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Prospects of biodiesel feedstock as an effective ecofuel source and their challenges  83

           across the globe. It has been found that oils from feedstocks can also be extracted by
           the enzymatic approach. Unfortunately, the major challenge of this technique is the
           cost of production for large-scale set-up and the need to improve the yield [22, 73].
              It has been found that most edible and nonedible oil feedstocks give a high yield of
           biodiesel. They have their biodiesel properties following the specified standard ASTM
           D6751. However, in order to improve their properties such as viscosity, cloud, flash,
           pour, and cold filter plugging points, blending of biodiesels from various feedstocks
           can help to achieve this. A typical example is the blending of Sterculia foetida methyl
           ester and coconut methyl ester, which improved the viscosity of SFME significantly
           [71]. In addition, microwave-assisted biodiesel production significantly helps in
           reducing reaction time and lessens the cost of production [76]. In order to lower sep-
           aration costs for fatty acid esterification, to reduce the maintenance cost (such as cor-
           rosion control), and the cost of neutralization associated with use of homogeneous
           catalysts for fatty acid esterification, the use of heterogeneous catalysts is advisable
           [19, 77]. These problems are best solved using a continuous set-up of reactive distil-
           lation. Reactive distillation is a process intensification method that incorporates mass
           transfer of species and simplifies the process flowsheet. It accommodates the biodiesel
           formation as well as the separation of reaction products [77, 78]. Extensive study on
           the various catalysts and their methods of preparation has been done and more work is
           ongoing [19]. Nevertheless, it is worthy to note that a highly active heterogeneous cat-
           alyst enhances the achievement of low residence time (20–60min), which in turn
           increases the rate of production. Similarly, membrane reactors can equally achieve
           this aim by also increasing conversion for the case of equilibrium-limited reactions
           by simply removing some product from the reactant stream via the membrane
           [79, 80]. This feature is an advantage of membrane reactor systems for biodiesel pro-
           duction over the reactive distillation. Dub  e et al. has a comprehensive study of the
           possibility of biodiesel production from canola oil with methanol using a two-phase
           tubular membrane reactor. A well-regulated flow rate of reacting species will help in
           achieving improved conversion without blockages of the pores of the membrane
           medium.



           3.5   Conclusion


           Biodiesel is gaining more attention as a result of its advantages over petroleum diesel,
           though its production is still faced with many challenges. These in relation to the
           choice of feedstocks include the feedstock cultivation process, postharvest technolo-
           gies, the presence of high free fatty acids in most oils used, and the nonavailability of
           the majority of oils in the open market. Among the various sources of feedstocks
           reviewed, nonedible oils seem to have more prospects than edible oils and animal fats
           in the biodiesel industry. This is because most of the nonedible oil plants are highly
           pest- and disease-resistant and noncompetitive with food, in additional to the fact that
           most of them can grow on wastelands. Furthermore, the advantages of nonedible oils
           are their liquid nature portability, ready availability, renewability, higher heat content,
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