JPS60166038A - Manufacture of oxidizing catalyst for catalytic combustion - Google Patents

Manufacture of oxidizing catalyst for catalytic combustion

Info

Publication number
JPS60166038A
JPS60166038A JP59020207A JP2020784A JPS60166038A JP S60166038 A JPS60166038 A JP S60166038A JP 59020207 A JP59020207 A JP 59020207A JP 2020784 A JP2020784 A JP 2020784A JP S60166038 A JPS60166038 A JP S60166038A
Authority
JP
Japan
Prior art keywords
activated carbon
elements
oxidizing catalyst
range
catalytic 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.)
Granted
Application number
JP59020207A
Other languages
Japanese (ja)
Other versions
JPH0346176B2 (en
Inventor
Kenji Tabata
研二 田畑
Ikuo Matsumoto
松本 郁夫
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 JP59020207A priority Critical patent/JPS60166038A/en
Publication of JPS60166038A publication Critical patent/JPS60166038A/en
Publication of JPH0346176B2 publication Critical patent/JPH0346176B2/ja
Granted legal-status Critical Current

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  • Catalysts (AREA)

Abstract

PURPOSE:To obtain a highly active oxidizing catalyst consisting of a composite metal oxide which has perovskite structure of large surface area by depositing various mixed salts soln. of prescribed ratio quantities on activated carbon and thereafter drying and calcining said activated carbon. CONSTITUTION:In case of adjusting an oxidizing catalyst for catalytic combustion consisting of a composite metal oxide provided with perovskite structure wherein in the crystal structures A1-xA'xB1-yB'yO3, A and A' are rare earth elements such as La and Ce or an element selected from the elements whose ion radiuses are >=0.90Angstrom among alkaline earth metals such as Sr and Ca, and x is number of 0-1.0 range and B, B' are an element selected from the elements whose ion radiuses are >=0.51Angstrom among transition-metallic elements such as Co, Fe, Ni and Mn and y has number of 0-1.0 range, a mixed soln. consisting of one kind of common salt among various salts such as nitrate and acetate of the prescribed ratio quantity is deposited at once the activated carbon and thereafter the activated carbon is dried and calcined. As a result, the oxidizing catalyst having a large surface area and high activity is obtained.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は天然ガス、プロパンガス等の比較的軽質な炭化
水素ガスを酸化触媒マット上で触媒燃焼させ、その時に
発生する熱を利用する触媒燃焼器の酸化触媒マットに関
するものである。
Detailed Description of the Invention: Industrial Application Field The present invention provides a catalytic combustor that catalytically combusts a relatively light hydrocarbon gas such as natural gas or propane gas on an oxidation catalyst mat, and utilizes the heat generated at the time. The present invention relates to an oxidation catalyst mat.

従来例の構成とその問題点 一般に炭化水素を空気の存在下、炭酸ガスと水に完全酸
化させる酸化触媒の活性については、白金、パラジウム
等の白金族を担持したものが最も活性が高いとされてき
た。しかしながら白金族はコストも高く、耐熱性にも問
題がある。これに対して最近、一部のべPプスヵイト構
造をもつ複合金属酸化物が白金族に匹敵する活性をもっ
ことが報告されている。ペロプスカイト構造をもつ複合
金属酸化物は耐熱性も高くコストの面からも比較的安価
であるが、その製造方法に問題がある0即ち現在は酢酸
塩、硝酸塩等の各種塩を焼成する方法によシペロプスカ
イト構造をもつ粉末を調整しているが、活性の基本因子
である表面積が1゜m″/y/y以下いという問題があ
った。
Structures of conventional examples and their problems In general, with regard to the activity of oxidation catalysts that completely oxidize hydrocarbons into carbon dioxide gas and water in the presence of air, those supporting platinum group metals such as platinum and palladium are said to have the highest activity. It's here. However, platinum group metals are expensive and have problems in heat resistance. On the other hand, it has recently been reported that some composite metal oxides having a bepskite structure have an activity comparable to that of platinum group metals. Composite metal oxides with a perovskite structure have high heat resistance and are relatively inexpensive in terms of cost, but there are problems in the manufacturing method. Powders with a cyperopskite structure have been prepared, but there is a problem in that the surface area, which is a basic factor for activity, is less than 1 mm''/y/y.

発明の目的 本発明の目的は高表面積のペロブスカイト構造を有する
複合金属酸化物からなる高活性な酸化触媒を提供するこ
とにある。
OBJECTS OF THE INVENTION An object of the present invention is to provide a highly active oxidation catalyst comprising a composite metal oxide having a perovskite structure with a high surface area.

発明の構成 この目的を達成するために酸化触媒を作成するに際し、
所定比量の各種混合塩溶液を活性炭に担持させた後、乾
燥、焼成する方法をとった。この方法によれば従来の粉
末法に比較すると単位重量当りの表面積が非常に大きく
、高活性の酸化触媒が得られる。
Structure of the Invention In preparing an oxidation catalyst to achieve this object,
A method was used in which a predetermined ratio of various mixed salt solutions was supported on activated carbon, followed by drying and firing. According to this method, compared to the conventional powder method, a highly active oxidation catalyst with a much larger surface area per unit weight can be obtained.

実施例の説明 次に本発明の実施例について説明する。Description of examples Next, examples of the present invention will be described.

酢酸ランタン63重量部と酢酸セシウム7重量部及び酢
酸コバル)50重量部を適当量の水に溶解した混合塩水
溶液に予め10%の硝酸溶液で2時間湯浴させ、水洗後
、乾燥させた活性炭を加え、−昼夜放置する。これを湯
浴乾燥させた後、300℃で1時間、eoocで1時間
焼成した後850℃で5時間焼成したものを触媒燃焼用
酸化触媒とする。
Activated carbon prepared by bathing a mixed salt aqueous solution prepared by dissolving 63 parts by weight of lanthanum acetate, 7 parts by weight of cesium acetate, and 50 parts by weight of cobal acetate in an appropriate amount of water in a 10% nitric acid solution for 2 hours, washing with water, and drying. Add and leave for day and night. After drying this in a hot water bath, it was calcined at 300° C. for 1 hour, at EOOC for 1 hour, and then at 850° C. for 5 hours to obtain an oxidation catalyst for catalytic combustion.

次の表1はメタン1%空気バランスの反応ガスのそれぞ
れの転換率を得る反応温度を示したものである。触媒A
は本発明に従って調製したもの、触媒Bは活性炭を添加
せずに従来の粉末法で調整したものである。
The following Table 1 shows the reaction temperatures to obtain the respective conversion rates of the reaction gas with methane and 1% air balance. Catalyst A
Catalyst B was prepared according to the present invention and Catalyst B was prepared by the conventional powder method without the addition of activated carbon.

S、V、 18000b71 発明の効果 前記衣1から分るようにペロブスカイト構造を有する複
合金属酸化物からなる触媒燃焼用酸化触媒調整時に所定
量の混合塩水溶液を活性炭に含浸する結果、活性炭の微
小な細孔を利用することができ、酸化触媒の粒子径が小
さくなり、表面積が大きくなる。したがって活性の高い
触媒燃焼用酸化触媒を得ることができる。
S, V, 18000b71 Effects of the Invention As can be seen from the above-mentioned Cloth 1, as a result of impregnating activated carbon with a predetermined amount of mixed salt aqueous solution when preparing an oxidation catalyst for catalytic combustion made of a composite metal oxide having a perovskite structure, it is possible to Pores can be utilized, reducing the particle size of the oxidation catalyst and increasing the surface area. Therefore, a highly active oxidation catalyst for catalytic combustion can be obtained.

Claims (1)

【特許請求の範囲】[Claims] 結晶構造A、−xA’xB1−.B’yO3のうち、A
 、 A’はランタン、セリウム等の希土類元素、もし
くはストロンチウム、カルシウム等のアルカリ土類金属
のうちイオン半径が0.90八以上の元素の中から選択
された1種もしくは2種以上の元素からなりXは0〜1
.0の範囲の数値を有する。B 、 B/はコバルト、
鉄、ニッケル、マンガン等の遷移金属元素のうち、イオ
ン半径が0.61 へ以上の元素の中から選択された1
種もしくは2種以上の元素からなり、yは0〜1.0の
範囲の数値を有するペロブスカイト構造を備えた複合金
属酸化物からなるゑ媒燃焼用酸化触媒を調整する際に、
所定比量の硝酸塩、ン酸塩等の各種塩のうち、1種の共
通塩からなる混合溶液を活性炭に一度担持させた後、乾
燥、焼成することを特徴とする触媒燃焼用酸化触媒の製
造方法。
Crystal structure A, -xA'xB1-. Of B'yO3, A
, A' consists of one or more elements selected from rare earth elements such as lanthanum and cerium, or alkaline earth metals such as strontium and calcium, with an ionic radius of 0.908 or more. X is 0-1
.. It has a numerical value in the range of 0. B, B/ is cobalt,
1 selected from transition metal elements such as iron, nickel, manganese, etc. with an ionic radius of 0.61 or more.
When preparing an oxidation catalyst for veneer combustion consisting of a composite metal oxide with a perovskite structure consisting of a species or two or more elements, and y having a value in the range of 0 to 1.0,
Production of an oxidation catalyst for catalytic combustion, characterized in that a mixed solution consisting of one type of common salt among various salts such as nitrates and phosphates in a predetermined ratio is supported on activated carbon, and then dried and calcined. Method.
JP59020207A 1984-02-06 1984-02-06 Manufacture of oxidizing catalyst for catalytic combustion Granted JPS60166038A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP59020207A JPS60166038A (en) 1984-02-06 1984-02-06 Manufacture of oxidizing catalyst for catalytic combustion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP59020207A JPS60166038A (en) 1984-02-06 1984-02-06 Manufacture of oxidizing catalyst for catalytic combustion

Publications (2)

Publication Number Publication Date
JPS60166038A true JPS60166038A (en) 1985-08-29
JPH0346176B2 JPH0346176B2 (en) 1991-07-15

Family

ID=12020716

Family Applications (1)

Application Number Title Priority Date Filing Date
JP59020207A Granted JPS60166038A (en) 1984-02-06 1984-02-06 Manufacture of oxidizing catalyst for catalytic combustion

Country Status (1)

Country Link
JP (1) JPS60166038A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62225250A (en) * 1986-03-25 1987-10-03 Matsushita Electric Ind Co Ltd Powder deposition type catalyst
JPS63146478A (en) * 1986-12-10 1988-06-18 Tohoku Ricoh Co Ltd Electrode for carbon dioxide gas laser
JPS63248441A (en) * 1987-04-06 1988-10-14 Agency Of Ind Science & Technol Production of catalyst
JP2001313059A (en) * 2000-04-27 2001-11-09 Toyota Motor Corp Fuel cell device and mobile structure equipped with above

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62225250A (en) * 1986-03-25 1987-10-03 Matsushita Electric Ind Co Ltd Powder deposition type catalyst
JPS63146478A (en) * 1986-12-10 1988-06-18 Tohoku Ricoh Co Ltd Electrode for carbon dioxide gas laser
JPS63248441A (en) * 1987-04-06 1988-10-14 Agency Of Ind Science & Technol Production of catalyst
JP2001313059A (en) * 2000-04-27 2001-11-09 Toyota Motor Corp Fuel cell device and mobile structure equipped with above

Also Published As

Publication number Publication date
JPH0346176B2 (en) 1991-07-15

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