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
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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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