Method for preparing butanedioic acid under catalytic hydrogenation

A technology for catalytic hydrogenation and succinic acid, which is used in the preparation of carboxylic acid by ozone oxidation, the preparation of carboxylic acid anhydride, and organic chemistry, etc. Low production cost and energy consumption, high yield, and the effect of saving raw materials

Active Publication Date: 2013-04-03
HUNAN CHANGLING PETROCHEM SCI & TECH DEV CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The catalyst has a good hydrogenation effect for the preparation of succinic acid, but the preparation of the catalyst is complicated, and its hydrogenation process is an intermittent and discontinuous process, which requires separation of the product and the catalyst. The catalyst is powder and can be recycled. low rate

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0012] Using Ni / SiO with 10.0w%Ni 2 The catalyst is catalytically hydrogenated in a fixed-bed reactor to prepare succinic acid. The raw material for hydrogenation is 25wt% maleic anhydride aqueous solution. The reaction conditions are: reaction inlet temperature 30°C, reaction outlet temperature 70°C, reaction hydrogen partial pressure 7.0MPa, volume Airspeed 0.1h -1 , Hydrogen acid molar ratio 30:1. The material obtained in the hydrogenation reaction is cooled and crystallized, filtered; the filter cake is dried to obtain succinic acid. The conversion rate of raw materials and the selectivity of succinic acid are 99.1% and 99.4% respectively, and the purity of the product after purification can reach 99.7%.

Embodiment 2

[0014] Using Fe-Pt / ZrO containing 0.6w%Fe-0.1w%Pt 2 Catalysts were tested in a fixed bed reactor to prepare succinic acid by catalytic hydrogenation. The raw material for hydrogenation was 40wt% maleic acid aqueous solution. The reaction conditions were: reaction inlet temperature 50°C, reaction outlet temperature 135°C, reaction hydrogen partial pressure 5.0MPa , with a volumetric space velocity of 0.5 h -1 , the molar ratio of hydrogen to acid is 5:1, the material obtained from the hydrogenation reaction is cooled and crystallized, filtered; the filter cake is dried to obtain succinic acid. The conversion rate of raw materials and the selectivity of succinic acid are 99.0% and 99.0% respectively, and the purity of the product after purification can reach 99.5%.

Embodiment 3

[0016] The Co-Pd / C catalyst containing 3.5w%Co-0.2w%Pd was used to carry out catalytic hydrogenation to prepare succinic acid in a fixed-bed reactor. The hydrogenation raw materials were 15wt% fumaric acid and maleic acid aqueous solution. Reaction conditions: reaction inlet temperature 50°C, reaction outlet temperature 130°C, reaction hydrogen partial pressure 0.1MPa, volumetric space velocity 1.0 h -1 , the molar ratio of hydrogen to acid is 8:1, the material obtained by the hydrogenation reaction is cooled and crystallized, filtered; the filter cake is dried to obtain succinic acid. The raw material conversion rate and succinic acid selectivity are 99.5% and 99.7% respectively, and the product purity after purification is 99.8%.

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Abstract

The invention discloses a method for preparing butanedioic acid under catalytic hydrogenation, which is characterized in that one or more of maleic anhydride water solution, fumaric acid water solution or maleic acid water solution are arranged inside a fixed bed reactor with catalyst to be hydrogenated to obtain butanedioic acid. By adopting the fixed bed, the catalytic hydrogenation preparationof butanedioic acid realizes the continuous mass production; transformation rate of raw materials and selectivity of the butanedioic acid reach more than 99 percent, and the purity of the product reaches more than 99.5 percent; the catalyst is of a particle-shaped load-type catalyst, and the separation of the product and the catalyst is not required; by adopting the mother liquid cycling utilization technology, raw material is saved, cost is reduced, yield can reach 100 percent, and zero emission of the three wastes is realized; and the process flow is simple, the economies of scale are large, the yield is high, and the production cost and the energy consumption are low.

Description

technical field [0001] The invention relates to a method for preparing succinic acid by catalytic hydrogenation, in particular to a method for preparing succinic acid by continuous catalytic hydrogenation in a fixed bed. Background technique [0002] Succinic acid, commonly known as succinic acid, is an important fine chemical product and organic synthesis intermediate, widely used in synthetic plastics, rubber, medicine, food, paint and other industries. In recent years, due to the continuous expansion of its application fields, the demand for this product in domestic and foreign markets is also increasing. Especially in the synthetic biodegradable plastic PBS, the demand for succinic acid will increase rapidly, and the market prospect is broad. [0003] There are many ways to produce succinic acid, but the only methods used in industry are microbial fermentation, electrochemical synthesis and catalytic hydrogenation. There are many reports on the microbial fermentation m...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C55/10C07C51/083C07C51/36
CPCY02P20/584
Inventor 李庆华周冬京佘喜春
Owner HUNAN CHANGLING PETROCHEM SCI & TECH DEV CO LTD
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