Currently monoglyceride and diglyceride are representing important products, as they have numerous applications such as modifying agents in food and pharmaceutical industries. In this work, the production of these economically value added compounds by estrifying the fatty acids with the glycerol is presented. Effects of various reaction parameters were optimized to obtain high yield of mono, di-and triglycerids. The effects of temperature (180˚C to 260˚C), ZnCl 2 catalyst concentration (0.1%, 0.2%, 0.3%), glycerol to fatty acids molar ratio (1:1, 1:2, 1:3, 3:1), agitation speeds (200, 500, 1000 rpm), type of reaction system (opened and closed) and type of fatty acids including oleic and palmatic acids on esterification efficiency of fatty acids were investigated. The optimum conditions of esterification reaction were at temperature 195˚C, molar ratio 1:1, amount of catalyst 0.3% Zncl 2 , and agitation 500 rpm. Analysis of yield showed that at the optimum conditions mondi and triglycerids were produced in high purity, up to 99%. Infrared spectroscopy IR and thin layer chromatograph TLC proved that the final product contains mono, di-and triglycerides.

This work represents the extraction of oil with high free fatty acid content from spent bleaching earth using sub-critical water technology as a greener production pathway. The extraction efficiencies under different conditions were investigated. The studied parameters include temperatures in the range of 180 to 270˚C, the feed to solventfeed-to-solvent (in this case water) ratio (1:1, 1:2, 1:3, 1:4 and 1:5) and extraction times in the range of 5-60 minutes. The results showed that the optimum temperature, feed to solventfeed-tosolvent ratio, and extraction time were 270˚C, 1:3, and 20 minutes, respectively. In another experiment, the extracted free fatty acids were converted into mono-, di-, and triglycerides through esterification with glycerol to increase the value added of the extracted products. The kinetics of the extraction process was found to be corresponding to an irreversible consecutive unimolecular-type first order reaction, consisting of the extraction step followed by the decomposition reaction step. Both reaction rates of extraction and decomposition were estimated using the reaction rate equations utilizing the nonlinear regression method. The apparent activation energy was calculated to be 46.1 kJ•mol −1. This result indicates a diffusion controlled reaction. For more exploration and deep understanding of the extraction mechanism, other thermodynamic parameters were also calculated and analyzed including, ∆H#, ∆S#, and ∆G# of the extraction step.

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