5.4. Extraction with dense or liquefied gases
5.4.1. Extraction with liquid CO2
There are several commercial plants in operation for extracting flavouring materials from herbs using liquid CO2. Moyler (1993) describes a plant at Bletchtley in England, in which extraction is coming out at about 8ºC and 60 bar (point 3 on the figure below). Product recovery involves boiling off this liquid carbon dioxide at 13 ºC, 48 bar.
In the subcritical state, liquid CO2, behaves as a non-polar solvent, with temperatures between -55ºC and 31ºC, and pressure between 5 and 74 bar.
Under normal working conditions (temperature 0º-10ºC, pressure 50-80 bar) it is a selective solvent, dissolving mainly non polar and slightly polar components with molecular weights up to about 400 (Moyler, 1988).
Components such as chlorophyll, carotenoids and alkaloids are virtually insoluble in liquid CO2. Water solubility is 0.1% (w/w) at 20ºC (Sims, 1982).
The relative solubilities in liquid CO2 of some classes of compounds typically present in herbs and other plant materials are summarised in the table below (Moyler, 1988). It is seen from this table that virtually all the useful flavour components are extracted.
Miscible/very miscible | Low solubility | Insoluble |
Non-polar and slightly
polar organic compounds
of low molecular weight (< 250). Examples include:
|
Higher molecular weight
compounds:
Carboxylic acids Relatively polar compounds with amino groups |
Sugars, proteins Polyphenols Tannins, some waxes, inorganic salts Chlorophyll, carotenoids, citric, malic acids Higher molecular weight compounds |