2016
DOI: 10.1016/j.supflu.2015.09.021
|View full text |Cite
|
Sign up to set email alerts
|

Fractionation technologies for liquid mixtures using dense carbon dioxide

Help me understand this report

Search citation statements

Order By: Relevance

Paper Sections

Select...
3
1
1

Citation Types

1
14
0

Year Published

2017
2017
2023
2023

Publication Types

Select...
4
2
2

Relationship

1
7

Authors

Journals

citations
Cited by 37 publications
(15 citation statements)
references
References 266 publications
1
14
0
Order By: Relevance
“…The temperature value of the ROLSI™ sampler (2) and its transfer line measurements. After each point was measured, the liquid phase sampling line was cleaned with fresh CO 2 , using two-way valves (15), and a vacuum pump (16). The vapour phase line was continuously cleaned by the carrier gas flow from its storage tank (11).…”
Section: Experimental Apparatus and Proceduresmentioning
confidence: 99%
See 1 more Smart Citation
“…The temperature value of the ROLSI™ sampler (2) and its transfer line measurements. After each point was measured, the liquid phase sampling line was cleaned with fresh CO 2 , using two-way valves (15), and a vacuum pump (16). The vapour phase line was continuously cleaned by the carrier gas flow from its storage tank (11).…”
Section: Experimental Apparatus and Proceduresmentioning
confidence: 99%
“…Alternative technologies for the recovery, concentration and fractionation of fruit aromas are membrane processes, such as pervaporation, and less common techniques such as Current Supercritical Fluid Fractionation (CC-SFF) in packed columns [14][15][16]. The applications of CC-SFF in packed columns of aqueous solutions are mainly related to alcoholic beverages.…”
Section: Introductionmentioning
confidence: 99%
“…At 30 MPa, the recovery ratio of AA in the CO 2 -free extract increased to 70 % and mass fraction of AA in the CO 2 -free extract from 41 % at 10 MPa to around 50 %, this latter exhibiting a plateau around 15 MPa. As already mentioned, note that higher pressures are usually not considered, according to literature reviews [17,38], mostly because, in the case of aqueous systems, density difference becomes too low for easy decantation of phases. At 30 MPa, density difference is around 110 kg/m 3 .…”
Section: Influence Of the Pressurementioning
confidence: 99%
“…So, usual drawbacks of liquid organic solvents could be alleviated. Such a process is usually operated using countercurrent packed columns in a continuous mode [17]. Supercritical extraction applied to liquids has been reported for separation of aqueous solutions (dealcoholisation of beverages [18,19] and recovery of aromas from fruit juices [20]) or for essential oil deterpenation [21].…”
Section: Introductionmentioning
confidence: 99%
“…Fractionation of liquid mixtures using supercritical solvents has been proposed and studied as a promising tool for new separation challenges, as well as an alternative to current separation processes [1,2]. In this way, the use of supercritical carbon dioxide (scCO 2 ) as a solvent proposes a more environmentally friendly technology when compared to conventional organic solvents.…”
Section: Introductionmentioning
confidence: 99%