Method for separating and purifying lecithin through fixed-bed adsorption method
A fixed-bed adsorption, separation and purification technology, applied in the direction of selective adsorption, edible phospholipid composition, ion exchange, etc., can solve the problems of difficult regeneration of adsorbents, large equipment investment, and low concentration, and achieve low energy consumption and simplified solvent recovery. The effect of simple process and operation process
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Embodiment 1
[0046] Put the macroporous weakly basic adsorption resin D303 with an average particle size of about 0.4mm into an adsorption column with a size of Φ2cm×25cm, and the column bed volume (abbreviated as BV) is about 76ml. The raw material solution for loading samples was prepared by dissolving soybean powder phospholipids (40% phosphatidylcholine content) in 95% ethanol to prepare a 25 mg / mL raw material solution. Continuously feed 15BV of powdered phospholipid raw material solution at a flow rate of 2BV / hr. When the adsorption column reaches the maximum adsorption performance, the sample loading is stopped, and the effluent is collected. After HPLC analysis, the content of phosphatidylcholine can reach 89.4%, and the yield is 85.3%. Then concentrated by vacuum distillation to obtain phosphatidylcholine product.
[0047] Rinse the adsorption column with 1BV of 95% ethanol to collect the eluate. The collected eluate contains phosphatidylcholine, which can be recycled as the colu...
Embodiment 2
[0049] Put the macroporous weakly basic adsorption resin D303 with an average particle size of about 0.4mm into an adsorption column with a size of Φ2cm×25cm, and the column bed volume (abbreviated as BV) is about 76ml. The raw material solution for loading samples was prepared by dissolving soybean powder phospholipids (60% phosphatidylcholine content) in 95% ethanol to prepare a 50 mg / mL raw material solution. Continuously feed 12BV of powdered phospholipid raw material solution at a flow rate of 3BV / hr. When the adsorption column reaches the maximum adsorption performance, the sample loading is stopped, the effluent is collected, and analyzed by HPLC, the content of phosphatidylcholine in it can reach 87.6%, and the yield is 82.1%. Then concentrated by vacuum distillation to obtain phosphatidylcholine product.
[0050] Rinse the adsorption column with 1BV of 95% ethanol to collect the eluate. The collected eluate contains phosphatidylcholine, which can be recycled as the c...
Embodiment 3
[0052] Put the macroporous weakly basic adsorption resin D303 with an average particle size of about 0.4mm into an adsorption column with a size of Φ2cm×25cm, and the column bed volume (abbreviated as BV) is about 76ml. The raw material solution for loading samples was prepared by dissolving soybean powder phospholipids (60% phosphatidylcholine content) in 95% ethanol to prepare a 100 mg / mL raw material solution. Continuously feed 6BV of powdered phospholipid raw material solution at a flow rate of 0.5BV / hr. When the adsorption column reaches the maximum adsorption performance, stop loading the sample, collect the effluent, and analyze by HPLC, the content of phosphatidylcholine in it can reach 86.5%, and the yield is 80.1%. Then concentrated by vacuum distillation to obtain phosphatidylcholine product.
[0053] Rinse the adsorption column with 1BV of 95% ethanol to collect the eluate. The collected eluate contains phosphatidylcholine, which can be recycled as the column mate...
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