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https://doi.org/10.15255/KUI.2020.016

High Yield Dihydroxystearic Acid (DHSA) Based on Kinetic Model from Epoxidized Palm Oil

Mohd Jumain Jalil orcid.org/0000-0001-5205-4287 ; Faculty of Chemical Engineering, Universiti Teknologi MARA Cawangan Pulau Pinang, Kampus Permatang Puah, 13 500 Permatang Pauh, Pulau Pinang
Khairul Azhar Kamal ; Faculty of Chemical Engineering, Universiti Teknologi MARA Cawangan Pulau Pinang, Kampus Permatang Puah, 13 500 Permatang Pauh, Pulau Pinang
Aliff Farhan Bin Mohd Yamin ; Faculty of Chemical Engineering, Universiti Teknologi MARA Cawangan Pulau Pinang, Kampus Permatang Puah, 13 500 Permatang Pauh, Pulau Pinang
Intan Suhada Azmi ; Faculty of Chemical Engineering, Universiti Teknologi Mara Cawangan Johor Kampus Pasir Gudang, 81 750 Masai, Johor
Mohamad Hasni Hassan ; Faculty of Chemical Engineering, Universiti Teknologi MARA Cawangan Pulau Pinang, Kampus Permatang Puah, 13 500 Permatang Pauh, Pulau Pinang
Abdul Rani Hidayu ; Faculty of Chemical Engineering, Universiti Teknologi Mara Cawangan Johor Kampus Pasir Gudang, 81 750 Masai, Johor
Kamariah Noor Ismail ; Faculty of Chemical Engineering, Universiti Teknologi MARA, 40 450 Shah Alam, Selangor

Sažetak

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 (C₁₈H₃₆O₄, 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, k parameters obtained were: k₁₁ = 6.6442, k₁₂ = 11.0185, k₂₁ = 0.1026 for epoxidation palm oleic acid, and k₄₁ = 0.0021, k₅₁ = 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 H₂O₂/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.




This work is licensed under a Creative Commons Attribution 4.0 International License.

Ključne riječi

epoxidation; kinetic rate; MATLAB; DHSA; Taguchi

Hrčak ID:

250595

URI

https://hrcak.srce.hr/250595

Datum izdavanja:

24.1.2021.

Podaci na drugim jezicima: hrvatski

Posjeta: 1.203 *