JPS59222214A - Reducing method of nox - Google Patents

Reducing method of nox

Info

Publication number
JPS59222214A
JPS59222214A JP58098246A JP9824683A JPS59222214A JP S59222214 A JPS59222214 A JP S59222214A JP 58098246 A JP58098246 A JP 58098246A JP 9824683 A JP9824683 A JP 9824683A JP S59222214 A JPS59222214 A JP S59222214A
Authority
JP
Japan
Prior art keywords
nox
platinum
catalyst
site
transition metal
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
JP58098246A
Other languages
Japanese (ja)
Inventor
Akio Fukuda
明雄 福田
Masao Maki
正雄 牧
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 JP58098246A priority Critical patent/JPS59222214A/en
Publication of JPS59222214A publication Critical patent/JPS59222214A/en
Pending legal-status Critical Current

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

Abstract

PURPOSE:To reduce NOx in a high temp. zone by using a catalyst carrying a platinum element and a transition metal on a perovskite type compound oxide. CONSTITUTION:The perovskite type compound oxide is expressed as a general formula ABO3, and the compd. SrFeO3, having Sr at the A site and Fe at the B site, is especially suitable. Platinum, which is comparatively resistant to poisoning, is suitably used as a platinum element. And nickel is suitable as a transition metal. Each amt. of Pt and Ni to be carried is preferably regulated to >=0.1wt%. By bringing the catalyst into contact with a gas contg. NOx under the inert or reducing atmosphere at 800-1,000 deg.C, NOx can be reduced.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、NOx を含有する気体を発生する機器又は
設備に関する。
DETAILED DESCRIPTION OF THE INVENTION Field of the Invention The present invention relates to equipment or equipment that generates gas containing NOx.

従来例の構成とその問題点 従来のNOx低減化の方法は、一般的には使用する触媒
が耐熱性に劣り高温での使用に問題があることや、面j
被毒性に劣るなどの問題点があった。
Conventional structure and its problems Conventional NOx reduction methods generally have problems with the use of catalysts at high temperatures due to poor heat resistance, and
There were problems such as poor toxicity.

2 、  ・ 発明の目的 本発明はこのような従来の問題点を解消するもので、耐
熱性、耐被毒性の優れた触媒を用いて、高温域でのNO
x 低減化を図ることを目的と(−でいる。
2. Purpose of the Invention The present invention solves these conventional problems, and uses a catalyst with excellent heat resistance and toxicity resistance to reduce NO in a high temperature range.
The purpose is to reduce x (-).

発明の構成 この目的を達成するために本発明は、ペロブスカイト型
複合酸化物に白金属元素、及び遷移金属を担持した触媒
を使用するものである。ペロブスカイト型複合酸化物は
、一般式ABO3で表わされ、AサイトはLa、Sr、
BサイトはFe、Co、Mn等を用いるのが良い。本発
明では特にAサイトがSr、BサイトがFeの5rFe
○3という化合物が適している。白金属元素としては、
ロジウム。
Structure of the Invention In order to achieve this object, the present invention uses a catalyst in which a platinum metal element and a transition metal are supported on a perovskite type composite oxide. Perovskite type composite oxide is represented by the general formula ABO3, and the A site is La, Sr,
It is preferable to use Fe, Co, Mn, etc. for the B site. In the present invention, in particular, 5rFe is used, in which the A site is Sr and the B site is Fe.
The compound ○3 is suitable. As a white metal element,
rhodium.

パラジウム、白金等が考えられるが、これらの中で比較
的被毒に強い白金を用いるのが良い。又、遷移金属とし
ては、鉄、コバルト、二、7ケル等が考えられるが、本
発明ではニッケルが適している。
Palladium, platinum, etc. are conceivable, but among these, it is better to use platinum, which is relatively resistant to poisoning. Further, as the transition metal, iron, cobalt, 2, 7 Kel, etc. can be considered, but nickel is suitable in the present invention.

本触媒は3 r F e O3に白金を0.1重l−く
−セント以上、ニッケルを0.1重量パーセント以ト担
持させたものである。この触媒を800〜1000℃で
、不活性雰囲気又は還元性雰囲気の下でNOx含有気体
と接触させることによりNOx の低減化を図ることが
できる。
This catalyst has platinum supported on 3rF e O3 in an amount of 0.1 cent by weight or more and nickel in an amount of 0.1 weight percent or more. NOx can be reduced by contacting this catalyst with a NOx-containing gas at 800 to 1000°C under an inert atmosphere or a reducing atmosphere.

実施例の説明 以下、本発明の一実施例を図を用すて説明する。Description of examples Hereinafter, one embodiment of the present invention will be described with reference to the drawings.

図において、1は本実施例による触媒、2は石英ウール
、3は反応管、4はヒータである。この構成において、
NOx含有気体は触媒と接触しNOxの接触分解ができ
る。第1表に本触媒の組成、第2表及び第4表にNOx
分解の例を示す。又、第3表にはSrFeO3に白金、
ニッケルを各々単独で担持した触媒によるNOx分解の
例を示す。これかられかるように、白金、ニッケルが単
独で担持された場合、NOx分解の活性は低く、本実施
例による白金と二、ケルを同時に担持した触媒が低NO
x化に有力であることがわかる。次に触媒調整の一例を
説明する。5rFe○s 2−5 gを蒸発(■に入れ
、INカセイソーダ2.5m/を加えた後、400℃、
30分間加熱した。次に塩化白金酸の6.7 jj /
 IJ水溶液を2.6ml加え、同じく400℃、30
分間の加熱を行った。7f]′i、塩化白金酸水溶液を
加え、同様の加熱を行った。更に、硝酸二。
In the figure, 1 is the catalyst according to this example, 2 is quartz wool, 3 is a reaction tube, and 4 is a heater. In this configuration,
The NOx-containing gas is brought into contact with the catalyst and NOx can be catalytically decomposed. Table 1 shows the composition of this catalyst, Tables 2 and 4 show NOx
An example of decomposition is shown. Table 3 also shows platinum in SrFeO3,
An example of NOx decomposition using a catalyst each carrying nickel alone will be shown. As will be seen, when platinum and nickel are supported alone, the NOx decomposition activity is low, and the catalyst in which platinum and nickel are simultaneously supported has a low NOx decomposition activity.
It can be seen that it is effective for x-ization. Next, an example of catalyst adjustment will be explained. Evaporate 2-5 g of 5rFe○s (into ■, add 2.5 m/in caustic soda,
Heated for 30 minutes. Next, 6.7 jj / of chloroplatinic acid
Add 2.6 ml of IJ aqueous solution and heat at 400°C for 30
Heating was performed for 1 minute. 7f]′i, a chloroplatinic acid aqueous solution was added, and the same heating was performed. Furthermore, nitric acid di.

ケルの5.ojj/l水溶液を2.6ml加え400℃
、30分の加熱という操作を2回繰り返した。このよう
にして調整された触媒は、NOx分解に対して第2表の
ような活性を示l〜だ。更にこの触媒を460℃で水素
還元すると、第4表のような活性を示しだ。
Kel's 5. Add 2.6ml of ojj/l aqueous solution and heat to 400°C.
The operation of heating for 30 minutes was repeated twice. The catalyst prepared in this manner exhibits the activity for NOx decomposition as shown in Table 2. Further, when this catalyst was subjected to hydrogen reduction at 460°C, it exhibited the activity shown in Table 4.

第   1   表 第   2   表 第   3   表 第  4  表 発明の効果 以−Lのように本発明はNOx 含有気体と、白金−ニ
ノケル担持5rFe03触媒を還元性又は不活性雰囲気
で、高温の下で接触させることにJ:す、低NOx 化
を図るものである。本触媒dニペロブス力イト型構造を
有し、白金とニッケルを担持したことにより、 1 耐熱性に優れており、1000℃近くでも使用でき
る。
Table 1 Table 2 Table 3 Table 4 Effects of the Invention As shown in Table 4, the present invention brings a NOx-containing gas into contact with a platinum-Ninochel-supported 5rFe03 catalyst at high temperatures in a reducing or inert atmosphere. In particular, it aims to reduce NOx. This catalyst has a niperobrite structure and supports platinum and nickel, so it has excellent heat resistance and can be used at temperatures close to 1000°C.

2 NOxの接触分解が可能である。2 Catalytic decomposition of NOx is possible.

3 反応系(機器、設備)に応じた形状に成形すること
が容易である。
3. It is easy to mold into a shape suitable for the reaction system (equipment, equipment).

4 ペロブスカイト型複合酸化物ばS r F e O
3だけでなく、Aサイト、Bサイトを任意に選択できる
4 Perovskite type composite oxide S r Fe O
In addition to 3, you can arbitrarily select site A and site B.

6 白金〜エソケル系以外の金属の組合せが可能である
6. Combinations of metals other than platinum to Esochel are possible.

6 使用する白金はペロブスカイト型複合酸化物に比べ
て少欲であるだめコスト低減となる。
6. The platinum used is less abundant than perovskite-type composite oxides, resulting in cost reduction.

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

図は本発明のNOx低減化方法を用いた反応装置の要部
断面図である。 1 ・・・白金−ニノケル担持5rFe○3゜代理人の
氏名 弁理士 中 尾 敏 男 ほか1名83−
The figure is a sectional view of a main part of a reaction apparatus using the NOx reduction method of the present invention. 1...Platinum-Ninokel-supported 5rFe○3゜Name of agent: Patent attorney Toshio Nakao and one other person83-

Claims (2)

【特許請求の範囲】[Claims] (1)ペロブスカイト型複合酸化物に白金属元素及び遷
移金属を担持した触媒を、還元性雰囲気又は不活性雰囲
気で800〜1000℃の温度下で、No  含有気体
と接触させるNOx低減化方法。
(1) A NOx reduction method in which a catalyst in which a platinum metal element and a transition metal are supported on a perovskite-type composite oxide is brought into contact with a No 2 -containing gas at a temperature of 800 to 1000° C. in a reducing atmosphere or an inert atmosphere.
(2)  ペロブスカイト型複合酸化物としてS r 
F e O3゜白金属元素として白金、遷移金属として
ニッケルを用いた特許請求の範囲第1項記載のNOx低
減化方法。
(2) Sr as a perovskite complex oxide
The NOx reduction method according to claim 1, wherein platinum is used as the F e O3 platinum metal element and nickel is used as the transition metal.
JP58098246A 1983-06-01 1983-06-01 Reducing method of nox Pending JPS59222214A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58098246A JPS59222214A (en) 1983-06-01 1983-06-01 Reducing method of nox

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58098246A JPS59222214A (en) 1983-06-01 1983-06-01 Reducing method of nox

Publications (1)

Publication Number Publication Date
JPS59222214A true JPS59222214A (en) 1984-12-13

Family

ID=14214594

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58098246A Pending JPS59222214A (en) 1983-06-01 1983-06-01 Reducing method of nox

Country Status (1)

Country Link
JP (1) JPS59222214A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006176346A (en) * 2004-12-21 2006-07-06 Dowa Mining Co Ltd Oxygen storage material

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006176346A (en) * 2004-12-21 2006-07-06 Dowa Mining Co Ltd Oxygen storage material

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