Extraction separation method of acetylpropionic acid
A levulinic acid and extraction technology, applied in chemical instruments and methods, separation/purification of carboxylic acid compounds, preparation of carboxylate, etc.
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Embodiment 1
[0026] Tributyl phosphate is used as a complexing agent, and propyl formate is used as a cosolvent. The mass ratio of the complexing agent and the co-solvent is 1:1 to prepare a complexing extractant, and the raw material hydrolyzate and the complexing extractant are mixed in a separatory funnel at a temperature of 25°C Shake and stand for one hour. After separation, take the upper organic phase for analysis. The separation coefficient is 4.98, and the extraction rate of levulinic acid is 83.28%.
Embodiment 2
[0028] Tributyl phosphate is used as a complexing agent, and propyl formate is used as a cosolvent. The mass ratio of the complexing agent and the co-solvent is 1:1 to prepare a complexing extractant, and the raw material hydrolyzate and the complexing extractant are mixed in a separatory funnel at a temperature of 25°C Shake and stand for one hour. After separation, take the upper organic phase for analysis. The separation coefficient is 4.43, and the extraction rate of levulinic acid is 81.58%.
Embodiment 3
[0030] Tributyl phosphate is used as a complexing agent, and ethyl acetate is used as a cosolvent. The mass ratio of the complexing agent and the co-solvent is 1:1 to prepare a complexing extractant, and the raw material hydrolyzate and the complexing extractant are mixed in a separatory funnel at a temperature of 25°C Shake and stand for one hour. After separation, take the upper organic phase for analysis. The separation coefficient is 9.51, and the extraction rate of levulinic acid is 90.49%.
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