Enzymatic method for preparing glyceryl butyrate
An enzymatic method for preparing glyceryl butyrate, comprising: (1) carrying out an esterification reaction between n-butyric acid and glycerol using lipase as a catalyst, ethyl acetate and/or ethyl formate as an additive; (2) separating the reaction product, recovering the additive by distillation under reduced pressure to obtain glyceryl butyrate. The invention uses lipase as a catalyst to catalyze the esterification reaction of n-butyric acid and glycerin at normal temperature and normal pressure, reduces the energy consumption of the reaction. Also, the reaction condition is mild, no side reaction happens, and no water-carrying agent is used. In addition, the additive increases the catalytic efficiency of the lipase and the conversion rate of butyric acid.
1. An enzymatic method for preparing glyceryl butyrate, comprising:
(1) carrying out an esterification reaction between n-butyric acid and glycerol using lipase as a catalyst and ethyl acetate and/or ethyl formate as an additive;
(2) separating the reaction product and recovering the additive by distillation under reduced pressure to obtain glyceryl butyrate.
2. The method according to claim 1 , wherein the additive is added in an amount of 10%-60% by mass of the n-butyric acid.
3. The method according to claim 1 , wherein the molar ratio of the n-butyric acid to the glycerol in step (1) is 3:1-1:3.
4. The method according to any of claim 1 , wherein the lipase is added in an amount of 0.5%-10% by mass of the n-butyric acid.
5. The method according to claim 4 , wherein the lipase in step (1) is selected from at least one of lipase of Rhizopus, Aspergillus, Mucor , bacteria and yeast, and pancreatic lipase.
6. The method according to claim 4 , wherein the esterification reaction is carried out at 20° C.-50° C. with stirring at a speed of 200 rpm or more.
7. The method according to claim 4 , wherein the separating in step (2) is natural stratification, then the organic phase is recovered, and ethyl acetate is distilled under reduced pressure to obtain glyceryl butyrate.
8. The method according to claim 2 , wherein the lipase is added in an amount of 0.5%-10% by mass of the n-butyric acid.
9. The method according to claim 8 , wherein the lipase in step (1) is selected from at least one of lipase of Rhizopus, Aspergillus, Mucor , bacteria and yeast, and pancreatic lipase.
10. The method according to claim 8 , wherein the esterification reaction is carried out at 20° C.-50° C. with stiffing at a speed of 200 rpm or more.
11. The method according to claim 8 , wherein the separating in step (2) is natural stratification, then the organic phase is recovered, and ethyl acetate is distilled under reduced pressure to obtain glyceryl butyrate.
12. The method according to claim 3 , wherein the lipase is added in an amount of 0.5%-10% by mass of the n-butyric acid.
13. The method according to claim 12 , wherein the lipase in step (1) is selected from at least one of lipase of Rhizopus, Aspergillus, Mucor , bacteria and yeast, and pancreatic lipase.
14. The method according to claim 12 , wherein the esterification reaction is carried out at 20° C.-50° C. with stiffing at a speed of 200 rpm or more.
15. The method according to claim 12 , wherein the separating in step (2) is natural stratification, then the organic phase is recovered, and ethyl acetate is distilled under reduced pressure to obtain glyceryl butyrate.