Membrane transport models of the extraction process based on local channel pressure and local saturation pressure are discussed.
Three ILs as extraction media are proposed for the extraction process based on phase equilibria in ternary systems {IL (1) + PEA (2) + water (3)} at temperature T = 308.15 K and ambient pressure.
Since the DNA extraction process based on solid phase extraction involves multiple sequential steps (i.e., loading, washing, and elution), an automated electromagnetically controlled valve-array was designed and used to control the flow sequence of the required reagents and washing buffer.
The obtained oil yield data has been used to validate a mathematical model of the extraction process, based in part on the information obtained from the microscopic structure of the hiprose seed particles.
An extraction, isolation, and purification process based on an accelerated solvent extraction system was designed, investigated, and optimized by means of statistical experimental design and multivariate data analysis and regression.
Extraction is a separation process based on differences in solubility.
The analysis of the phase diagram and water diagram of the quaternary system (Na+, K+//SO42−, H2PO4−-H2O) would be used to design a process based on the extraction technology process of KH2PO4.
In the present work, a new process based on the extraction with supercritical CO2 plus a co-solvent has been developed to purify reaction mixtures leading to pure prebiotic oligosaccharides.
A two step separation process based on liquid-liquid extraction was designed.
The context of this study is the modelling of reactive extrusion process based on an alginate extraction protocol.
