Method for extracting hydroxyacetic acid from water solution mixture containing hydroxyacetic acid
A technology for extracting glycolic acid and glycolic acid, which is applied in the separation/purification of carboxylic acid compounds, organic chemistry and other directions, can solve the problems of difficult recovery of ammonium sulfate from power consumption, limited application and development, and pollution of electrodialysis membranes. The extraction agent is convenient, the labor conditions are improved, and the separation efficiency is high.
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Embodiment 1
[0036] The hydrolyzate containing glycolic acid with a concentration of 260g / L at a pH of 2.2 and the extractant containing 60% trioctylamine, 5% trioctyl phosphate, 15% n-octanol and 20% sulfonated kerosene by volume at Φ500mm , In a kühni tower with a height of 1000mm, at 30°C, the hydrolyzate is used as the continuous phase, and the extractant is used as the dispersed phase for countercurrent extraction, and the liquid-liquid interface is controlled below the outlet position of the upper part of the tower (ie, the upper interface of the tower). The speed of the turbine turntable is 650rpm, and the feed volume ratio of the hydrolyzate to the extractant is 1:1.75.
[0037] The concentration of glycolic acid in the extract phase output is about 135g / L, and the concentration of glycolic acid in the raffinate phase output is lower than about 18g / L. Based on the transfer of glycolic acid from the hydrolyzate to the extraction phase, the extraction rate is more than 93%.
[0038] ...
Embodiment 2
[0041] The hydrolyzate containing glycolic acid concentration of 285.7g / L at a pH of 1.9 and the extractant composed of 50% tri-n-octylamine, 10% trioctyl phosphate, 30% n-octanol and 10% sulfonated kerosene by volume In the kühni tower with Φ500mm and height of 1000mm, at 25°C, the extraction agent is used as the continuous phase, and the hydrolyzate is used as the dispersed phase for countercurrent extraction, and the liquid-liquid interface is controlled to be above the outlet of the lower part of the tower (that is, the upper interface of the tower). The speed of the turbine turntable is 600rpm, and the feed volume ratio of the hydrolyzate to the extractant is 1:1.5.
[0042] After the operation of the extraction tower is stable, the concentration of glycolic acid in the output of the extraction phase is about 128g / L, and the concentration of glycolic acid in the output of the raffinate phase is lower than 15g / L. Based on the transfer of glycolic acid from the hydrolyzate t...
Embodiment 3
[0046] The hydrolyzate containing glycolic acid concentration is 305.4g / L and the pH is 1.8 and the extractant that contains volume ratio 50% trin-octylamine, 10% trioctyl phosphate, 20% n-octanol and 20% sulfonated kerosene is formed in In the kühni tower with Φ1500mm and height 9000mm, at 20°C, the oil phase is used as the continuous phase, and the water phase is used as the dispersed phase for countercurrent extraction, and the liquid-liquid interface is controlled to be above the outlet of the lower part of the tower (ie, the upper interface of the tower). The speed of the turbine turntable is 200rpm, and the feed volume ratio of the hydrolyzate to the extractant is 1:1.5.
[0047] After the operation of the extraction tower is stable, the concentration of glycolic acid in the output of the extraction phase is about 132g / L, and the concentration of glycolic acid in the output of the raffinate phase is lower than about 7g / L. The rate is above 97.7%.
[0048] The extraction...
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