“…In the last decades, research for new solvents has revived the interest for the use of liquefied gases as extraction solvents. Many studies have been performed on natural product extraction using supercritical CO 2 , but the high working pressure (7.5e45 MPa) has limited the industrial applications (Baysal, Ersus, & Starmans, 2000;Ben Rahal, Barba, Barth, & Chevalot, 2015;Coelho et al, 2012;Couto et al, 2010;Hubert & Vitzthum, 1978;Koubaa et al, 2015;Koubaa et al, 2016;Xu et al, 2011). More recently, some studies have been focused on extraction processes involving liquefied gases at lower pressure (200e1000 kPa), such as n-propane (da Sekhon, Maness, & Jones, 2015;Zanqui et al, 2015), n-butane (Novello et al, 2015;Yang, Teo, & Xu, 2004), dimethyl ether (Kanda & Li, 2011;Kanda & Makino, 2009;Oshita et al, 2015), tetrafluoropropene (Suberu, Yamin, Cornell, Sam, & Lapkin, 2016), tetrafluoroethane (Lapkin, Plucinski, & Cutler, 2006;Mustapa, Manan, Mohd Azizi, Nik Norulaini, & Omar, 2009), eventually with co-solvents (Jesus et al, 2013;Pessoa et al, 2015).…”