Ethanol was used as the solvent and compressed CO2 as the antisolvent. The effects of process operating conditions (pressure: 5–24 MPa, temperature: 308–328 K and CO2 flow rate: 0.5–1.5 g/min)
Ethanol was used as the solvent and compressed CO2 as the antisolvent. The effects of process operating conditions (pressure: 5–24 MPa, temperature: 308–328 K and CO2 flow rate: 0.5–1.5 g/min)