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Super critical Fluid Extraction Applications    449


                              Carbon Dioxide: Temperature-Pressure Diagram
             10000.0
                                                Melting line

             1000.0


                             Solid             Liquid             Critical
            Pressure, bar  10.0                 Saturation line    point
              100.0

                        Sublimation line  Triple point


                1.0                            Vapor
                                          Copyright 1999 Chemical logic corporation
                                          Drawn with CO Tab V1.0
                                                    2
                0.1
                 –100 –90 –80 –70 –60 –50 –40 –30 –20 –10  0  10  20  30  40  50
                                        Temperature, °C
          FIGURE 16.1  PT diagram of carbon dioxide. The supercritical region exists at all
          pressures and temperatures above the critical point. (source: http://www.
          chemicalogic.com/download/co2_phase_diagram.pdf)


               properties of carbon dioxide are shown in the pressure-temperature
               phase diagram (Fig. 16.1).
                   Supercritical CO  extraction of vegetable oil has been studied
                                 2
               from a processing point of view, and a wide range of seed species has
               been explored, including cottonseed, soybean, peanut, and rapeseed
               (Reverchon et al. 2000). Fattori et al. (1988) evaluated the feasibility
               and merits of supercritical CO  extraction as an alternative to hexane
                                         2
               extraction in the canola oilseed industry. The experiment was con-
               ducted at temperatures ranging from 25 to 90°C and pressures rang-
               ing from 10 to 36 MPa. The oil solubility in CO  was found to be
                                                         2
               strongly dependent on pressure and weakly dependent on temperature.
               The highest observed oil solubility was 11 mg/g CO  and occurred
                                                             2
               at 36 MPa and 55°C. The amount of oil extractable from flaked and
               cooked seeds was comparable to that obtained by conventional hex-
               ane extraction. Przybylski et al. (1998) analyzed the composition and
               oxidative stability of oil fractions collected during the process of
               supercritical CO  extraction at 40°C and 41.4 MPa. The results showed
                             2
               that linolenic acid composition decreased, and the amounts of phos-
               pholipid increased as the CO  volume increased. The fraction obtained
                                       2
               at the end of extraction contained higher amounts of unsaponifiables
               and phospholipids and showed better oxidative stability.
                   Supercritical CO  extraction of lipids from lipid-bearing fungal or
                                2
               algal biomass has also been studied (Walker et al. 1999; Badal and
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