JPS633653B2 - - Google Patents
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- JPS633653B2 JPS633653B2 JP2528280A JP2528280A JPS633653B2 JP S633653 B2 JPS633653 B2 JP S633653B2 JP 2528280 A JP2528280 A JP 2528280A JP 2528280 A JP2528280 A JP 2528280A JP S633653 B2 JPS633653 B2 JP S633653B2
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- alumina
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Description
本発明はハニカム触媒等の耐火物素材に対する
アルミナコーチング用液状組成物に関するもので
ある。
一般に触媒はアルミナ、シリカ、アルミナ−シ
リカ、コージライト、ムライト、ジルコニア等の
耐火物素材からなる担体に銅、ニツケル、コバル
ト、白金、パラジウム等の金属またはそれらの酸
化物よりなる触媒有効成分を含浸、担持して製造
される。その際、単に担体上に触媒有効成分を含
浸、担持したのでは十分な触媒活性を有する触媒
を得ることができないので、これらの担体は通常
活性アルミナコーチングを施して担体表面を触媒
的に活性な状態にしてから触媒有効成分を含浸、
担持するのが一般である。したがつて活性アルミ
ナコーチングの良否が触媒性能に極めて重大な影
響を与えるために、この活性アルミナコーチング
層は一般の触媒に要求されると同様、大きな比表
面積を有し、かつ振動、反応ガス流および熱衝撃
等によつても剥離することのないように強固な密
着性が必要である。
有機アルミニウム化合物から透明アルミナ溶液
を製造する方法はすでに知られているが、従来の
方法ではアルミナ含有量が2〜3重量%程度の透
明アルミナ溶液しか製造できないために、通常ア
ルミナ含有量が10重量%以上必要である活性アル
ミナコーチング(ウオツシユコーチング)用アル
ミナ液状組成物としてはアルミナ含有量が低すぎ
て使用できず、また高濃度透明アルミナ溶液を調
製しようとして希薄濃度の透明アルミナ溶液をそ
のまま蒸発濃度してもアルミナ濃度が5〜6重量
%になるとゲル化して放置するとプリン状の固形
物に変わりウオツシユコーチングには全く使用で
きなかつた。
また、アルミナコーチング層中に希土類元素を
併用せしめる方法として例えば米国特許第
3951860号に提案されてはいるが、従来の方法で
アルミナコーチング層中に希土類元素を添加して
アルミナの熱的特性を改良しようとすればかなり
多量の希土類を要し、反面多量の希土類の添加に
よつてむしろ活性アルミナの特性が失われるとい
う欠点があつた。また、ベーマイトから製造した
アルミナの液状組成物中に希土類塩を直接添加す
ると、その液状組成物が極めて短時間のうちにゲ
ル化してアルミナが均一に分散した液状を保持し
なくなりウオツシユコーチングが不可能であつ
た。そのためアルミナコーチング層中に希土類塩
を添加する従来の方法としては、まず最初にアル
ミナコーチングを行い、ついで希土類の水溶性塩
をそのアルミナコーチング層に含浸せしめ、仮焼
して希土類塩を希土類酸化物にするといつた方法
によりアルミナコーチング層を形成せしめてい
た。こうした方法では希土類添加工程が複雑とな
り、アルミナコーチング層中に希土類を効果的に
分散せしめることは極めて困難であつた。
本発明はこれらの要求を十分に満たす触媒担体
コーチング用アルミナ液状組成物を提供すること
を目的とする。
本発明者らは前記目的に沿つて、高濃度透明ア
ルミナ液状組成物を製造する方法およびその透明
液状組成物中に希土類塩を直接添加する方法を検
討した結果、高濃度透明アルミナ液状組成物はア
ルミニウムアルコキシドを温水中で加水分解した
後、そのまま湯浴中に静置すると加水分解物が凝
集、沈殿して、液部と沈殿部に分離して上澄液が
簡単に分離でき、沈殿部に無機酸もしくは有機酸
を混和した後、水蒸気処理もしくは乾燥して半透
明固形物にしてから水で解膠すると得られ、この
方法によつて従来の方法では全く不可能であつた
高濃度透明アルミナ液状組成物が得られることを
見出した。
また、アルミナコーチング層中に希土類を分散
させる方法として、希土類酸化物はこれまで直接
液状化することはできなかつたが、上記アルミニ
ウムアルコキシドから製造した透明アルミナ液状
組成物中では希土類酸化物のままで溶解して固溶
体化することができる。
さらに、本発明者らが先に活性アルミナコーチ
ング用として発明したコロイド状アルミナ液状組
成物(特開昭53−45314)と上記透明アルミナ液
状組成物あるいは希土類酸化物を固溶体化した上
記透明アルミナ液状組成物と混合するとゲル化を
起すことなく触媒担体コーチング用としてすぐれ
たアルミナ液状組成物が調製できることを見出し
た。
以下に本発明による触媒担体コーチング用アル
ミナ液状組成物の製造方法の好ましい一例につい
て詳細に説明する。
(1) 透明アルミナ液状組成物:
アルミニウムアルコキシド1molに水20〜
30molを加え70℃以上の温度で10〜30分間撹拌
して加水分解し、容器のまま80℃以上の湯浴中
に30分間以上放置すると液部と沈殿部が分離す
るので上澄液をデカンテーシヨンにより除去す
る。加水分解物を直接別しようとしても過
が極めて困難であり、またたとえ長時間要して
別できたとしてもこうして得られた加水分解
物は解膠時に透明にならない。
さらにまた遠心脱水装置を使用して加水分解
物と液部を分離しても脱水効果は、前記デカン
テーシヨンによる方法と大差なく、前記方法が
取扱上簡便である。また遠心脱水装置の使用は
別後のケーキが空気に長く触れていると透明
にならないという不味もある。前記のデカンテ
ーシヨンにより分離した加水分解中に塩酸、硝
酸等の無機酸もしくは酢酸、グリコール酸等の
有機酸を前記アルミニウムアルコキシド1mol
に対して0.1〜0.5mol相当量を添加して全体に
ゆき渡る程度に混和する。その混和物をそのま
ま水蒸気発生装置に入れて90℃以上で3時間以
上水蒸気処理するかもしくは200℃以下の温度
で3時間以上乾燥して半透明の固形物を得る。
このようにして調製された固形物を12〜20mol
の水で常温のまま2時間以上撹拌するとその固
形物が解膠して高濃度の透明アルミナ液状組成
物が得られる。
また、得られた透明アルミナ液状組成物(以
下、透明液状組成物という)中に酸化イツトリ
ウム、酸化ランタン、酸化ネオジウム、酸化サ
マリウム、酸化ユーロピウム、酸化ジスプロシ
ウム、酸化イツテルビウム等の1種または2種
以上の希土類酸化物を0.1〜1重量部加え、70
℃以上の温度で加温、撹拌すると希土類酸化物
は透明液状組成物中に完全に溶解する。希土類
酸化物を溶解するための透明液状組成物は希薄
な濃度であつてもよい。また、ここで用いられ
る希土類酸化物は希土類元素の単独の酸化物で
あつても、或いはまた混合酸化物であつてもよ
いが、可溶性塩のままで添加しておくとコロイ
ド状アルミナ液状組成物と混合する際ゲル化を
起すので希土類酸化物で添加しておくことが必
要である。希土類酸化物の添加量は透明液状組
成物中のアルミナ分に対して0.05〜5重量%、
好ましくは0.2〜2重量%であり、これより低
い濃度では希土類添加効果がなく、また、これ
より添加量を多くすると溶解して固溶体化しな
くなる。希土類を添加する際低濃度の透明アル
ミナ液状組成物で調製しておいて必要に応じて
濃縮することもできる。希土類酸化物の溶解温
度は70℃以上が好ましく、温度が高くなるほど
溶解速度は速くなる。しかし、希土類酸化物を
添加しない透明液状組成物も本発明の触媒担体
コーチング用液体組成物として用いられる。
(2) コロイド状アルミナ液状組成物:
一方、コロイド状のアルミナ液状組成物(以
下コロイド状液状組成物という)は次のように
して製造した。
80〜50重量部のベーマイト或いは擬ベーマイ
トに対して20〜50重量部の酸性水溶液を添加し
合計100重量部とニーダーなどで10〜30分間混
練する。ここで用いられる酸性水溶液は酢酸、
グリコール酸、ギ酸等の有機酸或いは塩酸、硝
酸等の無機酸を水に溶解して酸性水溶液とし、
酸性水溶液中の酸性物質の存在量はアルミナ1
グラム分子に対して、有機酸の場合、0.5〜
0.06グラム当量、無機酸の場合0.4〜0.04グラム
当量とした。ついでこの混練物を密閉容器中常
温で2時間以上養生した後、200℃以下の温度
で熱処理する。このようにして調製された被熱
処理物質に水を添加し、時々撹拌しながら5〜
6時間養生すれば前記固形物が解膠されてアル
ミナが均一に懸濁したコロイド状液状組成物が
得られる。このコロイド状液状組成物と前記透
明液状組成物あるいはこれに前記希土類酸化物
を添加せしめた透明液状組成物とを混合して
も、本発明による触媒担体コーチング用アルミ
ナ液状組成物が得られる。
触媒担体コーチング用アルミナ液状組成物中
の希土類酸化物の含有量は使用目的に応じてそ
の量を決めればよいが、例えばコーチングを施
す場合には触媒担体コーチング用アルミナ液状
組成物中のアルミナ分に対して5重量%以下で
十分であり、好ましくは0.5〜3重量%である
のでこのような希土類酸化物の含有量になるよ
うに両アルミナの液状組成物の混合比を決めれ
ばよい。
なお本発明において触媒担体コーチング用ア
ルミナ液状組成物は、透明アルミナ液状組成
物、希土類を添加した透明アルミナ液状組成物
およびこれらにコロイド状アルミナ液状組成物
を混合したものを総称し、以後単にコーチング
用アルミナ液状組成物という。
このように調製されたコーチング用アルミナ
液状組成物をアルミナ、シリカ、コージライ
ト、ムライト、ジルコニア等の耐火物素材から
なる担体上にコーチングして、白金、パラジウ
ム、ロジウム等の触媒有効成分を担持して得ら
れる触媒は、従来のアルミナコーチングを施し
て同様にして得られる触媒よりも一酸化炭素お
よび炭化水素の浄化性能とその耐久性が優れて
いることが判つた。
さらにまた自動車排ガス用としては一酸化炭
素、炭化水素、窒素酸化物を同時除去する三元
触媒用のアルミナコーチングにも効果がある。
このように本コーチング用アルミナ液状組成
物は自動車排ガス、工業廃ガス、家庭用燃料廃
ガス、各種脱臭装置等の一酸化炭素、炭化水素
および窒素酸化物の浄化に使用される触媒のア
ルミナコーチング用として極めて広い範囲に適
用できる。
以下に本発明を実施例でさらに具体的に説明す
るが、本発明はこれによつて限定されるものでは
ない。
実施例 1
アルミニウムイソプロポキシド204重量部を75
℃に加温した水450重量部中に添加して30分撹拌
した。撹拌後、容器全体を80〜90℃の湯湯浴中に
30分間浸漬すると、加水分解物が沈降、凝集して
上澄液と分離するのでその上澄液を除去した。こ
うして得られた加水分解物中に酢酸を18重量部加
え、全体に酢酸がゆき渡る程度にゆるやかに撹拌
して混和した。得られた乾固物は半透明の固形物
であつた。この固形物に30重量部の水を加え3時
間撹拌して透明液状組成物を得た。アルミナ濃度
は約15重量%であつた。
この透明液状組成物に酸化ジスプロシウムを0
〜2.5重量部加えコーチング用アルミナ液状組成
物溶液No.1〜5を調製した。
比較例 1
コンデイア製アルミナ50重量部に1規定の酢酸
溶液40重量部を添加し、リボン型ニーダーで10分
間混練した。ついでこの混練物をニーダーより取
り出しポリ容器に入れ密閉し常温で6時間養生し
た後、110℃に調整した乾燥機中で16時間乾燥し
た。この乾燥物を常温まで冷却した後117重量部
の水に徐々に解膠させ撹拌しながら5時間養生
し、コロイド状液状組成物を得た。アルミナ濃度
は約25重量%であつた。これを比較例として、ア
ルミナ液状組成物No.12とした。
実施例 2
酸化イツテルビウムを使用して実施例1と同様
な方法で調製した透明液状組成物10重量部と比較
例1で調製したコロイド状液状組成物10重量部を
混合してコーチング用アルミナ液状組成物溶液No.
6〜8を調製した。このアルミナ濃度は20重量
%、酸化ジスプロシウム濃度は0.1〜0.4重量%で
あつた。
実施例 3
アルミニウムブトキシド14重量部を80℃に加温
した水100重量部中に添加し、この中に酸化ネオ
ジム0.3重量部と酸化サマリウム0.3重量部を加え
60分間撹拌した。撹拌後、実施例1と同様にして
加水分解物を得た。こうして得られた加水分解物
中に塩酸1重量部を加え、全体に塩酸がゆき渡る
程度に混和した後、その混和物を密閉容器に入れ
95〜100℃の水蒸気中で5時間水蒸気処理を行つ
た。得られた乾固物は半透明の固形物であつた。
この固形物に30重量部の水を加え2時間撹拌して
透明液状組成物を得た。アルミナ濃度は約15重量
%、希土類酸化物濃度は約2重量%であつた。
この透明液状組成物10重量部と比較例1と同様
にして製造したコロイド状液状組成物10重量部お
よび20重量部とを混合して希土類酸化物を含有し
ているコーチング用アルミナ液状組成物溶液No.9
〜10を調製した。このアルミナ濃度は20重量%お
よび22重量%希土類酸化物濃度は1重量%および
0.7重量%であつた。
実施例 4
実施例1と同様にして得た透明の液状組成物に
希土類原料の硝酸抽出液から得たランタニド族混
合酸化物1重量部を加え、同様な方法で希土類混
合酸化物を溶解した。
この透明液状組成物30重量部と比較例1と同様
にして得たコロイド状液状組成物20重量部を混合
して希土類酸化物を含有しているコーチング用ア
ルミナ液状組成物溶液No.11を調製した。このアル
ミナ濃度は18重量%、希土類酸化物濃度は0.6重
量%であつた。
試験例
実施例1〜4で調製したコーチング用アルミナ
液状組成物、溶液No.1〜11および比較例で調製し
たアルミナ液状組成物溶液No.12を用い、コージラ
イト製ハニカム担体(セル密度:300セル/in2)
に約12重量%のアルミナコーチングを施した。ア
ルミナコーチング後は700℃で3時間仮焼した。
このハニカム担体1をパラジウムとして2g
含有する塩化パラジウムとパラジウム1重量部に
2重量部のアゾジカルボンアミドとの錯体水溶液
中に浸漬、含浸し、500℃で水素還元後溶液No.1
〜11および溶液No.12を使用した触媒を調製した。
触媒性能は次の条件により触媒活性判定試験を行
つた。判定試験は新品触媒と空気中で850℃で100
時間熱処理した触媒について触媒活性を評価し
た。
〔触媒活性判定試験〕
ガス組成(容量基準)
CO:1.05% O2:3.0%
H2:0.35% CO2:10%
C3H6:500ppm H2O:10%
NO:500ppm N2:残部
空間速度:75000Hr-1
試験結果は第1表の通り。
The present invention relates to a liquid composition for alumina coating on refractory materials such as honeycomb catalysts. Generally, catalysts are made by impregnating a carrier made of a refractory material such as alumina, silica, alumina-silica, cordierite, mullite, zirconia, etc. with a catalytic active ingredient made of metals such as copper, nickel, cobalt, platinum, palladium, or their oxides. , produced by supporting. At that time, it is not possible to obtain a catalyst with sufficient catalytic activity simply by impregnating and supporting the catalytic active component on the carrier, so these carriers are usually coated with activated alumina to make the carrier surface catalytically active. After making it into a state, impregnating it with catalytic active ingredients,
Generally, it is carried. Therefore, since the quality of the activated alumina coating has a very significant effect on catalyst performance, this active alumina coating layer must have a large specific surface area, as is required for general catalysts, and must be resistant to vibration and reaction gas flow. It also requires strong adhesion so that it will not peel off due to thermal shock or the like. A method for producing a transparent alumina solution from an organoaluminum compound is already known, but the conventional method can only produce a transparent alumina solution with an alumina content of about 2 to 3% by weight. The alumina content is too low to be used as an alumina liquid composition for activated alumina coating (wash coating), which requires more than 10% of active alumina, and when trying to prepare a highly concentrated transparent alumina solution, a diluted transparent alumina solution is evaporated as it is. Even when concentrated, when the alumina concentration reached 5 to 6% by weight, it gelled and turned into a pudding-like solid when left to stand, making it completely unusable for wash coating. In addition, as a method of combining rare earth elements in the alumina coating layer, for example, US Patent No.
Although it is proposed in No. 3951860, if an attempt is made to improve the thermal properties of alumina by adding rare earth elements into the alumina coating layer using the conventional method, a considerably large amount of rare earth elements is required; Rather, the disadvantage was that the properties of activated alumina were lost. Additionally, if a rare earth salt is directly added to a liquid composition of alumina produced from boehmite, the liquid composition will gel in a very short time and will not maintain a liquid state in which alumina is evenly dispersed, resulting in poor wash coating. It was possible. Therefore, the conventional method for adding rare earth salts into an alumina coating layer is to first perform alumina coating, then impregnate the alumina coating layer with a water-soluble rare earth salt, and calcinate to convert the rare earth salts into rare earth oxides. The alumina coating layer was formed by the method described in the previous paper. In such a method, the rare earth addition process becomes complicated, and it is extremely difficult to effectively disperse the rare earth into the alumina coating layer. An object of the present invention is to provide an alumina liquid composition for coating a catalyst carrier that fully satisfies these requirements. In line with the above objectives, the present inventors investigated a method for producing a highly concentrated transparent alumina liquid composition and a method for directly adding a rare earth salt to the transparent liquid composition. After hydrolyzing aluminum alkoxide in hot water, if you leave it in a hot water bath, the hydrolyzate will coagulate and precipitate, separating into a liquid part and a precipitate part.The supernatant liquid can be easily separated, and the precipitate part It is obtained by mixing inorganic or organic acids, steaming or drying to form a translucent solid, and peptizing it with water. This method produces highly concentrated transparent alumina, which is completely impossible with conventional methods. It has been found that a liquid composition can be obtained. In addition, as a method for dispersing rare earth elements in the alumina coating layer, it has not been possible to directly liquefy rare earth oxides, but in the transparent alumina liquid composition produced from the above aluminum alkoxide, rare earth oxides remain as they are. It can be dissolved to form a solid solution. Furthermore, a colloidal alumina liquid composition (Japanese Unexamined Patent Publication No. 53-45314) which the present inventors previously invented for active alumina coating and the above-mentioned transparent alumina liquid composition or the above-mentioned transparent alumina liquid composition obtained by making a rare earth oxide into a solid solution. It has been found that an excellent alumina liquid composition for coating a catalyst support can be prepared without gelation when mixed with alumina. A preferred example of the method for producing an alumina liquid composition for coating a catalyst carrier according to the present invention will be described in detail below. (1) Transparent alumina liquid composition: 1 mol of aluminum alkoxide to 20 ~
Add 30 mol and stir at a temperature of 70℃ or higher for 10 to 30 minutes to hydrolyze.If the container is left in a hot water bath of 80℃ or higher for 30 minutes or more, the liquid part and precipitate will separate, so decannize the supernatant liquid. Remove by tachion. Even if it is attempted to directly separate the hydrolyzate, it is extremely difficult to separate it, and even if it takes a long time to separate, the hydrolyzate thus obtained will not become transparent upon peptization. Furthermore, even if a centrifugal dehydrator is used to separate the hydrolyzate and the liquid part, the dehydration effect is not much different from the method using decantation, and the method is easier to handle. Another disadvantage of using a centrifugal dehydrator is that if the cake after separation is exposed to air for a long time, it will not become transparent. During hydrolysis separated by the above decantation, 1 mol of the aluminum alkoxide was added to an inorganic acid such as hydrochloric acid or nitric acid or an organic acid such as acetic acid or glycolic acid.
Add an amount equivalent to 0.1 to 0.5 mol to the solution and mix until thoroughly distributed. The mixture is directly placed in a steam generator and subjected to steam treatment at a temperature of 90°C or higher for 3 hours or more, or dried at a temperature of 200°C or lower for 3 hours or more to obtain a translucent solid.
12-20 mol of the solid thus prepared
When the mixture is stirred with water at room temperature for 2 hours or more, the solid material is peptized and a highly concentrated transparent alumina liquid composition is obtained. In addition, one or more of yttrium oxide, lanthanum oxide, neodymium oxide, samarium oxide, europium oxide, dysprosium oxide, ytterbium oxide, etc. are contained in the obtained transparent alumina liquid composition (hereinafter referred to as transparent liquid composition). Add 0.1 to 1 part by weight of rare earth oxide of 70
When heated and stirred at a temperature of 0.degree. C. or higher, the rare earth oxide is completely dissolved in the transparent liquid composition. The clear liquid composition for dissolving rare earth oxides may be of dilute concentration. Furthermore, the rare earth oxide used here may be a single oxide of a rare earth element or a mixed oxide, but if it is added as a soluble salt, it will form a colloidal alumina liquid composition. Since gelation occurs when mixed with rare earth oxides, it is necessary to add rare earth oxides. The amount of rare earth oxide added is 0.05 to 5% by weight based on the alumina content in the transparent liquid composition.
Preferably it is 0.2 to 2% by weight; if the concentration is lower than this, there is no effect of rare earth addition, and if the amount added is greater than this, it will not dissolve and become a solid solution. When adding rare earth elements, it is also possible to prepare a transparent alumina liquid composition with a low concentration and concentrate it as necessary. The dissolution temperature of the rare earth oxide is preferably 70°C or higher, and the higher the temperature, the faster the dissolution rate. However, transparent liquid compositions without the addition of rare earth oxides can also be used as liquid compositions for coating catalyst supports in the present invention. (2) Colloidal alumina liquid composition: On the other hand, a colloidal alumina liquid composition (hereinafter referred to as colloidal liquid composition) was produced as follows. 20 to 50 parts by weight of an acidic aqueous solution is added to 80 to 50 parts by weight of boehmite or pseudoboehmite, and the mixture is kneaded with a kneader or the like for 10 to 30 minutes with a total of 100 parts by weight. The acidic aqueous solution used here is acetic acid,
Organic acids such as glycolic acid and formic acid or inorganic acids such as hydrochloric acid and nitric acid are dissolved in water to form an acidic aqueous solution,
The amount of acidic substances present in the acidic aqueous solution is alumina 1
For organic acids, 0.5 to gram molecule
0.06 gram equivalent, and 0.4 to 0.04 gram equivalent for inorganic acids. Next, this kneaded product is cured in a closed container at room temperature for 2 hours or more, and then heat-treated at a temperature of 200°C or less. Add water to the material to be heat treated prepared in this way, and add it for 5 to 50 minutes while stirring occasionally.
After curing for 6 hours, the solid matter is peptized and a colloidal liquid composition in which alumina is uniformly suspended is obtained. The alumina liquid composition for coating a catalyst carrier according to the present invention can also be obtained by mixing this colloidal liquid composition with the transparent liquid composition or the transparent liquid composition to which the rare earth oxide is added. The content of rare earth oxide in the alumina liquid composition for catalyst carrier coating can be determined depending on the purpose of use, but for example, when coating is applied, the alumina content in the alumina liquid composition for catalyst carrier coating On the other hand, 5% by weight or less is sufficient, preferably 0.5 to 3% by weight, so the mixing ratio of the liquid compositions of both aluminas may be determined so as to have such a rare earth oxide content. In the present invention, the alumina liquid composition for coating a catalyst carrier is a general term for a transparent alumina liquid composition, a rare earth-added transparent alumina liquid composition, and a mixture of these with a colloidal alumina liquid composition, and hereinafter simply referred to as a coating alumina liquid composition. It is called an alumina liquid composition. The alumina liquid composition for coating thus prepared is coated onto a carrier made of a refractory material such as alumina, silica, cordierite, mullite, zirconia, etc. to support a catalyst active component such as platinum, palladium, or rhodium. It was found that the catalyst obtained by this method had better carbon monoxide and hydrocarbon purification performance and durability than a catalyst similarly obtained by applying conventional alumina coating. Furthermore, it is also effective as an alumina coating for three-way catalysts that simultaneously remove carbon monoxide, hydrocarbons, and nitrogen oxides for automobile exhaust gas. In this way, this coating alumina liquid composition is suitable for alumina coating of catalysts used in the purification of carbon monoxide, hydrocarbons, and nitrogen oxides in automobile exhaust gas, industrial waste gas, household fuel waste gas, various deodorizing devices, etc. It can be applied to a very wide range. EXAMPLES The present invention will be explained in more detail below with reference to Examples, but the present invention is not limited thereto. Example 1 75 parts by weight of 204 parts by weight of aluminum isopropoxide
It was added to 450 parts by weight of water heated to ℃ and stirred for 30 minutes. After stirring, place the entire container in a hot water bath at 80-90℃.
After soaking for 30 minutes, the hydrolyzate precipitated and coagulated and was separated from the supernatant, so the supernatant was removed. 18 parts by weight of acetic acid was added to the hydrolyzate thus obtained, and mixed by gentle stirring so that the acetic acid was distributed throughout. The dried product obtained was a translucent solid. 30 parts by weight of water was added to this solid and stirred for 3 hours to obtain a transparent liquid composition. The alumina concentration was about 15% by weight. This transparent liquid composition contains 0 dysprosium oxide.
~2.5 parts by weight were added to prepare alumina liquid composition solutions Nos. 1 to 5 for coating. Comparative Example 1 40 parts by weight of a 1N acetic acid solution was added to 50 parts by weight of alumina manufactured by Condeia, and the mixture was kneaded for 10 minutes using a ribbon kneader. The kneaded product was then taken out from the kneader, placed in a sealed plastic container, cured at room temperature for 6 hours, and then dried for 16 hours in a dryer adjusted to 110°C. After cooling this dried product to room temperature, it was gradually peptized in 117 parts by weight of water and cured for 5 hours with stirring to obtain a colloidal liquid composition. The alumina concentration was about 25% by weight. This was designated as alumina liquid composition No. 12 as a comparative example. Example 2 10 parts by weight of a transparent liquid composition prepared in the same manner as in Example 1 using ytterbium oxide and 10 parts by weight of the colloidal liquid composition prepared in Comparative Example 1 were mixed to prepare an alumina liquid for coating. Composition solution No.
6 to 8 were prepared. The alumina concentration was 20% by weight, and the dysprosium oxide concentration was 0.1 to 0.4% by weight. Example 3 14 parts by weight of aluminum butoxide was added to 100 parts by weight of water heated to 80°C, and 0.3 parts by weight of neodymium oxide and 0.3 parts by weight of samarium oxide were added to this.
Stir for 60 minutes. After stirring, a hydrolyzate was obtained in the same manner as in Example 1. Add 1 part by weight of hydrochloric acid to the hydrolyzate thus obtained, mix to the extent that the hydrochloric acid is distributed throughout, and then place the mixture in a sealed container.
Steam treatment was carried out for 5 hours in steam at 95-100°C. The dried product obtained was a translucent solid.
30 parts by weight of water was added to this solid and stirred for 2 hours to obtain a transparent liquid composition. The alumina concentration was about 15% by weight and the rare earth oxide concentration was about 2% by weight. An alumina liquid composition solution for coating containing a rare earth oxide is obtained by mixing 10 parts by weight of this transparent liquid composition with 10 parts by weight and 20 parts by weight of colloidal liquid compositions produced in the same manner as in Comparative Example 1. No.9
~10 were prepared. The alumina concentration is 20% by weight and 22% by weight, the rare earth oxide concentration is 1% by weight and
It was 0.7% by weight. Example 4 1 part by weight of a lanthanide group mixed oxide obtained from a nitric acid extract of a rare earth raw material was added to a transparent liquid composition obtained in the same manner as in Example 1, and the rare earth mixed oxide was dissolved in the same manner. Alumina liquid composition solution No. 11 for coating containing rare earth oxides was prepared by mixing 30 parts by weight of this transparent liquid composition and 20 parts by weight of a colloidal liquid composition obtained in the same manner as in Comparative Example 1. did. The alumina concentration was 18% by weight and the rare earth oxide concentration was 0.6% by weight. Test Example Using the coating alumina liquid compositions prepared in Examples 1 to 4, Solutions No. 1 to 11 and the alumina liquid composition solution No. 12 prepared in Comparative Example, a cordierite honeycomb carrier (cell density: 300 cell/in 2 )
was coated with approximately 12% by weight alumina. After alumina coating, it was calcined at 700°C for 3 hours. 2g of this honeycomb carrier 1 as palladium
Solution No. 1 was prepared by immersing it in an aqueous solution of a complex of palladium chloride and 1 part by weight of palladium and 2 parts by weight of azodicarbonamide, and reducing it with hydrogen at 500°C.
~11 and a catalyst using solution No.12 was prepared.
For catalyst performance, a catalyst activity determination test was conducted under the following conditions. The judgment test was conducted using a new catalyst in air at 850℃ for 100℃.
Catalytic activity was evaluated for the catalyst that had been heat treated for a period of time. [Catalytic activity determination test] Gas composition (volume basis) CO: 1.05% O 2 : 3.0% H 2 : 0.35% CO 2 : 10% C 3 H 6 : 500 ppm H 2 O: 10% NO: 500 ppm N 2 : Balance Space velocity: 75000Hr -1 The test results are shown in Table 1.
【表】
1) 希土類酸化物の濃度はアルミナ含有量に対する
濃度
[Table] 1) Rare earth oxide concentration relative to alumina content
Claims (1)
アルミナ水和物を酸性物質と混和し、90〜200℃
で加熱処理した後、水で解膠することにより得ら
れる触媒担体コーチング用透明アルミナ液状組成
物。 2 アルミニウムアルコキシドを出発原料とする
アルミナ水和物を酸性物質と混和し、90〜200℃
で加熱処理した後、水で解膠することにより得ら
れる透明アルミナ液状組成物と、ベーマイトある
いは擬ベーマイトを酸性水溶液と混練し、密閉容
器中常温で養生した後、200℃以下の温度で熱処
理し、さらに水を添加し養生することにより得ら
れるコロイド状アルミナ液状組成物とを混合して
なる触媒担体コーチング用アルミナ液状組成物。 3 さらに希土類酸化物を溶液として含む、前記
特許請求の範囲第1項または第2項記載のアルミ
ナ液状組成物。 4 前記希土類酸化物の含有量が前記アルミナ液
状組成物中のアルミナに対して5重量%以下であ
る前記特許請求の範囲第3項記載のアルミナ液状
組成物。[Claims] 1. Alumina hydrate using aluminum alkoxide as a starting material is mixed with an acidic substance and heated at 90 to 200°C.
A transparent alumina liquid composition for coating a catalyst carrier obtained by heat treating with water and peptizing with water. 2 Mix alumina hydrate using aluminum alkoxide as a starting material with an acidic substance and heat at 90 to 200℃.
A transparent alumina liquid composition obtained by heat treatment with water and peptization with water and boehmite or pseudoboehmite are kneaded with an acidic aqueous solution, cured at room temperature in a closed container, and then heat treated at a temperature of 200℃ or less. , and a colloidal alumina liquid composition obtained by further adding water and curing. 3. The alumina liquid composition according to claim 1 or 2, further comprising a rare earth oxide as a solution. 4. The alumina liquid composition according to claim 3, wherein the content of the rare earth oxide is 5% by weight or less based on the alumina in the alumina liquid composition.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2528280A JPS56121637A (en) | 1980-03-03 | 1980-03-03 | Alumina liquid composition for coating catalyst carrier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2528280A JPS56121637A (en) | 1980-03-03 | 1980-03-03 | Alumina liquid composition for coating catalyst carrier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56121637A JPS56121637A (en) | 1981-09-24 |
| JPS633653B2 true JPS633653B2 (en) | 1988-01-25 |
Family
ID=12161659
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2528280A Granted JPS56121637A (en) | 1980-03-03 | 1980-03-03 | Alumina liquid composition for coating catalyst carrier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56121637A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5948726A (en) * | 1994-12-07 | 1999-09-07 | Project Earth Industries, Inc. | Adsorbent and/or catalyst and binder system and method of making therefor |
| US5985790A (en) * | 1994-12-07 | 1999-11-16 | Project Earth Industries, Inc. | Method of making acid contacted enhanced aluminum oxide adsorbent particle |
| US6342191B1 (en) | 1994-12-07 | 2002-01-29 | Apyron Technologies, Inc. | Anchored catalyst system and method of making and using thereof |
| US5955393A (en) * | 1995-04-21 | 1999-09-21 | Project Earth Industries, Inc. | Enhanced adsorbent and room temperature catalyst particle and method of making therefor |
| JPH11503964A (en) * | 1995-04-21 | 1999-04-06 | エム アンド ケイ パテント カンパニー,インコーポレイテッド | Enhanced adsorbent and room temperature catalyst particles and methods of making and using same |
| EP3492431B1 (en) | 2016-07-29 | 2023-11-22 | Sumitomo Chemical Company Limited | Alumina and method for producing automotive catalyst using same |
-
1980
- 1980-03-03 JP JP2528280A patent/JPS56121637A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56121637A (en) | 1981-09-24 |
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