JPS61234948A - Catalyst body - Google Patents

Catalyst body

Info

Publication number
JPS61234948A
JPS61234948A JP60076927A JP7692785A JPS61234948A JP S61234948 A JPS61234948 A JP S61234948A JP 60076927 A JP60076927 A JP 60076927A JP 7692785 A JP7692785 A JP 7692785A JP S61234948 A JPS61234948 A JP S61234948A
Authority
JP
Japan
Prior art keywords
black
catalyst
powder
perovskite
raw material
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.)
Granted
Application number
JP60076927A
Other languages
Japanese (ja)
Other versions
JPH0347145B2 (en
Inventor
Ikuo Matsumoto
松本 郁夫
Kenji Tabata
研二 田畑
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP60076927A priority Critical patent/JPS61234948A/en
Publication of JPS61234948A publication Critical patent/JPS61234948A/en
Publication of JPH0347145B2 publication Critical patent/JPH0347145B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Abstract

PURPOSE:To blacken preliminarily a carrier itself by kneading previously the fine powder of a black transition metallic oxide with the powder of ceramic raw material, thereafter calcining the mixture to obtain a honeycomb type and furthermore depositing the black perovskite powder thereon. CONSTITUTION:In relation to a catalyst for purifying an exhaust gas which is provided to the inside of a combustion apparatus, the fine powder of a black transition metallic oxide is previously kneaded with the powder of a ceramic raw material being the raw material of a honeycomb structural body. After calcining the mixture to obtain a honeycomb type, a carrier 1 is immersed in a slurry-like liquid wherein the fine particles 5 of a perovskite composite oxide having the oxidation activity, colloidal alumina and a deposition aid such as Al(NO3)3 are mixed with water, dried and calcined. By such a way, even when the perovskite fine powder of the surface is separated, it is not unsightly in a fine view because the structure has the same color and the catalyst capacity is largely increased.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は燃焼の際発生する不完全燃焼成分、未焼成分あ
るいは各種調理の際発生する臭気の原因である炭化7X
素成を取シ除くため燃焼機器内に設けた排気ガス浄化触
媒に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is directed to carbonized 7X, which is the cause of incomplete combustion components and unburned components generated during combustion, and odors generated during various cooking processes.
This invention relates to an exhaust gas purification catalyst installed in combustion equipment to remove elemental components.

従来の技術 従来この種の触媒には各種のものが存在していた。すな
わちその中で最も一般的な白金族金属を担持している触
媒体は多孔質のセラミック担体に塩化白金酸水溶液の様
な白金族金属を含んだ水溶液を含浸させ、それを乾燥、
焼成させて担体細孔内の表面に金属微粒子としであるい
は金属酸化物微粒子として付着させたものである。白金
族触媒は活性は良いが、コストが非常に高いのが欠点で
ある。遷移金属酸化物あるいは遷移金属を一部取り込ん
だペロプスカイト複合酸化物は、その粒径を非常に小さ
くすれば白金数みの活性を持つことは公知であるが、単
独の遷移金属酸化物は高温に不安定で、活性劣化につな
がるのに対し、ある種のペロブスカイト構造を持った複
合酸化物は活性も相当にあシ、また耐熱性も有する。従
ってこれらペロゲスカイト化合物の微粉末を担体に付着
させれば優れた触媒体になるが、付着させた微粉末はど
うしても強度が弱く一部脱落しやすい。脱落するのはほ
んの一部で活性劣化に及ぼす影響は少ないが、黒色の多
いペロブスカイト化合物が脱落した後、白色の担体地肌
がむき出しになり美観的に好ましくない。特に家庭用燃
焼機器にはこの問題点を解決する必要がある。
BACKGROUND OF THE INVENTION Various types of catalysts of this type have existed in the past. Specifically, the most common catalyst supporting platinum group metals is a porous ceramic carrier impregnated with an aqueous solution containing a platinum group metal, such as an aqueous solution of chloroplatinic acid, and then dried.
It is baked and attached to the surface of the pores of the carrier as fine metal particles or fine metal oxide particles. Although platinum group catalysts have good activity, their disadvantage is that they are very expensive. It is known that transition metal oxides or perovskite composite oxides incorporating a portion of transition metals have an activity comparable to that of platinum if the particle size is made very small. However, some complex oxides with a perovskite structure have considerably low activity and are also heat resistant. Therefore, if fine powder of these perogeskite compounds is adhered to a carrier, it becomes an excellent catalyst, but the adhered fine powder is inevitably weak in strength and tends to partially fall off. Only a small portion of the perovskite compound falls off, which has little effect on activity deterioration, but after the perovskite compound, which is mostly black, falls off, the white carrier surface becomes exposed, which is aesthetically undesirable. In particular, it is necessary to solve this problem for household combustion equipment.

発明が解決しようとする問題点 この様に従来の担体はほとんど白色あるいは白色に近い
色であり、付着していた黒色粉末が脱落した場合どうし
ても目立ってしまう。本発明はかかる点に鑑みてなされ
たもので担体自身をあらかじめ黒色、あるいは黒色に近
い色にさせることを目的としている。
Problems to be Solved by the Invention As described above, conventional carriers are almost white or nearly white in color, and when the attached black powder falls off, it becomes noticeable. The present invention has been made in view of this point, and an object of the present invention is to make the carrier itself black or a color close to black in advance.

問題点を解決するための手段 本発明は上記問題点を解決するためハニカム構造体の触
媒担体を作成する段階において、ハニカム構造体の原料
である各種のセラミック原料の粉末に黒色の遷移金属酸
化物の微粉末をあらかじめ混練させておき、ハニカム型
に焼成させる。その結果出来た触媒担体は黒色をしてお
り、触媒体はその触媒担体の土にペロブスカイト黒色粉
末を担持したものである。
Means for Solving the Problems The present invention solves the above problems by adding a black transition metal oxide to powders of various ceramic raw materials, which are the raw materials for the honeycomb structure, at the stage of creating a catalyst carrier for the honeycomb structure. The fine powder is kneaded in advance and fired into a honeycomb mold. The resulting catalyst carrier is black in color, and the catalyst body is made by supporting the perovskite black powder on the soil of the catalyst carrier.

作  用 本発明は上記した構成によシ担持された触媒粉末が多少
欠落しても、外観的には全く異常が認められない。また
触媒担体内に遷移金属酸化物を混入させることにより、
混入させない触媒担体と比較して、触媒酸化能力を大き
く増大させることができる。
Function The present invention has the above-described structure, and even if some of the supported catalyst powder is missing, no abnormality is observed in appearance. In addition, by mixing transition metal oxides into the catalyst carrier,
The catalytic oxidation capacity can be greatly increased compared to a catalyst carrier that is not mixed.

実施例 第1図は本発明の触媒体の一実施例を示すモデル図であ
る。第1図において1は触媒担体、2は触媒担体1内に
存在する微小細孔で、3は触媒担体1内部に混入されて
いる遷移金属酸化物4である。触媒担体1外表面4には
ペロブスカイト複合酸化物5を担持助剤の焼成によって
できるアルミナ6によって強固に付着されている。担持
助剤はコロイダルアルミナや硝酸アルミニウムなど焼成
することによって多孔質で強固な接着性を有するものを
用いている。
Embodiment FIG. 1 is a model diagram showing an embodiment of the catalyst body of the present invention. In FIG. 1, 1 is a catalyst carrier, 2 is a micropore existing in the catalyst carrier 1, and 3 is a transition metal oxide 4 mixed inside the catalyst carrier 1. A perovskite composite oxide 5 is firmly adhered to the outer surface 4 of the catalyst carrier 1 with alumina 6 produced by firing a supporting agent. As the supporting agent, a material such as colloidal alumina or aluminum nitrate, which becomes porous and has strong adhesive properties by firing, is used.

上記の構成において触媒体の表面が何等かの機械的な衝
撃あるいは接触で付着されているペロプスカイト複合酸
化物5とアルミナ6の皮膜の一部が欠落しても、その下
の地肌が黒色であるだめの外見的には全く変ることがな
い。
In the above structure, even if a part of the film of perovskite composite oxide 5 and alumina 6 attached to the surface of the catalyst body is missing due to some mechanical impact or contact, the underlying surface will remain black. Arudame's appearance never changes at all.

以下本触媒の作成法の一例を述べる。An example of the method for producing this catalyst will be described below.

触媒担体は担体材料であるコーディエライト(2Mg0
 ・58i02 ・2A6203)粉末と二酸化マンガ
ン(Mn02)、四三酸化コバルト(Co304)、四
三酸化鉄(F e 304 )の各微粉末を100:1
:1:2の割合で混合させ、さらに気孔率を上げるため
、若干の有機物を加え、ハニカム状に成形し、焼成した
ものを触媒担体とした。また一方ベロブスカイト複合酸
化物の微粒子(La□、g Co□、I Co03)、
硝酸アルミニウム(A4(N03)3・9H2o)を2
:1の割合で混合させ、水を加えスラリー状にする。
The catalyst carrier is made of cordierite (2Mg0
・58i02 ・2A6203) powder and each fine powder of manganese dioxide (Mn02), tricobalt tetroxide (Co304), and triiron tetroxide (F e 304 ) at a ratio of 100:1.
: They were mixed at a ratio of 1:2, and in order to further increase the porosity, some organic matter was added, formed into a honeycomb shape, and fired, which was used as a catalyst carrier. On the other hand, fine particles of berovskite composite oxide (La□, g Co□, I Co03),
Aluminum nitrate (A4(N03)3.9H2o) 2
: Mix at a ratio of 1:1 and add water to make a slurry.

さらにスラリーを安定なものにさせるためCMC1PV
Aを若干加え所定の粘度に調整したものの中に先述した
ハニカム状の触媒担体を浸す。浸した触媒担体を取シ出
し、七p内に留ったスラリー液を風圧で吹き飛ばし、1
00’C:で約1hr乾燥した後、800℃で5m1n
〜10m1n焼成を行なう。
Furthermore, to make the slurry more stable, CMC1PV
The above-mentioned honeycomb-shaped catalyst carrier is immersed in the mixture, which has been adjusted to a predetermined viscosity by adding a small amount of A. Take out the soaked catalyst carrier, blow off the slurry liquid remaining in the 7p with wind pressure, and
After drying at 00'C for about 1 hour, drying at 800℃ for 5ml
~10 ml of firing is performed.

第2図は本発明の触媒体の一応用例でガス調理器内に触
媒体を搭載した例である。
FIG. 2 is an example of the application of the catalyst of the present invention, in which the catalyst is mounted in a gas cooker.

ハニカム形状をした触媒体7を調理器庫内8の上方にあ
る排気ガス出口9に設置させである。調理器庫内8の天
面には金網発熱体10を置き、ガスバーナ11によシ赤
熱させるようになっている。
A catalyst body 7 having a honeycomb shape is installed at an exhaust gas outlet 9 above an interior 8 of the cooking appliance. A wire mesh heating element 10 is placed on the top surface of the cooking chamber interior 8, and is heated to red heat by a gas burner 11.

さらに調理器庫内8下部には調理物12を置くための置
き台13、調理物12からの油を受ける受は皿14等が
設置されている。
Further, at the lower part of the interior 8 of the cooker, a stand 13 for placing food 12 to be cooked, a tray 14 for receiving oil from the food 12, etc. are installed.

上記の調理器において調理物12を置き台12の上に置
きガスバーナ11に点火させ、金網発熱体10を赤熱さ
せ、これから発生する輻射線及び、熱排気ガスにより調
理物12を調理する。この際調理物から発生する臭気を
含む炭化水素はガスバ−す11から発生する排気ガスと
共に排気ガス出口9に設置されている触媒体9を通過し
、炭化水素は浄化される。
In the above cooking device, the food 12 is placed on the table 12, the gas burner 11 is ignited, the wire mesh heating element 10 is made red hot, and the food 12 is cooked by the radiation and hot exhaust gas generated. At this time, odor-containing hydrocarbons generated from the food being cooked pass through the catalyst body 9 installed at the exhaust gas outlet 9 together with the exhaust gas generated from the gas bath 11, and the hydrocarbons are purified.

発明の効果 (1)微粉末の付着形の触媒であるので、表面に担持さ
れているペロプスカイト微粉末が脱離しても、地肌が同
色であるため美観的に見苦しくなく、特如家庭用燃焼器
内に用いるには最適である。
Effects of the invention (1) Since it is a catalyst in the form of a deposit of fine powder, even if the fine perovskite powder supported on the surface is detached, the background remains the same color, so it is not aesthetically unsightly, making it particularly suitable for household combustion. Ideal for use inside a vessel.

(2)本発明の触媒体は触媒担体内に遷移金属酸化物微
粒子を混入させて黒化させるため、黒化させない触媒担
体を用いた触媒体に比較して、触媒能力を大きく増大さ
せることができる。
(2) Since the catalyst body of the present invention blackens by mixing transition metal oxide fine particles into the catalyst carrier, it is possible to greatly increase the catalytic performance compared to a catalyst body using a catalyst carrier that does not blacken. can.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例である触媒体の縦断面図、第
2図は同触媒体を調理器に用いた縦断面図である。 1・・・・・・触媒担体、2・・・・・・微小細孔、3
・・・・・・遷移金属酸化物微粒子、6・・・・・・ペ
ロブスカイト複合酸化物、6・・・・・・アルミナ。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名j−
へp17メシ6イト ! 第2図 /ψ     13
FIG. 1 is a longitudinal sectional view of a catalyst body according to an embodiment of the present invention, and FIG. 2 is a longitudinal sectional view of the same catalyst body used in a cooking appliance. 1... Catalyst carrier, 2... Micropore, 3
...Transition metal oxide fine particles, 6...Perovskite composite oxide, 6...Alumina. Name of agent: Patent attorney Toshio Nakao and one other person
Hep17 Meshi 6ite! Figure 2/ψ 13

Claims (2)

【特許請求の範囲】[Claims] (1)内部に微小細孔を有した黒色あるいは灰色や濃茶
色など濃い有色の耐熱性セラミック材料からなるハニカ
ム構造体を触媒担体となし、この触媒担体を酸化活性を
有するペロブスカイト複合酸化物の微粒子、及びコロイ
ダルアルミナ、硝酸アルミニウムなど焼成することによ
って多孔質で強固な接着性を有する担持助剤を水と混合
したスラリー状液の中に浸し、乾燥、焼成した触媒体。
(1) A honeycomb structure made of a heat-resistant ceramic material with a deep color such as black, gray, or dark brown that has micropores inside is used as a catalyst carrier, and this catalyst carrier is used as fine particles of perovskite composite oxide having oxidizing activity. , and a catalyst body obtained by soaking a supporting agent such as colloidal alumina or aluminum nitrate, which becomes porous and has strong adhesive properties upon firing, in a slurry liquid mixed with water, drying, and firing.
(2)有色の耐熱性セラミック材料からなるハニカム構
造体はコーディエライト、γ及びαアルミナ、ムライト
、ジルコニア、ムライト−ジルコン、アルミニウムチタ
ネート、ペタライトなどの原料粉末とマンガン、コバル
ト、鉄など酸化物が黒色あるいはそれに近い有色を程す
る酸化物を混合させハニカム形に焼成した特許請求の範
囲第1項記載の触媒体。
(2) Honeycomb structures made of colored heat-resistant ceramic materials are made of raw material powders such as cordierite, gamma and alpha alumina, mullite, zirconia, mullite-zircon, aluminum titanate, and petalite, and oxides such as manganese, cobalt, and iron. The catalyst body according to claim 1, wherein an oxide having a black color or a color close to black is mixed and fired in a honeycomb shape.
JP60076927A 1985-04-11 1985-04-11 Catalyst body Granted JPS61234948A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60076927A JPS61234948A (en) 1985-04-11 1985-04-11 Catalyst body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60076927A JPS61234948A (en) 1985-04-11 1985-04-11 Catalyst body

Publications (2)

Publication Number Publication Date
JPS61234948A true JPS61234948A (en) 1986-10-20
JPH0347145B2 JPH0347145B2 (en) 1991-07-18

Family

ID=13619350

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60076927A Granted JPS61234948A (en) 1985-04-11 1985-04-11 Catalyst body

Country Status (1)

Country Link
JP (1) JPS61234948A (en)

Also Published As

Publication number Publication date
JPH0347145B2 (en) 1991-07-18

Similar Documents

Publication Publication Date Title
CA2042664C (en) Catalytic composite for purifying exhaust gases and a method for preparing the same
JPS61283348A (en) Oxidizing catalyst
JP3736242B2 (en) Exhaust gas purification material and method for producing the same
WO2023020495A1 (en) Monolithic cdpf composite material for diesel vehicle and preparation method therefor
CN110327968A (en) A kind of catalyst and preparation method thereof of purifying volatile organic matter
JPH02174937A (en) Molecular sieve on carrier- palladium-platinum catalyst
US5922294A (en) High surface area, thermally stabilized titania automotive catalyst support
JPH02187148A (en) Catalyst for decomposing ozone
JPH08131830A (en) Catalyst for purification of exhaust gas
JPH0616853B2 (en) Non-precious metal combustion catalyst and method for producing the same
CN101632926B (en) Exhaust gas catalysts and exhaust-gas catalytic converter
JPS61234948A (en) Catalyst body
JPH05168950A (en) Combustion exhaust gas purification catalyst
JPS61249540A (en) Catalyst
JPS6054736A (en) Oxidation catalyst
CN107288713A (en) The coating processes of environment-friendly type exhaust gas filter and honeycomb substrate
JPS61234947A (en) Catalyst body
JP4696392B2 (en) Exhaust gas purification catalyst and exhaust gas purification material using the same
JPH01142208A (en) Filter for collecting diesel particulate
JPS6260937B2 (en)
JPH04104838A (en) Waste gas purifying catalytic body
JPH04145946A (en) Catalyst for purification of exhaust gas
JPH02164456A (en) Gas purifying material
JPS61242640A (en) Oxidation catalyst
JPH04122455A (en) Exhaust gas purification catalyst body

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term