Technique for preparing phosphatidyl serine rich in highly-unsaturated fatty acid
An unsaturated fatty acid, phosphatidylserine technology, applied in the direction of fermentation, etc., can solve the problems of complicated product separation steps, low product yield, long reaction time, etc., and achieves a product that is conducive to reuse, high product yield, and fast reaction speed. Effect
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Embodiment 1
[0007] Heat the reactor to 40°C, weigh 75 mg of squid lecithin, and place it in the reactor; weigh 0.1 g of anhydrous calcium chloride (for maintaining the stability of the enzyme), and 0.85 g of solid L-serine, dissolve in 2.4 Add phosphate buffer solution of mlpH5.5 into the reaction kettle; accurately weigh 9.6U of phospholipase D and add it into the reaction kettle; ) storage tank, the R134a gas is liquefied by the condenser and then pressurized by the plunger pump into the reaction kettle. After the reactor pressure reached 6MPa, R134a reached the subcritical state. Stop the plunger pump, close the storage tank, and stir the reaction. After reacting for 3.5 hours, the shut-off valve was opened to reduce the pressure, and the reaction mixture was allowed to enter a separation tank with a temperature of 40° C. connected to the reaction tank. Turn on the compressor to recover R134a from the separation tank; after the recovery is complete, collect the reaction mixture from ...
Embodiment 2
[0009] Heat the reaction kettle and the separation kettle to 40°C, weigh 300mg of squid lecithin, and place it in the reaction kettle; weigh 0.4g of anhydrous calcium chloride, 3.5g of solid L-serine, and dissolve them in 10ml of phosphate buffered saline with a pH of 5.5 Add liquid into the reaction kettle; accurately weigh phospholipase D38U, and add it into the reaction kettle; after the system is sealed, open the R134a storage tank, let the R134a gas liquefy through the condenser, and then pressurized by the plunger pump into the reaction kettle. After the reactor pressure reached 6MPa, the plunger pump was stopped, the storage tank was closed, and the reaction was stirred. After reacting for 3.5 hours, the shut-off valve was opened to reduce the pressure, and the reaction mixture was allowed to enter a separation tank with a temperature of 40° C. connected to the reaction tank. Turn on the compressor to recover R134a from the separation tank; after the recovery is complet...
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