Method for extracting protodioscin from fenugreek seeds
A technology of protodioscin and fenugreek, which is applied in the field of extracting protodioscin, can solve the problems of low protodioscin content, affecting the efficacy of use, and high production costs, and achieves the effects of low cost, improved purity, and low requirements for production equipment
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Examples
Embodiment 1
[0021] 100 kg of fenugreek seeds were pressed with a screw oil press at a pressing temperature of 10° C. and a pressing pressure of 40 MPa to remove lipid components to obtain fenugreek seed cakes. The fenugreek seed cake was leached with 6 times of purified water, the leaching temperature was 50°C, and the leaching time was 1 hour, the extract was filtered to obtain the filtrate, and the purified water was leached again in the above-mentioned manner, and the filtrates were combined. Purify the combined filtrate with a CAD-40 macroporous adsorption resin column at a flow rate of 1BV / h, wherein the amount of resin is 3 times the amount of crude drug, and the diameter-height ratio of the resin column is 1:1, followed by 1BV of purified water at 4BV / h The resin column was cleaned at a flow rate of h, and then eluted with 1BV of 70% ethanol at a flow rate of 4BV / h, the eluate was collected, and the eluate was concentrated under reduced pressure to no alcohol. 0.07MPa, recover etha...
Embodiment 2
[0023] 100 kg of fenugreek seeds were pressed with a screw oil press at a pressing temperature of 25° C. and a pressing pressure of 25 MPa to remove lipid components to obtain fenugreek seed cakes. The fenugreek seed cake was leached with 7 times of purified water, the leaching temperature was 35°C, and the leaching time was 2 hours, the extract was filtered to obtain the filtrate, and the purified water was leached again in the above-mentioned manner, and the filtrates were combined. Purify the combined filtrate with a CAD-40 macroporous adsorption resin column at a flow rate of 0.5BV / h, wherein the amount of resin is 6 times the amount of crude drug, and the diameter-to-height ratio of the resin column is 1:5, followed by 2BV of purified water with 2BV Wash the resin column at a flow rate of 1.5BV / h, then elute with 1.5BV of 70% ethanol at a flow rate of 2BV / h, collect the eluate, and concentrate the eluent under reduced pressure to no alcohol. -0.08MPa, recover ethanol, spr...
Embodiment 3
[0025] 100 kg of fenugreek seeds were pressed with a screw oil press at a pressing temperature of 40° C. and a pressing pressure of 10 MPa to remove lipid components to obtain fenugreek seed cakes. The fenugreek seed cake was leached with 8 times of purified water, the leaching temperature was 20°C, and the leaching time was 2 hours, the extract was filtered to obtain the filtrate, and the purified water was leached again in the above-mentioned manner, and the filtrates were combined. Purify the combined filtrate with a CAD-40 macroporous adsorption resin column at a flow rate of 2BV / h, wherein the amount of resin is 4 times the amount of crude drug, and the ratio of diameter to height of the resin column is 1:3, followed by 3BV of purified water at 3BV / h The resin column is washed at a flow rate of h, and then eluted with 2BV of 70% ethanol at a flow rate of 3BV / h, the eluate is collected, and the eluate is concentrated under reduced pressure to no alcohol. 0.09MPa, recover e...
PUM
Abstract
Description
Claims
Application Information
- R&D Engineer
- R&D Manager
- IP Professional
- Industry Leading Data Capabilities
- Powerful AI technology
- Patent DNA Extraction
Browse by: Latest US Patents, China's latest patents, Technical Efficacy Thesaurus, Application Domain, Technology Topic, Popular Technical Reports.
© 2024 PatSnap. All rights reserved.Legal|Privacy policy|Modern Slavery Act Transparency Statement|Sitemap|About US| Contact US: help@patsnap.com