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Catalyst for preparing maleic anhydride by n-butane oxidation and preparation method thereof

A catalyst and n-butane technology, applied in physical/chemical process catalysts, chemical instruments and methods, organic chemistry, etc., can solve the problems of insignificant improvement, achieve aggregation prevention, high maleic anhydride selectivity and yield, and crystallization Fine-grained effects

Active Publication Date: 2021-05-25
常州新日催化剂股份有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The above-mentioned patents or documents improve the performance of the VPO catalyst by adding a co-catalyst, but the improvement is not significant

Method used

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  • Catalyst for preparing maleic anhydride by n-butane oxidation and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0040] In a reaction kettle with a stirring, heating and condensing reflux device, add 2700g of isobutanol and 600g of benzyl alcohol, then add 456g of vanadium pentoxide and 25.8g of silver citrate, stir evenly, and control the temperature at 110°C to 120°C, Pressure -10kPa~-20kPa, add 540g of phosphoric acid at a constant speed within 2h, then continue to reflux reaction at this temperature and pressure for 5h, cool and filter after the reaction, dry the filter cake at 110℃~130℃ for 20h, and then dry it at 300℃ Calcined at ~320°C for 6h to obtain an active precursor. The active precursor is granulated into 10 mesh to 40 mesh, mixed with 3% graphite, pressed into a hollow cylinder with an outer diameter of 5mm, an inner diameter of 2mm, and a height of 5mm, and then heated at 460°C to 480°C with an oxygen content of 9% to 11 % atmosphere activated for 6h to obtain catalyst A1.

Embodiment 2

[0042] In a reaction kettle with a stirring, heating and condensing reflux device, add 3000g of isobutanol and 600g of benzyl alcohol, then add 396g of vanadium pentoxide and 22.3g of silver citrate, stir evenly, and control the temperature at 110°C to 120°C, Pressure -10kPa~-20kPa, add 596g of phosphoric acid at a constant speed within 3h, and then continue to reflux reaction at this temperature and pressure for 5h, cool and filter after the reaction, dry the filter cake at 110℃~130℃ for 20h, and then reflux at 320℃ Calcined at ~340°C for 6h to obtain an active precursor. The active precursor is granulated into 15 mesh to 30 mesh, mixed with 2% graphite, pressed into a hollow cylinder with an outer diameter of 5 mm, an inner diameter of 2 mm, and a height of 5 mm, and then heated at 460°C to 480°C with an oxygen content of 9% to 11 % atmosphere activated for 6h to obtain catalyst A2.

Embodiment 3

[0044]In a reactor with a stirring, heating and condensing reflux device, add 3300 g of isobutanol and 660 g of benzyl alcohol, then add 456 g of vanadium pentoxide and 27 g of rhodium isooctanoate, stir evenly, control the temperature at 110°C to 120°C, and the pressure -10kPa~-20kPa, add 540g of phosphoric acid at a constant speed within 2h, and then continue to reflux reaction at this temperature and pressure for 5h, cool and filter after the reaction, dry the filter cake at 120℃~140℃ for 18h, and then reflux at 320℃~ Calcined at 340°C for 6h to obtain an active precursor. The active precursor is granulated into 15 mesh to 30 mesh, mixed with 2% graphite, pressed into a hollow cylinder with an outer diameter of 5mm, an inner diameter of 2mm, and a height of 5mm, and then heated at 460°C to 480°C with an oxygen content of 9% to 11 % atmosphere activated for 6h to obtain catalyst A3.

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Abstract

The invention discloses a catalyst for preparing maleic anhydride by n-butane oxidation and a preparation method thereof, belonging to the technical field of catalysts. The present invention forms V-X dual active centers in the catalyst by adding co-catalyst X (at least one of silver, ruthenium and rhodium) to the catalyst for preparing maleic anhydride by n-butane oxidation, so that the catalyst has a lower The selective oxidation active temperature can complete the reaction of butane oxidation to maleic anhydride at a lower temperature to obtain higher maleic anhydride selectivity and yield. The main application of the invention is to catalyze the selective oxidation reaction of n-butane to prepare maleic anhydride.

Description

technical field [0001] The invention relates to a catalyst for preparing maleic anhydride by n-butane oxidation and a preparation method thereof, belonging to the technical field of catalysts. Background technique [0002] Maleic anhydride, also known as maleic anhydride and maleic anhydride, is an important organic chemical raw material and the third largest anhydride in the world after phthalic anhydride and acetic anhydride. It is used in the production of unsaturated polyester resins and alkyd resins , pesticides, medicines, coatings, inks, lubricating oil additives, paper chemicals, textile finishing agents, food additives and surfactants, etc., can be used to produce a series of fine chemical products with a wide range of uses, and the development and utilization prospects are very broad. According to different raw materials used in the production of maleic anhydride, there are mainly two process routes: benzene oxidation method and butane oxidation method. In foreign...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/198C07D307/60
CPCB01J27/198C07D307/60
Inventor 刘先国魏士新王康军邹红旭胡佳陈鹏宋大朋潘蔚石龙
Owner 常州新日催化剂股份有限公司