JPS62140646A - Catalytic body for purifying exhaust gas - Google Patents
Catalytic body for purifying exhaust gasInfo
- Publication number
- JPS62140646A JPS62140646A JP60283438A JP28343885A JPS62140646A JP S62140646 A JPS62140646 A JP S62140646A JP 60283438 A JP60283438 A JP 60283438A JP 28343885 A JP28343885 A JP 28343885A JP S62140646 A JPS62140646 A JP S62140646A
- Authority
- JP
- Japan
- Prior art keywords
- palladium
- exhaust gas
- oxide
- lanthanide oxide
- lanthanide
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
本発明は排ガス中に含まれる一酸化炭素、炭火水素およ
び二酸化窒素等を、より無害な物質に浄化する触媒体に
関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a catalyst body that purifies carbon monoxide, hydrocarbons, nitrogen dioxide, etc. contained in exhaust gas into more harmless substances.
従来の技術
石油、ガス、固形燃料等の燃焼機器からの排ガス中には
、炭化水素のような臭いの元となる物質や、−酸化炭素
、二酸化窒素のような人体に有害な物質が含まれており
、住環境や大気汚染防止の意味から、これらの有害物質
の発生の少ない燃焼機器が強く要望されている。その一
つの手段として、アルミン酸石灰、二酸化ケイ素、二酸
化チタンから成るセラミック多孔体にパラジウムとラン
タニド酸化物とを担持させた触媒体を、燃焼排ガス流路
に設置して、排ガス中の一酸化炭素や二酸化窒素を浄化
する方法がある。Conventional technology Exhaust gas from combustion equipment such as oil, gas, and solid fuels contains substances that cause odors, such as hydrocarbons, and substances that are harmful to the human body, such as carbon oxide and nitrogen dioxide. In view of the living environment and the prevention of air pollution, there is a strong demand for combustion equipment that generates fewer harmful substances. As one method, a catalyst body in which palladium and lanthanide oxides are supported on a ceramic porous body made of lime aluminate, silicon dioxide, and titanium dioxide is installed in the combustion exhaust gas flow path, and carbon monoxide in the exhaust gas is There are ways to purify nitrogen dioxide.
発明が解決しようとする問題点
しかしこのような触媒体は、パラジウムとランタニド酸
化物の混合割合が変化することにより、−酸化炭素と二
酸化窒素の浄化能が低くなるという問題点があった。Problems to be Solved by the Invention However, such catalysts have a problem in that their ability to purify carbon oxide and nitrogen dioxide decreases due to changes in the mixing ratio of palladium and lanthanide oxides.
本発明はこのような問題点を解決するもので、触媒体の
組成を改良することを目的とするものである。The present invention aims to solve these problems and aims to improve the composition of the catalyst body.
問題点を解決するだめの手段
この問題点を解決するために、本発明はアルミン酸石灰
、二酸化ケイ素、二酸化チタンなどからなるセラミック
多孔体に、触媒としてランタニド酸化物とパラジウムを
担持させ、このランタニド酸化物/パラジウムの混合比
を重量比で5〜50の範囲としたものである。Means to Solve the Problem In order to solve this problem, the present invention supports a ceramic porous body made of lime aluminate, silicon dioxide, titanium dioxide, etc. as a catalyst, and supports this lanthanide oxide and palladium. The oxide/palladium mixing ratio is in the range of 5 to 50 by weight.
作 用
二酸化窒素浄化能はランタニド酸化物/パラジウムの混
合割合の増大と共に高くなり平衡値に近づく。しかしな
からランタニド酸化物は一酸化炭素の浄化触媒としての
働きをほとんど持っていない。このためランタニド酸化
物の混合割合が増大すると、パラジウムの表面がおおわ
れるため、−酸化炭素浄化能か低下する。ランタニド酸
化物/パラジウムの混合割合が5〜50であれば、二酸
化窒素と一酸化炭素の両方について高い浄化率を得るこ
とができる。Function: The nitrogen dioxide purification ability increases as the lanthanide oxide/palladium mixing ratio increases and approaches an equilibrium value. However, lanthanide oxides have almost no function as carbon monoxide purification catalysts. For this reason, when the mixing ratio of lanthanide oxide increases, the surface of palladium is covered, and the -carbon oxide purification ability decreases. If the mixing ratio of lanthanide oxide/palladium is 5 to 50, a high purification rate can be obtained for both nitrogen dioxide and carbon monoxide.
実施例 以下本発明の実施例を図面により詳細に説明する。Example Embodiments of the present invention will be described in detail below with reference to the drawings.
実施例1
アルミン酸石灰40M量部、二酸化ケイ素4゜重量部、
二酸化チタン20重量部に成形助剤としてカルボキシメ
チルセルロース6重量部を加えて混合する。この混合粉
体に対して26重量部の水を加えて混練して得た材料を
、ダイスを用いて押し出し成形し、固化、養生、乾燥を
経てセラミック多孔体の担体を得た。この担体をパラジ
ウム塩とセリウム塩の混合水溶液に10秒間浸漬するこ
とにより、パラジウムを担体の見かけ体積当り0.1y
/fl担持きせ、1000’Cで熱処理を施した。Example 1 40M parts of lime aluminate, 4 parts by weight of silicon dioxide,
6 parts by weight of carboxymethyl cellulose as a molding aid is added to 20 parts by weight of titanium dioxide and mixed. A material obtained by adding and kneading 26 parts by weight of water to this mixed powder was extruded using a die, solidified, cured, and dried to obtain a porous ceramic carrier. By immersing this carrier in a mixed aqueous solution of palladium salt and cerium salt for 10 seconds, palladium was added to 0.1y per apparent volume of the carrier.
/fl was supported and heat treated at 1000'C.
実施例2
実施例1と同一の担体にパラジウムo、1y7p、、セ
リウム酸化物o、2y/fl担持させ、10oo′Cで
熱処理を施した。Example 2 Palladium o, 1y7p, and cerium oxide o, 2y/fl were supported on the same carrier as in Example 1, and heat treated at 10oo'C.
実施例3
実施例1と同一の担体にパラジウムo、1y/It、セ
リウム酸化物o、5y/12担持させ、1ooo′Cで
熱処理を施した。Example 3 Palladium o, 1y/It and cerium oxide o, 5y/12 were supported on the same carrier as in Example 1, and heat treated at 1ooo'C.
実施例4
実施例1と同一の担体にパラジウムo、1y/II、セ
リウム酸化物1.oy/fl担持させ、1000°Cで
熱処理を施した。Example 4 Palladium o, 1y/II, cerium oxide 1. oy/fl was supported and heat treated at 1000°C.
実施例5
実施例1と同一の担体にパラジウムOAy/It、セリ
ウム酸化物3.Of/β担持させ、10oO′Cで熱処
理を施した。Example 5 Palladium OAy/It and cerium oxide 3. Of/β was supported and heat treated at 100O'C.
実施例6
実施例1と同一の担体にパラジウム0.1y/1.、セ
リウム酸化物5.oy/n担持させ、1000’Of熱
処理を施した。Example 6 The same carrier as in Example 1 was coated with palladium 0.1y/1. , cerium oxide5. oy/n was supported and subjected to 1000'Of heat treatment.
実施例7
実施例1と同一の担体にパラジウムo、1y /λ、セ
リウム酸化物7.oy/f)、担持させ、1000’C
で熱処理を施した。Example 7 Palladium o, 1y /λ and cerium oxide 7. were added to the same carrier as in Example 1. oy/f), supported, 1000'C
Heat treatment was performed.
実施例8
実施例1と同一の担体にパラジウムo、1y/fl、セ
リウム酸化物1o、09t/J2担持させ、1000’
Cで熱処理を施した。Example 8 Palladium o, 1y/fl and cerium oxide 1o, 09t/J2 were supported on the same carrier as in Example 1, 1000'
Heat treatment was performed at C.
上記8種の触媒体を調製し、それらについて300°C
における一酸化炭素浄化能と二酸化窒素浄化能を測定し
た。測定条件を表1に、その結果を図に示す。The above 8 types of catalyst bodies were prepared and heated to 300°C.
The carbon monoxide purification ability and nitrogen dioxide purification ability were measured. The measurement conditions are shown in Table 1, and the results are shown in the figure.
表 1 浄化能測定条件
二酸化窒素浄化率1はセリウム酸化物の混合割合が増す
につれて大きくなるが、パラジウムとの混合割合が5以
上ではほとんど変わらなくなる。一方、−酸化炭素浄化
率2は、パラジウムとの混合割合が60以下ではほぼ一
定の値を示すが、5゜を越えると急激に低下する。二酸
化窒素の浄化率の場合、パラジウム、セリウム酸化物の
両方とも低温において二酸化窒素浄化能を有している。Table 1 Purification performance measurement conditions Nitrogen dioxide purification rate 1 increases as the mixing ratio of cerium oxide increases, but it hardly changes when the mixing ratio with palladium is 5 or more. On the other hand, the -carbon oxide purification rate 2 shows a nearly constant value when the mixing ratio with palladium is 60 degrees or less, but sharply decreases when it exceeds 5 degrees. In the case of nitrogen dioxide purification efficiency, both palladium and cerium oxide have nitrogen dioxide purification ability at low temperatures.
両者を混合すると何らかの相乗作用により二酸化窒素浄
化能が増大するものと考えられる。−酸化炭素の浄化能
においてパラジウムは触媒能を有するが、セリウム酸化
物はほとんど触媒能を持っていない。従ってセリウム酸
化物の混合割合が50以上では、セリウム酸化物がパラ
ジウム粒子の表面をおおうようになり、浄化能が急激に
低下してくるものと考えられる。It is thought that when the two are mixed, the nitrogen dioxide purifying ability increases due to some synergistic effect. - Palladium has a catalytic ability to purify carbon oxide, but cerium oxide has almost no catalytic ability. Therefore, it is considered that when the mixing ratio of cerium oxide is 50 or more, the cerium oxide comes to cover the surface of the palladium particles, and the purification ability decreases rapidly.
以上はパラジウムとセリウム酸化物の系ンでついて述べ
たが、パラジウムとランタン酸化物の系についても、は
ぼ同様な傾向がみられた。The above was described for the system of palladium and cerium oxide, but a similar tendency was observed for the system of palladium and lanthanum oxide.
発明の効果
以上のように本発明によれば、ランタニド酸化物/パラ
ジウムの混合割合を5〜50の範囲に設定することによ
り二酸化窒素と一酸化炭素の両者に対し、高い浄化能を
有する触媒体を提供するものである。Effects of the Invention As described above, according to the present invention, by setting the mixing ratio of lanthanide oxide/palladium in the range of 5 to 50, a catalyst body having high purifying ability for both nitrogen dioxide and carbon monoxide can be obtained. It provides:
図はセリウム酸化物とパラジウムの混合割合を変えた触
媒体の、二酸化窒素と一酸化炭素の浄化率を示す図であ
る。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名混合
割合The figure shows the nitrogen dioxide and carbon monoxide purification rates of catalyst bodies with different mixing ratios of cerium oxide and palladium. Name of agent: Patent attorney Toshio Nakao and one other person
Claims (1)
ジウムを担持させ、ランタニド酸化物/パラジウムの混
合比を重量比で5〜50とした排ガス浄化用触媒体。A catalyst body for exhaust gas purification in which a porous ceramic body supports lanthanide oxide and palladium as a catalyst, and the mixture ratio of lanthanide oxide/palladium is 5 to 50 by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60283438A JPS62140646A (en) | 1985-12-17 | 1985-12-17 | Catalytic body for purifying exhaust gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60283438A JPS62140646A (en) | 1985-12-17 | 1985-12-17 | Catalytic body for purifying exhaust gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS62140646A true JPS62140646A (en) | 1987-06-24 |
Family
ID=17665545
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60283438A Pending JPS62140646A (en) | 1985-12-17 | 1985-12-17 | Catalytic body for purifying exhaust gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS62140646A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5378142A (en) * | 1991-04-12 | 1995-01-03 | Engelhard Corporation | Combustion process using catalysts containing binary oxides |
US5474441A (en) * | 1989-08-22 | 1995-12-12 | Engelhard Corporation | Catalyst configuration for catalytic combustion systems |
EP1008995A1 (en) * | 1998-12-12 | 2000-06-14 | Eurotope Entwicklungsgesellschaft für Isotopentechnologien mbH | Medical radioactive palladium-103 miniature radiation sources and methods of producing same |
-
1985
- 1985-12-17 JP JP60283438A patent/JPS62140646A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5474441A (en) * | 1989-08-22 | 1995-12-12 | Engelhard Corporation | Catalyst configuration for catalytic combustion systems |
US5378142A (en) * | 1991-04-12 | 1995-01-03 | Engelhard Corporation | Combustion process using catalysts containing binary oxides |
US5750458A (en) * | 1991-04-12 | 1998-05-12 | Kennelly; Teresa | Combustion catalysts containing binary oxides and processes using the same |
US5863851A (en) * | 1991-04-12 | 1999-01-26 | Engelhard Corporation | Combustion catalysts containing binary oxides and processes using the same |
EP1008995A1 (en) * | 1998-12-12 | 2000-06-14 | Eurotope Entwicklungsgesellschaft für Isotopentechnologien mbH | Medical radioactive palladium-103 miniature radiation sources and methods of producing same |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP3440290B2 (en) | Exhaust gas purification method | |
JP5815232B2 (en) | Selective catalytic reduction of nitrogen oxides in exhaust gas from diesel engines | |
JP2010519039A (en) | Bifunctional catalysts for selective ammonia oxidation | |
RU2010152011A (en) | DEVICE FOR REDUCING THE TOXICITY OF EXHAUST GASES OF THE DIESEL ENGINE | |
JP2006289211A (en) | Ammonia oxidation catalyst | |
US4710487A (en) | Diesel exhaust gas catalyst | |
US10408102B2 (en) | Oxidation catalyst device for exhaust gas purification | |
JPH03196837A (en) | Carrier for trifunctional catalyst containing platinum group metal for purifying exhaust gas of internal combustion engine | |
KR20010043862A (en) | Method for cleaning diesel engine exhaust gas | |
JPS62140646A (en) | Catalytic body for purifying exhaust gas | |
JP2004188388A (en) | Filter for cleaning diesel exhaust gas and its production method | |
JPH10118457A (en) | Exhaust gas cleaning apparatus for internal combustion engine | |
JPS637826A (en) | Removing method for nitrous oxide in gas mixture | |
CN1040953C (en) | Catalyst for purification of nitrogen oxides | |
JPH10109032A (en) | Exhaust gas purification catalyst for internal combustion engine | |
JPS6227041A (en) | Production of catalytic body for cleaning up of waste gas | |
JPS5820307B2 (en) | Catalyst for vehicle exhaust gas purification | |
JPH0615173A (en) | Gas purifying catalyst and gas purifying method | |
JPH0435744A (en) | Catalytic body for purification of exhaust gas | |
JP3925015B2 (en) | Internal combustion engine exhaust gas purification device, purification method, and purification catalyst | |
JPH06319949A (en) | Apparatus for treating exhaust gas | |
JPS6047449B2 (en) | Exhaust gas purification method | |
JPH06319948A (en) | Apparatus for treating exhaust gas | |
JPH07275709A (en) | Material and method for purifying exhaust gas | |
JPS63107749A (en) | Catalyst carrier for purifying exhaust gas |