JPS5952529A - High temperature combustion catalyst - Google Patents
High temperature combustion catalystInfo
- Publication number
- JPS5952529A JPS5952529A JP57163092A JP16309282A JPS5952529A JP S5952529 A JPS5952529 A JP S5952529A JP 57163092 A JP57163092 A JP 57163092A JP 16309282 A JP16309282 A JP 16309282A JP S5952529 A JPS5952529 A JP S5952529A
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- metal
- carrier
- combustion
- combustion catalyst
- 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
- 239000003054 catalyst Substances 0.000 title claims abstract description 44
- 238000002485 combustion reaction Methods 0.000 title claims description 28
- 229910052751 metal Inorganic materials 0.000 claims abstract description 19
- 239000002184 metal Substances 0.000 claims abstract description 19
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims abstract description 16
- 239000000919 ceramic Substances 0.000 claims abstract description 16
- 229910052726 zirconium Inorganic materials 0.000 claims abstract description 6
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 5
- 229910052718 tin Inorganic materials 0.000 claims abstract description 5
- 229910052684 Cerium Inorganic materials 0.000 claims abstract description 4
- 229910052746 lanthanum Inorganic materials 0.000 claims abstract description 4
- 229910052712 strontium Inorganic materials 0.000 claims abstract description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 11
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 9
- 239000011777 magnesium Substances 0.000 claims description 4
- 229910052697 platinum Inorganic materials 0.000 claims description 4
- 239000011247 coating layer Substances 0.000 claims description 3
- 229910052763 palladium Inorganic materials 0.000 claims description 3
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 claims description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims description 2
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 claims description 2
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 claims description 2
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 claims description 2
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 claims 1
- 239000000203 mixture Substances 0.000 abstract description 8
- 239000008199 coating composition Substances 0.000 abstract description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 3
- 239000007788 liquid Substances 0.000 abstract description 3
- 238000001035 drying Methods 0.000 abstract description 2
- 229910052593 corundum Inorganic materials 0.000 abstract 2
- 229910001845 yogo sapphire Inorganic materials 0.000 abstract 2
- 229910052681 coesite Inorganic materials 0.000 abstract 1
- 229910052906 cristobalite Inorganic materials 0.000 abstract 1
- 229910003465 moissanite Inorganic materials 0.000 abstract 1
- 229910010271 silicon carbide Inorganic materials 0.000 abstract 1
- 239000000377 silicon dioxide Substances 0.000 abstract 1
- 235000012239 silicon dioxide Nutrition 0.000 abstract 1
- 229910052682 stishovite Inorganic materials 0.000 abstract 1
- 229910052905 tridymite Inorganic materials 0.000 abstract 1
- 229910003158 γ-Al2O3 Inorganic materials 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 14
- 229910000510 noble metal Inorganic materials 0.000 description 12
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 4
- 230000007423 decrease Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- 239000000446 fuel Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 229910052878 cordierite Inorganic materials 0.000 description 2
- 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 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 description 2
- 230000014759 maintenance of location Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- PIBWKRNGBLPSSY-UHFFFAOYSA-L palladium(II) chloride Chemical compound Cl[Pd]Cl PIBWKRNGBLPSSY-UHFFFAOYSA-L 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910052710 silicon Inorganic materials 0.000 description 2
- 239000010703 silicon Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- DHEQXMRUPNDRPG-UHFFFAOYSA-N strontium nitrate Chemical compound [Sr+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O DHEQXMRUPNDRPG-UHFFFAOYSA-N 0.000 description 2
- OERNJTNJEZOPIA-UHFFFAOYSA-N zirconium nitrate Chemical compound [Zr+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O OERNJTNJEZOPIA-UHFFFAOYSA-N 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000007084 catalytic combustion reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000009841 combustion method Methods 0.000 description 1
- 239000007771 core particle Substances 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 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 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000010304 firing Methods 0.000 description 1
- 230000004927 fusion Effects 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 229910052863 mullite Inorganic materials 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- VSZWPYCFIRKVQL-UHFFFAOYSA-N selanylidenegallium;selenium Chemical compound [Se].[Se]=[Ga].[Se]=[Ga] VSZWPYCFIRKVQL-UHFFFAOYSA-N 0.000 description 1
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 1
- 229910052814 silicon oxide Inorganic materials 0.000 description 1
- SDKPSXWGRWWLKR-UHFFFAOYSA-M sodium;9,10-dioxoanthracene-1-sulfonate Chemical class [Na+].O=C1C2=CC=CC=C2C(=O)C2=C1C=CC=C2S(=O)(=O)[O-] SDKPSXWGRWWLKR-UHFFFAOYSA-M 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 229910052596 spinel Inorganic materials 0.000 description 1
- 239000011029 spinel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- YQMWDQQWGKVOSQ-UHFFFAOYSA-N trinitrooxystannyl nitrate Chemical compound [Sn+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O YQMWDQQWGKVOSQ-UHFFFAOYSA-N 0.000 description 1
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- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の技術分野〕
本発明は、高温燃焼触媒に関し、更に詳しくは、約80
0C〜1500 t:’の温度範囲において、高活性及
び長寿命を有する高温燃焼触媒に関する。DETAILED DESCRIPTION OF THE INVENTION [Technical Field of the Invention] The present invention relates to high temperature combustion catalysts, and more particularly to
It relates to a high temperature combustion catalyst with high activity and long life in the temperature range from 0C to 1500 t:'.
近年、石油資源等の枯渇化に伴い、エネルギー資源を効
率的に使用するため、例えば、ガスタービン等において
は、できるだけ高温において燃料を燃焼させることが望
まれている。In recent years, with the depletion of petroleum resources and the like, in order to use energy resources efficiently, for example, in gas turbines and the like, it is desired to burn fuel at as high a temperature as possible.
しかしながら、やt来は、燃料と空気の混合物を、スパ
ークプラグ等を用いて着火燃焼せしめる方法であるため
、燃焼器内において、部分的に2000Cを超える高温
部が存在する。そして、この高温部において、窒素酸化
物(NOx)が多量に生成し、環境汚染等の問題を生ず
ることが知られている。′ □
このような問題を解消するために、1独媒を用いて燃料
と空気の混合物を燃焼せしめる触媒燃焼方式が提案され
ている。この燃焼方式によれば、均一燃焼が可能で・あ
り、且つ、NOxが生成しない上限温度である1500
C程度まで、燃焼温度を高めることができる。However, since the current method uses a spark plug or the like to ignite and burn a mixture of fuel and air, there are parts of the combustor with high temperatures exceeding 2000C. It is known that a large amount of nitrogen oxides (NOx) is generated in this high temperature section, causing problems such as environmental pollution. ' □ In order to solve these problems, a catalytic combustion method has been proposed in which a mixture of fuel and air is combusted using a single solvent. According to this combustion method, uniform combustion is possible and the upper limit temperature at which no NOx is generated is 1500℃.
The combustion temperature can be raised to about C.
現在、触媒燃焼方式に使用される触媒としては、白金(
Pt)系の貴金属触媒が知られている。Currently, platinum (
Pt)-based noble metal catalysts are known.
このような貴金属系燃焼触媒は、例えばh第1図に示し
たように、一定の4U 41的強度を有する担体1上に
、活性担体としてγ−アルミナ(γAJ20s ) 2
を塗布し、更に、浸漬法にょシ、貴金属3を担持させた
ものである。尚、第1図は触媒体の断面図であシ、第2
図はその表面の平面図である。Such a noble metal combustion catalyst, for example, as shown in Fig. 1, is made of γ-alumina (γAJ20s) 2 as an active carrier on a carrier 1 having a certain 4U41 strength.
was applied, and further a noble metal 3 was supported using a dipping method. Note that Figure 1 is a cross-sectional view of the catalyst body, and Figure 2 is a cross-sectional view of the catalyst body.
The figure is a plan view of the surface.
しかしながら、上記した貴金属系燃焼触媒は、その耐熱
温度が通常600cと言われており、それ以上の温度域
では触媒活性が急速に低下し、使用することができない
という問題点を有している。However, the above-described noble metal combustion catalyst has the problem that its allowable temperature limit is usually said to be 600C, and that the catalyst activity rapidly decreases in a temperature range higher than that, making it unusable.
600C以上の温度において、触媒活性が急速に低下す
る原因は、次のように考えることができる。先ず、第1
に、担体表面の貴金属粒子が熱移動によ)凝集して粗大
化するため、触媒表面積が減少し、燃焼性能が低下する
。そして、第2に、γ−Aノ、03が1000 U付近
からそれ以上の温度において、α−M、03に相転移す
るため1、υ、03層内において或いはり20.と担体
との間においてクラックが生じ、 AjtOs層が触媒
金属と共に剥離脱落することに起因すると考えられる。The reason why the catalyst activity rapidly decreases at temperatures above 600C can be considered as follows. First, the first
Second, the noble metal particles on the surface of the carrier aggregate (due to heat transfer) and become coarse, reducing the catalyst surface area and deteriorating combustion performance. Second, since γ-A,03 undergoes a phase transition to α-M,03 at temperatures around 1000 U or higher, 1, υ, 03 or 20. This is thought to be due to cracks occurring between the AjtOs layer and the support, and the AjtOs layer peeling off together with the catalyst metal.
そこで、貴会り系燃焼触媒の耐熱性を向上せしめるため
に、r+、υ、01層を改良し、γ−A、/!203層
上のpt核粒子A71,0.に強く吸着させて熱移動に
よる凝集を防止すると共に、γ−AJ20.Nのα化を
防止してクラックの発生を防ぐことが試みられている。Therefore, in order to improve the heat resistance of the Kikai-based combustion catalyst, the r+, υ, 01 layer was improved, and γ-A, /! 203 layer on the pt core particles A71,0. γ-AJ20. is strongly adsorbed to prevent agglomeration due to heat transfer. Attempts have been made to prevent the occurrence of cracks by preventing N from becoming alpha.
その結果、 r −)J*Os層への金属の添加によ
シ。As a result, due to the addition of metal to the r − )J*Os layer.
自動車触媒の一部においては5ooc前後まで使用可能
な耐熱性燃焼触媒が開発され−Cいる。In some automobile catalysts, heat-resistant combustion catalysts that can be used up to around 500C have been developed.
本発明の目的は、約800〜1500t:’の温度範囲
においても高活性及び長寿命を有する高温燃焼触媒を提
供することにある。An object of the present invention is to provide a high temperature combustion catalyst having high activity and long life even in the temperature range of about 800 to 1500 t:'.
本発明者らは、上記した現況に鑑みて、5ooc以上の
高温において使用可能な触媒について鋭意検討を重ねた
結果、r−7u203I?4にCe s L a bS
r、 Sn、 Zr及びMgから成る群より選ばれた少
なくとも1−の金属並びにセラミックウィスカーを添加
することによシ、大幅に耐熱性が向上することを見出し
、本発明を完成する。に到りた。In view of the above-mentioned current situation, the inventors of the present invention have conducted extensive studies on catalysts that can be used at high temperatures of 5ooc or higher, and have found that r-7u203I? 4 to Ce s L a bS
The present invention has been completed based on the discovery that heat resistance can be significantly improved by adding at least one metal selected from the group consisting of Zr, Sn, Zr, and Mg and a ceramic whisker. It arrived.
即ち1本発明の高温燃焼触媒は、耐熱性担体;該担体上
に設けられたセリウム(Ce) 、ランタン(La)、
ストロンチウム(Sr)、スズ(Sn)、ジルコニウム
(Zr )及びマグネシウム(Mg)から成る群よシ選
ばれた少なくとも11ftの金属とセラミックウィスカ
ーを含有するr−アルミナ(r−2υ、0.)の被覆層
;及び該γ−アルミナ被覆層に担持された白金(Pt)
及び/又はパラジウム(Pd)から成ることを特徴とす
るものである。Namely, the high temperature combustion catalyst of the present invention has a heat-resistant carrier; cerium (Ce), lanthanum (La),
A coating of r-alumina (r-2υ, 0.) containing at least 11 ft of metal and ceramic whiskers selected from the group consisting of strontium (Sr), tin (Sn), zirconium (Zr) and magnesium (Mg). layer; and platinum (Pt) supported on the γ-alumina coating layer.
and/or palladium (Pd).
以下において、本発明を更に詳しく説明する。In the following, the invention will be explained in more detail.
本発明において使用される耐熱性担体は。The heat-resistant carrier used in the present invention is:
1500t:’程度の高温酸化性雰囲気中においても安
定な性質を有するものであればいかなるものでもよく、
これらの具体例としては、コージライト、ムライト、α
−アル、ミナ、ジルコニアスピネル、チタニア等のセラ
ミック製担体等が挙げられる。担体の形状は、通常、触
媒体として使用されている形状であれば特に制限はなく
、例えば、ペレット状、ハニカム状等が挙げられる。Any material may be used as long as it has stable properties even in a high temperature oxidizing atmosphere of about 1500 t:
Specific examples of these include cordierite, mullite, α
- Ceramic carriers such as aluminum, mina, zirconia spinel, titania, etc. can be mentioned. The shape of the carrier is not particularly limited as long as it is a shape normally used as a catalyst, and examples thereof include pellets, honeycomb shapes, and the like.
本発明において使用される金属及びセラミックウィスカ
ーを含有するr −Aj203相は、活性担体としての
機能を有するものである。r Altos層に添加さ
れる前記金属の配合量は、その総量がγ−M、0.に対
して5〜30重斌チであることが好ましく、更に好まし
くは10〜20重量%である。rAntOs層に添加す
る金属の量が5重量−未満であると、耐熱性の向上が認
められず、一方、30重量%を超えると、前記金属の酸
化物かり、0.の粒界に多量に析出り、 r−Aノ、
03層の機械的強度が低下する。The r-Aj203 phase containing metal and ceramic whiskers used in the present invention functions as an active carrier. r The amount of the metal added to the Altos layer is such that the total amount is γ-M, 0. It is preferably 5 to 30 weight percent, more preferably 10 to 20 weight percent. If the amount of metal added to the rAntOs layer is less than 5% by weight, no improvement in heat resistance will be observed, while if it exceeds 30% by weight, the metal oxide will be added to the rAntOs layer. A large amount precipitates at the grain boundaries of r-A,
The mechanical strength of the 03 layer decreases.
r −Q、0.層に添加されるセラミックウィスカーの
配合量は、その総量がr −AJ203に対して1〜3
0重*チであることが好ましく、更に好ましくは1〜1
0重邦−チである。r AJ203層に添加するセラ
ミックウィスカーの月がI N、 fi: %未満であ
ると、高温における強度の向上が認められず、一方、3
0重量%を超える場合には、高温における強度が飽和し
て触媒活性が低下する。r-Q, 0. The amount of ceramic whiskers added to the layer is such that the total amount is 1 to 3 with respect to r-AJ203.
It is preferably 0 weight*chi, more preferably 1 to 1
This is 0 Jubuni-chi. When the amount of ceramic whiskers added to the AJ203 layer is less than %, no improvement in strength at high temperatures is observed;
If it exceeds 0% by weight, the strength at high temperatures will be saturated and the catalyst activity will decrease.
本発明において使用されるセラミックウィスカーとして
は、例えば、炭化珪素(SiC)、[化珪素(Sio2
)bアルミナ()J20B )等のセラミックウィスカ
ーが挙げられ、これらから成る群よシ選ばれたxmもし
くは2種以上のものが使用される。Examples of ceramic whiskers used in the present invention include silicon carbide (SiC), [silicon whisker]
Ceramic whiskers such as )b alumina ()J20B) can be used, and xm or two or more selected from the group consisting of these whiskers are used.
本発明において使用される貴金属触媒のpt及び/又は
Pdの担持量は將に限定されないが、触媒全量に対し0
.01〜lO重量%であることが好ましい。The amount of pt and/or Pd supported on the noble metal catalyst used in the present invention is not limited to 0.
.. 01 to 10% by weight is preferred.
上記した本発明の高温燃焼触媒は、例えば、次のように
して製造することができる。The high-temperature combustion catalyst of the present invention described above can be manufactured, for example, as follows.
先ず、γ−A403から成るアルミナコーティング組成
物に、Ce%I、a、 Srs Sns Zr及びMg
から成る群よシ選はれた少なくとも1拙の金属及びセラ
ミックウィスカーをそれぞれ所定量添加する。尚、前記
金属は、例えに、その金1itS塩とが好ましい。First, an alumina coating composition consisting of γ-A403 was coated with Ce% I, a, Srs Sns Zr and Mg
A predetermined amount of at least one metal whisker and a ceramic whisker selected from the group consisting of the following are added. Note that the metal is preferably its gold 1itS salt, for example.
次いで、上記組成物を、例えd5ボールミル等を用いて
固形物を粉砕する。このようにして得たコーティング用
液体を、面j熱性担体に流しかける等の操作により被色
ぜしめ、常温で充分乾燥した後、例えば、650Cで3
時間和gt焼成する。Next, the above-mentioned composition is pulverized to form a solid substance using, for example, a D5 ball mill. The coating liquid obtained in this way is colored by pouring it onto a thermal carrier, and after sufficiently drying at room temperature, it is heated for example at 650C for 3
Time sum gt firing.
この焼成担体を、所定量の触媒金属を溶解した溶液に浸
漬し、再び、常温で充分乾燥した後、最後に、例えば、
水素雰囲気中、550Cで3時間和度焼成することによ
り、本発明の融結を得ることが可能である。This fired carrier is immersed in a solution in which a predetermined amount of catalyst metal is dissolved, and then sufficiently dried again at room temperature, and finally, for example,
It is possible to obtain the fusion of the present invention by calcination at 550C for 3 hours in a hydrogen atmosphere.
尚、上記触媒金属は1例えば、塩化白金酸、塩化パラジ
ウム等の金り塩を水等に溶解した形で使用することが好
ましい。It is preferable to use the catalyst metal in the form of a gold salt such as chloroplatinic acid or palladium chloride dissolved in water or the like.
本発明の高温燃焼触媒が優れた耐熱性を有する理由は明
らかではないが、次のように考えることができる。Although the reason why the high temperature combustion catalyst of the present invention has excellent heat resistance is not clear, it can be considered as follows.
即ち、前記全組をr Aj!tOs層に添加したこと
により、γ−Aノ、0.相の結晶粒界が微細化している
ことが考えられる。そして、この粒界上に前記添加金属
が酸化物として析出しておシ、これらが貴金属触媒粒子
を粒界上に強く捕捉し、貴金属触媒粒子の熱移動を阻止
しているものと思われる。更に、微細化したr IJ
tOs層及び添加したセラミックウィスカーが、クラッ
クの発生及び伝播を阻止するために耐熱性が向上したも
のと考えられる。That is, r Aj! By adding it to the tOs layer, γ-A, 0. It is thought that the grain boundaries of the phase have become finer. It is believed that the added metal precipitates as oxides on the grain boundaries, and these strongly capture the noble metal catalyst particles on the grain boundaries, thereby inhibiting heat transfer to the noble metal catalyst particles. Furthermore, the miniaturized r IJ
It is believed that the tOs layer and the added ceramic whiskers prevent the generation and propagation of cracks, thereby improving heat resistance.
実施例1
次に示す組成のアルミナコーティング組成物を調製した
。Example 1 An alumina coating composition having the composition shown below was prepared.
上記組成物を、ボールミルを用いて、常温で2時間混合
し、固型物を粉砕した。The above composition was mixed using a ball mill at room temperature for 2 hours to pulverize the solid matter.
次いで、コージライト製ノ1ニカム状担体に、前記アル
ミナコーティング組成物を水に分散した液体を数回流し
かけた後、常温で約1日乾燥した。このハニカム状担体
を、 650Cで3時間焼成した。Next, a liquid obtained by dispersing the alumina coating composition in water was poured several times onto the cordierite unicum-shaped carrier, and then dried at room temperature for about 1 day. This honeycomb-shaped carrier was fired at 650C for 3 hours.
一方、水2ノに白金及びパラジウムがそれぞれ金属とし
て0.9g存在するように塩化白金酸及び塩化パラジウ
ムを溶解した水溶液を調製した。この水溶液に、前記ハ
ニカム状担体を1時間浸漬して、担体に貴金属触媒を含
浸させた。On the other hand, an aqueous solution was prepared in which chloroplatinic acid and palladium chloride were dissolved in water so that 0.9 g of platinum and palladium were each present as metals. The honeycomb-shaped carrier was immersed in this aqueous solution for 1 hour to impregnate the carrier with the noble metal catalyst.
次いで、このハニカム状担体を乾燥した後、水素雰囲気
中において、550Cで3時間力);成し、本発明に係
る高温燃焼触媒(A)を得た。Next, this honeycomb-shaped carrier was dried and then heated at 550C for 3 hours in a hydrogen atmosphere to obtain a high-temperature combustion catalyst (A) according to the present invention.
実施例2
実施例1と同様の手法により、アルミナコーティング組
成物に添加する金属塩として、他に硝酸ランタン、硝酸
ストロンチウム、硝酸スズ、硝酸ジルコニウム及び硝酸
マグネシウムを使用し、又、セラミックウィスカーとし
て、炭化珪素ウィスカー、酸化珪素ウィスカー及びアル
ミナウィスカーを使用し、それらの組み合わせ及び添加
量を変えて、表に示すような(B)〜(S)の18種類
の高温燃焼触媒を調製した。Example 2 Using the same method as in Example 1, lanthanum nitrate, strontium nitrate, tin nitrate, zirconium nitrate, and magnesium nitrate were used as metal salts added to the alumina coating composition, and carbonized ceramic whiskers were added as ceramic whiskers. Using silicon whiskers, silicon oxide whiskers, and alumina whiskers, 18 types of high-temperature combustion catalysts (B) to (S) as shown in the table were prepared by changing their combinations and amounts added.
比較例
同時に比較例として、それぞれ、アルミナコーティング
組成物に金属又はセラミッククイスカーの一方を添加し
ていないもの或いは両者を添加していないもの又は金属
添加量の多いものを実施例1と同様の手法によシ4種類
調製した。Comparative Example At the same time, as a comparative example, an alumina coating composition in which either metal or ceramic Quisker was not added, or both were added, or a large amount of metal was added was prepared using the same method as in Example 1. Four different types were prepared.
その組成を表に示す。Its composition is shown in the table.
実施例3
上記実施例1及び2で得た19種類の高温燃焼触媒及び
比較例で得た4種類の燃焼触媒について、それぞれ、流
通系試験装俗を用いてその燃焼特性を評価した。Example 3 The combustion characteristics of the 19 types of high-temperature combustion catalysts obtained in Examples 1 and 2 and the 4 types of combustion catalysts obtained in Comparative Examples were evaluated using a distribution test equipment.
尚、試験条件は、ガス流量;5ノ/miR,燃焼ガス濃
度;メタン(CH,)1%、触媒景;10CC及び空間
速度; 3 X iQ’hr−”である。The test conditions were: gas flow rate: 5 no/miR, combustion gas concentration: methane (CH,) 1%, catalyst density: 10 CC, and space velocity: 3 X iQ'hr-''.
次いで上記燃焼触媒を、熱処理炉に入れ、1100C及
び1400Cでそれぞれ50時間の熱処理を施した後、
前記と同様の方法で、それぞれその燃焼特性を評価した
。Next, the combustion catalyst was placed in a heat treatment furnace and heat treated at 1100C and 1400C for 50 hours, respectively.
The combustion characteristics of each were evaluated in the same manner as above.
以上の試験により得られたそれぞれの燃焼触媒の熱処理
前後における燃焼特性の比を、触媒活性保持率として計
算した。そhらの結果を、組成と共に、表に併記した。The ratio of combustion characteristics before and after heat treatment of each combustion catalyst obtained through the above test was calculated as the catalyst activity retention rate. The results are also listed in the table along with the composition.
更に、熱処理後の表面を観察し、下記の4段階で評価を
行ない、その結果も表に併記した。Furthermore, the surface after the heat treatment was observed and evaluated in the following four stages, and the results are also listed in the table.
◎ ・・・・・クラックなし、 ○・・・・・・クラックあシ。◎・・・No cracks, ○...Crack foot.
△・・・・・・一部剥離、 × ・・・・・・多量の剥hltあシ。△・・・・・・Partial peeling, ×...A lot of peeling hlt feet.
表から明らかなように、本発明の高温燃焼触媒は、比較
例のものに比べて、触媒の耐熱性の指標となる触媒活性
保持率並びに熱処理後の表面の形状が、格段に優れてい
ることが確認された。As is clear from the table, the high-temperature combustion catalyst of the present invention is significantly superior to the comparative example in terms of catalyst activity retention, which is an indicator of the heat resistance of the catalyst, and the surface shape after heat treatment. was confirmed.
尚、上記実施例においてはハニカム状担体を使用したが
、ベレット状担体を使用した場合にも同様の結果が得ら
れた。Although a honeycomb-shaped carrier was used in the above example, similar results were obtained when a pellet-shaped carrier was used.
本発明の高温燃焼触媒は、従来の貴金属系燃焼触媒に比
べて、大幅にその耐熱性が向上されたものである。従っ
て、エネルギーの節約及び効率的利用が可能であり、又
、 NOx等を発生させることなく燃焼が可能であるた
め、環境汚染等を惹き起こすことがないものである。The high temperature combustion catalyst of the present invention has significantly improved heat resistance compared to conventional noble metal combustion catalysts. Therefore, it is possible to save and use energy efficiently, and since it is possible to burn without generating NOx, etc., it does not cause environmental pollution.
第1図は貴金属系燃焼触媒の断面図、第2図は同じく平
面図である。
1・・・担体、2・・・r−、υ、03.3・・・貴金
属。
第1図
第2回
川崎市幸区小向東芝町1番地束
京芝浦電気株式会社総合研究所
内
0発 明 者 山中矢
川崎市幸区小向東芝町1番地束
京芝浦電気株式会社総合研究所
内
0発 明 者 肥塚淳次
川崎市幸区小向東芝町1番地束
京芝浦電気株式会社総合研究所
内
153−FIG. 1 is a sectional view of a noble metal combustion catalyst, and FIG. 2 is a plan view thereof. 1... Support, 2... r-, υ, 03.3... Noble metal. Figure 1 2nd Place: Inside the Research Institute of Kyoshi Shibaura Electric Co., Ltd., 1 Komukai Toshiba-cho, Saiwai-ku, Kawasaki City0 Inventor: Yamanakaya Inside the Research Institute of Kyoshi Shibaura Electric Co., Ltd., 1 Komukai Toshiba-cho, Saiwai-ku, Kawasaki City 0 Invention Author: Junji Koizuka 153-1, Komukai Toshiba-cho, Saiwai-ku, Kawasaki City, Shibaura Electric Co., Ltd. General Research Center
Claims (1)
ランタン(La )、ストロンチウム(Sr)、スズ(
Sn) 、ジルコニウムCZr)及びマグネシウム(M
g)から成る群より選ばれた少なくとも1種の金属とセ
ラミックウィスカーを含有するγ−アルミナ(γ−kl
hos )の被覆層;及び該r−アルミナ被覆層に担持
された白金(Pt)及び/又はパラジウム(Pd)から
成ることを特徴とする高温燃焼触媒。Heat-resistant carrier; cerium (Ce) provided on the carrier;
Lanthanum (La), strontium (Sr), tin (
Sn), zirconium CZr) and magnesium (M
γ-alumina (γ-kl) containing at least one metal selected from the group consisting of g) and ceramic whiskers;
1. A high-temperature combustion catalyst comprising: a coating layer of R-alumina; and platinum (Pt) and/or palladium (Pd) supported on the r-alumina coating layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57163092A JPS5952529A (en) | 1982-09-21 | 1982-09-21 | High temperature combustion catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57163092A JPS5952529A (en) | 1982-09-21 | 1982-09-21 | High temperature combustion catalyst |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5952529A true JPS5952529A (en) | 1984-03-27 |
Family
ID=15767028
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57163092A Pending JPS5952529A (en) | 1982-09-21 | 1982-09-21 | High temperature combustion catalyst |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5952529A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6022929A (en) * | 1983-07-15 | 1985-02-05 | Hitachi Ltd | Heat-resistant carrier for catalyst |
JPS6135851A (en) * | 1984-07-30 | 1986-02-20 | Hitachi Ltd | Catalyst carrier stable at high temperature and its preparation |
JPS62153158A (en) * | 1985-08-30 | 1987-07-08 | 東洋シーシーアイ株式会社 | Heat resistant composition and manufacture |
JPH03186347A (en) * | 1987-03-06 | 1991-08-14 | Hitachi Ltd | Heat-resistant catalyst and catalytic combustion method using the same |
US7699975B2 (en) | 2007-12-21 | 2010-04-20 | Uop Llc | Method and system of heating a fluid catalytic cracking unit for overall CO2 reduction |
US7699974B2 (en) | 2007-12-21 | 2010-04-20 | Uop Llc | Method and system of heating a fluid catalytic cracking unit having a regenerator and a reactor |
US7767075B2 (en) | 2007-12-21 | 2010-08-03 | Uop Llc | System and method of producing heat in a fluid catalytic cracking unit |
US7811446B2 (en) | 2007-12-21 | 2010-10-12 | Uop Llc | Method of recovering energy from a fluid catalytic cracking unit for overall carbon dioxide reduction |
US7932204B2 (en) | 2007-12-21 | 2011-04-26 | Uop Llc | Method of regenerating catalyst in a fluidized catalytic cracking unit |
US7935245B2 (en) | 2007-12-21 | 2011-05-03 | Uop Llc | System and method of increasing synthesis gas yield in a fluid catalytic cracking unit |
-
1982
- 1982-09-21 JP JP57163092A patent/JPS5952529A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6022929A (en) * | 1983-07-15 | 1985-02-05 | Hitachi Ltd | Heat-resistant carrier for catalyst |
JPS6135851A (en) * | 1984-07-30 | 1986-02-20 | Hitachi Ltd | Catalyst carrier stable at high temperature and its preparation |
JPS62153158A (en) * | 1985-08-30 | 1987-07-08 | 東洋シーシーアイ株式会社 | Heat resistant composition and manufacture |
JPH03186347A (en) * | 1987-03-06 | 1991-08-14 | Hitachi Ltd | Heat-resistant catalyst and catalytic combustion method using the same |
US7699975B2 (en) | 2007-12-21 | 2010-04-20 | Uop Llc | Method and system of heating a fluid catalytic cracking unit for overall CO2 reduction |
US7699974B2 (en) | 2007-12-21 | 2010-04-20 | Uop Llc | Method and system of heating a fluid catalytic cracking unit having a regenerator and a reactor |
US7767075B2 (en) | 2007-12-21 | 2010-08-03 | Uop Llc | System and method of producing heat in a fluid catalytic cracking unit |
US7811446B2 (en) | 2007-12-21 | 2010-10-12 | Uop Llc | Method of recovering energy from a fluid catalytic cracking unit for overall carbon dioxide reduction |
US7932204B2 (en) | 2007-12-21 | 2011-04-26 | Uop Llc | Method of regenerating catalyst in a fluidized catalytic cracking unit |
US7935245B2 (en) | 2007-12-21 | 2011-05-03 | Uop Llc | System and method of increasing synthesis gas yield in a fluid catalytic cracking unit |
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