Original scientific paper
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
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 (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.
Keywords
epoxidation; kinetic rate; MATLAB; DHSA; Taguchi
Hrčak ID:
250595
URI
Publication date:
24.1.2021.
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