Page 480 - Biosystems Engineering
P. 480

452    Cha pte r  S i x tee n

               (Dunford and Temelli 1996; Bauer et al. 2000), disruption of microbial
               cells to aid extraction (Castor and Hong 1995), and pretreatment of
               lignocellulosic substrates (Zheng et al. 1998; Kim and Hong 2001).
               The mechanisms for these applications involve mechanical cell rup-
               ture, chemical and biochemical modification of structure of the treated
               sample and their synergistic effects, giving several advantages of
               high-pressure carbon dioxide (see Fig. 16.2).
                   The mechanism of cell disruption by pressure gradient for the
               application of explosion process was proposed and supported by x-ray
               and nuclear magnetic resonance examination (Zheng et al. 1998) and
               by scanning electron microscopy (Gaspar et al. 2001).
                   To extend the solubility-controlled period and improve the later
               diffusion-controlled period, some technologies were developed to
               improve the extraction by disrupting the cell wall (e.g., high-pressure
               homogenizer), agitating the biomass with glass beads, and even ultra-
               sonification. A high-pressure CO  explosion could take some physical
                                           2
               and chemical advantages of supercritical CO , comparing it to the
                                                      2
               high operation temperature of a steam explosion. Pretreatment using
               supercritical CO  explosion on pure cellulose and industrially processed
                             2
             1000


                                                   Critical point (73 bar, 31.2°C)
                                      6
                                     1    2     3   4  5
              100                      6′  2′  3′  7
            Pressure (bar)  Solid/Vliquid  Liquid/ 1′  vapour  Liquid/  8
                                  vapour


               10
                                                  Solid/vapour  25°C  35°C  45°C  55°C  65°C
                           Triple point (5.2 bar, –56.6°C)



                1
                                          Enthalpy
          FIGURE 16.2  Schematic diagram of the pressure-enthalpy of carbon dioxide
          (referenced from http://www.chemicalogic.com/download/phase_diagram.html, last
          updated 1999). Points corresponding to each initial pressure and temperature are
          shown by the open circle. A thin solid line indicates the temperature. The critical
          point is shown as a fi lled black circle. The region above the dashed line indicates
          the supercritical fl uid. Thick solid lines indicated the solid/liquid, solid/gas, liquid/
          gas, and triple point, respectively.
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