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Catalyst for synthesis of maleic anhydride and preparation method thereof

A technology of catalyst and maleic anhydride, applied in the field of catalyst for synthesizing maleic anhydride and its preparation, can solve problems such as affecting the morphology and performance of the catalyst, and achieve the effect of improving the catalytic performance

Active Publication Date: 2017-04-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] One of the technical problems to be solved by the present invention is to disclose a method for preparing a catalyst for the synthesis of maleic anhydride in view of the problem that the structure of the vanadium source affects the morphology and performance of the catalyst in the prior art. method to produce particles with a particle size of 1-8μm and a specific surface area of ​​10-25m 2 / g, the vanadium source with rich pore structure improves the structure and morphology of the catalyst, thereby improving the performance of the catalyst

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  • Catalyst for synthesis of maleic anhydride and preparation method thereof

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Effect test

Embodiment 1

[0025] After ball milling 1 part of industrial-grade ammonium metavanadate, the particle size is 1-15 μm, stirring in 3.6 parts of ethylene glycol solution at 350r / min for 5 hours, and then roasting in a roasting furnace at 350°C for 5 hours after suction filtration to obtain refined Ammonium metavanadate, the particle size is 1-8μm, and the specific surface area is 21m 2 / g, with a rich pore structure. Mix the refined 30g of ammonium metavanadate with 300ml of isobutanol, add 35g of 100wt% phosphoric acid and 1g of phosphomolybdic acid, heat and reflux under stirring for 15h, filter and dry the resulting product, and heat-treat at 400°C to obtain a catalyst . Gained catalyst is reacted with the butane raw material whose molar concentration is 1.5% mol, and its reaction process condition: 2000hr -1 Space velocity and 400°C normal pressure were evaluated in a fixed-bed reactor, and the conversion rate of butane was measured to be 83.5%, and the yield of maleic anhydride was 6...

Embodiment 2

[0027] After ball milling 1 part of industrial-grade ammonium metavanadate, the particle size is 1-15 μm, stirring in 3.6 parts of glycerol solution at 350 r / min for 5 hours, suction filtering and roasting at 350 °C for 5 hours in a roasting furnace to obtain refined Ammonium metavanadate, the particle size is 1-8μm, and the specific surface area is 22m 2 / g, with a rich pore structure. Mix the refined 30g of ammonium metavanadate with 300ml of isobutanol, add 35g of 100wt% phosphoric acid and 1g of phosphomolybdic acid, heat and reflux under stirring for 15h, filter and dry the resulting product, and heat-treat at 400°C to obtain a catalyst . Gained catalyst is reacted with the butane raw material whose molar concentration is 1.5% mol, and its reaction process condition: 2000hr -1 Space velocity and 400°C normal pressure were evaluated in a fixed-bed reactor, and the conversion rate of butane was measured to be 83.6%, and the yield of maleic anhydride was 61.7%. The evaluat...

Embodiment 3

[0029] After ball milling 1 part of industrial-grade ammonium metavanadate, the particle size is 1-15 μm, stirring in 3.6 parts of pentaerythritol solution at 350 r / min for 5 hours, and then roasting in a roasting furnace at 350 ° C for 5 hours after suction filtration to obtain refined metavanadate Ammonium vanadate, the particle size is 1-8μm, the specific surface area is 21m 2 / g, with a rich pore structure. Mix the refined 30g of ammonium metavanadate with 300ml of isobutanol, add 35g of 100wt% phosphoric acid and 1g of phosphomolybdic acid, heat and reflux under stirring for 15h, filter and dry the resulting product, and heat-treat at 400°C to obtain a catalyst . Gained catalyst is reacted with the butane raw material whose molar concentration is 1.5% mol, and its reaction process condition: 2000hr -1 The space velocity and 400°C normal pressure were evaluated in a fixed-bed reactor, and the conversion rate of butane was measured to be 83.3%, and the yield of maleic anh...

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Abstract

The invention relates to a catalyst for synthesis of maleic anhydride and a preparation method thereof, and mainly solves the problem that in the prior art the small catalyst specific surface area affects the contact between an active site and a reactant. The catalyst adopted by the invention comprises: 10-25% of vanadium, 10-25% of phosphorus, 15-40% of oxygen, and 0.001-5% of a metal additive, wherein vanadium is selected from at least one of refined ammonium metavanadate, vanadium pentoxide or organic acid vanadium; and the metal additive is selected from at least one of copper, nickel, molybdenum and zirconium. According to the technical scheme, a vanadium source with small particle size and large specific surface area is produced by a refining method combining physical and chemical processes, so that the formed catalyst has a stereostructure, can promote the exposure of the active site, and can be applied to the field of maleic anhydride preparation by n-butane oxidation.

Description

technical field [0001] The invention relates to a catalyst for synthesizing maleic anhydride and a preparation method thereof. Background technique [0002] Maleic anhydride, referred to as maleic anhydride, or maleic anhydride, is a commonly used important organic chemical raw material, and is the third largest anhydride in the world after phthalic anhydride and acetic anhydride. Maleic anhydride is widely used in petrochemical, food chemical, pharmaceutical, building materials and other industries, mainly for the synthesis of unsaturated polyester resin, lubricating oil additive, food additive, 1,4-butanediol (BDO), γ-butyrol Esters (GBL), tetrahydrofuran (THF) and a series of important important organic chemicals and fine chemicals. [0003] The early production of maleic anhydride was prepared by the selective oxidation of benzene, but due to the harmfulness of benzene to the human body and the environment, as well as the influence of economic factors, the proportion of...

Claims

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Application Information

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IPC IPC(8): B01J27/199B01J35/10C07D307/60
Inventor 徐俊峰顾龙勤曾炜陈亮赵欣王丹柳曹艳萍
Owner CHINA PETROLEUM & CHEM CORP