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Rajak, et al.

                The impregnation process is also known as capillary   to create a sol and a gel. Due to its great versatility, the
                and dry impregnation.  The solution is absorbed into   approach may work with a wide range of pre-cursors,
                the supporting material and then dried to remove the   most frequently alkoxides (M(OR)n)‐. 269
                solvent from its substrate.                            A solid-particle-based colloidal solution called  the
                  The two main categories of this technique are wet   sol and a continuous  liquid  phase called  the gelation
                impregnation  and dry impregnation.  The size of the   phase are the two main stages of the sol-gel process. 273,274
                solution  and  the  method  of solid-solution  interaction   Numerous  benefits,  including  excellent  yields,  low
                are the primary distinctions between the two.  Wet   temperatures  of  operation,  and  cost-effectiveness,  are
                impregnation uses an excess solution that is then dried   provided by the sol-gel technique.  This method has
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                after a pre-determined amount of time. In dry starting   been  used  effectively  in  many  research  studies,  such
                wetness impregnation, the quantity of solution utilized   as those by Sharm et al.,  Ciesielczyk et al.,  Danks
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                is at least as large as the amount of pore space of the   et al.,  Navas et al.,  and Rahman et al.,  Based on
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                active  phase  or sustaining  solid. 263,264   A number  of   the  following  equations,  the  sol-gel  process  usually
                variables, such as temperature and the starting solution’s   involves three primary routes: hydrolysis (Equation I),
                concentration,  might  impact  the  effectiveness  of  the   condensation  (Equation  II),  and  mixed  condensation
                impregnation  methods. 265,266   Wetting  time,  solution   (Equation III).
                viscosity, and pre-cursor solubility are all impacted by   –MOR+H O→–MOH+ROH                       (I)
                temperature. 267,268  Studies have successfully used the     2
                impregnation approach, such as the creation of potassium   –MOH+ROM–→–MOM+ROH                     (II)
                fluoride/CaO  nano-catalysts. 269,270   For  instance, to   –MOH+HOM–→MOM+H O                    (III)
                transesterify soybean oil, a lithium/zinc oxide catalyst                    2
                was made through impregnation  and calcination.
                Catalytic  activity  and  catalyst  characteristics  were   4.6. Co-solvent preparation method
                shown to be correlated in the study, which also noted   A co-solvent system consists of water mixed with a
                that  the calcination  temperature  and  lithium  loading   miscible or partially miscible organic solvent, creating
                affected lithium/zinc oxide performance.            a  modified  aqueous  medium.  This  phenomenon,
                  Benefits of the impregnation process include reduced   termed  cosolvency, relies on the solvent’s dual
                expenses, quicker preparation,  and improved control   characteristics:  hydrogen-bonding capacity  (either as
                over the end-product  catalyst properties.  However,   donor or acceptor)  and the presence of hydrophobic
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                achieving  a homogeneous  catalytic  component      domains. These properties enable co-solvents to modify
                dispersion on the support surface is a difficult task.  solution  thermodynamics  and enhance  the  solubility
                                                                    of diverse compounds.  To increase catalytic  activity
                4.5. The sol-gel process                            and accelerate the catalyzed processes, the co-solvent
                The sol-gel method serves as a versatile approach for   approach  is a catalyst  preparation  methodology  that
                both  catalyst  synthesis and feedstock  preparation.   overcomes limitations in mass transfer between oil and
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                This  wet-chemical  technique  involves  the  transition   methanol.   In  several  transesterification  processes,
                of a colloidal suspension (sol) into a continuous three-  tetrahydrofuran is frequently employed as a co-solvent
                dimensional network (gel), enabling the production of   in co-solvent catalyst systems. The effectiveness of this
                homogeneous, high-purity materials  with controlled   strategy has been shown in a number of investigations,
                porosity.  The process begins with nanoparticle     with the co-solvent technique producing FAME yields
                dispersion in the liquid phase, followed by controlled   that range from 90% to 98.5% conversion. 282,283
                agglomeration  and gelation,  making it particularly
                valuable for creating tailored catalytic materials and pre-  5. The impact of heterogeneous catalysts’
                cursor formulations. A popular technique for catalytic   chemical and physical characteristics on
                feedstocks having colloidal characteristics,  such as   biodiesel production
                silicon dioxide, the sol-gel method is comparable to the
                precipitation process.  The sol-gel procedure ensures   The functionality of catalysts that are uniform, which
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                a consistent distribution  of components  and allows   usually appear in the liquid state, differs from that of
                for the  fabrication  of porous materials,  in  contrast  to   catalysts that are heterogeneous and have a solid shape.
                conventional  catalyst  preparation  methods. Usually,   Although homogeneous catalysts are readily accessible,
                inorganic pre-cursors or colloidal dispersions are used   reasonably priced, have quick processing times, and



                Volume 22 Issue 5 (2025)                        20                           doi: 10.36922/AJWEP025130095
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