JPS58131123A - Filter for purifying exhaust gas in internal combustion engine - Google Patents
Filter for purifying exhaust gas in internal combustion engineInfo
- Publication number
- JPS58131123A JPS58131123A JP57013311A JP1331182A JPS58131123A JP S58131123 A JPS58131123 A JP S58131123A JP 57013311 A JP57013311 A JP 57013311A JP 1331182 A JP1331182 A JP 1331182A JP S58131123 A JPS58131123 A JP S58131123A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- filter
- purifying
- columnar body
- internal combustion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 238000002485 combustion reaction Methods 0.000 title claims description 9
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 11
- 239000003054 catalyst Substances 0.000 claims abstract description 10
- 229910052709 silver Inorganic materials 0.000 claims description 10
- 239000004332 silver Substances 0.000 claims description 10
- 239000000463 material Substances 0.000 abstract description 16
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 abstract description 8
- QAOWNCQODCNURD-UHFFFAOYSA-L sulfate group Chemical group S(=O)(=O)([O-])[O-] QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 abstract description 8
- 239000000203 mixture Substances 0.000 abstract description 5
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(I) nitrate Inorganic materials [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 abstract description 5
- 229910052763 palladium Inorganic materials 0.000 abstract description 4
- 229910052697 platinum Inorganic materials 0.000 abstract description 4
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 abstract description 2
- 239000004927 clay Substances 0.000 abstract description 2
- 229910052737 gold Inorganic materials 0.000 abstract description 2
- 229910052741 iridium Inorganic materials 0.000 abstract description 2
- 229910052762 osmium Inorganic materials 0.000 abstract description 2
- 229910052703 rhodium Inorganic materials 0.000 abstract description 2
- 229910052623 talc Inorganic materials 0.000 abstract description 2
- 239000000454 talc Substances 0.000 abstract description 2
- 229910002666 PdCl2 Inorganic materials 0.000 abstract 1
- 229910021502 aluminium hydroxide Inorganic materials 0.000 abstract 1
- 229910052570 clay Inorganic materials 0.000 abstract 1
- 229910001679 gibbsite Inorganic materials 0.000 abstract 1
- 229910052745 lead Inorganic materials 0.000 abstract 1
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 10
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 9
- 229910052751 metal Inorganic materials 0.000 description 8
- 239000002184 metal Substances 0.000 description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 239000010419 fine particle Substances 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 239000000919 ceramic Substances 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 229910052878 cordierite Inorganic materials 0.000 description 3
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 210000004027 cell Anatomy 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910001961 silver nitrate Inorganic materials 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000012050 conventional carrier Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000011147 inorganic material Substances 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- SYQBFIAQOQZEGI-UHFFFAOYSA-N osmium atom Chemical compound [Os] SYQBFIAQOQZEGI-UHFFFAOYSA-N 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 229910052705 radium Inorganic materials 0.000 description 1
- HCWPIIXVSYCSAN-UHFFFAOYSA-N radium atom Chemical compound [Ra] HCWPIIXVSYCSAN-UHFFFAOYSA-N 0.000 description 1
- RWRDJVNMSZYMDV-UHFFFAOYSA-L radium chloride Chemical compound [Cl-].[Cl-].[Ra+2] RWRDJVNMSZYMDV-UHFFFAOYSA-L 0.000 description 1
- 229910001630 radium chloride Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052701 rubidium Inorganic materials 0.000 description 1
- IGLNJRXAVVLDKE-UHFFFAOYSA-N rubidium atom Chemical compound [Rb] IGLNJRXAVVLDKE-UHFFFAOYSA-N 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust 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
- F01N3/033—Exhaust 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 in combination with other devices
- F01N3/035—Exhaust 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 in combination with other devices with catalytic reactors, e.g. catalysed diesel particulate filters
Abstract
Description
【発明の詳細な説明】
本発明は内燃機関の排出ガス処理用のフィルタに関する
。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a filter for treating exhaust gas from an internal combustion engine.
自動車の内燃機関からの排出ガスが大気中に安全に放出
されるように処理することは環境保全上特に望ましいこ
とである。しかしある種のエンジン、特にディーゼルエ
ンジンにおいては排出ガス気流中に含まれる微粒子の存
在が問題となる。この微粒子はカーボン、炭化水素、金
属等からなシ、特別な運転状態における炭化水素燃料の
不完全燃焼などによって発生する。従来よシ前記微粒子
を除去又は最少にするために種々の技術が提案されてい
る。しかし、従来の技術では前述の微粒子は適切な構成
のフィルタによればある程度良好に除去されるけれども
、微粒子がフィルタに過度に蓄積すると飽和し又は動作
不能になることが判明しておシ、その効果は完全に満足
し得るものということはできない。It is particularly desirable from an environmental standpoint to treat exhaust gases from automobile internal combustion engines so that they can be safely released into the atmosphere. However, in some types of engines, particularly diesel engines, the presence of particulates in the exhaust gas stream is a problem. These particles may be made of carbon, hydrocarbons, metals, etc., and may be generated by incomplete combustion of hydrocarbon fuels under special operating conditions. Conventionally, various techniques have been proposed to remove or minimize the fine particles. However, in the prior art, it has been found that although the aforementioned particulates are reasonably well removed by a properly constructed filter, if the particulates accumulate too much on the filter, it becomes saturated or becomes inoperable. The effect cannot be said to be completely satisfactory.
またある種のフィルタでは二次的に発生する有害成分で
あるサルフェートが大幅に増加し、人体に悪影響を及ぼ
すという欠点があった。In addition, some types of filters have the disadvantage that sulfate, which is a secondary harmful component, increases significantly, which has an adverse effect on the human body.
本発明は以上のような従来技術の問題点に鑑み、微粒子
の排出を長時間安定的に抑制し、かつサルフェートの放
出も少ない、内燃機関の排出ガス浄化用フィルタを提供
することを目的とするものである。SUMMARY OF THE INVENTION In view of the problems of the prior art as described above, an object of the present invention is to provide a filter for purifying exhaust gas of an internal combustion engine, which stably suppresses the emission of particulates over a long period of time and also releases less sulfate. It is something.
そして、本発明は、少なくとも1種類の貴金属に加えて
銀を排出ガス浄化用触媒として用いることを特徴とする
内燃機関の排出ガス浄化用フィルタを提供することによ
って、上記目的を達成する。The present invention achieves the above object by providing a filter for purifying exhaust gas of an internal combustion engine, which uses silver in addition to at least one type of noble metal as a catalyst for purifying exhaust gas.
排出ガス浄化用触媒としては従来から貴金属その他の金
属及びそれらの塩や酸化物等が用いられていたが、本発
明ではそれらの触媒に加えて新しく銀を併用することを
特徴としている。こうして銀を併用すると、原因は必ず
しも明らかではないが、微粒子における可燃性成分の燃
焼温度が相対的に低下し、従って微粒子排出量が減少す
ると共に、二次的なサルフェートの発生量も減少する。Conventionally, precious metals and other metals, their salts, oxides, etc. have been used as exhaust gas purifying catalysts, but the present invention is characterized by the use of silver in addition to these catalysts. In this way, when silver is used in combination, the combustion temperature of combustible components in fine particles is relatively lowered, although the cause is not necessarily clear, and the amount of fine particle emissions is therefore reduced, as well as the amount of secondary sulfate generated.
ここにおいて、「貴金属」とは白金、ノ臂ラジウム、ロ
ジウム、イリジウム、金、ルビジウム、オスミウムなど
を指称し、そして用語「貴金属」及び「銀」は元素状の
金属として存在するそれらのみならずそれらの塩、酸化
物等のすべての原子及びイオンの形で存在するものをも
含む意味で用いている。iた、これら貴金属及び銀は慣
用の触媒担体に担持されてフィルタ材を形成するが、そ
の担持のあシ方は発明の本質上特別の限定はない。As used herein, "noble metals" refers to platinum, radium, rhodium, iridium, gold, rubidium, osmium, etc., and the terms "noble metals" and "silver" refer not only to those that exist as elemental metals, but also to those that exist as elemental metals. This term is used to include all forms of atoms and ions, such as salts and oxides. In addition, these noble metals and silver are supported on a conventional catalyst carrier to form a filter material, but the manner in which they are supported is not particularly limited in view of the essence of the invention.
また担体も例えば発泡状若しくはハニカム状の無機質(
コージェライト、スピネル、アルミナなど)の担体、又
は発泡状若しくは線状金属若しくはそうした金属の表面
に無機質層を形成した担体など慣用のものを用いること
ができる。コージェライト表面に活性アルミナ層を形成
した担体が好ましい。The carrier may also be a foamed or honeycomb-shaped inorganic material (
A conventional carrier such as a carrier (cordierite, spinel, alumina, etc.), a foamed or linear metal, or a carrier with an inorganic layer formed on the surface of such metal can be used. A carrier having an activated alumina layer formed on the surface of cordierite is preferred.
貴金属及び銀の量(ここでは原子又はイオンの量を意味
する。)はフィルタ1を当シ合計502以下であシかつ
それぞれ0.1〜502及び1〜502であることが好
ましく、銀1〜201、貴金属0.1〜3tが最適であ
る。The amount of noble metal and silver (herein means the amount of atoms or ions) in the filter 1 must be 502 or less in total and preferably 0.1 to 502 and 1 to 502, respectively, and silver 1 to 502, respectively. 201, 0.1 to 3 t of noble metal is optimal.
以下、例を用いて本発明ヲ更に詳しく説明する。The present invention will be explained in more detail below using examples.
実施例1
コージェライト製発泡状担体(密度0.3f/i、平均
細孔径0.5wn、容積0.4t)を活性アルミナ50
0重量部、アルミナゾル(pH5、比重1.1、AI、
0310%、その他は水と安定剤としての有機酸である
)350重量部、水135M量部からなるスラリーに浸
漬後、取シ出して余分なスラリーを吹き払い、120℃
で3時間乾燥し、それから、電気炉で800℃にて1時
間焼成し、活性アルミナコート層を形成した。コート量
は20重i−%である。次にそれを蒸留水に浸漬して十
分に吸水させた後白金酸0.4f/L水溶液1tに浸漬
して活性アルミナ層に白金を吸着させ、取シ出して余分
な水分を吹き払い、乾燥後500℃で1時間焼成した。Example 1 A cordierite foam carrier (density 0.3 f/i, average pore diameter 0.5 wn, volume 0.4 t) was coated with activated alumina 50
0 parts by weight, alumina sol (pH 5, specific gravity 1.1, AI,
After immersing the slurry in a slurry consisting of 350 parts by weight of 0310% (the rest being water and an organic acid as a stabilizer) and 135 M parts of water, it was taken out, the excess slurry was blown off, and the mixture was heated to 120°C.
was dried for 3 hours, and then fired in an electric furnace at 800° C. for 1 hour to form an activated alumina coat layer. The coating amount is 20% by weight. Next, it is immersed in distilled water to absorb enough water, then immersed in 1 t of platinic acid 0.4 f/L aqueous solution to adsorb platinum to the activated alumina layer, taken out, blown off excess water, and dried. After that, it was baked at 500°C for 1 hour.
白金の担持量は担体1を当シ12である。The amount of platinum supported is 12 to 1 of the carrier.
次にこれをさらに硝酸銀17wt%溶液1tで含浸させ
、取シ出して120℃で3時間乾燥後600℃で2時間
焼成し、銀担持量が5重量%であるフィルタ材1(第1
図参照)を得た。Next, this was further impregnated with 1 t of a 17 wt% silver nitrate solution, taken out, dried at 120°C for 3 hours, and then fired at 600°C for 2 hours.
(see figure).
実施例2
Si0251重量%、Al、0.35重量%、MgO1
4重it%の化学組成になるように選択した滑石、水酸
化アルミニウム又はアルミナ、及び粘土からなる粉末配
合物を可塑化し、ハニカム状円柱体(100セル/イン
チ3、セル壁厚0.4m、嵩密度0.4f/cd、容積
1t;第2図の左図2参照)に成形し、次に第2同右図
に示したようにその円柱体の端部にセルの一つおきにか
つ両端でそれぞれ一方のみが閉鎖されるように上記と同
じ材料を充填し、乾燥後1400°Cで3時間焼成し、
次に蒸留水に浸漬して十分に吸水させた後、それを塩化
ノ4ラジウム1 f/を水溶液1tに浸漬し、パラジウ
ムを吸着させ、取シ出して余分な水を吹き払い、乾燥後
500℃で1時間焼成した。パラジウム担持量はフィル
タ材1を当シ11である。次にこれをさらに硝酸銀17
wt%水溶液1tに浸漬した後、取シ出して120”C
で3時間乾燥後600℃で2時間焼成し、銀担持量が5
重量%であるフィルタ材2(第2図)を得た。Example 2 Si0251% by weight, Al, 0.35% by weight, MgO1
A powder mixture consisting of talc, aluminum hydroxide or alumina, and clay selected to have a chemical composition of 4 it% was plasticized to form a honeycomb-like cylinder (100 cells/in3, cell wall thickness 0.4 m, The bulk density is 0.4 f/cd, the volume is 1 t; see Figure 2 on the left in Figure 2), and then, as shown in the second Figure on the right, the ends of the cylinder are filled with a cylindrical material at every other cell and at both ends. Filled with the same material as above so that only one side of each was closed, dried and baked at 1400°C for 3 hours,
Next, it was immersed in distilled water to absorb enough water, then immersed in 1 t of an aqueous solution of 1 f/4 radium chloride to adsorb palladium, taken out, blown off excess water, and dried for 500 ml. It was baked at ℃ for 1 hour. The amount of palladium supported was 11 for the filter material 1. Next, add this to 17 silver nitrate
After immersing in 1 ton of wt% aqueous solution, take it out and heat it at 120"C.
After drying for 3 hours at 600°C for 2 hours, the amount of silver supported was 5
Filter material 2 (FIG. 2), which is % by weight, was obtained.
比較例1
白金を担持させた後鍋については担持させなかった点を
除いて、実施例1におけると同様にしてフィルタ材3(
第1図)を得た。Comparative Example 1 Filter material 3 (
Figure 1) was obtained.
比較例2
パラジウムを担持させた後鍋については担持させなかっ
た点を除いて、実施例2におけると同様にしてフィルタ
材4(第2図)を得た。Comparative Example 2 Filter material 4 (FIG. 2) was obtained in the same manner as in Example 2, except that palladium was not supported on the ladle.
試験及びその結果
以上の例において作成したフィルタ材1〜4を第3図に
示したような金属製容器10に第3図下図11で示され
るように配置し、これを実際のディーゼルエンジンの排
気系に装着し、エンジンを2000rpm、6KPf−
zで定常運転し、20時間抜の背圧上列、微粒子捕集率
、サルフェート排出量を測定した。その結果をまとめる
と下表の通シである。Tests and Results The filter materials 1 to 4 prepared in the above examples were placed in a metal container 10 as shown in FIG. 3, as shown in FIG. installed on the system, and the engine was set to 2000 rpm, 6KPf-
It was operated steadily at z, and the back pressure, particulate collection rate, and sulfate emission amount were measured for 20 hours. The results are summarized in the table below.
表
表から明らかなように、貴金属のみを担持した比較例の
フィルタ材では、背圧上昇は少なくて良好であるが、微
粒子捕集率は低く、またサルフェート排出量が異常に多
い。これに対し、貴金属と共に銀を担持した本発明の実
施例では、背圧上昇、サルフェート排出量がいずれも低
く、しかも微粒子捕集率が高く良好である。As is clear from the table, the filter material of the comparative example that supports only noble metals has a good result with a small increase in back pressure, but the particulate collection rate is low and the amount of sulfate discharged is abnormally large. On the other hand, in the example of the present invention in which silver was supported together with the noble metal, both the increase in back pressure and the amount of sulfate discharged were low, and the fine particle collection rate was high and favorable.
本発明に依る内燃機関の排出ガス浄化用フィルタを用い
れば、排出ガス中に含まれる微粒子の可燃性成分を低温
でしかも高能率で燃焼することができるので、40h+
/hr 走行のような通常の運転状態における排出ガス
の熱エネルギーによって前記微粒子を燃焼し、無害化す
ることが可能となシ、しかも二次的に発生するサルフェ
ート量も少なくすることができる。By using the filter for purifying exhaust gas of an internal combustion engine according to the present invention, flammable components of particulates contained in exhaust gas can be combusted at low temperature and with high efficiency.
/hr It is possible to burn the fine particles and render them harmless by using the thermal energy of the exhaust gas under normal operating conditions such as driving, and furthermore, the amount of sulfate generated secondarily can be reduced.
第1図は発泡状セラミックに触媒を担持したフィルタ材
の透視図、第2図はノ・二カム状セラミックに触媒を担
持したフィルタ材の透視図、第3図はフィルタ材を内燃
機関の排気系へ装着するための金属製容器の透視図及び
縦断面図である。
1.3・・・発泡状フィルタ材、2,4・・・ノ・ニカ
ム状フィルタ材、10・・・フィルタ容器、11・・・
フィルタ材。Figure 1 is a perspective view of a filter material in which a catalyst is supported on a foamed ceramic, Figure 2 is a perspective view of a filter material in which a catalyst is supported in a cam-shaped ceramic, and Figure 3 is a perspective view of a filter material in which a catalyst is supported on a cam-shaped ceramic. FIG. 2 is a perspective view and a longitudinal cross-sectional view of a metal container for attachment to a system. 1.3... Foamed filter material, 2, 4... Nicum-like filter material, 10... Filter container, 11...
filter material.
Claims (1)
化用触媒として用いたことを特徴とする、内燃機関の排
出ガス浄化用フィルタ。1. A filter for purifying exhaust gas from an internal combustion engine, characterized in that silver is used as a catalyst for purifying exhaust gas in addition to at least one kind of noble metal.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57013311A JPS58131123A (en) | 1982-02-01 | 1982-02-01 | Filter for purifying exhaust gas in internal combustion engine |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57013311A JPS58131123A (en) | 1982-02-01 | 1982-02-01 | Filter for purifying exhaust gas in internal combustion engine |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58131123A true JPS58131123A (en) | 1983-08-04 |
Family
ID=11829620
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57013311A Pending JPS58131123A (en) | 1982-02-01 | 1982-02-01 | Filter for purifying exhaust gas in internal combustion engine |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58131123A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59148254U (en) * | 1983-03-25 | 1984-10-03 | 本田技研工業株式会社 | Multi-burnishing processing equipment |
JPS6298718U (en) * | 1985-12-13 | 1987-06-23 | ||
JP2007296518A (en) * | 2006-04-07 | 2007-11-15 | Honda Motor Co Ltd | Catalyst and device for cleaning exhaust gas |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4934474A (en) * | 1972-08-02 | 1974-03-29 | ||
JPS5061373A (en) * | 1973-10-03 | 1975-05-26 | ||
JPS5078588A (en) * | 1973-11-14 | 1975-06-26 | ||
JPS52116779A (en) * | 1976-03-18 | 1977-09-30 | Johnson Matthey Co Ltd | Gas treating method |
JPS5337194A (en) * | 1976-09-17 | 1978-04-06 | Iwasaki Yasutada | Exhaust gas scrubbing metall catalysts |
JPS5347392A (en) * | 1976-10-13 | 1978-04-27 | Matsushita Electric Ind Co Ltd | Catalyst for purification of exhaust gas |
JPS5640433A (en) * | 1979-09-10 | 1981-04-16 | Agency Of Ind Science & Technol | Ternary oxide catalyst for catalytic combustion of carbon monoxide and hydrocarbon |
-
1982
- 1982-02-01 JP JP57013311A patent/JPS58131123A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4934474A (en) * | 1972-08-02 | 1974-03-29 | ||
JPS5061373A (en) * | 1973-10-03 | 1975-05-26 | ||
JPS5078588A (en) * | 1973-11-14 | 1975-06-26 | ||
JPS52116779A (en) * | 1976-03-18 | 1977-09-30 | Johnson Matthey Co Ltd | Gas treating method |
JPS5337194A (en) * | 1976-09-17 | 1978-04-06 | Iwasaki Yasutada | Exhaust gas scrubbing metall catalysts |
JPS5347392A (en) * | 1976-10-13 | 1978-04-27 | Matsushita Electric Ind Co Ltd | Catalyst for purification of exhaust gas |
JPS5640433A (en) * | 1979-09-10 | 1981-04-16 | Agency Of Ind Science & Technol | Ternary oxide catalyst for catalytic combustion of carbon monoxide and hydrocarbon |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS59148254U (en) * | 1983-03-25 | 1984-10-03 | 本田技研工業株式会社 | Multi-burnishing processing equipment |
JPS6237632Y2 (en) * | 1983-03-25 | 1987-09-25 | ||
JPS6298718U (en) * | 1985-12-13 | 1987-06-23 | ||
JPH0420971Y2 (en) * | 1985-12-13 | 1992-05-13 | ||
JP2007296518A (en) * | 2006-04-07 | 2007-11-15 | Honda Motor Co Ltd | Catalyst and device for cleaning exhaust gas |
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