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Heteropolyacid catalyst, and preparation method and application thereof

A technology of catalysts and heteropolyacids, which is applied in the preparation of carboxylate salts, chemical instruments and methods, and the preparation of organic compounds. It can solve problems such as catalyst activity, selectivity reduction, shortened catalyst life, and uneven catalyst components.

Active Publication Date: 2013-06-26
SHANGHAI HUAYI NEW MATERIAL
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

The disadvantage of this method is that a large amount of water is used to dissolve molybdenum trioxide in the preparation process, so a large amount of energy is required to dry these compound-containing slurries in the subsequent process, resulting in a great consumption of energy
[0004] Chinese patent CN 1212302C proposes that ammonium paramolybdate, ammonium metavanadate and cesium nitrate are dissolved in a certain amount of water, and then mixed with other material precursor aqueous solutions such as phosphoric acid to prepare the method of phosphomolybdenum heteropolyacid catalyst. It has been controlled, but when the material slurry is formed, the liquid level stratification phenomenon will occur, and a large amount of sediment will be deposited at the bottom, resulting in uneven catalyst components, directly affecting the reaction performance of the catalyst, reducing the activity and selectivity of the catalyst, and shortening the life of the catalyst. Catalyst life
However, it was found that the use or non-use of ultrasonic dispersion technology had no significant effect on the reaction rate of methacrolein and the selectivity of methacrylic acid

Method used

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  • Heteropolyacid catalyst, and preparation method and application thereof
  • Heteropolyacid catalyst, and preparation method and application thereof

Examples

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preparation example Construction

[0047] The invention relates to a heteropolyacid catalyst and a preparation method thereof. The heteropolyacid catalyst of the present invention has following general formula:

[0048] Mo 12 P a V b Cu c A d D. e E. f o g

[0049] in,

[0050] A is at least one element selected from tungsten (W), silicon (Si), iron (Fe), cobalt (Co), zinc (Zn), lead (Pb), palladium (Pd) and antimony (Sb), relatively preferably iron and / or cobalt;

[0051] D is at least one element selected from boron (B), arsenic (As), tellurium (Te) and cerium (Ce), preferably arsenic and / or tellurium;

[0052] E is at least one element selected from potassium (K), rubidium (Rb) and cesium (Cs), preferably potassium and / or cesium;

[0053] a=0.1~3, preferably 0.5~2, more preferably 0.8~1.6;

[0054] b=0.01~5, preferably 0.1~2, more preferably 0.3~1;

[0055] c=0.01~5, preferably 0.05~2, more preferably 0.1~1;

[0056] d=0.001~1, preferably 0.005~0.8, more preferably 0.1~0.7;

[0057] e=0.01~2,...

Embodiment 1

[0088] Catalyst preparation

[0089] A kind of 85(Mo 12 P 1.5 V 0.5 Cu 0.3 Fe 0.2 PD 0.05 As 0.2 Cs 0.7 ) / 15SiC represents the preparation method of the heteropolyacid catalyst as follows:

[0090] 200 grams of ammonium paramolybdate and 5.5 grams of ammonium metavanadate were dissolved in 400 grams of distilled water to obtain solution A; 6.9 grams of copper nitrate, 7.7 grams of iron nitrate, 0.41 grams of palladium chloride and 13 grams of cesium nitrate were dissolved in 150 gram of distilled water to obtain solution B; 16.2 grams of phosphoric acid and 3.5 grams of arsenic acid were dissolved in 30 grams of distilled water to obtain solution C. Under the condition of stirring, the solution B is first added to the solution A, and then the solution C is added to obtain a suspension slurry, and the color of the slurry is blue at this time.

[0091] Adopt the SY-3300 type ultrasonic cleaner purchased from Shanghai Sanyou Ultrasonic Equipment Co., Ltd. to ultrasonic...

Embodiment 2

[0096] Except that the ultrasonic frequency 30KHz was changed to ultrasonic frequency 40KHz, the catalyst was prepared in the same manner as in Example 1. The catalyst composition is 85(Mo 12 P 1.5 V 0.5 Cu 0.3 Fe 0.2 PD 0.05 As 0.2 Cs 0.7 ) / 15SiC.

[0097] The selective oxidation reaction was carried out in the same manner as in Example 1, and the results obtained are shown in Table 1.

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Abstract

The invention discloses a heteropolyacid catalyst, and a preparation method and application thereof. The catalyst has the following formula: Mo12PaVbCucAdDeEfOg, wherein A represents at least one element of tungsten, silicon, iron, cobalt, zinc, lead, palladium and stibium; D represents at least one element of boron, arsenic, tellurium and cerium; E represents at least one element of potassium, rubidium and caesium; a equals to 0.1-0.3; b equals to 0.01-5; c equals to 0.01-5; d equals to 0.001-1; e equals to 0.01-2; f equals to 0.01-2; and g represents an atom ratio of oxygen needed for meeting valences of the components. The preparation method disclosed by the invention comprises the following steps of: (a) dissolving compounds of the corresponding elements respectively; (b) mixing the compounds and applying ultrasonic waves with the frequency of 10-180 kHz to the compounds at 30-90 DEG C for 0.1-3 hours, thereby preparing suspended dispersion size containing catalyst precursors of all the catalyst components; and (c) drying the suspended dispersion size to obtain the catalyst precursors, and roasting the catalyst precursors.

Description

technical field [0001] The invention relates to a catalyst for synthesizing methacrylic acid (MAA) from methacrolein (MAL) through a selective oxidation reaction and a preparation method of the catalyst. The catalyst prepared by the method of the invention not only has high reaction conversion rate, but also has high product selectivity. Background technique [0002] Catalysts for the synthesis of methacrylic acid (MAA) from methacrolein (MAL) by selective oxidation are known. For this selective oxidation catalyst, activity and selectivity are always a contradiction. An increase in activity often leads to a decrease in selectivity; an increase in selectivity often leads to a decrease in activity. However, catalysts must meet considerable activity and certain selectivity in order to meet the requirements of industrial scale-up production. For this reason, many methods have been proposed in the prior art to balance activity and selectivity. [0003] The method of producing...

Claims

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Application Information

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IPC IPC(8): B01J31/18C07C57/055C07C51/235
Inventor 温新罗鸽吴通好赵小岐金鑫磊庄岩褚小东邵敬铭
Owner SHANGHAI HUAYI NEW MATERIAL
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