves in water, the lower the temperature of the liquid, the more the gas dissolves. In addition, the larger the surface area of water in contact with the gas, the more easily it is dissolved or absorbed. Therefore, by spraying water into the exhaust gas, the temperature of the exhaust gas is lowered and the surface area of the water is increased to increase the contact ratio with SOx and NOx and enhance the collection effect. The amount of water added is such that the exhaust gas temperature is kept below 98 ° C. Preferably
70 ° C or lower is more effective. At temperatures above 98 ° C,
SOx and NOx are volatilized again from the aqueous solution, and the absorption effect does not increase. The total amount of water added to the exhaust gas depends on the amount of harmful components in the exhaust gas. The amount of water expected from the temperature of the exhaust gas varies depending on the structure of the treatment equipment, but it is 150
40 to 20 liters per hour at ℃, the amount of harmful components is 400 to 1500 m
In g / m 3 , 4 to 20 liters / hour is a preferable amount of water added. Addition of a large amount of water is uneconomical and the function of the neutralizer is significantly deteriorated. If water is insufficient, sufficient removal of harmful components cannot be achieved.

【0011】上記のようにして有害成分であるSOx , NO
x を吸収した水は、中和器に収納された固体アルカリに
接触して中和される。固体アルカリとしては炭酸カルシ
ウム、炭酸カリウム、炭酸ナトリウム等の塩類または水
酸化カルシウム等が使用できる。水に不溶性の炭酸カル
シウムあるいは難溶性の水酸化カルシウムを使用する
と、処理された水は中性 (pH7) になり易いので好都合
である。
As described above, SOx and NO which are harmful components
The water that has absorbed x comes into contact with the solid alkali contained in the neutralizer and is neutralized. As the solid alkali, salts such as calcium carbonate, potassium carbonate and sodium carbonate, calcium hydroxide and the like can be used. The use of water-insoluble calcium carbonate or sparingly soluble calcium hydroxide is advantageous because the treated water tends to be neutral (pH 7).

【0012】水を使用することなく、単に排気ガスを中
和器に通す場合、有害成分を殆んど除去されない。有害
成分を含有している水のpHは5ないし6程度であるのが
望ましい。水添加による有害成分の水との反応は次のと
おりである。 1. NO+NO2+H2O → 2HNO2 2. 3NO2+H2O → 2HNO3+NO 3. 4NO2+2H2O+O2 → 4HNO3 またこれら水溶液と中和剤とは次のように反応する。 CaCO3+2HNO2 → Ca(NO2)2+H2CO3 Ca(OH)2+2HNO3 → Ca(NO3)2+H2O Ca(OH)2+2HNO3 → Ca(NO2)2+H2O また、燃料ガス中に着臭剤にもとづくSO2 が入ってきた
場合は次のとおりである。 1. 2NO+SO2+H2O → N2O+H2SO4 2. H2O+SO3 → H2SO4 3. NO+NO2+H2O → 2HNO2 4. 3NO2+H2O → 2HNO3+NO 5. 4NO2+2H2O+O2 → 4HNO3 上記水溶液の中和反応は次のとおりである。
When the exhaust gas is simply passed through the neutralizer without using water, almost no harmful components are removed. The pH of the water containing the harmful components is preferably about 5 to 6. The reaction of harmful components with water by adding water is as follows. 1. NO + NO 2 + H 2 O → 2HNO 2 2.3NO 2 + H 2 O → 2HNO 3 + NO 3.4NO 2 + 2H 2 O + O 2 → 4HNO 3 In addition, these aqueous solutions and the neutralizing agent react as follows. CaCO 3 + 2HNO 2 → Ca (NO 2 ) 2 + H 2 CO 3 Ca (OH) 2 + 2HNO 3 → Ca (NO 3 ) 2 + H 2 O Ca (OH) 2 + 2HNO 3 → Ca (NO 2 ) 2 + H 2 O The following is the case when SO 2 based on the odorant enters the fuel gas. 1.2NO + SO 2 + H 2 O → N 2 O + H 2 SO 4 2. H 2 O + SO 3 → H 2 SO 4 3. NO + NO 2 + H 2 O → 2HNO 2 4.3NO 2 + H 2 O → 2HNO 3 + NO 5.4NO 2 + 2H 2 O + O 2 → 4HNO 3 The neutralization reaction of the above aqueous solution is as follows.

【0013】 上記の水との反応は、図1、図2および図3の水添加部
において行なわれ、中和反応は中和器内で行なわれる。
[0013] The above-mentioned reaction with water is carried out in the water addition section shown in FIGS. 1, 2 and 3, and the neutralization reaction is carried out in the neutralizer.

【0014】また、オゾン発生機により O3 を排気ガス
に添加した場合以下のような反応が考えられる。 NOx : 1. NO+O3 → NO2+O2 └→ 4NO2+2H2O+O2 → 4HNO3 2HNO3+CaCO3 → Ca(NO3)2+H2O+CO2 着臭成分: CH3−SH+O3 → CH3−OH+SO2 3CH3−S−CH3+4O3 → 6CH3OH+3SO2 SO2+H2O+1/2O2 → H2SO4 H2SO4+CaCO3 → CaSO4+H2O+CO2 図4は上記反応を行わせる装置の概要図である。また、
図5に本発明を実施する装置の模式的断面図を示す。
When O 3 is added to the exhaust gas by the ozone generator, the following reaction is considered. NOx: 1. NO + O 3 → NO 2 + O 2 └ → 4NO 2 + 2H 2 O + O 2 → 4HNO 3 2HNO 3 + CaCO 3 → Ca (NO 3 ) 2 + H 2 O + CO 2 Odorant: CH 3 −SH + O 3 → CH 3 OH + SO 2 3CH 3 -S- CH 3 + 4O 3 → 6CH 3 OH + 3SO 2 SO 2 + H 2 O + 1/2 O 2 → H 2 SO 4 H 2 SO 4 + CaCO 3 → CaSO 4 + H 2 O + CO 2 4 the reaction It is a schematic diagram of an apparatus for performing. Also,
FIG. 5 shows a schematic sectional view of an apparatus for carrying out the present invention.

【0015】[0015]

【実施例】本発明を実施例によって具体的に説明する
が、これによって本発明が限定されるものではない。 (実施例1)NOx量 700ppmの排気ガスに図5のように組
合せて水を4L/H の割合で添加する装置を使用し、オゾ
ンを発生、添加、分解する装置〔オゾン発生機:日本特
殊陶業(株) OU-65A、オゾン分解触媒:堺化学工業(株)
SCH-120 〕と炭酸カルシウム2kg〔白石工業(株)〕を使
用した中和装置を使用した結果次のような効果があっ
た。
EXAMPLES The present invention will be specifically described by way of examples, which should not be construed as limiting the invention. (Example 1) A device for generating, adding, and decomposing ozone by using a device for adding water at a rate of 4 L / H by combining exhaust gas with NOx amount of 700 ppm as shown in Fig. 5 [Ozone generator: Nippon Special Ceramic Industry Co., Ltd. OU-65A, Ozone decomposition catalyst: Sakai Chemical Industry Co., Ltd.
SCH-120] and 2 kg of calcium carbonate [Shiraishi Industry Co., Ltd.] were used to obtain the following effects.

【0016】[0016]

【表1】 [Table 1]

【0017】(実施例2)NOx量 1300ppmの排気ガスに
実施例1と同様に組合せて水を6L/H の割合で添加する
装置を使用し、炭酸カルシウム3kg〔白石工業(株)〕を
使用した中和装置を使用した結果次のような効果があっ
た。
(Example 2) Using an apparatus for adding water at a rate of 6 L / H in combination with exhaust gas having an NOx amount of 1300 ppm in the same manner as in Example 1, and using 3 kg of calcium carbonate [Shiraishi Industry Co., Ltd.] As a result of using the neutralizing device, the following effects were obtained.

【0018】[0018]

【表2】 [Table 2]

【0019】(実施例3)NOx量 1100ppmの排気ガスに
実施例1と同様に組合せて水を1L/H の割合で添加する
装置を使用し、炭酸カルシウム2kg〔白石工業(株)〕を
使用した中和装置を使用した結果次のような効果があっ
た。
(Example 3) An apparatus for adding water at a rate of 1 L / H in combination with exhaust gas having NOx amount of 1100 ppm in the same manner as in Example 1 was used, and 2 kg of calcium carbonate [Shiraishi Industry Co., Ltd.] was used. As a result of using the neutralizing device, the following effects were obtained.

【0020】[0020]

【表3】 [Table 3]

【0021】(実施例4)NOx量 1100ppmの排気ガスに
実施例1と同様に組合せて水を1L/H の割合で添加する
装置を使用し、オゾンを発生、添加、分解する装置〔オ
ゾン発生機:日本特殊陶業(株) OU-65A、オゾン分解触
媒:堺化学工業(株) SCH-120 〕と炭酸カルシウム2kg
〔白石工業(株)〕を使用した中和装置を使用した結果次
のような効果があった。
(Embodiment 4) An apparatus for generating, adding and decomposing ozone by using an apparatus for adding 1100 ppm of NOx to the exhaust gas in the same manner as in Example 1 and adding water at a rate of 1 L / H [Ozone generation Machine: Nippon Special Ceramics Co., Ltd. OU-65A, ozone decomposition catalyst: Sakai Chemical Industry Co., Ltd. SCH-120] and calcium carbonate 2 kg
The following effects were obtained as a result of using the neutralization device using [Shiraishi Industry Co., Ltd.].

【0022】[0022]

【表4】 [Table 4]

【0023】(実施例5)NOx量 1100ppmの排気ガスに
図4のように組合せて水を循環させる外部冷却機と水を
4L/H の割合で添加する装置を使用し、炭酸カルシウム
2kg〔白石工業 (株)〕を使用した中和装置を使用した
結果次のような効果があった。
(Example 5) Using an external cooler for circulating water by combining exhaust gas with NOx amount of 1100 ppm as shown in FIG. 4 and a device for adding water at a rate of 4 L / H, 2 kg of calcium carbonate [Shiraishi] The following effects were obtained as a result of using a neutralization device using Industrial Co., Ltd.].

【0024】[0024]

【表5】 [Table 5]

【0025】(実施例6)臭気成分ジメチルサルファイ
ド (DMS): H3C−S−CH3 10ppmを含む排気ガスに実施
例1と同様に組合せて、オゾンを発生、添加、分解する
装置を使用した。オゾン発生機〔日本特殊陶業(株) OU-
65A、オゾン分解触媒:堺化学工業(株) SCH-120 〕と水
を4L/H の割合で添加する装置と炭酸カルシウム3kg
〔白石工業(株)〕を使用した中和装置を使用した結果次
のような効果があった。
(Example 6) Exhaust gas containing odorous component dimethyl sulfide (DMS): H 3 C-S-CH 3 10 ppm was combined in the same manner as in Example 1, and an apparatus for generating, adding and decomposing ozone was used. did. Ozone generator [Nippon Special Ceramics Co., Ltd. OU-
65A, ozone decomposition catalyst: SCH-120 of Sakai Chemical Industry Co., Ltd.] and equipment for adding water at a rate of 4 L / H and calcium carbonate 3 kg
The following effects were obtained as a result of using the neutralization device using [Shiraishi Industry Co., Ltd.].

【0026】[0026]

【表6】 [Table 6]

【0027】[0027]

【発明の効果】本発明は以上説明したように構成されて
いるから、水噴霧により排気ガスの温度が下るため、排
気ガス中に含有されているSOx , NOx が捕足され易く、
中和反応も確実に行うことができ、オゾン添加によって
着臭成分の分解も行われ、排気ガスを無臭化できるの
で、酸性雨、コンクリートやその他の構造物に対する腐
食や光化学スモッグの原因が確実に取り除かれ、産業上
極めて有用である。
Since the present invention is constructed as described above, the temperature of the exhaust gas is lowered by the water spray, so SOx and NOx contained in the exhaust gas are easily trapped,
Neutralization reaction can be performed reliably, and odor components can be decomposed by addition of ozone, and exhaust gas can be deodorized.Therefore, the cause of acid rain, corrosion on concrete and other structures, and photochemical smog can be ensured. Removed and extremely useful in industry.

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

【図1】本発明の基本的構成図である。FIG. 1 is a basic configuration diagram of the present invention.

【図2】本発明を一部改良した構成図である。FIG. 2 is a configuration diagram in which the present invention is partially improved.

【図3】本発明の他の実施例を示す構成図である。FIG. 3 is a configuration diagram showing another embodiment of the present invention.

【図4】脱臭機をもつ本発明の構成図である。FIG. 4 is a configuration diagram of the present invention having a deodorizer.

【図5】本発明を実施する装置の模式的断面図である。FIG. 5 is a schematic sectional view of an apparatus for carrying out the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 都市ガスまたは液化石油ガスを燃料とす
る内燃機関の排気ガス排出口に、排気ガスの温度低下用
水添加部を設けて、排気ガスを所定温度まで低下させ、
引続き低温となった前記排気ガスを固体アルカリを収納
した中和器に送通して、水に付着・吸収されたSOx ・ NO
x その他有害成分を中和除去せしめることを特徴とす
る、内燃機関の排気ガス処理方法。
1. An exhaust gas outlet for an internal combustion engine that uses city gas or liquefied petroleum gas as a fuel is provided with a water addition unit for lowering the temperature of the exhaust gas to lower the exhaust gas to a predetermined temperature.
The exhaust gas, which has become low in temperature, continues to be sent to a neutralizer containing solid alkali, and SOx and NO adsorbed and absorbed in water.
x An exhaust gas treatment method for an internal combustion engine, characterized by neutralizing and removing other harmful components.
【請求項2】 都市ガスまたは液化石油ガスを燃料とす
る内燃機関の排気ガス処理装置において、排気ガス通路
に、排気ガス温度低下用水添加部と、固体アルカリを内
蔵した中和器とを順次配置してなることを特徴とする内
燃機関の排気ガス処理装置。
2. In an exhaust gas treatment device for an internal combustion engine using city gas or liquefied petroleum gas as a fuel, an exhaust gas temperature lowering water addition section and a neutralizer containing solid alkali are sequentially arranged in an exhaust gas passage. An exhaust gas treatment device for an internal combustion engine, comprising:
JP32996992A 1992-11-16 1992-11-16 Exhaust gas treatment method for internal combustion engine and device for the same Pending JPH06146862A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP32996992A JPH06146862A (en) 1992-11-16 1992-11-16 Exhaust gas treatment method for internal combustion engine and device for the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP32996992A JPH06146862A (en) 1992-11-16 1992-11-16 Exhaust gas treatment method for internal combustion engine and device for the same

Publications (1)

Publication Number Publication Date
JPH06146862A true JPH06146862A (en) 1994-05-27

Family

ID=18227296

Family Applications (1)

Application Number Title Priority Date Filing Date
JP32996992A Pending JPH06146862A (en) 1992-11-16 1992-11-16 Exhaust gas treatment method for internal combustion engine and device for the same

Country Status (1)

Country Link
JP (1) JPH06146862A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008188569A (en) * 2007-02-08 2008-08-21 Mitsubishi Heavy Ind Ltd Waste gas treatment method and apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008188569A (en) * 2007-02-08 2008-08-21 Mitsubishi Heavy Ind Ltd Waste gas treatment method and apparatus

Similar Documents

Publication Publication Date Title
RU2429900C1 (en) Method and device for treating flue gas
US6638485B1 (en) Process for treating exhaust gas and exhaust gas treating equipment
US8980207B1 (en) Method and system for removal of mercury from a flue gas
US9308496B2 (en) System and method for controlling and reducing NOx emissions
EP2578298A1 (en) Exhaust gas processing system and method
US20100239480A1 (en) Method And Apparatus For The Treatment Of Nitrogen Oxides Using An Ozone And Catalyst Hybrid System
CN101274207A (en) Method for oxidizing and denitrating ozone containing industrial waste gas HCl
JP4936002B2 (en) Exhaust gas treatment method and exhaust gas treatment apparatus
JPH0262297B2 (en)
RU2469949C2 (en) Method of purifying smoke gases, containing nitrogen oxides
JPH06146862A (en) Exhaust gas treatment method for internal combustion engine and device for the same
JP3366417B2 (en) Prevention method of ammonium sulfate precipitation in selective reduction denitration method
KR100550603B1 (en) NOx REMOVAL APPARATUS and METHOD USING DRY SCRUBBER
CN115253633A (en) Waste incineration flue gas purification method and system
JPH0394813A (en) Method for removing harmful gas in waste gas generated by incineration of refuse
KR20190142352A (en) Method and system for removing particulate matter and harmful compounds from flue gas using ceramic filter with SCR catalyst
JP2006007118A (en) Waste gas purifying apparatus
KR100406510B1 (en) Method and system for removing nitrogen oxide using oxidation catalyst
JPH07328378A (en) Treatment of exhaust gas
KR20030006429A (en) The reduction method of nitrogen oxides and sulfur oxides using hydrogen peroxide solution and calcium oxide solution
JP2928983B2 (en) Nitrous oxide containing gas decomposition method
JPS60251917A (en) Desulfurization and denitration of waste gas
KR200279995Y1 (en) NOx REMOVAL APPARATUS USING DRY SCRUBBER
KR200234632Y1 (en) System for removing nitrogen oxide using oxidation catalyst
JP4228152B2 (en) Waste heat recovery method by low temperature denitration of cogeneration exhaust gas