Abstract

In recent years, studies related to the epoxidation of fatty acids have garnered much interest due to the rising demand for eco-friendly epoxides derived from vegetable oils. From the epoxidation reaction, there is a side reaction involving epoxide and water. This reaction produces a by-product – dihydroxystearic acid (C<sub>18</sub>H<sub>36</sub>O<sub>4</sub>, DHSA). DHSA is one of the chemical precursors in the production of cosmetic products. Therefore, a kinetic model was developed to determine the optimised epoxidation process and concentration of DHSA, where each of the reactions was identified. The kinetic rate, <i>k</i> parameters obtained were: <i>k</i><sub>11</sub> = 6.6442, <i>k</i><sub>12</sub> = 11.0185, <i>k</i><sub>21</sub> = 0.1026 for epoxidation palm oleic acid, and <i>k</i><sub>41</sub> = 0.0021, <i>k</i><sub>51</sub> = 0.0142 in degradation process. The minimum error of the simulation was 0.0937. In addition, DHSA yield optimisation was done through Taguchi method, and the optimum conditions obtained were H<sub>2</sub>O<sub>2</sub>/oleic acid – OA unsaturation molar ratio 1 : 1 (level 2), formic acid – FA/OA unsaturation molar ratio 0.5 : 1 (level 1), temperature 35 °C (level 1), and agitation speed 100 rpm (level 1). A high yield of DHSA can be achieved under these conditions.

Highlights

  • The growth in vegetable oil demand has increased compared to the petroleum-based polymer.[1]

  • 3.1 Reaction rate of DHSA production Kinetic model for catalytic epoxidation of palm oleic acid based on palm oil (PO) was developed by MATLAB simulation

  • There were 27 experiments run in the simulation, in order to ensure the optimal value of epoxidation

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Summary

Introduction

The growth in vegetable oil demand has increased compared to the petroleum-based polymer.[1]. Since petroleum causes environmental pollution concerns, vegetable oil has become an alternative in the production of the epoxide. The oxirane ring-opening depletes the yield and can cause high peroxide values of epoxidized vegetable oils, so the opening needs to be minimised.[3]. The commercial production of palm oil is quite high compared to that of other vegetable oils.[4]. EPO is obtained from renewable resources, and can be regarded as biodegradable and non-toxic. It is suitable in replacing petroleum, since petroleum is toxic and harmful to the environment. The oxirane-ring degradation of epoxidation palm oil was determined through MATLAB simulation.

Kinetic model
Optimisation procedure
Reaction rate of DHSA production
Optimisation of DHSA through Taguchi method
Conclusion
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