Abstract:Epoxidized oleic acid is often regarded as a high value oleochemical due to the wide range of industrial applications including cosmetics, personal care and pharmaceutical products. Epoxidized oleic acid also extensively chosen by industry due to its advantages on the good performance as intermediate chemicals and can be obtained from renewable sources. Synthesis and physicochemical properties of oleic acid palm oil was analyzed for further reaction of epoxidation. In this study, the epoxidation of oleic acid … Show more
“…FTIR spectra were recorded on a Perkin Elmer Infrared Spectrophotometer in 400-4000 cm -1 . In addition, the 1 H (16 scans) and 13 C-NMR (3000 scans) spectra were recorded on JEOL-ECP 400 spectrometer (400 MHz 1 H/100.61 MHz 13 C) using CDCl 3 as a solvent.…”
Section: Instrumentationmentioning
confidence: 99%
“…Plant oils or fatty acids epoxidation can be economically accomplished by reacting the unsaturated double bonds of the fatty acid with a peracid reagent such as peracetic [11] or performic acid [1,12]. Currently, epoxides plant oils [13][14][15][16] or fatty acids are prepared on an industrial scale through in situ generated peracids [14]. The epoxidations of ricinoleic acid, for example, have been reported elsewhere [8][9][17][18][19][20][21][22].…”
Epoxidized castor oil (ECO) has shown high potential for industrial applications as value-added products such as polymer coating, plasticizer, and biolubricant. Epoxidized ricinoleic acid recovered from ECO has potential for industrial usage. In this work, epoxidized ricinoleic acid (ERA) was synthesized through in situ generated performic acid epoxidation of ricinoleic acid (RA). The epoxidation process was optimized by several reaction parameters, such as the molar ratio of formic acid to ethylenic unsaturation, the molar ratio of hydrogen peroxide to ethylenic unsaturation, and reaction temperature. The response reaction parameters of oxirane oxygen content (OOC) and iodine value (IV) were then evaluated. The results showed the optimal condition for the epoxidation of RA was obtained at 50 °C, the molar ratio of formic acid and hydrogen peroxide to ethylenic unsaturation of 1:8:1 for 4 h reaction time. A high yield of ERA of 86% with relative conversion into oxirane of 85.3% was achieved at the optimum condition. The optimum ERA showed a high OOC value of 4.00% and a low IV value of 2.24 mg/g. It is plausible that ERA can be used as an intermediate starting material to prepare value-added products such as biosurfactants, biopolymer additives, or biolubricants.
“…FTIR spectra were recorded on a Perkin Elmer Infrared Spectrophotometer in 400-4000 cm -1 . In addition, the 1 H (16 scans) and 13 C-NMR (3000 scans) spectra were recorded on JEOL-ECP 400 spectrometer (400 MHz 1 H/100.61 MHz 13 C) using CDCl 3 as a solvent.…”
Section: Instrumentationmentioning
confidence: 99%
“…Plant oils or fatty acids epoxidation can be economically accomplished by reacting the unsaturated double bonds of the fatty acid with a peracid reagent such as peracetic [11] or performic acid [1,12]. Currently, epoxides plant oils [13][14][15][16] or fatty acids are prepared on an industrial scale through in situ generated peracids [14]. The epoxidations of ricinoleic acid, for example, have been reported elsewhere [8][9][17][18][19][20][21][22].…”
Epoxidized castor oil (ECO) has shown high potential for industrial applications as value-added products such as polymer coating, plasticizer, and biolubricant. Epoxidized ricinoleic acid recovered from ECO has potential for industrial usage. In this work, epoxidized ricinoleic acid (ERA) was synthesized through in situ generated performic acid epoxidation of ricinoleic acid (RA). The epoxidation process was optimized by several reaction parameters, such as the molar ratio of formic acid to ethylenic unsaturation, the molar ratio of hydrogen peroxide to ethylenic unsaturation, and reaction temperature. The response reaction parameters of oxirane oxygen content (OOC) and iodine value (IV) were then evaluated. The results showed the optimal condition for the epoxidation of RA was obtained at 50 °C, the molar ratio of formic acid and hydrogen peroxide to ethylenic unsaturation of 1:8:1 for 4 h reaction time. A high yield of ERA of 86% with relative conversion into oxirane of 85.3% was achieved at the optimum condition. The optimum ERA showed a high OOC value of 4.00% and a low IV value of 2.24 mg/g. It is plausible that ERA can be used as an intermediate starting material to prepare value-added products such as biosurfactants, biopolymer additives, or biolubricants.
“…The kinetic model of the epoxidation process and epoxide ring degradation can be developed based on the following rate constants: k 11 , k 12 , k 2 , and k 3 . The following rate equations were modeled, and the set of simultaneous differential equations is given as Equations (7)(8)(9)(10)(11)(12)(13). Figure 1 shows the flow chart of the procedure used to determine the rate constants.…”
Section: Kinetic Modeling Of the In Situ Hydrolysis Of Eoa For Dhsa Productionmentioning
confidence: 99%
“…6 In addition, the process allows for conversion of low value resources into a desirable, high value epoxy materials. 7 There are various methods to produces epoxide groups such as epoxidation with organic or inorganic oxidants, epoxidation with halohydrins and molecular hydrogens and epoxidations with percaboxylic acid generated with in situ or preformed. 8 The common method used is epoxidations with percaboxylic acid which is by using fatty acid such as acetic acid or formic acid.…”
Epoxidized vegetable oils are great concern as they are obtained from sustainable, and renewable natural resources. The epoxidation of palm oil-derived oleic acid was carried out by using in situ generated performic acid to produce epoxidized palm oil-derived oleic acid. The maximum conversion of palm oil-derived oleic acid into oxirane was 86% by applying the in situ peracid mechanism. Based on the Fourier-transform infrared spectrum, the hydroxyl group was observed within a wavenumber range of 1210-1320 cm À1 . Last, a mathematical model was developed using Runge-Kutta method and after 100 iterations, the reaction rate parameters were obtained as follows: k 11 = 0.046 molÁL À1 Ámin À1 , k 12 = 39.058 molÁL À1 Ámin À1 , k 2 = 2.789 molÁL À1 Ámin À1 , and k 3 = 0.0235 molÁL À1 Ámin À1 for of dihydroxystearic acid production.
“…EPOA has been widely used as an intermediate product, such as stabilizer and plasticizer of polyvinylchloride, as well as a solvent to replace volatile organic solvents in paints. 2,3 The cost-effectiveness and environmentally friendly material traits of vegetable oil renders vegetable oil a favourable alternative to produce epoxides as well as derivatives from epoxide. 4 To date, there are no studies on the effect of oxidising agent on the epoxidation process, while there are only a few studies pertaining to the degradation of epoxides, where the researchers attempt to control the process in order to achieve a high conversion of oxirane.…”
The global consumption of raw materials has shifted from the use of non-renewable materials to renewable materials. Studies on greener epoxidation by using vegetable oils to produce eco-friendly epoxides have also increased. In this study, the epoxidation of palm oleic acid was carried out by in situ generated performic acid. Fourier transform infrared spectroscopy of the products was conducted to confirm the success of the epoxidation. Lastly, a mathematical model was developed using the numerical integration of the 4 th order Runge-Kutta method, and the results showed good agreement between the simulation and experimental data, which validates the kinetic model.
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