Jump to main content
US EPA
United States Environmental Protection Agency
Search
Search
Main menu
Environmental Topics
Laws & Regulations
About EPA
Health & Environmental Research Online (HERO)
Contact Us
Print
Feedback
Export to File
Search:
This record has one attached file:
Add More Files
Attach File(s):
Display Name for File*:
Save
Citation
Tags
HERO ID
3115142
Reference Type
Journal Article
Title
Extraction of lignans from the seed of Schisandra chinensis by supercritical fluid extraction and subsequent separation by supercritical fluid simulated moving bed
Author(s)
Lin, CH; Lin, HWei; Wu, JauY; Houng, JerY; Wan, HouP; Yang, TzuY; Liang, MT
Year
2015
Is Peer Reviewed?
Yes
Journal
Journal of Supercritical Fluids
ISSN:
0896-8446
Volume
98
Page Numbers
17-24
DOI
10.1016/j.supflu.2014.12.025
Web of Science Id
WOS:000350519000003
Abstract
In this study, the lignans in the seed of Schisandra chinensis were extracted by supercritical fluid extraction (SFE), and the lignans in the obtained seed oil were subsequently separated by simulated moving bed (SMB) chromatography with supercritical fluid as the desorbent (SF-SMB). Four lignans: Schisandrol A, Schisandrol B, Schisandrin A and Schisandrin B, in the seed oil are monitored to study the extraction and separation. Effects of the extraction temperature (40-60 degrees C), pressure (20-35 MPa) and the content of ethanol as a cosolvent (0-10.8 wt%) on the yield of seed oil were investigated. Sovova's equation was applied to fit the experimental results to investigate the extraction kinetics. A three-section SMB with six packed columns configured as 2/2/2 was employed to separate the lignans in the seed oil. Preparative silica gel was selected as the adsorbent, and 2-propanol was used as the cosolvent for supercritical carbon dioxide at 40 degrees C and 13.6 MPa. The separation of lignans by the SF-SMB was conducted by creating a slight concentration gradient of 2-propanol (14.8-15.5%) along the six packed columns. The experimental results showed that Schisandrol A with 42.9 wt% and Schisandrin B with 4.34 wt% can be individually separated from the seed oil, and the separation of Schisandrol A and B and Schisandrin A and B was successfully achieved. This study demonstrates that the extraction and separation of bioactive ingredients from herbs can be finished by solely using the supercritical fluid related technologies. (C) 2015 Elsevier B.V. All rights reserved.
Keywords
Schisandra lignans; Supercritical fluid extraction; Simulated moving bed; Schisandrol; Schisandrin
Home
Learn about HERO
Using HERO
Search HERO
Projects in HERO
Risk Assessment
Transparency & Integrity