Spray drying |
Rapid, cost-effective, easy to scale up. C-PC retention, and relatively good storage stability. |
Production of nonuniform particles with a wide size distribution. C-PC degradation and loss of product. |
[19,20,21,22,23,24] |
Electrospinning |
Suitable for heat-sensitive compounds. |
Slow, produces low encapsulation yield, and limited scope of application. |
[25,26,27,28,29] |
Electrospraying |
Produces particles with a high surface-to-volume ratio, controlled release, improved functionality, and physical properties. |
Time-consuming and hardly repeatable, especially at the industrial level. |
[30,31,32] |
Liposome delivery |
Increased adsorption bioavailability, and nontoxic. |
Low encapsulation efficiency. Lipid oxidation, poor physicochemical stability, and wide particle size distribution. Postprocess step is required. |
[33,34,35,36,37] |
Sharp-hole coagulation bath |
High loading capacity, low temperature operating requirements, reduced evaporation losses of volatile compounds, and thermal degradation. Tailored release of active compounds. |
Special instruments are required and are not suitable for large-scale industrial production. |
[38,39,40,41,42] |
Ion Gelation |
Low cost and does not require advanced equipment, high temperatures, and organic solvents. |
Produced particles are very sensitive to pH and ionic strength. Agglomeration of particles and particle size control. |
[43,44,45,46,47,48,49] |