2015
DOI: 10.1590/1678-457x.6786
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Developing novel one-step processes for obtaining food-grade O/W emulsions from pressurized fluid extracts: processes description, state of the art and perspectives

Abstract: In this work, a novel on-line process for production of food-grade emulsions containing oily extracts, i.e. oil-in-water (O/W) emulsions, in only one step is presented. This process has been called ESFE, Emulsions from Supercritical Fluid Extraction. With this process, emulsions containing supercritical fluid extracts can be obtained directly from plant materials. The aim in the conception of this process is to propose a new rapid way to obtain emulsions from supercritical fluid extracts. Nowadays the conventi… Show more

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Cited by 4 publications
(5 citation statements)
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“…
Fig. 5 PLE process using organic solvent as extracting solvent coupled with supercritical antisolvent (SAS) precipitation process (1) heat exchanger for cooling, (2) pump, (3) heat exchanger for heating, (4) extractor, (5) T-mixer, (6) precipitation vessels, and (7) filter (Santos and Meireles 2015 )
…”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…
Fig. 5 PLE process using organic solvent as extracting solvent coupled with supercritical antisolvent (SAS) precipitation process (1) heat exchanger for cooling, (2) pump, (3) heat exchanger for heating, (4) extractor, (5) T-mixer, (6) precipitation vessels, and (7) filter (Santos and Meireles 2015 )
…”
Section: Resultsmentioning
confidence: 99%
“…(2) Those compounds are then recovered from the solvent to produce the end product. The use of supercritical fluids is advantageous as at room temperature they are in a gaseous, allowing for recovery of extract via simple evaporation (Santos and Meireles 2015 ). The differing solubilities of different solvents allow for selective extraction, as small variations to pressure and/or temperature can allow for selectivity (Perrotin-Brunel 2011 ).…”
Section: Resultsmentioning
confidence: 99%
“…Most of the time, co-extraction of unwanted compounds occurs during the extraction process, which might result in a poor-quality extract. Thanks to advanced technology, this problem can be solved by conducting SFE with a fractional separation process, allowing the improvement of selectivity in SFE [ 23 ]. This concept can be conducted in multiple steps during separation, by coupling some separators in series and adjusting processing conditions, such as pressure and temperature, according to the equilibrium solubilities of the targeted compounds [ 24 ].…”
Section: Characteristics Of Supercritical Fluids As a Novel Extracmentioning
confidence: 99%
“…Carbon dioxide is an appropriate solvent for essential oil extraction from natural products because it is readily available, non‐inflammable, has high diffusivity, low viscosity, low surface tension and low reactivity. It has a critical temperature of only 31°C and critical pressure above 71 bar 19 …”
Section: Introductionmentioning
confidence: 99%
“…It has a critical temperature of only 31°C and critical pressure above 71 bar. 19 There are several reasons for the growing increase in research involving the extraction of terpenes and oxygenated compounds from essential oils with supercritical fluids (see Figure 1), especially the production of products with high added value in the market, such as limonene and linalool, which widely used by the medical, agrochemical, food and cosmetic industries. [20][21][22] Raeissi et al 22 investigated the effect of ethane in comparison with CO 2 as a supercritical extraction solvent in the citrus oil separation process.…”
mentioning
confidence: 99%