New developments in the modelling of carotenoids extraction from microalgae with supercritical CO2.
Identifikátory výsledku
Kód výsledku v IS VaVaI
<a href="https://www.isvavai.cz/riv?ss=detail&h=RIV%2F67985858%3A_____%2F19%3A00512086" target="_blank" >RIV/67985858:_____/19:00512086 - isvavai.cz</a>
Výsledek na webu
<a href="http://hdl.handle.net/11104/0302289" target="_blank" >http://hdl.handle.net/11104/0302289</a>
DOI - Digital Object Identifier
<a href="http://dx.doi.org/10.1016/j.supflu.2019.03.002" target="_blank" >10.1016/j.supflu.2019.03.002</a>
Alternativní jazyky
Jazyk výsledku
angličtina
Název v původním jazyce
New developments in the modelling of carotenoids extraction from microalgae with supercritical CO2.
Popis výsledku v původním jazyce
Literature data on the extraction of carotenoids from microalgae with supercritical carbon dioxide (scCO2) were used to describe the process as an extraction of a solution of carotenoids in oil. A mathematical model for oil extraction from microalgae, including also the adsorption on microalgal surfaces, was extended for this purpose. The working hypothesis was that the extraction process is primarily controlled by phase equilibrium where the solubility of carotenoids in scCO2, as minor components, depends on the solubility of the major component – microalgal triglycerides. The above assumption was supported and confirmed by the results of the modelling of the vapor-liquid phase equilibria of the system carotenoid + oil + scCO2, which was performed applying the predictive Soave–Redlich–Kwong cubic equation of state. The well-known increase of extraction rate and yield with extraction pressure and temperature was shown to be a result of both increasing carotenoid solubility in scCO2 and decreasing adsorption capacity of microalga.
Název v anglickém jazyce
New developments in the modelling of carotenoids extraction from microalgae with supercritical CO2.
Popis výsledku anglicky
Literature data on the extraction of carotenoids from microalgae with supercritical carbon dioxide (scCO2) were used to describe the process as an extraction of a solution of carotenoids in oil. A mathematical model for oil extraction from microalgae, including also the adsorption on microalgal surfaces, was extended for this purpose. The working hypothesis was that the extraction process is primarily controlled by phase equilibrium where the solubility of carotenoids in scCO2, as minor components, depends on the solubility of the major component – microalgal triglycerides. The above assumption was supported and confirmed by the results of the modelling of the vapor-liquid phase equilibria of the system carotenoid + oil + scCO2, which was performed applying the predictive Soave–Redlich–Kwong cubic equation of state. The well-known increase of extraction rate and yield with extraction pressure and temperature was shown to be a result of both increasing carotenoid solubility in scCO2 and decreasing adsorption capacity of microalga.
Klasifikace
Druh
J<sub>imp</sub> - Článek v periodiku v databázi Web of Science
CEP obor
—
OECD FORD obor
20402 - Chemical process engineering
Návaznosti výsledku
Projekt
—
Návaznosti
I - Institucionalni podpora na dlouhodoby koncepcni rozvoj vyzkumne organizace
Ostatní
Rok uplatnění
2019
Kód důvěrnosti údajů
S - Úplné a pravdivé údaje o projektu nepodléhají ochraně podle zvláštních právních předpisů
Údaje specifické pro druh výsledku
Název periodika
Journal of Supercritical Fluids
ISSN
0896-8446
e-ISSN
—
Svazek periodika
148
Číslo periodika v rámci svazku
JUN 15
Stát vydavatele periodika
NL - Nizozemsko
Počet stran výsledku
11
Strana od-do
93-103
Kód UT WoS článku
000465053500011
EID výsledku v databázi Scopus
2-s2.0-85062811444