The reaction conversion into UDA monomer during this step is quantitative (~100%).
Reaction temperature and pressure were important factors influencing the reaction conversion for different size reactors.
The extent of the reaction conversion was thus obtained and subsequently modeled.
We demonstrate that the reaction conversion is highly depended on the substrate reactivity.
Supercritical methylation of the hydrolyzed oil following subcritical hydrolysis of the scCO2 extract yielded a methylation reaction conversion of 98.3%.
Furthermore, water by-product in the reactive distillation column is withdrawn from a side-draw to increase the reaction conversion.
However, in this study, some factors such as protein loss, enzyme inactivation, and acetaldehyde damage greatly reduced the reaction conversion.
Additionally, it is found that with increasing the reaction stage number, the residence time and the reaction conversion increase.
Obtained results demonstrate the ability of the membrane to increase the reaction conversion.
Any substitution in the para position of the Bpy ring decreases the reaction conversion.
Interestingly, the fluid dynamics imposed severe limitations to the reaction conversion.
