Method for preparing anhydrous citric acid crystal
A technology of citric acid and crystals, which is applied in the field of preparing anhydrous citric acid crystals, can solve the problems of low impurity content, low product quality of anhydrous citric acid crystals, low moisture content, etc., achieve low impurity content, improve the first pass rate, Uniform particle size effect
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[0011] The method for preparing anhydrous citric acid crystals provided by the present invention comprises carrying out concentrated crystallization of citric acid feed liquid, wherein, when the crystal content in the feed liquid reaches 20-40% by weight (preferably 25-35% by weight), the concentrated The crystal slurry liquid obtained by crystallization is classified, and the classification conditions are controlled so that crystals with a particle size of less than 600 μm are separated from the crystal slurry liquid, and part or all of the crystal slurry liquid obtained by classification containing crystals with a particle size of less than 600 μm is returned to the citric acid feed Liquids are mixed together for concentrated crystallization.
[0012] According to the present invention, the conditions of the concentrated crystallization can be the conditions routinely used in the art. Preferably, the conditions of the concentrated crystallization make the particle size of the...
Embodiment 1
[0022] The continuous injection of the citric acid feed solution with a citric acid content of 60% by weight into an effective volume of 20m 3 In the crystallizer, carry out concentrated crystallization at 60 ℃, when the crystal content in the feed liquid reaches 35% by weight, control the feed rate of the citric acid feed liquid and the discharge speed of the crystal slurry liquid that the concentrated crystallization obtains to make the feed liquid The crystal content of the crystal is kept constant, and the crystal slurry obtained by concentrated crystallization (the particle size of the crystal contained is not more than 850 μm) is passed into the hydrocyclone for classification, and the feeding pressure is controlled to be 0.4MPa, and the feeding speed is 3m 3 / h, so that the crystals with a particle size of less than 600 μm are separated from the crystal slurry, and the obtained crystal slurry containing crystals with a particle size of less than 600 μm is returned to the...
Embodiment 2
[0025] The continuous injection of the citric acid feed solution with a citric acid content of 55% by weight into an effective volume of 20m 3 In the crystallizer, carry out concentrated crystallization at 60 ℃, when the crystal content in the feed liquid reaches 30% by weight, control the feed rate of the citric acid feed liquid and the discharge speed of the crystal slurry liquid that the concentrated crystallization obtains to make the feed liquid The crystal content of the crystal is kept constant, and the crystal slurry obtained by concentrated crystallization (the particle size of the crystal contained is not more than 850 μm) is passed into the hydrocyclone for classification, and the feeding pressure is controlled to be 0.2MPa, and the feeding speed is 10m 3 / h, so that the crystals with a particle size of less than 600 μm are separated from the crystal slurry, and the obtained crystal slurry containing crystals with a particle size of less than 600 μm is returned to th...
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