Process for the production of diacylglycerol
a technology of diacylglyceride and process, which is applied in the field of process for the production of diacylglyceride, can solve the problems of insufficient purity of resulting diglyceride and industrial scale-up technique, reaction rate, and inability to investigate production conditions at an industrial level, and achieve the effect of short period of tim
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example 1
[0036] In a 5 L flask, 1000 g of refined palm olein was mixed with 1000 g of distilled water and 100 g of “Lipozyme RM IM”, an immobilised 1,3-position selective lipase obtained from Rhizomucor miehei lipase. The mixture was reacted for 10 hours under stirring at 60° C. Thereafter, the lipase preparation was removed from the reaction product. Samples of the product were removed, and the amount of free fatty acids and partial acylglycerols was determined by gas chromatography. The results are shown in Table 1.
example 2
[0037] In a 5 L flask, 1000 g of refined soybean oil was mixed with 1000 g of distilled water and 100 g of “Lipozyme RM IM”, an immobilised 1,3-position selective lipase obtained from Rhizomucor miehei lipase. The mixture was reacted for 10 hours under stirring at 60° C. Thereafter, the lipase preparation was removed from the reaction product. Samples of the product were removed, and the amount of free fatty acids and partial acylglycerols was determined by gas chromatography. The results are shown in Table 1.
TABLE 1Reactants beforeReactionhydrolysisHydrolysis productcomponentsExample 1Example 2Example 1Example 2Free Fatty acids (%)0.030.0425.2122.74Monoacylglycerols (%)0.931.1721.9823.22Diacylglycerols (%)2.643.3641.5643.68Triacylglycerols (%)96.4095.4311.2510.36
example 3
[0038] The hydrolysis products from Examples 1 and 2 were centrifuged at 5000 rpm for 10 minutes to separate the oil phase from the aqueous phase. The oil phase was subjected to molecular distillation at a temperature of 160° C. and at a pressure of 0.001 mbar to obtain the free fatty acids and monoacylglycerols as distillate 1 and diacylglycerol and triacylglycerol as residue 1. A further molecular distillation step at 210° C. and 0.001 mbar was performed to obtain the diacylglycerol as distillate 2 and triacylglycerol as residue 2. The results are shown in Table 2.
TABLE 2Diacylglycerol purity (%)Hydrolysis productBefore purificationAfter purificationExample 141.5688.70Example 243.6890.83
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