Page 241 - Biofuels Refining and Performance
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224   Chapter Eight


           8.2.1  Catalytic cracking (CC)
           In 1979, a paper [22] from the petrochemical industry reported for the
           first time that high-molecular-weight triglycerides such as corn oil
           (C H 104 O ) and castor oil (C H 104 O ) were convertible to a high-grade
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           gasoline when passed over H-ZSM-5, a catalyst. The latter is a synthetic,
           medium-pore, shape-selective acid catalyst. Lipids were fed with a piston
           displacement pump at a rate of 2 mL/h with flowing hydrogen (300 mL/h)
           over 2 mL of H-ZSM-5 catalyst (0.77 g, 14–30 mesh) contained in a ver-
           tical Pyrex reactor at atmospheric pressure and  T   400–450 C.
           Paraffins, olefins, aromatics, and nonaromatics could be detected in the
           product mixture. The distribution of hydrocarbons is similar to selective
           conversion of methanol into hydrocarbon units with up to 10 carbon
           atoms per molecule. In all cases, a high degree of BTX aromatics (ben-
           zene, toluene, and xylene) was achieved. The precondition for the catalytic
           conversion is that the molecule penetrate the cavities of microporous
           zeolite.
             This new catalytic approach has paved the way for a variety of appli-
           cations. A schematic diagram of experimental arrangements for pyrol-
           ysis and catalytic conversion is given in Fig. 8.1.
             Conversion of different kinds of vegetable oils over medium-pore H-
           ZSM-5 have been investigated in detail [23–26]. Catalytic cracking of
           by-products from palm oil mills with a selectivity of 51wt.% toward aro-
           matic hydrocarbon formation has been reported [27]. To achieve higher
           yields, this type of work was extended to pyrolysis and zeolite conver-
           sion of both whole algae and their major components as well as whole
           seeds and selected vegetable oils [18, 28–31]. Hot vapors from solid
           organic material (microalgae, seeds, etc.) or vaporized vegetable oils
           were passed directly over the H-ZSM-5 catalyst. Products of different


                                      Cooling water

                                                             NCG
                              TIR  TIR
            Residual
               solid
           Substrate,
            nitrogen

                                  TIC
                            el.

                                                             Biocrude/Biofuel
                                                             Reaction water
           Figure 8.1 General scheme of pyrolysis and catalytic conversion reactor.
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