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248                              Advances in Eco-Fuels for a Sustainable Environment

         3h reaction time, and 43.8wt% methanol), 100% oil in the bran can be recovered and
         67.4% FAME yield can be achieved. Complex carbohydrates in the bran were also
         hydrolyzed into soluble sugars. Sugar concentration in the aqueous phase was higher
         under a CO 2 atmosphere than that under an N 2 atmosphere due to the higher hydrolysis
         rate of starch at lower pH. The highest sugar concentration of about 1g/L was achieved
         at 180°C. Higher temperature and longer reaction time caused sugar degradation while
         higher methanol concentration decreased the hydrolysis rate.
            For oils with high saturated to unsaturated fatty acid ratio (S/U), such as palm oil,
         winterization is needed before use as a biodiesel feedstock. For biodiesel feedstock
         with low S/U and a high content of polyunsaturated fatty acid such as soybean oil,
         oxidation and polymerization may occur. From Table 9.5, the S/U value of RBO is
         intermediate and therefore suitable as a feedstock for biodiesel production without
         any further refining.


         9.3.2 Catalytic and noncatalytic biodiesel conversion from
                microalgae
         Extraction of lipids from the microalgae cell followed by transesterification is usually
         employed for biodiesel production from microalgae. Extraction assisted by rupturing
         the cell helps release more lipids because such pretreatment is able to break down the
         thick and rigid cell wall, which makes lipid extraction easier and more lipids can be
         extracted. Either a mechanical or a nonmechanical (chemical and biological) method
         can be applied to disrupt the cell wall. Mechanical methods such as microwave,
         ultrasonication, or high-pressure homogenization (HPH) result in a higher lipid yield
         with a shorter extraction time and can be scaled up easily. However, those processes
         are energy intensive. In comparison, chemical methods using acids, salts, surfactants,
         or ionic liquid/DES as the solvent are efficient, selective, and scalable. Huang and
         Kim [73] used a mixture of trimethylamine and methanol as the solvent for the simul-
         taneously disrupted cell wall and extracted lipids in wet Chlorella vulgaris. Their pro-
         cess resulted in a 95% lipid yield. However, the method depends on microalgae
         composition, environmental condition, and the later separation process used. Biolog-
         ical methods use enzymes such as cellulase, lipase, and protease, or a combination of
         multiple enzymes to disrupt the cell wall. The advantages of this method are low
         energy consumption and milder operating conditions. Wu et al. [74] extracted lipid


          Table 9.5 Typical fatty acid composition (%) of RBO and other refined vegetable oils
                                       a           b            b           b
          Fatty acids    RBO        RBO        RBO        Soybean       Palm
          Palmitic       17.7       18.7       14.7       10.4          40.2
          Oleic          47.3       43.4       42.2       24.8          43.3
          Linoleic       31.3       37.9       37.8       52.5          9.0
          S/U            0.25       0.28       0.21       0.19          0.86
          a
           [63].
          b
           [5].
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