Pupal fat alpha-linolenic acid ethyl ester crude drug dewaxing method and pupal fat alpha-linolenic acid ethyl ester crude drug production method
A technology of ethyl linolenate and its production method, which is applied to the treatment of pupa oil α-ethyl linolenic acid raw material, the production of pupa oil α-ethyl linolenic acid raw material, and the production of pupa oil α-linolenic acid ethyl ester raw material In the field of dewaxing, it can solve the problems of time-consuming, unsatisfactory effect and complexity, and achieve the effect of reducing production cost, good effect and simple method
Patent Information
- Authority / Receiving Office
- CN · China
- Current Assignee / Owner
- Publication Date
- 2017-06-13
Abstract
Description
technical field
[0001] The invention belongs to the field of pharmacy, and relates to a method for processing pupa oil α-ethyl linolenate bulk drug, in particular to a dewaxing method for producing pupa oil α-ethyl linolenate bulk drug and pupa oil α-ethyl linolenate The method of production of the raw material drug. Background technique
[0002] α-Linolenic acid (ALA, octadeca 9,12,15-trienoic acid) is a polyunsaturated fatty acid with three double bonds (C 18 h 30 o 2 ), which is an omega-3 essential fatty acid. α-linolenic acid is the basic substance that constitutes cell membrane and biological enzymes, and plays a decisive role in human health. α-linolenic acid can be converted into DHA, DPA, EPA, etc. in the body. Since there are three conjugated double bonds in the α-linolenic acid molecule, it has very strong reducibility. It can be oxidized by high temperature, oxygen in the air, ultraviolet rays and some heavy metal ions, so it is often converted into ethyl es...
Examples
Embodiment 1
[0029] Embodiment 1 prepares dewaxed pupal oil
[0030] 10kg of waxy pupae oil containing about 25% is added with ethanol aqueous solution. The aqueous ethanol solution is prepared by dissolving 0.9kg of NaOH in 6kg of aqueous ethanol (weight ratio ethanol:water=1:1). After stirring at a temperature of 60° C. for 30 minutes, the layers were statically separated, the sediment and water in the lower layer were discarded, and the oily matter in the upper layer was collected to obtain about 8 kg of dewaxed pupal oil. The effect of residual wax on inclusion content decreased from 25% to about 2%.
Embodiment 2
[0031] Embodiment 2 prepares dewaxed pupal oil
[0032] 10kg of waxy pupae oil containing about 25% is added with ethanol aqueous solution. The ethanol aqueous solution is prepared by dissolving 1.4kg of NaOH in 6kg of ethanol aqueous solution (weight ratio ethanol:water=1:1). After stirring at a temperature of 75° C. for 20 minutes, the layers were statically separated, the sediment and water in the lower layer were discarded, and the oily matter in the upper layer was collected to obtain about 7.5 kg of dewaxed pupal oil. The effect of residual wax on inclusion content decreased from 25% to about 1.4%.
Embodiment 3
[0033] Embodiment 3 prepares dewaxed pupal oil
[0034] 10kg of waxy pupae oil containing about 18% is added with ethanol aqueous solution. The ethanol aqueous solution is prepared by dissolving 1kg of NaOH in 6kg of ethanol aqueous solution (weight ratio ethanol:water=1:1). After stirring at a temperature of 70° C. for 25 minutes, the layers were statically separated, the sediment and water in the lower layer were discarded, and the upper layer oil was collected to obtain about 8 kg of dewaxed pupal oil. The effect of residual wax on inclusion content decreased from 18% to about 0.8%.