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JPH0438690B2 - - Google Patents
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JPH0438690B2 - - Google Patents

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Publication number
JPH0438690B2
JPH0438690B2 JP59024348A JP2434884A JPH0438690B2 JP H0438690 B2 JPH0438690 B2 JP H0438690B2 JP 59024348 A JP59024348 A JP 59024348A JP 2434884 A JP2434884 A JP 2434884A JP H0438690 B2 JPH0438690 B2 JP H0438690B2
Authority
JP
Japan
Prior art keywords
alumina
porous
bubbles
porous body
producing
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
Application number
JP59024348A
Other languages
Japanese (ja)
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JPS60171220A (en
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 filed Critical
Priority to JP2434884A priority Critical patent/JPS60171220A/en
Publication of JPS60171220A publication Critical patent/JPS60171220A/en
Publication of JPH0438690B2 publication Critical patent/JPH0438690B2/ja
Granted legal-status Critical Current

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  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Description

【発明の詳細な説明】 本発明はアルミナ多孔体の製造方法に関し、さ
らに詳しくは結晶水を有するアルミニウム塩粉末
またはそれらの濃厚溶液、例えば硫酸アルミニウ
ム粉末、硝酸アルミニウム粉末またはそれらの濃
厚溶液を加熱することにより発泡させて微細な気
泡を多量に有する極めて多孔性でカサ密度が非常
に小さい、特に触媒担体、吸着材、フイルターお
よび高温断熱材として好適なアルミナ多孔体の製
造方法に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for producing an alumina porous body, and more specifically, the present invention relates to a method for producing an alumina porous body, and more particularly, the present invention relates to a method for producing an alumina porous body, and more particularly, aluminum salt powder or a concentrated solution thereof having water of crystallization, such as aluminum sulfate powder, aluminum nitrate powder, or a concentrated solution thereof, is heated. The present invention relates to a method for producing an alumina porous material that is foamed to have a large amount of fine air bubbles, is extremely porous, has a very low bulk density, and is particularly suitable as a catalyst carrier, an adsorbent, a filter, and a high-temperature heat insulating material.

アルミナは耐熱度が高く化学的安定性、耐薬品
性に優れているため工業的に広く利用されてい
る。特に多孔性のアルミナ、アルミナバブルの成
形品は触媒、触媒担体、吸着材、フイルターおよ
び高温断熱材としてその用途は広い。
Alumina is widely used industrially because it has high heat resistance, chemical stability, and chemical resistance. In particular, porous alumina and alumina bubble molded products have a wide range of uses as catalysts, catalyst carriers, adsorbents, filters, and high-temperature insulation materials.

しかし従来のアルミナ多孔体の製造方法は以下
に挙げる如き方法があるが、それぞれ欠点があ
る。すなわち 1 電融アルミナを空気ジエツトで飛ばしてバブ
ルとし、該バブルをバインダーで固める方法 2 ポリアルミナキサンを媒体中に滴下して球状
物となし、該球状物を分離し、焼成してアルミ
ナ微小中空体となしたのちバインダーと混合し
て成形する方法 3 アルミナ質原料に可燃物を混合し成形後、焼
成して可燃物を燃焼消失させる方法 4 アルミナ質泥漿原料に発泡剤を混合して焼成
する方法 5 ウレタンフオームにアルミナの泥漿原料を固
着させたのち、焼成しウレタンフオームを燃焼
消失させる方法 などであるが、いずれの方法も種々の欠点があ
る。これらの製造方法に共通する欠点としては製
造方法が複雑で製造コストが高いことである。さ
らに1)はバブル製造中にアルミナが繊維状とな
りバブルの収率が悪いこと、2)は1)も同様の
欠点を有するが、バブルをバインダーと混合して
成形するため最終製品が均一な気泡を有する多孔
体になりにくいことなどである。
However, conventional methods for producing porous alumina bodies include the following methods, each of which has drawbacks. Namely, 1. A method in which fused alumina is blown away with an air jet to form bubbles, and the bubbles are solidified with a binder. 2. Polyaluminaxane is dropped into a medium to form spherical objects, and the spherical objects are separated and fired to form alumina micro-hollows. Method 3: Mixing a combustible material with an alumina raw material, molding it, and then firing it to burn out the combustible material. Method 4: Mixing a foaming agent with an alumina slurry raw material and firing it. Method 5 There is a method in which an alumina slurry raw material is fixed to a urethane foam and then the urethane foam is burnt out by firing, but each method has various drawbacks. A common drawback of these manufacturing methods is that they are complicated and the manufacturing costs are high. Furthermore, in 1), the alumina becomes fibrous during bubble production, resulting in a poor bubble yield, and in 2), although 1) has the same drawbacks, the final product has uniform bubbles because the bubbles are mixed with a binder and molded. The reason for this is that it is difficult to become a porous body.

本発明者らはこれら欠点のないアルミナ多孔体
の製造方法につき種々研究を重ねた結果、結晶水
を有するアルミニウム塩を原料として選ぶことに
より製造工程が簡単で極めて安定した気泡を導入
できカサ密度が小さく、しかも製造コストが安い
アルミナ多孔体の製造方法を見出し本発明を完成
した。その要旨は結晶水を有する硫酸アルミニウ
ム及び/または硝酸アルミニウム、またはそれら
の濃厚溶液を特定条件で加熱処理することにより
アルミナ多孔体を製造する方法にある。
The inventors of the present invention have conducted various studies on a method for producing porous alumina that does not have these drawbacks, and found that by selecting an aluminum salt containing water of crystallization as a raw material, the production process is simple, extremely stable bubbles can be introduced, and the bulk density can be reduced. The present invention was completed by discovering a method for producing an alumina porous body that is small and inexpensive to produce. The gist is a method for producing an alumina porous body by heat-treating aluminum sulfate and/or aluminum nitrate containing water of crystallization, or a concentrated solution thereof under specific conditions.

本発明をさらに詳しく述べると、硫酸アルミニ
ウム(Al2(SO43・3〜18H2O)、硝酸アルミニ
ウム(Al(NO33・9H2O)の如き結晶水を有す
るアルミニウム塩の1種または2種を約300メツ
シユ以下に粉砕または粉砕せずして粉状のまま、
あるいは該塩に水等の溶剤を加えて濃厚溶液とし
たものを耐熱容器、例えば白金ルツボに入れ電気
炉中で加熱する。加熱昇温速度および加熱温度は
それぞれ毎分0.5〜30℃及び980℃以上である。
To describe the present invention in more detail, one of the aluminum salts having water of crystallization such as aluminum sulfate (Al 2 ( SO 4 ) 3.3-18H 2 O) and aluminum nitrate (Al(NO 3 ) 3.9H 2 O) The seeds or two seeds are crushed to less than about 300 mesh, or left in powder form without being crushed,
Alternatively, a concentrated solution by adding a solvent such as water to the salt is placed in a heat-resistant container, such as a platinum crucible, and heated in an electric furnace. The heating rate and heating temperature are 0.5 to 30°C per minute and 980°C or higher, respectively.

本発明方法は出発原料、原料の量、昇温速度お
よび加熱最高温度を制御することにより各種のア
ルミナ多孔体を得ることができる。例えば硫酸ア
ルミニウム(18水塩)を数グラム〜10グラム程度
を内容積約30c.c.の白金ルツボに入れ毎分10℃で約
980℃まで加熱するとχアルミナ多孔体が得られ、
さらに1100℃以上まで加熱するとαアルミナ多孔
体が得られる。また硝酸アルミニウム(9水塩)
では他の条件は硫酸アルミニウムと同じにして、
1000℃以上まで加熱するとαアルミナ多孔体が得
られる。
In the method of the present invention, various porous alumina bodies can be obtained by controlling the starting raw materials, the amount of raw materials, the heating rate, and the maximum heating temperature. For example, several grams to 10 grams of aluminum sulfate (18 hydrate) are placed in a platinum crucible with an internal volume of approximately 30 c.c. and heated at 10°C per minute.
When heated to 980℃, χ alumina porous material is obtained,
Further heating to 1100°C or higher yields an α-alumina porous material. Also aluminum nitrate (9 hydrate)
Now, keeping the other conditions the same as for aluminum sulfate,
When heated to 1000℃ or higher, an α-alumina porous material is obtained.

加熱過程での電気炉内の雰囲気は酸化性雰囲
気、還元性雰囲気、中性雰囲気、硫化水素等の腐
食性雰囲気のいずれでもよいが、経済的には空気
中が有利である。
The atmosphere in the electric furnace during the heating process may be an oxidizing atmosphere, a reducing atmosphere, a neutral atmosphere, or a corrosive atmosphere such as hydrogen sulfide, but air is economically advantageous.

電気炉を加熱して行く過程での原料の変化は例
えば硫酸アルミニウム18水塩の場合、加熱し始め
てから約120℃に達したとき原料が発泡し始め、
約380℃で発泡は終了するが、脱硫を完全にして
アルミナ多孔体にするためには、980℃以上まで
加熱処理するのが好ましい。
For example, in the case of aluminum sulfate 18 hydrate, the raw material begins to foam when it reaches approximately 120°C after heating begins.
Foaming ends at about 380°C, but in order to complete desulfurization and create a porous alumina material, it is preferable to heat the material to 980°C or higher.

本発明方法において使用する原料は粉末で使用
する場合は300メツシユ以下が好ましい。原料の
粒度が粗いと気孔体中の気泡が粗大となり気泡の
小さいものが得られる。また均一な気泡のものを
得ようとするならば原料粒度をできるだけ狭い範
囲に揃える方がよい。
When the raw material used in the method of the present invention is used in the form of powder, it is preferably 300 mesh or less. If the particle size of the raw material is coarse, the bubbles in the porous body will become coarse and a product with small bubbles will be obtained. In addition, in order to obtain uniform bubbles, it is better to adjust the particle size of the raw material within the narrowest possible range.

原料は粉末のままでもよいし、水等の溶剤を加
えて濃厚溶液にしてから加熱処理してもよい。ま
た溶液濃度はできるだけ濃厚な方がよい。
The raw material may be used as a powder, or it may be heat-treated after being made into a concentrated solution by adding a solvent such as water. In addition, the solution concentration should be as high as possible.

さらに微細な気泡を得たい場合電気炉内雰囲気
を加圧下で加熱するのが有利である。電気炉内の
昇温速度は0.5〜30℃/分が好ましく、昇降温度
が遅いと微細な気泡が得られ、速いと粗大な気泡
となる傾向がある。
If it is desired to obtain even finer bubbles, it is advantageous to heat the atmosphere in the electric furnace under pressure. The temperature increase rate in the electric furnace is preferably 0.5 to 30°C/min; if the temperature increase/decrease is slow, fine bubbles are obtained, and if it is fast, coarse bubbles tend to occur.

本発明を実施するに当り、原料中にあらかじめ
無機質繊維、例えばアルミナ繊維を短く切断した
ものを添加混合しておけば繊維を複合したアルミ
ナ多孔体を製造することができる。
In carrying out the present invention, if inorganic fibers, such as alumina fibers cut into short lengths, are added and mixed into the raw materials in advance, an alumina porous body containing fibers can be produced.

次に本発明の実施例を示す。 Next, examples of the present invention will be shown.

実施例 1 試薬の硫酸アルミニウム18水塩を300メツシユ
以下に粉砕し出発原料とした。
Example 1 Aluminum sulfate 18 hydrate, a reagent, was ground to 300 mesh or less and used as a starting material.

前記粉砕原料を3g採り、内容積10cm3の白金ル
ツボに入れ横型電気炉内に挿入した。10℃/分の
一定昇温速度で約980℃まで加熱すると多孔体が
得られた。カサ密度は約0.08g/mlであつた。X
線粉末回折測定では極めて非晶質に近いパターン
を示しχアルミナと同定された。
3 g of the pulverized raw material was taken and placed in a platinum crucible with an internal volume of 10 cm 3 and inserted into a horizontal electric furnace. A porous body was obtained by heating to about 980°C at a constant heating rate of 10°C/min. The bulk density was approximately 0.08 g/ml. X
Line powder diffraction measurements showed an extremely amorphous pattern and it was identified as χ alumina.

この多孔体をさらに1100℃まで加熱し放冷する
とカサ密度約0.14g/mlのαアルミナ多孔体が得
られた。
This porous body was further heated to 1100° C. and allowed to cool, yielding an α-alumina porous body having a bulk density of about 0.14 g/ml.

実施例 2 試薬の含水硫酸アルミニウム(14〜18水塩)50
gを44mμ以下に粉砕し、内寸法5×10×2cmの
焼結アルミナ製型わくに入れ、昇温速度10℃/分
で1000℃まで加熱し、その温度で30分間保持した
ところ、X線回折ではηアルミナと同定されるア
ルミナ多孔体(カサ密度約0.06g/ml)が得られ
た。
Example 2 Reagent hydrated aluminum sulfate (14-18 hydrate) 50
g was crushed to 44 mm or less, placed in a sintered alumina mold with internal dimensions of 5 x 10 x 2 cm, heated at a temperature increase rate of 10°C/min to 1000°C, and held at that temperature for 30 minutes. A porous alumina material identified by diffraction as η alumina (bulk density approximately 0.06 g/ml) was obtained.

このアルミナ多孔体の組織は径約0.1mmの気泡
体からなつており、その壁(1〜3μm厚)は極
く微粒のηアルミナ粒子(X線回折のピークの広
がりから約30Å程度と推定される)で形成される
ため、その比表面積は比較的大きく、BET1点法
による比表面積は156m2/gであつた。これは当
初類似の構造をもつと思われた発泡パーライトの
比表面積1m2/g(上記と同様の方法で測定)に
比べて極めて大である。
The structure of this alumina porous material is composed of bubbles with a diameter of about 0.1 mm, and the walls (1 to 3 μm thick) are made up of extremely fine η-alumina particles (estimated to be about 30 Å from the broadening of the X-ray diffraction peak). The specific surface area was relatively large, and the specific surface area measured by the BET 1-point method was 156 m 2 /g. This is extremely large compared to the specific surface area of 1 m 2 /g (measured by the same method as above) of expanded pearlite, which was initially thought to have a similar structure.

またこのアルミナ多孔体は独立した気泡体から
なつているため、断熱性が高く、20〜25℃の熱伝
導率は0.028Kcal/m・h・℃であつた。
Moreover, since this alumina porous body is composed of independent cells, it has high heat insulation properties, and its thermal conductivity at 20 to 25°C was 0.028 Kcal/m·h·°C.

実施例 3 試薬の含水硫酸アルミニウム(14〜18水塩)50
gを水50c.c.に溶解して濃厚溶液とし、蒸発皿にて
加温して若干の水をとばして粘稠な液体を得た。
これを実施例2と同様の型わくに流し込み、室温
で冷却して固化した後、実施例2と同様の方法で
加熱した。
Example 3 Reagent hydrated aluminum sulfate (14-18 hydrate) 50
g was dissolved in 50 c.c. of water to make a concentrated solution, and heated in an evaporating dish to evaporate some of the water to obtain a viscous liquid.
This was poured into the same mold as in Example 2, cooled at room temperature to solidify, and then heated in the same manner as in Example 2.

得られたアルミナ多孔体(X線回折はηアルミ
ナと同定)は実施例2の多孔体とほぼ同様の組
織・性状を有し、そのカサ密度は0.06g/ml、比
表面積は150m2/g、20〜25℃の熱伝導率は
0.031Kcal/m・h・℃であつた。
The obtained porous alumina material (identified as η alumina by X-ray diffraction) had almost the same structure and properties as the porous material of Example 2, with a bulk density of 0.06 g/ml and a specific surface area of 150 m 2 /g. , the thermal conductivity at 20-25℃ is
It was 0.031Kcal/m・h・℃.

Claims (1)

【特許請求の範囲】[Claims] 1 結晶水を有する硫酸アルミニウム粉末及び/
または硝酸アルミニウム粉末、またはそれらの濃
厚溶液を毎分0.5〜30℃の加熱昇温速度および980
℃以上の加熱温度で加熱処理することを特徴とす
るアルミナ多孔体の製造方法。
1 Aluminum sulfate powder with water of crystallization and/or
or aluminum nitrate powder, or their concentrated solutions at a heating rate of 0.5-30℃ per minute and 980℃
1. A method for producing an alumina porous material, characterized by heat treatment at a heating temperature of ℃ or higher.
JP2434884A 1984-02-14 1984-02-14 Manufacture of porous alumina body Granted JPS60171220A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2434884A JPS60171220A (en) 1984-02-14 1984-02-14 Manufacture of porous alumina body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2434884A JPS60171220A (en) 1984-02-14 1984-02-14 Manufacture of porous alumina body

Publications (2)

Publication Number Publication Date
JPS60171220A JPS60171220A (en) 1985-09-04
JPH0438690B2 true JPH0438690B2 (en) 1992-06-25

Family

ID=12135685

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2434884A Granted JPS60171220A (en) 1984-02-14 1984-02-14 Manufacture of porous alumina body

Country Status (1)

Country Link
JP (1) JPS60171220A (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE69112514T3 (en) * 1990-06-29 1999-10-21 Sumitomo Chemical Co., Ltd. Heat-resistant transition alumina and process for their production.
JPH05238729A (en) * 1991-12-18 1993-09-17 Sumitomo Chem Co Ltd Production of transitional alumina
JP2003007682A (en) 2001-06-25 2003-01-10 Matsushita Electric Ind Co Ltd Electrode member for plasma processing equipment
JP5248054B2 (en) * 2007-07-23 2013-07-31 関西電力株式会社 Method for producing spherical alumina particles

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5424298A (en) * 1977-07-26 1979-02-23 Kato Etsurou Method of making alumina flakes having high surface area and low bulk density
FR2486058A1 (en) * 1980-07-01 1982-01-08 Ugine Kuhlmann NOVEL PROCESS FOR THE PREPARATION OF HIGH-PURITY ALUMINA FROM AMMONIUM ALUM
FR2518986B1 (en) * 1981-12-30 1985-09-06 Criceram PROCESS FOR THE PREPARATION OF HIGH-PURITY ALUMINS FROM IMPURE SOLUTIONS OF ALUMINUM CHLORIDE

Also Published As

Publication number Publication date
JPS60171220A (en) 1985-09-04

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