Compound containing DAG and the method for preparing the same
A technology containing diacylglycerol and diacylglycerol is applied in the field of compositions containing diacylglycerol, can solve the problems of high melting point, increase production cost and high cost, and achieve the advantages of inhibiting accumulation in the body, preventing arteriosclerosis and reducing production cost. Effect
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Embodiment 1
[0078] Step 1: Preparation and Fractionation of Fatty Acids
[0079] 16 kg of sodium hydroxide (purity 96%) was dissolved in 70 kg of water, and added to the reaction tank, 100 kg of soybean oil was added, heated to 85°C, stirred (rotating speed 200rpm), after reacting for 4 hours, 50 kg of hot water was added, Slowly add hydrochloric acid (6mol / L), check the pH value of the system with pH test paper, keep the system acidic until the soap is completely dissolved (pH5 or so), and continue to stir for 1 hour. Stand for stratification, take out the fatty acid in the upper layer, wash with 30% (mass ratio) hot water at 80°C for several times until neutral, spin thin film evaporation and dehydration at 80°C for 1 hour to obtain crude fatty acid. The crude fatty acid is refined by short-path distillation at temperature (160° C.) and vacuum (<10 Pa).
[0080] Melt soybean fatty acid at 60°C, add solvent (acetone) in proportion and shake well (fatty acid / acetone, 1:3), keep warm at a...
Embodiment 2
[0098] Prepare the monoacylglycerol raw material according to the method of step 1 and step 2 of Example 1, and perform the following operations on the prepared monoacylglycerol raw material A;
[0099] Step 1: Conversion of monoacylglycerols to diacylglycerols
[0100] 500 grams of monoacylglycerol A are heated to 65° C., and the reactant is passed through a column continuous reactor filled with immobilized Geotrichum candidum lipase at a flow rate of 3.0 ml / min (jacketed glass column: L=38 cm, o.d.=5 cm, i.d. = 2.6 cm, 65°C). The reaction product was distilled at 100°C and vacuum (<10Pa) to remove the glycerol in the product; and at 190°C and vacuum (<5Pa) to distill the monoacylglycerol to obtain product II.
[0101] Step 4: Product Analysis
[0102] (1) According to mass percentage, the mass percentage content of diacylglycerol in product II is 95.1%, monoacylglycerol 1.6%, and triacylglycerol 3.2%;
[0103] (2) The molar percentage of saturated fatty acid in product II...
Embodiment 3
[0112] Step 1: Preparation of canola fatty acid fractionation liquid
[0113] The method is the same as step 1 in Example 1, wherein the soybean oil is replaced with double-low rapeseed oil to obtain the double-low rapeseed fatty acid fractionation liquid.
[0114] Step 2: Preparation of monoacylglycerol
[0115] Mix 360 grams of glycerin with 2000 grams of double-low rapeseed fatty acid fractionation liquid, stir (250rpm), heat to 60°C, add 200 grams of catalyst Lipozyme RM IM, vacuum (<100Pa), and react for 40 minutes; add 1000 grams of double-low rapeseed Seed fatty acid fractionation liquid, 160 grams of Lipozyme RM IM, reacted for 20 minutes; the catalyst was separated by vacuum filtration, and the liquid product was removed at 130° C. under vacuum (<10 Pa) to remove the remaining fatty acid and glycerol from the reaction to obtain monoacylglycerol raw material B, which The fatty acid composition is shown in Table 2.
[0116] The fatty acid composition of table 2 monoac...
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