JPS61249540A - Catalyst - Google Patents
CatalystInfo
- Publication number
- JPS61249540A JPS61249540A JP60090029A JP9002985A JPS61249540A JP S61249540 A JPS61249540 A JP S61249540A JP 60090029 A JP60090029 A JP 60090029A JP 9002985 A JP9002985 A JP 9002985A JP S61249540 A JPS61249540 A JP S61249540A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- carrier
- black
- nitrate
- catalyst body
- 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
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 46
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(2+);dinitrate Chemical compound [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 239000002002 slurry Substances 0.000 claims abstract description 5
- 150000003839 salts Chemical class 0.000 claims abstract description 4
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 claims abstract description 3
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910001981 cobalt nitrate Inorganic materials 0.000 claims abstract description 3
- 229910052878 cordierite Inorganic materials 0.000 claims abstract 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 claims abstract description 3
- 229910010293 ceramic material Inorganic materials 0.000 claims abstract 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 5
- 239000010419 fine particle Substances 0.000 claims description 4
- 229910052751 metal Inorganic materials 0.000 claims description 4
- 239000002184 metal Substances 0.000 claims description 4
- 230000001070 adhesive effect Effects 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 239000000463 material Substances 0.000 claims description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims 2
- UBEWDCMIDFGDOO-UHFFFAOYSA-N cobalt(2+);cobalt(3+);oxygen(2-) Chemical compound [O-2].[O-2].[O-2].[O-2].[Co+2].[Co+3].[Co+3] UBEWDCMIDFGDOO-UHFFFAOYSA-N 0.000 claims 2
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims 2
- 229910000505 Al2TiO5 Inorganic materials 0.000 claims 1
- 230000010718 Oxidation Activity Effects 0.000 claims 1
- 229940011182 cobalt acetate Drugs 0.000 claims 1
- QAHREYKOYSIQPH-UHFFFAOYSA-L cobalt(II) acetate Chemical compound [Co+2].CC([O-])=O.CC([O-])=O QAHREYKOYSIQPH-UHFFFAOYSA-L 0.000 claims 1
- KZHJGOXRZJKJNY-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Si]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O.O=[Al]O[Al]=O KZHJGOXRZJKJNY-UHFFFAOYSA-N 0.000 claims 1
- 229940071125 manganese acetate Drugs 0.000 claims 1
- UOGMEBQRZBEZQT-UHFFFAOYSA-L manganese(2+);diacetate Chemical compound [Mn+2].CC([O-])=O.CC([O-])=O UOGMEBQRZBEZQT-UHFFFAOYSA-L 0.000 claims 1
- 229910052863 mullite Inorganic materials 0.000 claims 1
- AABBHSMFGKYLKE-SNAWJCMRSA-N propan-2-yl (e)-but-2-enoate Chemical compound C\C=C\C(=O)OC(C)C AABBHSMFGKYLKE-SNAWJCMRSA-N 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 229910052845 zircon Inorganic materials 0.000 claims 1
- 239000000843 powder Substances 0.000 abstract description 9
- 239000002131 composite material Substances 0.000 abstract description 5
- 229940125898 compound 5 Drugs 0.000 abstract 1
- 230000007704 transition Effects 0.000 abstract 1
- 230000000694 effects Effects 0.000 description 7
- 238000010411 cooking Methods 0.000 description 6
- 229910000314 transition metal oxide Inorganic materials 0.000 description 6
- 238000010304 firing Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 3
- -1 platinum group metals Chemical class 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 229910001111 Fine metal Inorganic materials 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 235000019645 odor Nutrition 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- 229910001361 White metal Inorganic materials 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000012050 conventional carrier Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000005855 radiation Effects 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 239000010969 white metal Substances 0.000 description 1
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
本発明は燃焼の際発生する不完全燃焼成分、未燃成分あ
るいは各種調理の際発生する臭気の原因である炭化水素
成分を取り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 a method for removing incompletely burned components and unburned components generated during combustion, as well as hydrocarbon components that cause odors generated during various types of cooking. The present invention relates to an exhaust gas purification catalyst provided therein.
従来の技術
従来この種の触媒体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
んだペロブスカイト復合酸化物はその粒径を非常に小さ
くすれば白金釜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、ある種のベロゲスカイト構造を持った複
合酸化物は活性も相当にあり、また耐熱性も有する。従
ってこれらペロプ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
いペロプ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 Conventionally, there have been various types of catalyst bodies of this type. In other words, the catalyst supporting platinum group metals, which is the most common among them, is produced by impregnating a porous ceramic carrier with an aqueous solution containing platinum group metals, such as an aqueous solution of chloroplatinic acid, and then drying and calcining it. It is 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 the activity of a platinum pot if the particle size is made very small, but transition metal oxides alone have no resistance to high temperatures. In contrast, some complex oxides with a vergeskite structure have considerable activity and are also heat resistant. Therefore, if fine powder of these perovskite 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. Although only a small portion of the perovskite compound falls off and has little effect on activity deterioration, after the black peropskite compound 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Pf1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 that Pf1 is intended to solve As described above, conventional carriers are almost white or nearly white in color, and if the attached black powder falls off, it will be 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
触媒担体にペロゲスカイト触媒粉末を担持させる時、同
時に硝酸マンガンなど空気中で焼成すると黒色を呈する
白属塩の溶液をハニカム構造体の微細孔に含浸させ、焼
成時に担体を黒化させる。その結果出来た触媒体は黒色
担体に黒色触媒粉末を担持させたものとなる。Means for Solving the Problems In order to solve the above-mentioned problems, the present invention, when supporting perogeskite catalyst powder on a catalyst carrier of a honeycomb structure, simultaneously uses a white metal salt, such as manganese nitrate, which becomes black when fired in air. The solution is impregnated into the micropores of the honeycomb structure, and the carrier is blackened during firing. The resulting catalyst body has black catalyst powder supported on a black carrier.
作 用
零発+3Aは上記した構成により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。Due to the above-described structure, even if some of the supported catalyst powder is missing, no abnormality is observed in the appearance of the zero-action +3A.
また触媒担体内の細孔内部において遷移金属酸化物を形
成させるため、黒化させた触媒担体は黒化させない触媒
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。Further, since transition metal oxides are formed inside the pores of the catalyst carrier, the blackened catalyst carrier can greatly increase the catalytic oxidation ability compared to the non-blackened catalyst carrier.
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図においては触媒担体、2は触媒担体1内に存
在する微小細孔で、その内壁面には遷移金属酸化物微粒
子3が担持されている。触媒担体1外表面4にはペロブ
スカイト復合酸化物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。担持助剤に
はコロイダルアルミナや硝酸アルミニクムなど焼成する
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, a catalyst carrier 2 is a micropore existing in the catalyst carrier 1, and transition metal oxide fine particles 3 are supported on the inner wall surface thereof. 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4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ゲスカイト複合
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ため外観的には全く変ることがな
い。In the above structure, even if a part of the film of perogeskite composite oxide 5 and alumina 6 attached to the surface 4 of the catalyst body is lost due to some mechanical impact or contact, the underlying surface will remain black. There is no change in appearance 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.
ベロゲスカイト複合酸化物の微粒子(””0.9Ce
o、l+ CoO3)硝酸コバルト(co(No3)2
・6 H20)及び硝酸7 /I/ ミニクA、(A
I (NO3) 3 ・9 H20)を重量比で4:3
:2の割合で混合させ、水を加えスラリー状にする。さ
らにスラリーを安定なものにさせるためCMC,PVA
等を若干加え所定の粘度に調整したもの\中に内部に微
小細孔を有したコーディエライトのハニカム構造体を浸
す。浸したハニカム構造体を取り出し、セル内円に留っ
たスラリー液を風圧で吹き飛ばし、100℃で約1 h
r乾燥した後、800℃で5 m1n−40min焼成
を行なう。Fine particles of vergeskite composite oxide (""0.9Ce
o, l+ CoO3) Cobalt nitrate (co(No3)2
・6 H20) and nitric acid 7 /I/ Minik A, (A
I (NO3) 3 ・9 H20) in a weight ratio of 4:3
: Mix at a ratio of 2 parts and add water to make a slurry. Furthermore, to make the slurry stable, CMC, PVA
A cordierite honeycomb structure with micropores inside is immersed in the mixture, which has been adjusted to a predetermined viscosity by adding a small amount of the following ingredients. The soaked honeycomb structure was taken out, the slurry liquid remaining in the inner circle of the cells was blown away by wind pressure, and then heated at 100°C for about 1 hour.
After drying, firing is performed at 800°C for 5 m1n for 40 min.
第2図は本発明の触媒担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 carrier of the present invention, in which the catalyst body 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。調理庫内80天面
には金網発熱体10を置き、ガスバーナ11により赤熱
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 80, 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を置くだめの置
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 cooking chamber 8, 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13から発生する臭
気を含む炭化水素はガスバーナ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7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 heated, and the food 12 is cooked by the radiation and hot exhaust gas generated. At this time, odor-containing hydrocarbons generated from the cooked food 13 pass through the catalyst body 7 installed at the exhaust gas outlet 9 together with the exhaust gas generated from the gas burner 11, and the hydrocarbons are purified.
発明の効果
本発明の触媒体の効果は次の通り、
(1)微粉末の付着形の触媒体であるので、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、特に家庭用燃焼
器内に用いるには最適である。Effects of the Invention The effects of the catalyst body of the present invention are as follows: (1) Since it is a catalyst body in which fine powder is attached, even if the perovskite fine powder supported on the surface is detached, the background color remains the same. This makes it aesthetically pleasing, making it especially suitable for use in household combustors.
(11)本発明の触媒体は触媒担体内の細孔内部に遷移
金属酸化物を形成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。(11) Since the catalyst body of the present invention forms transition metal oxides inside the pores of the catalyst carrier to cause blackening, the catalytic ability is greatly increased compared to a catalyst body using a catalyst carrier that does not blacken. can be done.
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内に応用した縦断面図である。
1・・・・・・触媒担体、2・・・・・・微小細孔、3
・・・・・・遷移金属酸化物微粒子、5・・・・・・ペ
ロブスカイト復合酸化物、6・・・・・・アルミナ。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図
!
第2図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 catalyst body applied to a cooking appliance. 1... Catalyst carrier, 2... Micropore, 3
... Transition metal oxide fine particles, 5 ... Perovskite compound oxide, 6 ... Alumina. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
figure! Figure 2
Claims (3)
る金属塩、酸化活性を有するペロブスカイト復合酸化物
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
る担持助剤を水と撹拌混合させ、スラリー状液にさせた
中に内部に微小細孔を有した耐熱性セラミック材料から
なるハニカム構造体の触媒担体を浸し、乾燥、焼成した
触媒体。(1) Metal salts such as manganese nitrate that turn black when fired in air, fine particles of perovskite compound oxides that have oxidation activity, and support materials that become porous and have strong adhesive properties when fired, such as colloidal alumina and aluminum nitrate. A catalyst body made by stirring and mixing a catalyst with water to form a slurry liquid, in which a honeycomb structured catalyst carrier made of a heat-resistant ceramic material with micropores inside is immersed, dried, and fired.
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などである特許請求の範囲第
1項に記載の触媒体。(2) Heat-resistant ceramics include cordierite, T and γ
The catalyst body according to claim 1, which is alumina, mullite, zirconia, mullite-zircon, aluminum titanate, etc.
ガン、酢酸コバルトなど空気中で焼成することによって
二酸化マンガン(MnO_2)、や四三酸化コバルト(
Co_3O_4)など黒色を呈するものでである特許請
求の範囲第1項に記載の触媒体。(3) Metal salts such as manganese nitrate, cobalt nitrate, manganese acetate, and cobalt acetate are calcined in air to produce manganese dioxide (MnO_2) and tricobalt tetroxide (
The catalyst body according to claim 1, which exhibits a black color, such as Co_3O_4).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60090029A JPS61249540A (en) | 1985-04-26 | 1985-04-26 | Catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60090029A JPS61249540A (en) | 1985-04-26 | 1985-04-26 | Catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS61249540A true JPS61249540A (en) | 1986-11-06 |
JPH0545294B2 JPH0545294B2 (en) | 1993-07-08 |
Family
ID=13987245
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60090029A Granted JPS61249540A (en) | 1985-04-26 | 1985-04-26 | Catalyst |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61249540A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63232854A (en) * | 1987-03-20 | 1988-09-28 | Toshiba Corp | High-temperature combustion catalyst and its production |
KR100425254B1 (en) * | 2001-05-16 | 2004-03-30 | 한국표준과학연구원 | Nearly zero temperature coefficient of resistance in manganese nitride |
-
1985
- 1985-04-26 JP JP60090029A patent/JPS61249540A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63232854A (en) * | 1987-03-20 | 1988-09-28 | Toshiba Corp | High-temperature combustion catalyst and its production |
KR100425254B1 (en) * | 2001-05-16 | 2004-03-30 | 한국표준과학연구원 | Nearly zero temperature coefficient of resistance in manganese nitride |
Also Published As
Publication number | Publication date |
---|---|
JPH0545294B2 (en) | 1993-07-08 |
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