Since SCCO
2 has poor solubility for the majority of pharmaceuticals in the RESS process, another approach using SCCO
2 as an antisolvent was devised. The basic principle is that when SCCO
2 is dissolved in an organic solvent solution containing a solute, the solution expands in volume, gets less dense, and the solute's solubility in the solvent decreases, eventually precipitating to form solid particles [
54]. The gaseous antisolvent (GAS) process was first proposed in 1992, employing SCF as an antisolvent [
55]. The mixing unit in the GAS process also functions as a precipitation unit, where the particles are gathered. GAS is an intermittent process in which SCCO
2 needs to be continuously introduced after particle precipitation has occurred to avoid a loss of pressure that would cause the solution to regain solubility. In addition, the GAS process is prone to organic residues. The supercritical antisolvent (SAS) [
54] method and solution enhanced dispersion by supercritical fluids (SEDS) [
56] are two antisolvent procedures with semi-continuous operation that have been designed to address drawbacks in the GAS process. The SAS process only requires the selection of a suitable solvent, which greatly compensates for the shortcomings of the RESS method and is well developed and widely used. For example, SAS-treated gefitinib has a higher solubility and faster dissolution rate compared with the original drug, which is conducive to improving its bioavailability, reducing dose requirements, and lowering the incidence of adverse reactions [
57]. Biodegradable nanoparticles were produced by the SAS method for controlled delivery of paclitaxel. The particle size was controlled by enhancing the mixing between solvent and SCCO
2 through ultrasonic treatment, and the resulting composite particles had homogeneous sizes with high encapsulation efficiency and a controlled release of paclitaxel for more than 30 days [
58]. The SEDS technology is a variant of the SAS method, which involves nozzle spraying followed by the coaxial nozzle mixing of a solute/drug solution with SCCO
2. For improved premixing conditions, the nozzle typically contains two channels as well as a mixing length at the end of the nozzle. The SCCO
2 is typically introduced along the outer channel, while the solute/drug solution is usually introduced along the inner channel, which decreases drying time and the chance of particle agglomeration by improving mass transfer efficiency and solvent elimination [
59-
62]. Therefore, the SEDS technique has been widely used for particle formation. For instance, water-soluble and nanoscale (100–200 nm) PVP/astaxanthin inclusion complexes were successfully made utilizing the SEDS technology [
62]. It was discovered that the particle size in the coprecipitates was influenced by the operating pressure, temperature, and PVP/astaxanthin ratio. By maximizing these parameters, high astaxanthin content and fine, water-soluble particles can be produced. Moreover, the biological functions of drugs can be improved after micronization by this technology. In one study, the SEDS technology was applied to micronize curcumin, which not only improved its water solubility, but also its bacteriostatic activity against
Pseudomonas aeruginosa [
63]. Additionally, using the right organic solvents or adding additives to increase the inter-solubility of water and SCCO
2 can micronize various protein and peptide hydrophilic medications for both SAS technology and SEDS technique. The application will be covered in more detail in the following section.