## Abstract A dynamic model of a supercritical fluid extraction (SFE) process was developed and applied to the fractionation of the binary mixture squalene/methyl oleate by supercritical carbon dioxide. The model combines a mathematical model for each main piece of equipment of the SFE process, nam
Optimization of supercritical fluid extraction of volatile constituents from a model plant matrix
β Scribed by Roger M. Smith; Mark D. Burford
- Publisher
- Elsevier Science
- Year
- 1992
- Tongue
- English
- Weight
- 677 KB
- Volume
- 600
- Category
- Article
- ISSN
- 1873-3778
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