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A plug-flow or contact-type reactor design may improve overall ultrasonic utilization in the transesterification reaction under continuous sonication.
It was observed that small reactor design such as plug-flow or contact-type reactor design may improve overall ultrasonic utilization in the transesterification reaction due to increased energy density and ultrasonic intensity.
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Mg1.7Co0.3O2 catalyst was more active than Mg0.3Co1.7O2 in the transesterification of palm oil with methanol.
Copper vanadium phosphate CuVOP resulted very active in the transesterification reaction for biodiesel production.
Glycerol is the side product in the transesterification reaction.
The amount of catalyst used in the transesterification is shown in Fig. 4.
Lastly, ultrasonically pre-irradiated lipase was also used in the transesterification of Jatropha oil to biodiesel.
Further study is needed to determine whether water is really involved in the transesterification reaction.
These enzymes were tested in the transesterification of a 50 50 PS/PO (w,w) mixture.
No previous studies involving ROL in the transesterification reaction to produce fat phase suitable for margarine preparation were reported.
In this paper, the transesterification of soybean oil with ethanol is studied.
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