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Cracking of Lipids for Fuels and Chemicals  223


           TABLE 8.2 Comparison of Fuel Properties
                                      Distilled                     High oleic
            ASTM                     soybean oil   No. 2   Soybean   safflower
           test no.   Specification  (N 2 sparge)  diesel fuel  oil   oil

            D613   Cetane rating        43 *     40 (min.)  37.9 *    49.1
                   Higher heating      17,333     19,572   17,035    17,030
                    value, BTU/Ib
            D129   Sulfur, %           <0.005      <0.5     0.01      0.02
            D130   Copper corrosion,     1 *       <3        1 *       1 *
                    3 h at 50 C
                    standard strip
            D524   Carbon residue      0.45%     <0.35%     0.27%     0.24
                    at 10% residium
            D1796  Water and sediment,  0.05      <0.05     Trace    Trace
                    % by volume
            D482   Ash, % by weight    0.015      <0.01     <0.01    <0.01
            D97    Pour point,  C        7       7C (max.)   12        21
                              2
            D445   Viscosity, mm /s    10.21     1.9–4.1    32.6      38.2
                    at 38 C
            DE191  Carbon, %           79.00      86.61      —        —
                   Hydrogen, %         11.88      13.20      —        —
             *
             ASTM test D613 with ignition delays observed visually.

           oil. This indicates considerable amounts of oxygenated compounds in the
           distillate. Consequently, methylation of these oils has revealed 9.6–12.2%
           of carboxylic acids ranging from C-3 to over C-18. This is reflected in the
           higher viscosity compared to diesel.
             Mass-spectral fingerprints of the entire pyrolysis product slate from
           tripalmitin, different vegetable oils, and extracted oils from microalgae
           confirm that the decomposition of ester bonds in the absence of external
           catalysts is extensive [16–18]. However, a great variability in primary
           pyrolysis/vaporization product slates was observed [18].
             Thermodynamic calculation in the degradation process shows that the
           cleavage of C-O bond takes place at 288 C and fatty acids are the main
           product [19]. The actual pyrolysis temperature should be higher than
           400 C to obtain maximum diesel yield [20]. The mechanism of pyrolysis
           of vegetable oil has been discussed by various authors [9, 15, 19]. Generally,
           thermal decomposition proceeds through either a free-radical or carbonium
           ion mechanism. The primary R-COO splits off carbon dioxide. The alkyl
           radicals (R), upon disproportionation and elimination of ethene, give rise
           to alkanes and alkenes. The formation of aromatics is facilitated by a
           Diels-Alder addition of ethene to a conjugated diene formed in the pyrol-
           ysis reactions. However, the product mix and product quality are influenced
           by many factors such as feed pretreatment, heating rate, and temperature.
           As vegetable oils may contain trace elements, catalytic effects cannot be
           completely excluded from any thermal degradation process [21].
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