Fluid-bed catalyst for ammoxidation of aromatic hydrocarbon

A technology of fluidized bed catalyst and ammoxidation, which is applied in the direction of preparation of hydrocarbon ammoxidation, metal/metal oxide/metal hydroxide catalyst, physical/chemical process catalyst, etc. Oxidation and other problems to achieve the effect of improving activity and selectivity, overcoming engineering amplification effect, and enhancing oxygen adsorption capacity

Inactive Publication Date: 2004-04-21
CHINA PETROLEUM & CHEM CORP +1
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  • Abstract
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  • Application Information

AI Technical Summary

Problems solved by technology

Sb catalyst has good activity, but due to factors such as the complicated preparation method of Sb catalyst and special requirements for reactors, the economics of this catalyst, especially for small batches of multi-variety aromatic hydrocarbon ammoxidation products, are unreasonable.
The V-Cr catalyst is relatively simple to prepare, has good repeatability, and has high reactivity for the ammoxidation of aromatic hydrocarbons, but it is easy to cause deep oxidation and has strong decomposition ability for ammonia.
[0005] There are many kinds of multi-component catalysts for the ammoxidation of alkylaromatics to prepare aromatic nitriles, such as ternary composition catalysts: V-Cr-B (JP19284), with SiO 2 As a carrier, fixed bed evaluation, the product yield has reached a good level, but with the increase of the reaction time, the catalytic activity of the catalyst has a downward trend, so it is difficult to industrialize; V-Cr-Ba (JP61-4388) is made of SiC Carrier, at a temperature of 370°C, fixed bed evaluation, the yield of benzonitrile is 82.3%, and the best yield of isophthalonitrile is 54.0%
Quaternary composition catalyst: V-Cr-B-Mo / SiO 2 (JP01-275551), V-Cr-B-P / SiO 2 (JP76-15028), V-Cr-Sn-P / SiO 2 (JP Zhao 45-19285) are the patents disclosed by Mitsubishi Gas and Nippon Chemical Gas Corporation respectively. Under the conditions of 410°C, 412°C, and 435°C respectively, the small-scale fixed-bed evaluation shows the best yield of benzonitrile 83.3%, 85.2%, and 83.2%, when used for the ammoxidation of picoline to prepare the corresponding heterocyclic aromatic nitrile, the product has reached a good yield; but the reactivity and stability are not ideal, and the wear resistance of the catalyst is relatively poor; the reaction By-products especially CO, CO 2 , HCN content is still high; Mitsubishi Gas announced V-Cr-B-P-Mo / SiO in the 1990s 2 (EP0525367A 1 ) five-component catalyst, but the catalyst must use more expensive phosphomolybdic acid or ammonium phosphomolybdate raw materials in order to obtain ideal reaction results
Generally speaking, the fixed bed inspection results show that the yield of aromatic nitrile is 3-5% higher than that of the fluidized bed, so it is difficult for the above-mentioned catalysts to truly represent the actual level of the fluidized bed catalyst

Method used

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  • Fluid-bed catalyst for ammoxidation of aromatic hydrocarbon
  • Fluid-bed catalyst for ammoxidation of aromatic hydrocarbon
  • Fluid-bed catalyst for ammoxidation of aromatic hydrocarbon

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0057] Catalyst preparation:

[0058] 224g V 2 o 5 Add it into a solution at a temperature of 80-90° C. consisting of 490 milliliters of water and 468 grams of oxalic acid, stir well, and react to obtain a vanadium oxalate solution.

[0059] Set the weight percent concentration to 40% SiO 2 1250 grams of silica sol are slowly added in the above-mentioned solution under stirring, then add respectively by 886 grams of Cr (NO 3 ) 3 9H 2 A solution of O and 300 ml of water, 76.3 g of H 3 BO 3 and 560 ml of water and 85 g of 85% H 3 PO 4 and 50 milliliters of water, then add 190 grams of 30% (by weight) TiCl 3 Hydrochloric acid solution, finally added containing 24.9 g KNO 3 20 milliliters of the aqueous solution, stirred, heated and evaporated to a solid content of 40% (weight), to obtain a thick slurry.

[0060] The catalyst precursor formed by spray drying the above slurry was dried at 120°C for 12 hours and calcined at 650°C for 5 hours to obtain the catalyst composi...

Embodiment 2

[0069] The preparation method of the catalyst is the same as in Example 1, except that the composition of the catalyst is changed, and the prepared slurry is spray-dried and calcined. The catalyst composition of making is: V 1.00 Cr 0.95 Ti 0.10 B 0.50 P 0.10 mn 0.2 K 0.005 / SiO 2 , The catalyst main loading weight ratio is 50 / 50.

[0070] P-xylene: ammonia: air = 1:8:40 (mol), catalyst weight loading (WWH) 0.06 hours -1 , the reaction temperature is 425°C, and the reaction pressure is 0.01MPa.

[0071] 98.6% p-xylene conversion

[0072] Selectivity to p-dibenzonitrile 92.3%

[0073] p-dibenzonitrile yield 91.0%

Embodiment 3

[0075] 224g V 2 o 5 Add it into a solution at a temperature of 80-90° C. consisting of 490 milliliters of water and 468 grams of oxalic acid, stir well, and react to obtain a vanadium oxalate solution.

[0076] The weight percent concentration is 40% SiO 2 1250 grams of silica sol are slowly added in the above-mentioned solution under stirring, then add respectively by 886 grams of Cr (NO 3 ) 3 9H 2 O. 12.4 g KNO 3 and 500 ml of water, 76.4 g of H 3 BO 3 , a solution composed of 85.1 grams of 85% phosphoric acid and 500 milliliters of water and 43.5 grams (NH 4 ) 6 Mo 7 o 24 4H 2 O and the solution that 100 milliliters of waters form, add the TiCl of 63.3 grams 30% (weight) again 3 Hydrochloric acid solution, stirred, heated and evaporated to a solid content of 40% (weight), to obtain a viscous slurry.

[0077] The catalyst precursor formed by spray-drying the above slurry was pre-calcined at 300°C for 2 hours, and then calcined at 650°C for 5 hours to obtain a ca...

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Abstract

A granular fluidized-bed catalyst for ammoxidizing arylhydrocarbon to preparing arylnitrile has a chemical formula: V1.0CraTibAcBdCeOx, where A is chosen from P, B, Bi, Sb and As, B is chosen from alkali metals and alkali-earth metals, and C is choosen from Mn, Ni, Co, Sn, Pb, Fe, Mo, W and ER. Its advantage is high output rate.

Description

technical field [0001] The invention relates to a fluidized bed catalyst for the ammoxidation of aromatic hydrocarbons, in particular to a fluidized bed catalyst for the ammoxidation of substituted aromatic hydrocarbons or heterocyclic aromatic hydrocarbons. Background technique [0002] Due to the chemical activity of the aromatic nitrile cyano group, a series of fine chemical products can be synthesized through hydrolysis, hydrogenation, addition or polycondensation reactions, which are important raw materials for the manufacture of pesticides, medicines, dyes, spices, resins, etc. For example, 2-cyano-4-nitroaniline can be obtained through nitration ammonolysis reaction of o-chlorobenzonitrile, which is an important intermediate of various azo disperse dyes; p-chlorobenzonitrile is used to prepare high-grade car paint Pigments; isophthalonitrile (abbreviated as IPN), tetrachloroisophthalonitrile synthesized by chlorination is an efficient and low-...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/16C07C253/24
Inventor 陈金华顾龙勤施惠肖景娴金文清
Owner CHINA PETROLEUM & CHEM CORP
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