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Publication number
JPH024525B2
JPH024525B2 JP55184291A JP18429180A JPH024525B2 JP H024525 B2 JPH024525 B2 JP H024525B2 JP 55184291 A JP55184291 A JP 55184291A JP 18429180 A JP18429180 A JP 18429180A JP H024525 B2 JPH024525 B2 JP H024525B2
Authority
JP
Japan
Prior art keywords
vanadium
crystalline oxide
phosphorus
solid solution
oxide
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
JP55184291A
Other languages
Japanese (ja)
Other versions
JPS57111219A (en
Inventor
Masayuki Ootake
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Industries Ltd
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 by Mitsubishi Chemical Industries Ltd filed Critical Mitsubishi Chemical Industries Ltd
Priority to JP55184291A priority Critical patent/JPS57111219A/en
Publication of JPS57111219A publication Critical patent/JPS57111219A/en
Publication of JPH024525B2 publication Critical patent/JPH024525B2/ja
Granted legal-status Critical Current

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  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は気相酸化触媒、特にC4炭化水素より
無水マレイン酸を製造するための触媒の前駆体と
して有用な新規置換固溶型結晶性酸化物に関する
ものである。 C4炭化水素の気相酸化による無水マレイン酸
製造用触媒としては、V−P−O系複合酸化物
(特開昭48−63982、同51−95990、同52−156193、
同53−146992、特公昭53−39037等)、あるいは、
バナジウム、リンおよび第三成分として鉄あるい
はクロムなどを含む多成分系の酸化物触媒(特公
昭53−43928、同53−43929、特開昭53−60391、
同53−61587、USP3,156,705等)が知られて
いる。これらの公知の酸化物触媒のうち前者は結
晶性酸化物であり、後者は非晶質である。 本発明者は多成分系の酸化触媒の気相酸化反応
に対する適性について種々検討した結果、結晶性
のバナジウム−リン系酸化物にコバルト、ニツケ
ルなどの第三成分を添加しただけの触媒は、公知
の結晶性バナジウム−リン系酸化物に比較して、
気相酸化反応における活性および選択性が低くな
るが、コバルト、ニツケル、チタンなどを結晶性
バナジウム−リン系酸化物の結晶構造を崩さずに
バナジウムの一部と置換して得られる新規な置換
固溶型結晶性酸化物が高活性で選択性のすぐれた
気相酸化触媒の前駆体となることを見い出し、本
発明に到達したものである。 以下に本発明を詳細に説明する。 本発明の置換固溶型結晶性酸化物はバナジウ
ム、リン、酸素、水素及びチタンから成るか、さ
らにこれにマンガン、コバルト、ニツケル、鉄、
クロム及びアルミニウムから選ばれた元素をも含
有する結晶性酸化物であつて、結晶を形成するバ
ナジウムの一部が上記バナジウム以外の金属によ
り置換された青色結晶である。該置換固溶型結晶
性酸化物の酸素、水素および結晶水を除く組成
は、下記式〔〕 V1.0-a-b-cTiaXbYcP1.0 …〔〕 (但し、XはMn,CoおよびNiから選ばれれる
少くとも一種を表わし、YはFe,Cr、およびAl
から選ばれる少くとも一種を表わし、0<a≦
0.4、好ましくは0.001≦a≦0.4、さらに好ましく
は0.005≦a≦0.25、0≦b≦0.4、好ましくは
0.001≦b≦0.4、さらに好ましくは0.005≦b≦
0.25、0<a+b≦0.4好ましくは0.001≦a+b
≦0.4、さらに好ましくは0.005≦a+b≦0.25、
0≦c≦0.4、好ましくは0≦c≦0.2、0<a+
b+c≦0.4、好ましくは0.001≦a+b+c≦
0.4、さらに好ましくは0.005≦a+b+c≦0.25
である。)で示される。 本発明の置換固溶型結晶性酸化物は、特開昭51
−95990号明細書に記載されたバナジウム−リン
系結晶性酸化物と殆ど−致するX線回折パターン
を示し、その回折ピークの回折角および強度は、
下記表−1のとおりであるが、
The present invention relates to a novel substituted solid solution crystalline oxide useful as a precursor of a gas phase oxidation catalyst, particularly a catalyst for producing maleic anhydride from C4 hydrocarbons. As a catalyst for producing maleic anhydride by gas phase oxidation of C4 hydrocarbons, V-P-O complex oxides (JP-A No. 48-63982, No. 51-95990, No. 52-156193,
53-146992, Special Publication No. 53-39037, etc.), or
Multi-component oxide catalysts containing vanadium, phosphorus, and iron or chromium as a third component (Japanese Patent Publications No. 53-43928, No. 53-43929, No. 53-60391,
53-61587, USP3, 156, 705, etc.) are known. Among these known oxide catalysts, the former is a crystalline oxide, and the latter is amorphous. As a result of various studies on the suitability of multi-component oxidation catalysts for gas phase oxidation reactions, the present inventor found that catalysts made by simply adding a third component such as cobalt or nickel to a crystalline vanadium-phosphorus oxide were not known in the art. Compared to the crystalline vanadium-phosphorus oxide of
Although the activity and selectivity in gas-phase oxidation reactions are lower, new substituted solids obtained by substituting cobalt, nickel, titanium, etc. for a part of vanadium without destroying the crystal structure of crystalline vanadium-phosphorus oxides. The present invention was achieved by discovering that a dissolved crystalline oxide can serve as a precursor for a gas-phase oxidation catalyst with high activity and excellent selectivity. The present invention will be explained in detail below. The substituted solid solution crystalline oxide of the present invention consists of vanadium, phosphorus, oxygen, hydrogen and titanium, or further includes manganese, cobalt, nickel, iron,
It is a crystalline oxide that also contains an element selected from chromium and aluminum, and is a blue crystal in which a part of the vanadium forming the crystal is replaced with a metal other than the vanadium. The composition of the substituted solid solution crystalline oxide excluding oxygen, hydrogen, and water of crystallization is the following formula [] V 1.0-abc Ti a X b Y c P 1.0 ... [] (However, Y represents at least one selected from Fe, Cr, and Al.
represents at least one type selected from 0<a≦
0.4, preferably 0.001≦a≦0.4, more preferably 0.005≦a≦0.25, 0≦b≦0.4, preferably
0.001≦b≦0.4, more preferably 0.005≦b≦
0.25, 0<a+b≦0.4 preferably 0.001≦a+b
≦0.4, more preferably 0.005≦a+b≦0.25,
0≦c≦0.4, preferably 0≦c≦0.2, 0<a+
b+c≦0.4, preferably 0.001≦a+b+c≦
0.4, more preferably 0.005≦a+b+c≦0.25
It is. ). The substituted solid solution type crystalline oxide of the present invention is disclosed in Japanese Unexamined Patent Publication No. 51
It shows an X-ray diffraction pattern that almost matches that of the vanadium-phosphorus crystalline oxide described in the specification of 95990, and the diffraction angle and intensity of the diffraction peak are as follows:
As shown in Table 1 below,

【表】 バナジウムの置換程度が高くなるに従つて、回
折角が極く僅かずつシフトする傾向を示す。 本発明の置換固溶型結晶性酸化物を製造するた
めの原料としては、五酸化バナジウム、メタバナ
ジン酸、ピロバナジン酸、オキシ三塩化バナジウ
ム等の五価のバナジウム化合物、オキシ二塩化バ
ナジウム等の四価のバナジウム化合物、五酸化リ
ン、オルトリン酸、ピロリン酸、トリポリリン
酸、オキシ三塩化リン等の五価のリン化合物、マ
ンガン、コバルト、ニツケルの塩化物等のハロゲ
ン化物、酢酸塩等の有機酸塩、水酸化物、炭酸塩
または硝酸塩、チタンの塩化物または硫酸塩、
鉄、クロム、アルミニウムのハロゲン化物オキシ
酸または酢酸塩などが使用される。五価のバナジ
ウム化合物を原料として用いる場合には、ヒドラ
ジン、ヒドロキシルアミン、またはこれらのハロ
ゲン化水素酸塩あるいはハロゲン化水素などの還
元剤を併用し、四価のバナジウム、五価のリンの
オキシ酸、他の金属成分およびハロゲンイオンを
含む均−な水溶液を調製し、濃縮、蒸発乾固等の
手法により本発明の置換固溶型結晶性酸化物を得
ることができる。また、水溶液の濃縮に先だつて
エチレンオキサイド、エチレンカーボネート等の
ハロゲン化水素捕捉剤を添加することにより、結
晶の純度を高めることが可能になり、高比表面積
を有する結晶を得ることができる。あるいは、蒸
発乾固を行なつて大部分のハロゲン化水素を除去
したのち、水を添加して煮沸洗浄し、可溶性物質
を除去することにより結晶の純度を高めることが
できる。 各原料の使用量比は、リンのバナジウムおよび
バナジウム以外の金属成分の合計に対する原子比
で0.8〜1.25、特に1.00〜1.10とすることが好まし
く、バナジウムおよびバナジウム以外の金属成分
の合計に対するバナジウム以外の金属成分の原子
比は前記式〔〕に示した比に調整することが好
ましい。また、水溶液中のリン酸の初濃度は5〜
50重量%好ましくは10〜35重量%に調整される。 本発明の置換固溶型結晶性酸化物は、担体に担
持したのち、または常法により成形し、250〜650
℃で焼成することにより、気相酸化触媒、特に
C4炭化水素より無水マレイン酸を製造するため
の触媒として使用することができる。 次に本発明を実施例により更に具体的に説明す
るが、本発明はその要旨を越えない限り以下の実
施例に限定されるものではない。 実施例 1 2.52Mのオルトリン酸水溶液40mlに、ヒドラジ
ン二塩酸塩2.378gを水50mlに溶解させた水溶液
を加えて、還流冷却器付きのフラスコ中、75℃の
水浴上で撹拌しつつ五酸化バナジウム8.2379gを
少量ずつ添加した。約30分間、バナジウムの還元
の進行に伴い窒素等のガスが発生したが、発泡が
殆ど認められなくなつたのち、30分間ほぼ100℃
で煮沸還流して還元を完結させた。放冷後、四塩
化チタン0.573g及び塩化コバルト1.676gを水10
mlに溶解させた溶液を加え、再度1時間ほぼ100
℃で煮沸還流を行なつた。次いで内溶液を蒸発皿
に移し、130℃の恒温槽内で、内溶液を撹拌しな
がら塩酸臭が認められなくなるまで乾固した。析
出物に水約100mlを加えて煮沸したのち過、水
洗および乾燥を行ない、青色の結晶を得た。 得られた結晶Co/Ti原子比7/3、(Co+Ti)
(V+Co+Ti)原子比0.1、P/(V+Co+Ti)
原子比1.0であり、X線回折スペクトル(対陰
極;Cu−Kα)による分析の結果、表−1に記載
したものとほぼ−致するX線回折パターンが得ら
れた。〔X線スペクトル図(対陰極:Cu−Kα)
を第1図に示す。〕また、2θ≒27.0および2θ≒
24.2゜の回折ピークについてα−アルミナ内標
(λ=1.54050Å)にて面間隔を精密測定した結
果、及び収量を表−2に示す。 比較例 1 85重量%オルトリン酸11.529gを水60mlに加
え、これにヒドラジン二塩酸塩2.625gを水30ml
に溶解して得た水溶液を添加した。この水溶液を
水浴上で80℃に加熱し、五酸化バナジウム9.095
gを撹拌下に少量ずつ添加したのち30分間撹拌を
継続し、さらに30分間ほぼ100℃で煮沸還流を行
ない青色水溶液を得た。得られた水溶液を実施例
1と同様に130℃の恒温槽中で蒸発乾固し、淡青
色結晶を得た。得られた結晶のP/V比は1.0で
あり、X線回折パターンは表−1に記載したもの
と−致した。また、2θ≒27.0゜および2θ≒24.2゜の
回折ピークについての面間隔の精密測定結果及び
収量を表−2に示す。
[Table] As the degree of vanadium substitution increases, the diffraction angle tends to shift very slightly. Raw materials for producing the substituted solid solution crystalline oxide of the present invention include pentavalent vanadium compounds such as vanadium pentoxide, metavanadic acid, pyrovanadic acid, vanadium oxytrichloride, and tetravalent vanadium compounds such as vanadium oxydichloride. vanadium compounds, pentavalent phosphorus compounds such as phosphorus pentoxide, orthophosphoric acid, pyrophosphoric acid, tripolyphosphoric acid, phosphorus oxytrichloride, halides such as chlorides of manganese, cobalt, and nickel, organic acid salts such as acetates, hydroxides, carbonates or nitrates, chlorides or sulfates of titanium,
Halide oxyacids or acetates of iron, chromium, and aluminum are used. When a pentavalent vanadium compound is used as a raw material, a reducing agent such as hydrazine, hydroxylamine, or their hydrohalides or hydrogen halides is used in combination to reduce the oxyacid of tetravalent vanadium or pentavalent phosphorus. The substituted solid solution type crystalline oxide of the present invention can be obtained by preparing a homogeneous aqueous solution containing halogen ions, other metal components, and halogen ions, and performing techniques such as concentration and evaporation to dryness. Furthermore, by adding a hydrogen halide scavenger such as ethylene oxide or ethylene carbonate prior to concentrating the aqueous solution, it is possible to increase the purity of the crystals and obtain crystals with a high specific surface area. Alternatively, the purity of the crystals can be increased by evaporating to dryness to remove most of the hydrogen halide, followed by adding water and washing by boiling to remove soluble substances. The usage ratio of each raw material is preferably 0.8 to 1.25, especially 1.00 to 1.10 in atomic ratio of phosphorus to the total of vanadium and metal components other than vanadium, and The atomic ratio of the metal components is preferably adjusted to the ratio shown in the above formula []. Also, the initial concentration of phosphoric acid in the aqueous solution is 5~
It is adjusted to 50% by weight, preferably 10 to 35% by weight. The substituted solid solution type crystalline oxide of the present invention is prepared by supporting it on a carrier or molding it by a conventional method,
By calcining at °C, the gas phase oxidation catalyst, especially
It can be used as a catalyst for producing maleic anhydride from C4 hydrocarbons. Next, the present invention will be explained in more detail with reference to examples, but the present invention is not limited to the following examples unless it exceeds the gist thereof. Example 1 An aqueous solution of 2.378 g of hydrazine dihydrochloride dissolved in 50 ml of water was added to 40 ml of a 2.52 M aqueous orthophosphoric acid solution, and vanadium pentoxide was added in a flask equipped with a reflux condenser while stirring on a water bath at 75°C. 8.2379g was added in portions. For about 30 minutes, gases such as nitrogen were generated as the reduction of vanadium progressed, but after almost no bubbling was observed, the temperature was kept at about 100℃ for 30 minutes.
The reduction was completed by boiling and refluxing. After cooling, add 0.573 g of titanium tetrachloride and 1.676 g of cobalt chloride to 10 ml of water.
Add the dissolved solution to 100 ml for 1 hour again.
Boiling and refluxing was carried out at °C. Next, the inner solution was transferred to an evaporating dish, and the inner solution was dried in a constant temperature bath at 130° C. while stirring until the odor of hydrochloric acid was no longer observed. Approximately 100 ml of water was added to the precipitate and the mixture was boiled, filtered, washed with water, and dried to obtain blue crystals. Obtained crystal Co/Ti atomic ratio 7/3, (Co+Ti)
(V+Co+Ti) atomic ratio 0.1, P/(V+Co+Ti)
The atomic ratio was 1.0, and as a result of analysis using an X-ray diffraction spectrum (anticathode; Cu-Kα), an X-ray diffraction pattern almost identical to that described in Table 1 was obtained. [X-ray spectrum diagram (Anticathode: Cu-Kα)
is shown in Figure 1. ] Also, 2θ≒27.0 and 2θ≒
Table 2 shows the results of precisely measuring the interplanar spacing of the 24.2° diffraction peak using an α-alumina internal standard (λ = 1.54050 Å) and the yield. Comparative Example 1 11.529 g of 85% by weight orthophosphoric acid was added to 60 ml of water, and 2.625 g of hydrazine dihydrochloride was added to 30 ml of water.
An aqueous solution obtained by dissolving the mixture was added. This aqueous solution was heated to 80°C on a water bath, and 9.095% vanadium pentoxide was added.
g was added little by little with stirring, stirring was continued for 30 minutes, and boiling and refluxing was carried out at approximately 100° C. for another 30 minutes to obtain a blue aqueous solution. The resulting aqueous solution was evaporated to dryness in a constant temperature bath at 130°C in the same manner as in Example 1 to obtain pale blue crystals. The P/V ratio of the obtained crystal was 1.0, and the X-ray diffraction pattern matched that shown in Table 1. In addition, Table 2 shows the results of precision measurement of interplanar spacing and yield for the diffraction peaks at 2θ≒27.0° and 2θ≒24.2°.

【表】 実施例 2 四塩化チタン及び塩化コバルトのかわりに四塩
化チタン0.573gおよび三塩化鉄(FeCl3・6H2O)
1.892gを使用して実施例1と同様に置換固溶型
結晶性酸化物を調製し、Fe/Ti原子比7/3、
(Fe+Ti)/(V+Fe+Ti)原子比0.1、P/
(V+Fe+Ti)原子比1.0の青色結晶収量14.2gを
得た。 反応使用例 実施例1及び2において製造した置換固溶型結
晶性酸化物、比較例1において製造したV−P−
O系結晶性酸化物および比較例1において製造し
た結晶性酸化物7.74gとリン酸ニツケル(Ni3
(PO42)1.647gの混合物(組成;V1.0Ni0.1P1.07
をそれぞれ550℃、窒素気流下に2時間焼成し、
7mmφ×3mmに打錠成形したのち破砕して14〜24
メツシユ(JIS規格)の粒度の触媒を得た。 上記触媒の0.5mlを内径6mmのガラス製マイク
ロリアクターに充填し、n−ブタン1.5容量%を
含有する空気をGHSV500hr-1または2000hr-1
流通させ、各触媒の最適反応温度においてn−ブ
タンの気相酸化反応を行なつた。反応生成ガスは
保温ガスサンプラーを通して直接ガスクロマトグ
ラフに導入し、分析、定量した。各触媒につい
て、GHSV、最適反応温度、n−ブタン転化率
および無水マレイン酸収率を表−3に示す。
[Table] Example 2 Titanium tetrachloride 0.573g and iron trichloride (FeCl 3 6H 2 O) instead of titanium tetrachloride and cobalt chloride
A substituted solid solution crystalline oxide was prepared in the same manner as in Example 1 using 1.892 g, and the Fe/Ti atomic ratio was 7/3.
(Fe+Ti)/(V+Fe+Ti) atomic ratio 0.1, P/
A yield of 14.2 g of blue crystals with a (V+Fe+Ti) atomic ratio of 1.0 was obtained. Reaction usage example Substituted solid solution type crystalline oxide produced in Examples 1 and 2, V-P- produced in Comparative Example 1
O-based crystalline oxide and 7.74 g of the crystalline oxide produced in Comparative Example 1 and nickel phosphate (Ni 3
(PO 4 ) 2 ) 1.647g mixture (composition; V 1.0 N i0.1 P 1.07 )
Each was baked at 550℃ for 2 hours under a nitrogen stream,
Formed into tablets of 7 mmφ x 3 mm and then crushed into 14 to 24
A catalyst with particle size of mesh (JIS standard) was obtained. 0.5ml of the above catalyst was packed into a glass microreactor with an inner diameter of 6mm, and air containing 1.5% by volume of n-butane was passed through it at a GHSV of 500hr -1 or 2000hr -1 . A gas phase oxidation reaction was performed. The reaction product gas was directly introduced into a gas chromatograph through a heat-insulated gas sampler, and analyzed and quantified. Table 3 shows the GHSV, optimum reaction temperature, n-butane conversion rate, and maleic anhydride yield for each catalyst.

【表】【table】 【図面の簡単な説明】[Brief explanation of drawings]

第1図は実施例1で得られた結晶性酸化物のX
線回折スペクトルである。
Figure 1 shows the crystalline oxide X obtained in Example 1.
This is a line diffraction spectrum.

Claims (1)

【特許請求の範囲】[Claims] 1 バナジウム、リン、酸素、水素およびチタン
から成るか、さらにこれにマンガン、コバルト、
ニツケル、鉄、クロム及びアルミニウムから選ば
れた元素をも含有する結晶性酸化物であつて、X
線回折スペクトル(対陰極;Cu−Kα)において
15.7゜、19.8゜、24.4゜、27.3゜、30.6゜および40.6゜
なる
回折角(2θ)にピークを有するバナジウム、リン
および酸素により構成される結晶性酸化物と同型
の結晶型を有する結晶性酸化物であつて、バナジ
ウムの−部が上記バナジウム以外の金属により置
換されていることを特徴とする置換固溶型結晶性
酸化物。
1 Consists of vanadium, phosphorus, oxygen, hydrogen and titanium, or further contains manganese, cobalt,
A crystalline oxide also containing an element selected from nickel, iron, chromium and aluminum,
In line diffraction spectrum (anticathode; Cu-Kα)
A crystalline oxide having the same crystal form as a crystalline oxide composed of vanadium, phosphorus, and oxygen having peaks at diffraction angles (2θ) of 15.7°, 19.8°, 24.4°, 27.3°, 30.6°, and 40.6°. 1. A substituted solid solution type crystalline oxide, characterized in that - part of vanadium is substituted with a metal other than vanadium.
JP55184291A 1980-12-25 1980-12-25 Substitutional solid solution crystalline oxide Granted JPS57111219A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP55184291A JPS57111219A (en) 1980-12-25 1980-12-25 Substitutional solid solution crystalline oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP55184291A JPS57111219A (en) 1980-12-25 1980-12-25 Substitutional solid solution crystalline oxide

Publications (2)

Publication Number Publication Date
JPS57111219A JPS57111219A (en) 1982-07-10
JPH024525B2 true JPH024525B2 (en) 1990-01-29

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JPS51117191A (en) * 1973-06-25 1976-10-15 Monsanto Co Catalysts for manufacture of maleic acid anhydride
GB1475309A (en) * 1973-08-03 1977-06-01 Ucb Sa Process for the production of maleic anhydride
US4018709A (en) * 1975-03-17 1977-04-19 Petro-Tex Chemical Corporation Catalyst for preparing maleic anhydride from C4 hydrocarbons

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