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Catalyst for hydrogenating cis-butenedioic anhydride to prepare butanedioic anhydride and its preparation method and application

A technology for the preparation of succinic anhydride and hydrogen, which is applied in the catalyst for the preparation of succinic anhydride by maleic anhydride hydrogenation and its preparation and application fields, and can solve the problems of high nickel content in active components, large solvent circulation, and low processing capacity of maleic anhydride, etc. problems, achieve high selectivity, simple preparation method, and enhanced acid resistance

Active Publication Date: 2014-05-07
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has the disadvantages of high content of nickel in the active component, low treatment capacity of maleic anhydride, large solvent circulation, high energy consumption, and high separation cost.

Method used

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  • Catalyst for hydrogenating cis-butenedioic anhydride to prepare butanedioic anhydride and its preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Put diatomite (Jilin Changbai Diatomite Co., Ltd.) into dilute nitric acid solutions of different concentrations for soaking treatment. The concentration of nitric acid solution is 0.3mol / L, 0.2mol / L, 0.1mol / L, 0.08mol / L respectively; the soaking temperature is 60℃, 70℃, 80℃, 90℃ respectively; the soaking time is 2h respectively , 3h, 4h, 5h; filter after soaking. After the above treatment, an appropriate amount of diatomite and an appropriate amount of silica sol were kneaded and molded, dried at room temperature for 30 h, 25 h, 20 h, and 15 h, and then placed in an oven at 80°C, 100°C, 120°C, and 140°C respectively. Dry at ℃ for 50 h, 35 h, 20 h, 15 h. Finally, under the air atmosphere, keep the temperature at 300°C, 350°C, 400°C, and 350°C for 5h, 3h, 4h, and 2h, and then keep the temperature at 650°C, 700°C, 750°C, and 700°C for 10h, 8h, and 10h, respectively. , 12h, prepared different catalyst supports, the weight content of diatomaceous earth in the catalyst sup...

Embodiment 2

[0027] Use equal volumes of nickel nitrate hexahydrate and copper nitrate ammonia solution to impregnate the carrier with a weight content of 50% diatomite prepared in Example 1, let it stand at room temperature for 2 hours, and dry it at 100°C for 6 hours. In a muffle furnace, the air atmosphere Calcined at 550°C for 24 hours to obtain catalyst A, the content of nickel in the catalyst was 5wt%, and the content of copper was 2wt%.

Embodiment 3

[0029] Use nickel nitrate hexahydrate and copper nitrate ammonia solution to impregnate the carrier with a diatomite weight content of 80% prepared in Example 1, let it stand at room temperature for 2 hours, and dry it at 100°C for 6 hours. In a muffle furnace, the air atmosphere Calcined at 550°C for 24 hours to obtain catalyst B, the content of nickel in the catalyst was 7wt%, and the content of copper was 5wt%.

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Abstract

The invention discloses a preparation method of a catalyst for hydrogenating cis-butenedioic anhydride to prepare butanedioic anhydride, the preparation method comprises the following steps: firstly, kneading a proper amount of diatomite and silica sol for molding, drying, roasting to prepare a catalyst carrier, using an immersion method to load active component nickel and a catalyst aid onto the catalyst carrier, and the catalyst aid comprising at least one from chromium, molybdenum, tungsten, manganese, rhenium, ruthenium, cobalt, rhodium, palladium, platinum, silver, copper, magnesium, lanthanum, cerium, calcium, potassium, germanium and tin, and preferably comprising copper, palladium and the like. The catalyst for hydrogenating the cis-butenedioic anhydride to prepare the butanedioic anhydride comprises, by catalyst weight, 3-8wt% of nickel, and 0.1-10wt% and preferably 0.5-5wt% of the catalyst aid, and the content of the diatomite in the catalyst carrier is 50-80 wt%. The catalyst is low in active component content, can process high-concentration and high-space-velocity cis-butenedioic anhydride solutions, and has the advantages of high activity, high selectivity, long life and the like.

Description

technical field [0001] The invention relates to a catalyst for preparing succinic anhydride by hydrogenating maleic anhydride, a preparation method and application thereof. Background technique [0002] Succinic anhydride, also known as succinic anhydride, has extensive and important uses in the fields of food, medicine, pesticides, dyes, spices, paints, plastics and material industries. With the development of my country's pharmaceutical, pesticide, material, petrochemical and other industries, the demand for succinic anhydride has increased rapidly, and there is a certain gap in domestic succinic anhydride, especially the refined succinic anhydride with a mass content of more than 99% is almost entirely dependent on import. [0003] Succinic anhydride is currently mainly prepared by succinic acid dehydration method or maleic anhydride hydrogenation method. The disadvantages of succinic acid dehydration method are high energy consumption, difficult operation process control...

Claims

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Application Information

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IPC IPC(8): B01J23/755B01J23/89C07D307/60
Inventor 吕清林霍稳周范丹丹
Owner CHINA PETROLEUM & CHEM CORP