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Application of heterogeneous acid catalyst derived from biomass for biodiesel process  97


           catalysts was confirmed from the images of Scanning Electron Microscopy (SEM)
           technique (Konwar et al., 2015).
              Report from Liu et al. (2010b) suggested that catalyst derived from the 4-BDS sul-
           fonation method showed a relatively less difference in the patterns of X-ray
           Diffraction (XRD) between the sulfonated and nonsulfonated carbon. These results
           clearly indicated a reduction in arylation, though it did not affect the microstructure
           of the carbon materials. However, it was observed that there was a reduction in the
           pore volume after sulfonation which proved that a part of these pore spaces had been
           filled by sulfonic group. It was also reported that there existed a close relationship
           between the increase in sulfur content and total acid density in sulfonation process.
              In general, these catalysts played a significant role in esterification, although the
           same was comparatively less in the transesterification process that was because phe-
           nolic and carboxylic did not display adequate acid strength to catalyze the transes-
           terification reaction. These groups are created due to the oxidization of aliphatic
           groups by strong sulfonation and incomplete carbonization of the supporting mate-
           rial. Therefore, the sulfonic group having ample acid strength alone can take part in
           transesterification reaction. The total acid density of the sulfonated catalyst impreg-
           nated with concentrated sulfuric acid is found to be 100 times lower than that of
           catalyst synthesized using fuming acids. This is majorly because of the strong
           nature of the sulfonation reagent and higher solid-to-acid ratio during fuming sulfu-
           ric acid catalyst preparation (Dehkhoda et al., 2010).
              The preparation of the catalyst with the help of special sulfonating agents other
           than sulfuric acid exhibit an extraordinary acid exchange capacity, thermal stability,
           and reusability. It has been found that they could act as a favorable waste-derived
           substitute to H 2 SO 4 for both pretreatment and transesterification of acidic feedstock.




           4.3.3 Special ingredient loaded on carbonized biomass
           The solid catalyst recovery is usually carried out by means of filtration or centrifugation
           method that consumes more time and energy. The magnetization of the catalyst aims to
           render help for the simplification of the catalyst separation and recycle process (Liu
           et al., 2013b).
              Zhang et al. (2017) magnetized the catalyst prepared from pyrolysis and subse-
           quent sulfonation. They incorporated magnetic material in the form of γ-Fe 2 O 3 into
           the carbon structure. Acid functional groups loaded onto the sulfonated carbon
           formed a difunctional acid catalyst that consists of both Lewis as well as Bronsted
           acid sites. Hence, the magnetized catalyst is more efficient in biodiesel production.
           These above discussions indicate that the sulfonated carbon material can be treated
           with the special loaded ingredients to enhance easier separation. Further research in
           difunctional or multifunctional catalyst production would be promising.
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