Extraction Technologies For Medicinal And Aromatic Plants - Unido
Extraction Technologies For Medicinal And Aromatic Plants - Unido
Extraction Technologies For Medicinal And Aromatic Plants - Unido
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EXTRACTION TECHNOLOGIES FOR MEDICINAL AND AROMATIC PLANTS<br />
that ultrasound waves can produce free radicals and that many active molecules<br />
are susceptible to such highly reactive species, this approach does<br />
not seem feasible.<br />
8.3 Solvent <strong>Extraction</strong> of MAPs<br />
This process entails the extraction of solid MAPs by liquid solvents.<br />
This is a typical solid-liquid extraction process. Two factors that affect<br />
the extent and rate of extraction are the thermodynamics and kinetics (rate<br />
of mass transfer) of the process.<br />
8.3.1 Thermodynamics of Solvent <strong>Extraction</strong> and Choice<br />
of Solvent<br />
Relative sorption of solutes in the solvent depends on the interactions<br />
between the solutes and the solvent. Solubility or miscibility of a<br />
component with the solvent depends on their relative solubility parameters.<br />
<strong>For</strong> mutual solubility of two components, their free energy of mixing, ΔGm<br />
should be negative. ΔGm is defi ned as<br />
ΔGm = ΔHm – T ΔSm (3.1)<br />
Enthalpy of mixing, ΔHm can be correlated to cohesive energy<br />
density, i.e. solubility parameter (δ) as:<br />
ΔHm = n1 n2 V1 (δ1 – δ2) 2 (3.2)<br />
In equation (3.2), the solubility parameter is that due to only<br />
dispersive forces between structural units of the concerned solute and solvent,<br />
since the original regular solution theory of Scatchard and Hildebrand<br />
was restricted to non-polar, non-hydrogen bonding solute-solvent systems.<br />
However, for many liquids and solutes, contributions from polar and hydrogen<br />
bonding forces need to be considered. Accordingly, equation (3.2) becomes:<br />
ΔHm = n1 n2 V1 [(Δδd) 2 + (Δδp) 2 + (Δδh) 2 ] (3.3)<br />
From equations (3.2) and (3.3), it is clear that to make ΔGm<br />
negative, the difference between δi (solvent) and δi (solute), i.e. (Δδ) for<br />
all the three forces of interactions, should be as small as possible. It implies<br />
that the solvent and the desired solute to be extracted should have<br />
comparable polarity and hydrogen bonding capabilities to achieve similar<br />
solubility parameter values. Grulke has given an exhaustive tabulation of<br />
solubility parameters for the most common chemical compounds. The in-<br />
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