JPH0771633B2 - Method for producing large surface area alumina for high temperature catalytic combustion - Google Patents
Method for producing large surface area alumina for high temperature catalytic combustionInfo
- Publication number
- JPH0771633B2 JPH0771633B2 JP4084740A JP8474092A JPH0771633B2 JP H0771633 B2 JPH0771633 B2 JP H0771633B2 JP 4084740 A JP4084740 A JP 4084740A JP 8474092 A JP8474092 A JP 8474092A JP H0771633 B2 JPH0771633 B2 JP H0771633B2
- Authority
- JP
- Japan
- Prior art keywords
- surface area
- alumina
- high temperature
- catalytic combustion
- large surface
- 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.)
- Expired - Lifetime
Links
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 title claims description 25
- 238000007084 catalytic combustion reaction Methods 0.000 title claims description 13
- 238000004519 manufacturing process Methods 0.000 title claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 26
- 239000000377 silicon dioxide Substances 0.000 claims description 13
- 238000000576 coating method Methods 0.000 claims description 8
- 238000002485 combustion reaction Methods 0.000 claims description 8
- 239000013078 crystal Substances 0.000 claims description 8
- 238000010304 firing Methods 0.000 claims description 8
- 239000011248 coating agent Substances 0.000 claims description 7
- -1 aluminum carboxyhydroxide Chemical compound 0.000 claims description 4
- 239000003054 catalyst Substances 0.000 claims description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 14
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 6
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 238000000034 method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 3
- ATRRKUHOCOJYRX-UHFFFAOYSA-N Ammonium bicarbonate Chemical compound [NH4+].OC([O-])=O ATRRKUHOCOJYRX-UHFFFAOYSA-N 0.000 description 2
- 229910000013 Ammonium bicarbonate Inorganic materials 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- SNAULWNXYOHFLC-UHFFFAOYSA-L [O-]C([O-])=O.N.[Al+3] Chemical compound [O-]C([O-])=O.N.[Al+3] SNAULWNXYOHFLC-UHFFFAOYSA-L 0.000 description 2
- 235000011124 aluminium ammonium sulphate Nutrition 0.000 description 2
- LCQXXBOSCBRNNT-UHFFFAOYSA-K ammonium aluminium sulfate Chemical compound [NH4+].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O LCQXXBOSCBRNNT-UHFFFAOYSA-K 0.000 description 2
- 235000012538 ammonium bicarbonate Nutrition 0.000 description 2
- 239000001099 ammonium carbonate Substances 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000003345 natural gas Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 229910015999 BaAl Inorganic materials 0.000 description 1
- 229910000873 Beta-alumina solid electrolyte Inorganic materials 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 239000012876 carrier material Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01F—COMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
- C01F7/00—Compounds of aluminium
- C01F7/02—Aluminium oxide; Aluminium hydroxide; Aluminates
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)
- Catalysts (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、高温触媒燃焼用の担体
材料となるアルミナの製造法に係り、特に大表面積を有
する高温触媒燃焼用アルミナの製造法に関するものであ
る。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing alumina , which is a carrier material for high temperature catalytic combustion, and has a large surface area.
The present invention relates to a method for producing alumina for high temperature catalytic combustion .
【0002】[0002]
【従来の技術】現在、ボイラーやガスタービン等を稼働
させるに必要なエネルギーは、石油、石炭、天然ガス等
を触媒不在下で空気により燃焼させる火炎燃焼でまかな
われている。火炎燃焼では燃焼温度が2000℃にも達
するので、空気中の窒素が酸化されて窒素酸化物(サー
マルNOxという)となり、燃焼排ガスと共に大気中に
放出されて地球環境に有害な影響を与える。これに対し
て、触媒燃焼では大過剰の空気で希釈された天然ガス等
の燃料を触媒層で着火・燃焼させるので、火炎燃焼の場
合ほど高温にはならず、窒素酸化物の生成を極めて少な
くすることができる。さらに、触媒不在下では燃焼不可
能な希薄な燃料でも触媒燃焼では安定燃焼が継続可能で
あるため、省資源の観点からも極めて好都合な燃焼シス
テムと言える。2. Description of the Related Art Currently, the energy required to operate a boiler, a gas turbine, etc. is provided by flame combustion in which oil, coal, natural gas, etc. are burned by air in the absence of a catalyst. In flame combustion, the combustion temperature reaches 2000 ° C., so that nitrogen in the air is oxidized to form nitrogen oxides (referred to as thermal NOx), which are released into the atmosphere together with the combustion exhaust gas, which adversely affects the global environment. On the other hand, in catalytic combustion, a fuel such as natural gas diluted with a large excess of air is ignited and burned in the catalyst layer, so the temperature does not become as high as in flame combustion and the generation of nitrogen oxides is extremely small. can do. Furthermore, even a lean fuel that cannot be combusted in the absence of a catalyst can continue stable combustion by catalytic combustion, so it can be said that it is an extremely convenient combustion system from the viewpoint of resource saving.
【0003】高温触媒燃焼用担体材料として、従来ラン
タン・β―アルミナ(La・β-Al2O3)やバリウムヘキサ
アルミネート(BaAl12O19)等が知られているが、これ
らは結晶構造上アルミナとは別種のものである。アルミ
ナは1100℃以上で加熱すると容易に相転移して結晶
構造的に安定なα―アルミナとなり、表面積が5m2/g
以下に激減する。アルミナ表面をシリカコーティングし
て相転移を抑制し、大表面積化する方法が知られている
が、その製品を1300℃以上で高温焼成した後の表面
積について調べられた例は皆無である。参考例に示すよ
うに、表面をシリカコーティングしたη―アルミナ(触
媒学会参照アルミナ,ALO―4)の場合、1300〜
1400℃焼成後の表面積は20m2/gに遠く及ばず、
ALO―4へのシリカコーティング法では大表面積化し
得ない。[0003] As support material for high temperature catalytic combustion, although conventional lanthanum · beta-alumina (La · β-Al 2 O 3) or barium hexaaluminate (BaAl 12 O 19) or the like are known, which are crystal structures It is a different kind of upper alumina. Alumina easily undergoes a phase transition when heated above 1100 ° C to become α-alumina with a stable crystal structure, and has a surface area of 5 m 2 / g.
Decrease to the following. There is known a method of coating the alumina surface with silica to suppress the phase transition and increase the surface area, but there is no example where the surface area of the product after high temperature firing at 1300 ° C. or higher was examined. As shown in the reference example, in the case of η-alumina whose surface is coated with silica (alumina referenced by the Catalysis Society, ALO-4), 1300-300
The surface area after firing at 1400 ° C is far below 20 m 2 / g,
The silica coating method on ALO-4 cannot increase the surface area.
【0004】本発明者らは鋭意研究を進めた結果、アル
ミナ源として針状結晶のカルボキシ水酸化アルミニウム
アンモニウムを選び、この表面をシリカコーティングし
て焼成する方法により、1300℃焼成後で35m2/g
以上、1400℃焼成後で20m2/g以上という大表面
積を有するアルミナの製造に成功したものである。As a result of intensive studies, the inventors of the present invention selected needle-shaped crystal ammonium carboxyaluminum hydroxide as an alumina source, coated the surface with silica, and baked it at 1300 ° C. for 35 m 2 / g
As described above, the alumina having a large surface area of 20 m 2 / g or more after firing at 1400 ° C. has been successfully manufactured.
【0005】[0005]
【発明が解決しようとする課題】本発明が解決しようと
する課題は、1400℃という過酷な温度条件下におい
て焼成されても、なお20m2/gを上回る大表面積が
維持され得る、熱安定性に優れた高温触媒燃焼用アルミ
ナの製造法を提供することにある。 An object of the present invention is [0005] to be Solved, severe temperature conditions smell that 1400 ℃
Be fired Te still greater than 20 m 2 / g larger surface area
Aluminum for high temperature catalytic combustion with excellent thermal stability that can be maintained
To provide a manufacturing method for the
【0006】[0006]
【課題を解決するための手段】そして、上記の如き課題
を解決するために、本発明は、カルボキシ水酸化アルミ
ニウムアンモニウム[Al(NH4)CO3(O
H)2]の針状結晶をアルミナ源として用い、その表面
をシリカコーティングした後、焼成することにより、高
温触媒燃焼用大表面積アルミナを製造することを特徴と
する。また、このような本発明手法の好ましい態様によ
れば、前記シリカコーティングには、テトラエトキシシ
ランが用いられ、更に高温触媒燃焼への適用を考慮すれ
ば、前記焼成は1300〜1400℃で実施されること
となる。 [Means for Solving the Problems] And the above problems
In order to solve the above, the present invention provides an aluminum ammonium carboxyhydroxide [Al (NH 4 ) CO 3 (O
H) 2 ] needle-like crystals are used as a source of alumina, and the surface thereof is coated with silica, followed by firing to obtain a high
Characterized by producing large surface area alumina for warm catalytic combustion
To do. In addition, according to such a preferred embodiment of the method of the present invention,
If the silica coating is
Runs are used, and even considering application to high temperature catalytic combustion
For example, the firing should be performed at 1300 to 1400 ° C.
Becomes
【0007】より具体的には、本発明にかかわるアルミ
ナの調製は、以下の通りである。まず、出発物質となる
カルボキシ水酸化アルミニウムアンモニウムの針状結晶
は、既に確立された方法(特開平2−62485)によ
り合成する。すなわち、炭酸水素アンモニウム水溶液に
アンモニウム明ばん水溶液を室温下で攪はんしながら加
え、生成した沈殿を密封容器に移して100℃で24時
間熟成する。得られた内容物を吸引ろ過して水洗後、エ
タノール洗浄を繰り返して水をエタノールで置換し、テ
トラエトキシシランのエタノール溶液を添加して乾燥す
る。その後電気炉中で1300〜1400℃で焼成して
本発明品とする。 More specifically, the preparation of alumina according to the present invention is as follows. First, needle-like crystals of ammonium aluminum carboxyhydroxide as a starting material are synthesized by the method already established (JP-A-2-62485). That is, an aqueous solution of ammonium alum is added to an aqueous solution of ammonium hydrogen carbonate with stirring at room temperature, and the generated precipitate is transferred to a sealed container and aged at 100 ° C. for 24 hours. The obtained contents are suction filtered and washed with water, and then ethanol washing is repeated to replace water with ethanol, and an ethanol solution of tetraethoxysilane is added and dried. After that, the product of the present invention is obtained by firing at 1300 to 1400 ° C in an electric furnace.
【0008】[0008]
【発明の効果】本発明に従う高温触媒燃焼用大表面積ア
ルミナの製造法によれば、アルミナ源として、カルボキ
シ水酸化アルミニウムアンモニウム[Al(NH 4 )C
O 3 (OH) 2 ]の針状結晶を用い、その表面をシリカ
コーティングした後に焼成するところから、目的とする
アルミナが高温で焼成される場合でも、アルミナの相転
移が有利に抑制され得、以てこれまでに報告されている
何れの例よりも大きな表面積を有する高温触媒燃焼用ア
ルミナが有利に得られるのである。以下、実施例におい
て本発明を詳細に説明する。The large surface area for high temperature catalytic combustion according to the present invention
According to the method of manufacturing Lumina, the
Aluminum ammonium hydroxide [Al (NH 4 ) C
O 3 (OH) 2 ] needle-like crystals are used, and the surface thereof is silica.
From the place of baking after coating, make the target
Even when alumina is fired at high temperature
Transfer can be advantageously suppressed and thus has a higher surface area for high temperature catalytic combustion than any of the previously reported examples.
Lumina is obtained in an advantageous manner. Hereinafter, the present invention will be described in detail with reference to Examples.
【0009】[0009]
【実施例】まず、出発物質となるカルボキシ水酸化アル
ミニウムアンモニウムの針状結晶は、既に確立された方
法(特開平2―62485)により合成した。すなわ
ち、濃度1.2モル/lの炭酸水素アンモニウム水溶液
に0.1モル/lのアンモニウム明ばん水溶液を室温下
で攪はんしながら加え、生成した沈澱をテフロン製の密
封容器に移して100℃で24時間熟成する。得られた
内容物を吸引ろ過して水洗後、エタノール洗浄を繰り返
して水をエタノールで置換し、テトラエトキシシランの
エタノール溶液を添加して80℃で乾燥する。得られた
乾燥粉末を電気炉中で1300〜1400℃で5時間焼
成して本発明品とした。なお、昇温速度は10℃/分で
あり、降温は自然放冷にまかせた。また、表面コーティ
ングに用いたテトラエトキシシランの量は、アルミナ単
位重量当り0.046〜0.173gである。EXAMPLES First, needle-shaped crystals of ammonium carboxyaluminum hydroxide as a starting material were synthesized by an already established method (JP-A-2-62485). That is, an aqueous solution of ammonium hydrogen carbonate having a concentration of 1.2 mol / l and an aqueous solution of ammonium alum having a concentration of 0.1 mol / l were added with stirring at room temperature, and the formed precipitate was transferred to a Teflon-sealed container to obtain 100 Aging at 24 ° C for 24 hours. The obtained content is suction filtered and washed with water, and then ethanol washing is repeated to replace water with ethanol, an ethanol solution of tetraethoxysilane is added, and the mixture is dried at 80 ° C. The obtained dry powder was fired in an electric furnace at 1300 to 1400 ° C. for 5 hours to obtain a product of the present invention. The temperature rising rate was 10 ° C./minute, and the temperature was left to cool naturally. The amount of tetraethoxysilane used for the surface coating is 0.046 to 0.173 g per unit weight of alumina.
【0010】表1に、シリカ量を変えて表面コーティン
グを行ったアルミナの表面積測定結果をまとめた。同表
にはシリカコーティングを行っていないアルミナの表面
積も示してある。Table 1 summarizes the surface area measurement results of alumina surface-coated with varying amounts of silica. The table also shows the surface area of alumina without silica coating.
【0011】[0011]
【表1】 [Table 1]
【0012】[0012]
【参考例】触媒学会参照アルミナ(ALO―4)の粉末
をアルミナ源とし、これをそのままエタノール中に分散
させてテトラエトキシシランを0.1,0.2および
0.5CC加え、80℃で一夜乾燥した後、それぞれの温
度で5時間焼成したものを、参照シリカコーティングア
ルミナとし、表面積測定結果を表2にまとめた。同表に
は、シリカコーティングを行っていないALO−4の表
面積も示した。[Reference Example] Catalysis Society Reference Alumina (ALO-4) powder was used as an alumina source, and this was dispersed in ethanol as it was, and tetraethoxysilane was added at 0.1, 0.2 and 0.5 CC, and the mixture was kept at 80 ° C overnight. After being dried and calcined at each temperature for 5 hours, reference silica-coated alumina was used, and the surface area measurement results are summarized in Table 2. The table also shows the surface area of ALO-4 without silica coating.
【0013】[0013]
【表2】 [Table 2]
Claims (3)
ウム[Al(NH 4 )CO 3 (OH) 2 ]の針状結晶を
アルミナ源とし、その表面をシリカコーティングした
後、焼成することを特徴とする高温触媒燃焼用大表面積
アルミナの製造法。 1. Ammoni of aluminum carboxyhydroxide
Needle crystals of um [Al (NH 4 ) CO 3 (OH) 2 ]
Alumina source, whose surface was coated with silica
Large surface area for high temperature catalytic combustion characterized by subsequent firing
Alumina manufacturing method.
キシシランを用いて行なわれる請求項1記載の高温触媒
燃焼用大表面積アルミナの製造法。 2. The silica coating is tetraeth
The high temperature catalyst according to claim 1, which is carried out using xylsilane.
A method for producing large surface area alumina for combustion.
度で実施される請求項1又は請求項2記載の高温触媒燃
焼用大表面積アルミナの製造法。 3. The firing is performed at a temperature of 1300 to 1400 ° C.
High temperature catalytic combustion according to claim 1 or 2
Manufacturing method of large surface area alumina for baking.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4084740A JPH0771633B2 (en) | 1992-03-06 | 1992-03-06 | Method for producing large surface area alumina for high temperature catalytic combustion |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4084740A JPH0771633B2 (en) | 1992-03-06 | 1992-03-06 | Method for producing large surface area alumina for high temperature catalytic combustion |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH05245369A JPH05245369A (en) | 1993-09-24 |
| JPH0771633B2 true JPH0771633B2 (en) | 1995-08-02 |
Family
ID=13839098
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4084740A Expired - Lifetime JPH0771633B2 (en) | 1992-03-06 | 1992-03-06 | Method for producing large surface area alumina for high temperature catalytic combustion |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0771633B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111484052B (en) * | 2020-04-21 | 2023-07-07 | 哈尔滨霈泽材料科技有限公司 | Preparation method of needled alumina carrier |
| CN111468109B (en) * | 2020-04-21 | 2023-06-20 | 天津泽希新材料有限公司 | Alumina material |
-
1992
- 1992-03-06 JP JP4084740A patent/JPH0771633B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH05245369A (en) | 1993-09-24 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |