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The main purpose is to investigate the efficiency and applicability of micro-mixers in supercritical fluid extraction processes.
For the proper design of supercritical fluid extraction processes, it is essential to have a sound knowledge of the mass transfer mechanism of the extraction process and the appropriate mathematical representation.
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With this goal, in the present work a supercritical fluid extraction process (SFE) has been studied to extract carotenoids and phenolic compounds from Cladophora glomerata, Ulva flexuosa and Chara fragilis.
The first item concerns CO2 recovery by membranes during a supercritical fluid extraction process.
To design and operate the supercritical fluid extraction process using scCO2, high pressure phase behaviour data are required.
The single pArameter is calculated from vaperturbedure datum.
In this study is presented a general methodology to predict the performance of a continuous near-critical fluid extraction process to remove compounds from aqueous solutions using a hollow fiber membrane contactor.
The purpose of this study was to produce an oil-in-water (O/W) emulsion of δ-tocotrienol-rich oil obtained from annatto seeds by a supercritical fluid extraction process.
The average absolute deviation (AAD) of 5.42% compared to those of density-based and equation of state models, representing the reasonable accuracy of the developed model for estimating the solubility of solutes in supercritical fluid extraction process.
In reviewing a report of gross alpha levels in fluids from Marcellus Shale, we observed that reported Ra radioactivity concentrations were similar to maximum gross alpha levels (Barbot et al. 2013), indicating that Ra had been selectively extracted into the liquid wastes, while alpha-emitting daughters remained insoluble under the geochemical conditions of the fluid extraction process.
A profitability analysis of a large scale supercritical fluid extraction (SFE) process to obtain natural extracts from rocket salad is presented in this work.
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