JP3273820B2 - Cerium-containing composite oxide having oxygen absorbing / releasing ability and method for producing the same - Google Patents

Cerium-containing composite oxide having oxygen absorbing / releasing ability and method for producing the same

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Publication number
JP3273820B2
JP3273820B2 JP03851493A JP3851493A JP3273820B2 JP 3273820 B2 JP3273820 B2 JP 3273820B2 JP 03851493 A JP03851493 A JP 03851493A JP 3851493 A JP3851493 A JP 3851493A JP 3273820 B2 JP3273820 B2 JP 3273820B2
Authority
JP
Japan
Prior art keywords
cerium
composite oxide
oxide
solution
weight
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 - Fee Related
Application number
JP03851493A
Other languages
Japanese (ja)
Other versions
JPH06246155A (en
Inventor
忠俊 室田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Santoku Corp
Original Assignee
Santoku Corp
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Filing date
Publication date
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Priority to JP03851493A priority Critical patent/JP3273820B2/en
Publication of JPH06246155A publication Critical patent/JPH06246155A/en
Application granted granted Critical
Publication of JP3273820B2 publication Critical patent/JP3273820B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F17/00Compounds of rare earth metals
    • C01F17/20Compounds containing only rare earth metals as the metal element
    • C01F17/206Compounds containing only rare earth metals as the metal element oxide or hydroxide being the only anion
    • C01F17/224Oxides or hydroxides of lanthanides
    • C01F17/235Cerium oxides or hydroxides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01FCOMPOUNDS OF THE METALS BERYLLIUM, MAGNESIUM, ALUMINIUM, CALCIUM, STRONTIUM, BARIUM, RADIUM, THORIUM, OR OF THE RARE-EARTH METALS
    • C01F17/00Compounds of rare earth metals
    • C01F17/20Compounds containing only rare earth metals as the metal element
    • C01F17/206Compounds containing only rare earth metals as the metal element oxide or hydroxide being the only anion
    • C01F17/224Oxides or hydroxides of lanthanides

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、排ガス清浄用触媒、セ
ラミックス等に利用可能であり、特に優れた酸素吸収・
放出能を有する複合酸化物及びその製造法に関する。
The present invention can be used for exhaust gas cleaning catalysts, ceramics, etc.
The present invention relates to a composite oxide having a releasing ability and a method for producing the same.

【0002】[0002]

【従来の技術】従来、酸化セリウムは、排ガス清浄用触
媒、セラミックス等として大量に使用されており、例え
ば触媒分野においては、酸化雰囲気下で酸素を吸収し、
還元雰囲気下で酸素を放出するという酸化セリウムの特
性を利用して、排ガス成分であるHC・CO・NOx等
に対する浄化率の向上等が行われており、またセラミッ
クス分野においては、前記酸化セリウムの特性を利用し
て、固体電解質等の導電性セラミックス等に利用されて
いる。このような従来の酸化セリウムは、通常、例えば
セリウムの硝酸塩溶液又は塩酸塩溶液に、シュウ酸若し
くは重炭酸アンモニウムを添加し、得られる沈澱物をろ
別、洗浄、乾燥及び焼成する方法等により製造されてい
る。
2. Description of the Related Art Conventionally, cerium oxide has been used in large quantities as an exhaust gas purifying catalyst, ceramics and the like. For example, in the field of catalysts, cerium oxide absorbs oxygen in an oxidizing atmosphere,
Utilizing the property of cerium oxide that releases oxygen under a reducing atmosphere, the purification rate of exhaust gas components such as HC, CO, and NOx has been improved, and in the ceramics field, the cerium oxide has been improved. Utilizing its characteristics, it is used for conductive ceramics such as solid electrolytes. Such a conventional cerium oxide is usually produced, for example, by a method of adding oxalic acid or ammonium bicarbonate to a cerium nitrate solution or a hydrochloride solution, and filtering, washing, drying and calcining the obtained precipitate. Have been.

【0003】しかしながら、前記方法等により製造され
た従来の酸化セリウムを主成分とする酸化物は、酸素吸
収・放出能を有するものの、300℃以下においては十
分な酸素を吸収・放出できないという欠点がある。
[0003] However, the conventional oxide containing cerium oxide as a main component produced by the above-described method or the like has oxygen absorbing / releasing ability, but has a drawback that it cannot absorb and release sufficient oxygen at 300 ° C or lower. is there.

【0004】[0004]

【発明が解決しようとする課題】従って本発明の目的
は、特に優れた酸素吸収・放出能を有するセリウム含有
複合酸化物及びその製造法を提供することにある。
SUMMARY OF THE INVENTION Accordingly, an object of the present invention is to provide a cerium-containing composite oxide having particularly excellent oxygen absorbing / releasing ability and a method for producing the same.

【0005】本発明の別な目的は、特に優れた酸素吸収
・放出能を有するセリウム含有複合酸化物を、再現性良
く、且つ容易に調製することが可能な製造法を提供する
ことにある。
Another object of the present invention is to provide a production method capable of easily preparing a cerium-containing composite oxide having particularly excellent oxygen absorbing / releasing ability with good reproducibility.

【0006】[0006]

【課題を解決するための手段】本発明によれば、主成分
として酸化セリウムを含む複合酸化物であって、該複合
酸化物が、300℃以下において100μmol/g以
上の酸素吸収・放出能を有し、且つ貴金属0.01〜1
0.0重量%を含むことを特徴とする酸素吸収・放出能
を有するセリウム含有複合酸化物が提供される。
According to the present invention, there is provided a composite oxide containing cerium oxide as a main component, the composite oxide having an oxygen absorbing / releasing ability of 100 μmol / g or more at 300 ° C. or less. Have and noble metal 0.01-1
A cerium-containing composite oxide having an oxygen absorbing / releasing ability characterized by containing 0.0% by weight is provided.

【0007】また本発明によれば、セリウムイオンと、
貴金属イオンとを含む溶液を、還元剤を含む、アンモニ
ア水溶液、重炭酸アンモニウム水溶液又はシュウ酸水溶
液に混合して、複合塩沈殿物を調製した後、該複合塩沈
殿物を250℃以上で焼成することを特徴とする前述の
酸素吸収・放出能を有するセリウム含有複合酸化物の製
造法が提供される。
Further, according to the present invention, cerium ions,
A solution containing a noble metal ion is mixed with an aqueous ammonia solution, an aqueous ammonium bicarbonate solution or an aqueous oxalic acid solution containing a reducing agent to prepare a composite salt precipitate, and then the composite salt precipitate is calcined at 250 ° C. or higher. A method for producing a cerium-containing composite oxide having the oxygen absorbing / releasing ability described above is provided.

【0008】以下本発明を更に詳細に説明する。Hereinafter, the present invention will be described in more detail.

【0009】本発明の酸素吸収・放出能を有するセリウ
ム含有複合酸化物は、300℃以下の温度範囲におい
て、100μmol/g以上、好ましくは150μmo
l/g以上の酸素吸収・放出能を有する。
The cerium-containing composite oxide having an oxygen absorbing / releasing ability of the present invention is at least 100 μmol / g, preferably at least 150 μmol, in a temperature range of 300 ° C. or less.
It has an oxygen absorption / release capacity of 1 / g or more.

【0010】また本発明の複合酸化物は、主成分として
酸化セリウムを、必須成分としてパラジウム、白金、ロ
ジウム等の貴金属、必要に応じて、酸化ジルコニウム、
酸化チタン、酸化タングステン、酸化ニッケル、酸化
銅、酸化鉄、酸化アルミニウム、酸化珪素等の遷移金属
酸化物を含んでいる。前記貴金属の含有割合は、複合酸
化物の全重量に対して0.01〜10.0重量%、好ま
しくは0.1〜5重量%である。この際、貴金属の含有
割合が0.01重量%未満の場合、酸素放出量が不足
し、10.0重量%を超えても、酸素放出量が減少す
る。一方前記遷移金属酸化物を使用する場合の含有割合
は、複合酸化物の全重量に対して0.01〜10.0重
量%、好ましくは0.1〜5重量%である。この際、遷
移金属酸化物の含有割合が0.01重量%未満の場合、
酸素放出量が不足し、10.0重量%を超えても、酸素
放出量が減少する。更に必須成分である貴金属の他に、
酸化ベリリウム、酸化マグネシウム、酸化カルシウム、
酸化ストロンチウム、酸化バリウム、酸化ラジウムから
なるアルカリ土類金属酸化物;セリウム酸化物以外の希
土類元素酸化物又はこれらの混合物を含有しても良い。
前記必須成分及び遷移金属酸化物以外の他の金属酸化物
の含有割合は、複合酸化物の全重量に対して10重量%
以下であるのが好ましい。
The composite oxide of the present invention comprises cerium oxide as a main component, a noble metal such as palladium, platinum and rhodium as an essential component , and zirconium oxide if necessary .
It contains transition metal oxides such as titanium oxide, tungsten oxide, nickel oxide, copper oxide, iron oxide, aluminum oxide, and silicon oxide. The content ratio of the noble metal is 0.01 to 10.0% by weight, preferably 0.1 to 5% by weight, based on the total weight of the composite oxide. At this time, when the content ratio of the noble metal is less than 0.01% by weight, the amount of released oxygen is insufficient, and when the content exceeds 10.0% by weight, the amount of released oxygen decreases. On the other hand, when the transition metal oxide is used, its content is 0.01 to 10.0% by weight, preferably 0.1 to 5% by weight, based on the total weight of the composite oxide. At this time, when the content ratio of the transition metal oxide is less than 0.01% by weight,
Even if the amount of released oxygen is insufficient and exceeds 10.0% by weight, the amount of released oxygen decreases. Other precious metals is a further essential component,
Beryllium oxide, magnesium oxide, calcium oxide,
An alkaline earth metal oxide composed of strontium oxide, barium oxide, and radium oxide; a rare earth element oxide other than cerium oxide, or a mixture thereof may be contained.
The content ratio of the metal oxide other than the essential component and the transition metal oxide is 10% by weight based on the total weight of the composite oxide.
It is preferred that:

【0011】本発明の複合酸化物は、前記酸素吸収・放
出能を有しておれば特に限定されるものではなく、その
形状は、例えば球形、立方型等であるのが好ましい。ま
た粒径は、0.1〜0.5μmであるのが好ましい。更
に800℃における比表面積は、好ましくは30m2
g以上、特に好ましくは50m2/g以上であるのが望
ましい。
The composite oxide of the present invention is not particularly limited as long as it has the oxygen absorbing / releasing ability, and its shape is preferably, for example, spherical, cubic, or the like. The particle size is preferably from 0.1 to 0.5 μm. Further, the specific surface area at 800 ° C. is preferably 30 m 2 /
g or more, particularly preferably 50 m 2 / g or more.

【0012】本発明の複合酸化物を調製するには、まず
セリウムイオンと、貴金属イオン、必要に応じて遷移金
属イオン等を含む溶液を、還元剤を含むアンモニア水
溶液、重炭酸アンモニウム水溶液又はシュウ酸水溶液に
混合し、セリウムと、貴金属と、必要により遷移金属等
を含む複合塩沈殿物を調製する。該セリウムイオン
と、貴金属イオンと、必要により遷移金属イオンとを含
む溶液は、例えば硝酸セリウム水溶液と、貴金属遷移
金属を溶解した硝酸水溶液とを混合する方法等により得
ることができ、またこの際、更に必要に応じてアルカリ
土類金属イオン、セリウムイオン以外の他の希土類金属
イオン又はこれらの混合イオンを含む溶液を混合するこ
ともできる。該セリウムイオンと、貴金属イオンとを含
む溶液の濃度は、総イオン濃度換算で、好ましくは10
〜300g/l、特に好ましくは30〜100g/lの
範囲である。更にセリウムイオンと、貴金属イオン及び
遷移金属イオンとに、更に必要に応じて添加混合する他
の金属イオンとの配合割合は、酸化物としての重量比で
99.99〜70.0:0.01〜20.0:0〜1
0.0であるのが好ましい。
To prepare the composite oxide of the present invention, first, cerium ions, noble metal ions , and, if necessary, transition gold
The solution containing the genus ions, containing a reducing agent, aqueous ammonia, mixed with ammonium bicarbonate solution or oxalic acid solution, cerium, a noble metal and a transition necessary metals
And preparing a complex salt precipitate comprising: The solution containing the cerium ion, the noble metal ion, and if necessary, the transition metal ion can be obtained by, for example, a method of mixing an aqueous cerium nitrate solution and an aqueous nitric acid solution in which the noble metal or the transition metal is dissolved. Further , if necessary, a solution containing a rare earth metal ion other than the alkaline earth metal ion and the cerium ion or a mixed ion thereof may be mixed. The concentration of the solution containing the cerium ion and the noble metal ion is preferably 10% in terms of total ion concentration.
~300g / l, particularly preferably area by Der of 30~100g / l. Further, the mixing ratio of the cerium ion, the noble metal ion and the transition metal ion, and other metal ions to be added and mixed as necessary, is 99.99 to 70.0% by weight as an oxide. : 0.01 to 20.0: 0 to 1
It is preferably 0.0.

【0013】前記アンモニア水溶液、重炭酸アンモニウ
ム水溶液又はシュウ酸水溶液に含有させる還元剤として
は、例えばNH2NH2(ヒドラジン)、NH2NH22H
Cl(塩酸ヒドラジン)、HCOOH(ギ酸)等を挙げ
ることができ、その配合量は、貴金属に対し、好ましく
は1〜30倍モル、特に好ましくは5〜15倍モルの範
囲である。前記範囲外であれば、貴金属が十分に配合さ
れず、得られる酸化物の酸素放出量が不足するので好ま
しくない。また前記アンモニア水溶液を用いる場合の濃
度は、好ましくは1〜2N、特に好ましくは1〜1.5
N、重炭酸アンモニウム水溶液を用いる場合の濃度は、
好ましくは50〜200g/l、特に好ましくは100
〜150g/l、シュウ酸水溶液を用いる場合の濃度は
50〜100g/l、特に好ましくは50〜60g/l
の範囲である。
Examples of the reducing agent contained in the aqueous ammonia solution, the aqueous ammonium bicarbonate solution or the aqueous oxalic acid solution include, for example, NH 2 NH 2 (hydrazine), NH 2 NH 2 2H
Examples thereof include Cl (hydrazine hydrochloride) and HCOOH (formic acid), and the amount thereof is preferably 1 to 30 moles, more preferably 5 to 15 moles with respect to the noble metal. If the amount is outside the above range, the noble metal is not sufficiently blended, and the amount of oxygen released from the obtained oxide is insufficient. When the aqueous ammonia solution is used, the concentration is preferably 1 to 2N, particularly preferably 1 to 1.5N.
N, the concentration when using an aqueous solution of ammonium bicarbonate is
Preferably 50 to 200 g / l, particularly preferably 100
To 150 g / l, the concentration when using an oxalic acid aqueous solution is 50 to 100 g / l, particularly preferably 50 to 60 g / l.
Range.

【0014】前記セリウムイオンと、貴金属イオンとを
含む溶液と、前記還元剤を含むアンモニア水溶液、重
炭酸アンモニウム水溶液又はシュウ酸水溶液との混合割
合は、それぞれ重量比で1:1〜1:2が好ましい。こ
の際得られる複合塩沈殿物は、例えば複合水酸化物等で
ある。
The mixing ratio of the solution containing the cerium ion and the noble metal ion and the aqueous ammonia solution, the aqueous ammonium bicarbonate solution or the aqueous oxalic acid solution containing the reducing agent is 1: 1 by weight, respectively. 1 : 1: 2 is preferred. The composite salt precipitate obtained at this time is, for example, a composite hydroxide.

【0015】次いで前記複合塩沈殿物を250℃以上、
好ましくは300〜400℃において焼成することによ
り本発明の複合酸化物を製造することができる。また本
発明の製造法においては、必要に応じて前記複合塩沈殿
物を焼成する前に、予め水熱処理等してから、前記焼成
工程を行うこともできる。該水熱処理は、通常のオート
クレーブ等により実施でき、その際の温度は100〜1
35℃、処理時間は0.5〜1時間の範囲であることが
望ましい。前記焼成温度が250℃未満の場合には、酸
化物になりにくい。また焼成時間は1〜10時間行うの
が好ましい。
Next, the complex salt precipitate is heated at 250 ° C. or higher,
Preferably, the composite oxide of the present invention can be produced by firing at 300 to 400 ° C. Further, in the production method of the present invention, if necessary, before firing the complex salt precipitate, a hydrothermal treatment or the like may be performed before the firing step. The hydrothermal treatment can be performed by a usual autoclave or the like, and the temperature at that time is 100 to 1
It is desirable that the treatment time is 35 ° C. and the treatment time is in the range of 0.5 to 1 hour. When the firing temperature is lower than 250 ° C., the oxide hardly becomes an oxide. The firing time is preferably 1 to 10 hours.

【0016】本発明の製造法により得られる複合酸化物
は、そのまま使用することもできるが、例えば希土類硝
酸塩等を添加して用いることもできる。
The composite oxide obtained by the production method of the present invention can be used as it is, but it can also be used after adding a rare earth nitrate or the like.

【0017】[0017]

【発明の効果】本発明のセリウム含有複合酸化物は、貴
属を必須成分として含むので、300℃以下の温度範
囲において、100μmol/g以上の酸素吸収・放出
能を示す。従って触媒分野及びセラミックス分野等にお
いて極めて有用である。また本発明の製造法では、優れ
た酸素吸収・放出能を有する本発明の複合酸化物を、再
現性良く容易に製造することができる。
Cerium-containing composite oxide of the present invention exhibits, because it contains a noble <br/> metals as an essential component, in the temperature range of 300 ° C. or less, an oxygen absorbing and desorbing capability over 100 [mu] mol / g. Therefore, it is extremely useful in the field of catalysts, ceramics, and the like. Further, according to the production method of the present invention, the composite oxide of the present invention having excellent oxygen absorbing / releasing ability can be easily produced with good reproducibility.

【0018】[0018]

【実施例】以下本発明を実施例により更に詳細に説明す
るが、本発明はこれらに限定されるものではない。
EXAMPLES The present invention will be described in more detail with reference to the following Examples, but it should not be construed that the invention is limited thereto.

【0019】[0019]

【実施例1】高純度硝酸セリウム溶液(三徳金属工業株
式会社製、純度99.9%)を水に溶解して調製した、
酸化セリウム濃度300g/lの硝酸セリウム水溶液1
65mlに、硝酸パラジウム溶液(和光純薬社製、純度
99.9%)を水に溶解して調製した、硝酸パラジウム
水溶液6mlとを混合し、Ce:Pd=99:1(重量
比)とし、複合酸化物濃度50g/lとしたセリウムイ
オン及びパラジウムイオン含有溶液を調製した。次い
で、得られた溶液1リットルに、別に調製した還元剤と
して(NH222HClを5mol含む1Nアンモニア
水溶液1リットルを添加混合し、セリウム及びパラジウ
ム含有複合水酸化物の沈殿を得た。得られた複合水酸化
物を300℃で4時間焼成し、比表面積が110m2
g、900℃再焼成後比表面積5m2/gのセリウム及
びパラジウム含有複合酸化物50gを得た。得られた複
合酸化物の酸素吸収・放出量を測定するために、筒状炉
中に、複合酸化物1gを仕込み、水素ガス及び酸素ガス
を流し込みながら、ガスクロマトグラフィーにより測定
したところ、酸素吸収・放出能は、150〜250℃に
おいて、100μmol/gであった。また複合酸化物
中のパラジウムの含有割合は1重量%であった。
Example 1 A high-purity cerium nitrate solution (manufactured by Santoku Metal Industry Co., Ltd., purity 99.9%) was prepared by dissolving in water.
Cerium nitrate aqueous solution 1 with a cerium oxide concentration of 300 g / l
To 65 ml, 6 ml of an aqueous palladium nitrate solution prepared by dissolving a palladium nitrate solution (purity 99.9%, manufactured by Wako Pure Chemical Industries, Ltd.) in water was mixed to make Ce: Pd = 99: 1 (weight ratio), A solution containing cerium ions and palladium ions having a composite oxide concentration of 50 g / l was prepared. Next, 1 liter of the obtained solution was mixed with 1 liter of a 1N aqueous ammonia solution containing 5 mol of (NH 2 ) 2 2HCl as a separately prepared reducing agent to obtain a precipitate of a composite hydroxide containing cerium and palladium. The obtained composite hydroxide was calcined at 300 ° C. for 4 hours to have a specific surface area of 110 m 2 /
After recalcination at 900 ° C., 50 g of a cerium- and palladium-containing composite oxide having a specific surface area of 5 m 2 / g was obtained. In order to measure the amount of oxygen absorption and release of the obtained composite oxide, 1 g of the composite oxide was charged into a cylindrical furnace, and the mixture was measured by gas chromatography while flowing hydrogen gas and oxygen gas. -The release ability was 100 mol / g at 150 to 250C. The content of palladium in the composite oxide was 1% by weight.

【0020】[0020]

【実施例2】実施例1で調製した硝酸セリウム水溶液1
50mlと、硝酸パラジウム水溶液60mlとを混合
し、Ce:Pd=90:10(重量比)とし、複合酸化
物濃度50g/lとしたセリウムイオン及びパラジウム
イオン含有溶液を調製した。次いで、実施例1と同様に
複合酸化物を製造し、酸素吸収・放出量を測定した。そ
の結果得られた複合酸化物の酸素吸収・放出能は、15
0〜250℃において、130μmol/gであった。
また複合酸化物中のパラジウムの含有割合は、それぞれ
10重量%であった。
Example 2 Cerium nitrate aqueous solution 1 prepared in Example 1
50 ml and 60 ml of an aqueous solution of palladium nitrate were mixed to make Ce: Pd = 90: 10 (weight ratio), and a cerium ion and palladium ion-containing solution having a composite oxide concentration of 50 g / l was prepared. Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured. The resulting composite oxide has an oxygen absorption / release capacity of 15
At 0 to 250 ° C, it was 130 µmol / g.
The content of palladium in the composite oxide was 10% by weight.

【0021】[0021]

【実施例3】実施例1で調製した硝酸セリウム水溶液1
65mlと、硝酸白金(和光純薬社製、純度99.9
%)を水に溶解して調製した硝酸白金水溶液10mlと
を混合し、Ce:Pt=99:1(重量比)とし、複合
酸化物濃度50g/lとしたセリウムイオン及び白金イ
オン含有溶液を調製した。次いで、実施例1と同様に複
合酸化物を製造し、酸素吸収・放出量を測定した。その
結果得られた複合酸化物の酸素吸収・放出能は、150
〜250℃において、120μmol/gであった。ま
た複合酸化物中の白金の含有割合は、1重量%であっ
た。
Example 3 Cerium nitrate aqueous solution 1 prepared in Example 1
65 ml of platinum nitrate (purity 99.9, manufactured by Wako Pure Chemical Industries, Ltd.)
%) Dissolved in water and mixed with 10 ml of an aqueous solution of platinum nitrate to prepare a solution containing cerium ions and platinum ions with a composite oxide concentration of 50 g / l at a Ce: Pt = 99: 1 (weight ratio). did. Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured. The resulting composite oxide has an oxygen absorption / release capacity of 150
At 〜250 ° C., it was 120 μmol / g. The content of platinum in the composite oxide was 1% by weight.

【0022】[0022]

【実施例4】実施例1で調製した硝酸セリウム水溶液1
65mlと、硝酸ロジウム(和光純薬社製、純度99.
9%)を水に溶解して調製した硝酸ロジウム水溶液10
mlとを混合し、Ce:Rh=99:1(重量比)と
し、複合酸化物濃度50g/lとしたセリウムイオン及
びロジウムイオン含有溶液を調製した。次いで、実施例
1と同様に複合酸化物を製造し、酸素吸収・放出量を測
定した。その結果得られた複合酸化物の酸素吸収・放出
能は、150〜250℃において、110μmol/g
であった。また複合酸化物中のロジウムの含有割合は、
1重量%であった。
Example 4 Cerium nitrate aqueous solution 1 prepared in Example 1
65 ml, and rhodium nitrate (purity 99.
9%) in water.
Then, a solution containing cerium ions and rhodium ions having a composite oxide concentration of 50 g / l was prepared by mixing Ce: Rh = 99: 1 (weight ratio). Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured. The resulting composite oxide has an oxygen absorption / release capacity of 110 μmol / g at 150 to 250 ° C.
Met. The content of rhodium in the composite oxide is
It was 1% by weight.

【0023】[0023]

【実施例5】実施例1で調製した硝酸セリウム水溶液1
65mlと、硝酸パラジウム水溶液30mlと、硝酸ネ
オジム(三徳金属工業社製、純度99.9%)を水に溶
解して調製した酸化ネオジム濃度100g/lの硝酸ネ
オジム水溶液25mlとを混合し、Ce:Pd:Nd=
90:5:5(重量比)とし、複合酸化物濃度50g/
lとしたセリウムイオン、パラジウムイオン及びネオジ
ムイオン含有溶液を調製した。次いで、実施例1と同様
に複合酸化物を製造し、酸素吸収・放出量を測定した。
その結果得られた複合酸化物の酸素吸収・放出能は、1
50〜250℃において、112μmol/gであっ
た。また複合酸化物中のパラジウム及び酸化ネオジムの
含有割合は、それぞれ5重量%及び5重量%であった。
Example 5 Cerium nitrate aqueous solution 1 prepared in Example 1
65 ml, 30 ml of an aqueous solution of palladium nitrate, and 25 ml of an aqueous solution of neodymium nitrate having a neodymium oxide concentration of 100 g / l prepared by dissolving neodymium nitrate (manufactured by Santoku Metal Industry Co., Ltd., purity 99.9%) in water, Ce: Pd: Nd =
90: 5: 5 (weight ratio), and a composite oxide concentration of 50 g /
A solution containing cerium ion, palladium ion and neodymium ion was prepared. Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured.
The resulting composite oxide has an oxygen absorption / release capacity of 1
At 50 to 250 ° C, it was 112 µmol / g. The contents of palladium and neodymium oxide in the composite oxide were 5% by weight and 5% by weight, respectively.

【0024】[0024]

【実施例6】実施例1で調製した硝酸セリウム水溶液1
34mlと、硝酸パラジウム水溶液30mlと、硝酸ユ
ーロピウム(三徳金属工業社製、純度99.9%)を水
に溶解して調製した酸化ユーロピウム濃度100g/l
の硝酸ユーロピウム水溶液5mlと、硝酸アルミニウム
(和光純薬社製、純度99.9%)を水に溶解して調製
した酸化アルミニウム濃度100g/lの硝酸アルミニ
ウム水溶液25mlとを混合し、Ce:Pd:Eu:A
l=89:5:1:5(重量比)とし、複合酸化物濃度
50g/lとしたセリウムイオン、パラジウムイオン、
ユーロピウムイオン及びアルミニウムイオン含有溶液を
調製した。次いで、実施例1と同様に複合酸化物を製造
し、酸素吸収・放出量を測定した。その結果得られた複
合酸化物の酸素吸収・放出能は、150〜250℃にお
いて、112μmol/gであった。また複合酸化物中
のパラジウム、酸化ユーロピウム及び酸化アルミニウム
の含有割合は、それぞれ5重量%、1重量%及び5重量
%であった。
Example 6 Cerium nitrate aqueous solution 1 prepared in Example 1
34 ml, an aqueous solution of palladium nitrate 30 ml, and europium nitrate (purity 99.9%, manufactured by Santoku Metal Industry Co., Ltd.) dissolved in water to prepare a europium oxide concentration 100 g / l.
5 ml of an aqueous solution of europium nitrate and 25 ml of an aqueous solution of aluminum nitrate (100 g / l) prepared by dissolving aluminum nitrate (purity: 99.9%, manufactured by Wako Pure Chemical Industries, Ltd.) in water were mixed with Ce: Pd: Eu: A
l = 89: 5: 1: 5 (weight ratio), cerium ion, palladium ion at a composite oxide concentration of 50 g / l,
A solution containing europium ions and aluminum ions was prepared. Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured. The resulting composite oxide had an oxygen absorbing / releasing ability of 112 µmol / g at 150 to 250 ° C. The contents of palladium, europium oxide and aluminum oxide in the composite oxide were 5% by weight, 1% by weight and 5% by weight, respectively.

【0025】[0025]

【実施例7】実施例1で調製した硝酸セリウム水溶液1
34mlと、硝酸パラジウム水溶液6mlと、硝酸ジル
コニウム溶液(第1希元素社製、純度99.9%)を水
に希釈して調製した酸化ジルコニウム濃度375g/l
の硝酸ジルコニウム水溶液12mlとを混合し、Ce:
Pd:Zr=89:1:10(重量比)とし、複合酸化
物濃度50g/lとしたセリウムイオン、パラジウムイ
オン及びジルコニウムイオン含有溶液を調製した。次い
で、実施例1と同様に複合酸化物を製造し、酸素吸収・
放出量を測定した。その結果得られた複合酸化物の酸素
吸収・放出能は、150〜250℃において、113μ
mol/gであった。また複合酸化物中のパラジウム及
び酸化ジルコニウムの含有割合は、それぞれ1重量%及
び10重量%であった。
Example 7 Cerium nitrate aqueous solution 1 prepared in Example 1
34 ml, an aqueous solution of palladium nitrate 6 ml, and a zirconium nitrate solution (manufactured by Daiichi Kagaku Kabushiki Kaisha, purity 99.9%) diluted with water to prepare a zirconium oxide concentration of 375 g / l
And 12 ml of an aqueous solution of zirconium nitrate, Ce:
A solution containing cerium ion, palladium ion and zirconium ion with a Pd: Zr = 89: 1: 10 (weight ratio) and a composite oxide concentration of 50 g / l was prepared. Next, a composite oxide was produced in the same manner as in Example 1,
The release was measured. The resulting composite oxide has an oxygen absorbing / releasing ability of 113 μm at 150 to 250 ° C.
mol / g. The contents of palladium and zirconium oxide in the composite oxide were 1% by weight and 10% by weight, respectively.

【0026】[0026]

【実施例8】実施例1で調製した硝酸セリウム水溶液1
34mlと、硝酸パラジウム水溶液20mlと、硝酸プ
ラセオジム(三徳金属工業社製、純度99.9%)を水
に溶解して調製した酸化プラセオジム濃度100g/l
の硝酸プラセオジム水溶液5mlと、硝酸アルミニウム
水溶液25mlとを混合し、Ce:Pd:Pr:Al=
89:5:1:5(重量比)とし、複合酸化物濃度50
g/lとしたセリウムイオン、パラジウムイオン、プラ
セオジムイオン及びアルミニウムイオン含有溶液を調製
した。次いで、実施例1と同様に複合酸化物を製造し、
酸素吸収・放出量を測定した。その結果得られた複合酸
化物の酸素吸収・放出能は、150〜250℃におい
て、111μmol/gであった。また複合酸化物中の
パラジウム、酸化プラセオジム及び酸化アルミニウムの
含有割合は、それぞれ5重量%、1重量%及び5重量%
であった。
Example 8 Cerium nitrate aqueous solution 1 prepared in Example 1
34 ml, a palladium nitrate aqueous solution 20 ml, and praseodymium nitrate (purity: 99.9%, manufactured by Santoku Metal Industry Co., Ltd.) dissolved in water to prepare praseodymium oxide at a concentration of 100 g / l.
Of a praseodymium nitrate aqueous solution of 5 ml and an aluminum nitrate aqueous solution of 25 ml were mixed, and Ce: Pd: Pr: Al =
89: 5: 1: 5 (weight ratio) and a composite oxide concentration of 50
A solution containing cerium ion, palladium ion, praseodymium ion, and aluminum ion at g / l was prepared. Next, a composite oxide was produced in the same manner as in Example 1,
The amount of oxygen absorption / release was measured. The resulting composite oxide had an oxygen absorbing / releasing ability of 111 μmol / g at 150 to 250 ° C. The contents of palladium, praseodymium oxide and aluminum oxide in the composite oxide were 5% by weight, 1% by weight and 5% by weight, respectively.
Met.

【0027】[0027]

【実施例9】実施例1で調製した硝酸セリウム水溶液1
50mlと、硝酸パラジウム水溶液30mlと、硝酸珪
素(和光純薬社製、純度99.9%)を水に溶解して調
製した酸化珪素濃度100g/lの硝酸珪素水溶液25
mlとを混合し、Ce:Pd:Si=90:5:5(重
量比)とし、複合酸化物濃度50g/lとしたセリウム
イオン、パラジウムイオン及び珪素イオン含有溶液を調
製した。次いで、実施例1と同様に複合酸化物を製造
し、酸素吸収・放出量を測定した。その結果得られた複
合酸化物の酸素吸収・放出能は、150〜250℃にお
いて、105μmol/gであった。また複合酸化物中
のパラジウム及び酸化珪素の含有割合は、それぞれ5重
量%及び5重量%であった。
Example 9 Cerium nitrate aqueous solution 1 prepared in Example 1
50 ml, an aqueous solution of palladium nitrate 30 ml, and an aqueous solution of silicon nitrate 25 having a silicon oxide concentration of 100 g / l prepared by dissolving silicon nitrate (Wako Pure Chemical Industries, purity 99.9%) in water.
and mixed with Ce: Pd: Si = 90: 5: 5 (weight ratio) to prepare a solution containing cerium ion, palladium ion and silicon ion at a composite oxide concentration of 50 g / l. Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured. The resulting composite oxide had an oxygen absorbing / releasing ability of 105 µmol / g at 150 to 250 ° C. The contents of palladium and silicon oxide in the composite oxide were 5% by weight and 5% by weight, respectively.

【0028】[0028]

【実施例10】実施例1で調製した硝酸セリウム水溶液
165mlと、硝酸パラジウム水溶液30mlと、硝酸
バリウム(和光純薬社製、純度99.9%)を水に溶解
して調製した酸化バリウム濃度100g/lの硝酸バリ
ウム水溶液25mlとを混合し、Ce:Pd:Ba=9
0:5:5(重量比)とし、複合酸化物濃度50g/l
としたセリウムイオン、パラジウムイオン及びバリウム
イオン含有溶液を調製した。次いで、実施例1と同様に
複合酸化物を製造し、酸素吸収・放出量を測定した。そ
の結果得られた複合酸化物の酸素吸収・放出能は、15
0〜250℃において、111μmol/gであった。
また複合酸化物中のパラジウム及び酸化バリウムの含有
割合は、それぞれ5重量%及び5重量%であった。
Example 10 A barium oxide concentration of 100 g was prepared by dissolving 165 ml of the cerium nitrate aqueous solution prepared in Example 1, 30 ml of the palladium nitrate aqueous solution, and barium nitrate (purity 99.9%, manufactured by Wako Pure Chemical Industries, Ltd.) in water. / L nitric acid burr
And 25 ml of an aqueous solution of Ce: Pd: Ba = 9.
0: 5: 5 (weight ratio), composite oxide concentration 50 g / l
A solution containing cerium ion, palladium ion and barium ion was prepared. Next, a composite oxide was produced in the same manner as in Example 1, and the amount of oxygen absorption / release was measured. The resulting composite oxide has an oxygen absorption / release capacity of 15
At 0 to 250 ° C, it was 111 µmol / g.
The contents of palladium and barium oxide in the composite oxide were 5% by weight and 5% by weight, respectively.

【0029】[0029]

【比較例1】実施例1で調製した硝酸セリウム水溶液1
50mlと、硝酸ジルコニウム水溶液13mlとを混合
し、Ce:Zr=90:10(重量比)とし、複合酸化
物濃度50g/lとしたセリウムイオン及びジルコニウ
ムイオン含有溶液を調製した。次いで、還元剤を使用し
ない以外は実施例1と同様に複合酸化物を製造し、酸素
吸収・放出量を測定した。その結果得られた複合酸化物
の酸素吸収・放出能は、150〜250℃において、0
μmol/gであった。また複合酸化物中の酸化ジルコ
ニウムの含有割合は、10重量%であった。
Comparative Example 1 Cerium nitrate aqueous solution 1 prepared in Example 1
50 ml and 13 ml of an aqueous solution of zirconium nitrate were mixed to prepare Ce: Zr = 90: 10 (weight ratio), and a solution containing cerium ions and zirconium ions having a composite oxide concentration of 50 g / l was prepared. Next, a composite oxide was produced in the same manner as in Example 1 except that no reducing agent was used, and the amount of oxygen absorption / release was measured. The oxygen absorption / desorption ability of the resulting composite oxide is 0 at 150 to 250 ° C.
μmol / g. The content of zirconium oxide in the composite oxide was 10% by weight.

【0030】[0030]

【比較例2】実施例1で調製した硝酸セリウム水溶液1
67mlを、酸化物濃度50g/lとしたセリウムイオ
ン含有溶液を調製した。次いで、還元剤を使用しない以
外は実施例1と同様にセリウム酸化物を製造し、酸素吸
収・放出量を測定した。その結果得られたセリウム酸化
物の酸素吸収・放出能は、150〜250℃において、
0μmol/gであった。
Comparative Example 2 Cerium nitrate aqueous solution 1 prepared in Example 1
A cerium ion-containing solution having an oxide concentration of 50 g / l was prepared from 67 ml. Next, a cerium oxide was produced in the same manner as in Example 1 except that no reducing agent was used, and the amount of oxygen absorption / release was measured. The resulting cerium oxide has the ability to absorb and release oxygen at 150-250 ° C.
It was 0 μmol / g.

【0031】[0031]

【実施例11】実施例1で用いた(NH222HClを
5mol含む1Nアンモニア水溶液を(NH222HC
lを5mol含む1mol/l重炭酸アンモニウム水溶
液に代えた以外は実施例1と同様にセリウム酸化物を製
造し、酸素吸収・放出量を測定した。その結果得られた
セリウム酸化物の酸素吸収・放出能は、150〜250
℃において、108μmol/gであった。
Example 11 used in Example 1 (NH 2) 1N aqueous ammonia containing 5mol a 2 2HCl (NH 2) 2 2HC
A cerium oxide was produced in the same manner as in Example 1 except that an aqueous solution of 1 mol / l ammonium bicarbonate containing 5 mol of 1 was prepared, and the amount of oxygen absorption / release was measured. The resulting cerium oxide has an oxygen absorption / release capacity of 150-250.
At 108 ° C., it was 108 μmol / g.

【0032】[0032]

【実施例12】実施例1で用いた(NH222HClを
5mol含む1Nアンモニア水溶液を(NH222HC
lを5mol含む1mol/lシュウ酸水溶液に代えた
以外は実施例1と同様にセリウム酸化物を製造し、酸素
吸収・放出量を測定した。その結果得られたセリウム酸
化物の酸素吸収・放出能は、150〜250℃におい
て、105μmol/gであった。
Example 12 used in Example 1 (NH 2) 1N aqueous ammonia containing 5mol a 2 2HCl (NH 2) 2 2HC
A cerium oxide was produced in the same manner as in Example 1 except that an aqueous solution of 1 mol / l oxalic acid containing 1 mol of 1 was prepared, and the amount of oxygen absorption / release was measured. The resulting cerium oxide had an oxygen absorbing / releasing ability of 105 μmol / g at 150 to 250 ° C.

【0033】[0033]

【実施例13】高純度硝酸セリウム溶液(三徳金属工業
株式会社製、純度99.9%)を水に溶解して調製し
た、酸化セリウム濃度300g/lの硝酸セリウム水溶
液165mlに、硝酸パラジウム溶液(和光純薬社製、
純度99.9%)を水に溶解して調製した、硝酸パラジ
ウム水溶液6mlとを混合し、Ce:Pd=99:1
(重量比)とし、複合酸化物濃度50g/lとしたセリ
ウムイオン及びパラジウムイオン含有溶液を調製した。
次いで、得られた溶液1リットルに、別に調製した還元
剤としてHCOOHを5mol含む1Nアンモニア水溶
液1リットルを添加混合し、セリウム及びパラジウム含
有複合水酸化物の沈殿を得た。得られた複合水酸化物を
300℃で4時間焼成し、比表面積が115m2/g、
900℃再燃成後比表面積8m2/gのセリウム及びパ
ラジウム含有複合酸化物55gを得た。得られた複合酸
化物の酸素吸収・放出量を測定するために、筒状炉中
に、複合酸化物1gを仕込み、水素ガス及び酸素ガスを
流し込みながら、ガスクロマトグラフィーにより測定し
たところ、酸素吸収・放出能は、150〜250℃にお
いて、104μmol/gであった。また複合酸化物中
のパラジウムの含有割合は1重量%であった。
Example 13 A palladium nitrate solution was added to 165 ml of an aqueous cerium nitrate solution having a cerium oxide concentration of 300 g / l prepared by dissolving a high-purity cerium nitrate solution (purity: 99.9%, manufactured by Santoku Metal Industry Co., Ltd.) in water. Wako Pure Chemical Co., Ltd.
(99.9% purity) dissolved in water and mixed with 6 ml of an aqueous solution of palladium nitrate, and Ce: Pd = 99: 1.
(Weight ratio), a solution containing cerium ions and palladium ions with a composite oxide concentration of 50 g / l was prepared.
Then, 1 liter of a 1N aqueous ammonia solution containing 5 mol of HCOOH as a separately prepared reducing agent was added to 1 liter of the obtained solution and mixed to obtain a precipitate of a composite hydroxide containing cerium and palladium. The obtained composite hydroxide is calcined at 300 ° C. for 4 hours to have a specific surface area of 115 m 2 / g,
After reheating at 900 ° C., 55 g of a cerium and palladium-containing composite oxide having a specific surface area of 8 m 2 / g was obtained. In order to measure the amount of oxygen absorbed and released from the obtained composite oxide, 1 g of the composite oxide was charged into a cylindrical furnace, and the mixture was measured by gas chromatography while flowing hydrogen gas and oxygen gas. -Release ability was 104 micromol / g at 150-250 degreeC. The content of palladium in the composite oxide was 1% by weight.

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Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 主成分として酸化セリウムを含む複合酸
化物であって、該複合酸化物が、300℃以下において
100μmol/g以上の酸素吸収・放出能を有し、且
つ貴金属0.01〜10.0重量%を含むことを特徴と
する酸素吸収・放出能を有するセリウム含有複合酸化
物。
1. A composite oxide containing cerium oxide as a main component, wherein the composite oxide has an oxygen absorbing / releasing ability of 100 μmol / g or more at 300 ° C. or less, and a noble metal of 0.01 to 10 mol / g. A cerium-containing composite oxide having an oxygen absorbing / releasing ability, wherein the cerium-containing composite oxide contains 0.1 % by weight.
【請求項2】 更に遷移金属酸化物0.01〜10.0
重量%を含むことを特徴とする請求項1記載の酸素吸収
・放出能を有するセリウム含有複合酸化物。
2. The method according to claim 1, wherein the transition metal oxide is 0.01 to 10.0.
2. Oxygen absorption according to claim 1, characterized in that it contains% by weight.
-A cerium-containing composite oxide having a releasing ability.
【請求項3】 前記複合酸化物が、更にアルカリ土類金
属酸化物及び/又はセリウム酸化物以外の希土類元素酸
化物を10重量%以下含むことを特徴とする請求項1
は2記載の酸素吸収・放出能を有するセリウム含有複合
酸化物。
Wherein the composite oxide, and claim 1 further comprising an alkaline earth metal oxides and / or other than cerium oxide a rare earth element oxide 10 wt% or less
Is a cerium-containing composite oxide having oxygen absorbing / releasing ability according to 2 .
【請求項4】 セリウムイオンと、貴金属イオンとを
む溶液を、還元剤を含むアンモニア水溶液、重炭酸ア
ンモニウム水溶液又はシュウ酸水溶液に混合して、複合
塩沈殿物を調製した後、該複合塩沈殿物を250℃以上
で焼成することを特徴とする請求項1記載の酸素吸収・
放出能を有するセリウム含有複合酸化物の製造法。
4. A mixed salt precipitate is prepared by mixing a solution containing cerium ions and noble metal ions with an aqueous ammonia solution, aqueous ammonium bicarbonate solution or aqueous oxalic acid solution containing a reducing agent. 2. The method according to claim 1, wherein the composite salt precipitate is calcined at 250 ° C. or higher.
A method for producing a cerium-containing composite oxide having a releasing ability.
JP03851493A 1993-02-26 1993-02-26 Cerium-containing composite oxide having oxygen absorbing / releasing ability and method for producing the same Expired - Fee Related JP3273820B2 (en)

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