| 3rd International Conference on Global Sustainability and Chemical Engineering | |
| Kinetic Study on the Esterification of Palm Fatty Acid Distillate (PFAD) Using Heterogeneous Catalyst | |
| 工业技术;化学工业 | |
| Rofiqah, U.^1 ; Djalal, R.A.^2 ; Sutrisno, B.^1 ; Hidayat, A.^1 | |
| Chemical Engineering Department, Universitas Islam Indonesia, Indonesia^1 | |
| Industrial Engineering Department, Universitas Islam Indonesia, Indonesia^2 | |
| 关键词: First order; Heterogeneous catalyst; Homogeneous catalyst; Increasing temperatures; Kinetic study; Palm fatty acid distillate; Pseudo-homogeneous modeling; Temperature variation; | |
| Others : https://iopscience.iop.org/article/10.1088/1757-899X/358/1/012069/pdf DOI : 10.1088/1757-899X/358/1/012069 |
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| 学科分类:工业工程学 | |
| 来源: IOP | |
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【 摘 要 】
Esterification with heterogeneous catalysts is believed to have advantages compared to homogeneous catalysts. Palm Fatty Acid Distillate (PFAD) was esterified by ZrO2 -SO4 2-/natural zeolite at temperature variation of 55°C, 60°C, and 65°C to produce biodiesel. Determination of reaction kinetics was done by experiment and modeling. Kinetic study was approached using pseudo-homogeneous model of first order. For experiment, reaction kinetics were 0.0031 s-1, 0.0054 s-1, and 0.00937 s-1 for a temperature of 55 °C, 60 °C and 65 °C, respectively. For modelling, reaction kinetics were 0.0030 s-1, 0.0055 s-1, and 0.0090 s-1 for a temperature of 55°C, 60°C and 65°C, respectively. Rate and conversion of reaction are getting increased by increasing temperature.
【 预 览 】
| Files | Size | Format | View |
|---|---|---|---|
| Kinetic Study on the Esterification of Palm Fatty Acid Distillate (PFAD) Using Heterogeneous Catalyst | 575KB |
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