Page 116 - Refining Biomass Residues for Sustainable Energy and Bioproducts
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90                      Refining Biomass Residues for Sustainable Energy and Bioproducts





















         Figure 4.2 Chemical reaction pathway of an acid catalyzed esterification reaction.


         densities. They are synthesized using different techniques such as direct sulfonation,
         carbonation followed by sulfonation or carbonization with distinct activating agents.
         These catalysts have remarkable performance in biodiesel production by both esteri-
         fication and transesterification reactions. In comparison, they exhibit highly admira-
         ble catalytic activity for esterification than transesterification under identical
         reaction conditions. This is due to the complication in transesterification reaction
         mechanism and the requirement of lower activation energy for a faster reaction rate
         (Yin et al., 2012). Due to these reasons, it is considered the best choice for the pre-
         treatment of low-value acid feedstock. Furthermore, it can be easily regenerated
         and reused for multiple times after a more straightforward recovery through reacti-
         vation. The other factors that determine the efficiency of biodiesel yield include
         high active sites and stability of the catalyst. Summarily, this strategy may act as an
         efficient and economic way to produce biodiesel.


         4.3.1 Direct sulfonation method

         Direct sulfonation proves to be the simplest and the most commonly used method
         among the existing acid catalyst preparation techniques in which direct carboniza-
         tion and sulfonation of biomass are carried out by sulfuric acid at a predetermined
         time and temperature (Kang et al., 2014; Guo et al., 2017). The main advantage of
         this process is the economical aspect since it does not require any complicated
         pretreatment.
           Savaliya and Dholakiya (2015) synthesized acid catalyst from sugarcane bagasse
         through in-situ sulfonation and carbonization. They recognized this process to be
         convenient giving a yield of 25 35 wt.% catalyst. Further, this catalyst was investi-
         gated to catalyze soap stock that resulted in a maximum FFA conversion of 97.2%.
         A study on its reusability showed that it can be used up to three consecutive cycles
         without any significant loss in its activity.
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