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Transesterification of palm oil and esterification of palm fatty acid in near- and super-critical methanol with SO4-ZrO2 catalysts
Authors:Akaraphol Petchmala  Bunjerd Jongsomjit  Joongjai Panpranot  Artiwan Shotipruk
Affiliation:a Department of Chemical Engineering, Faculty of Engineering, Chulalongkorn University, Patumwan, Phayathai Road, Bangkok 10330, Thailand
b The Joint Graduate School of Energy and Environment, King Mongkut’s University of Technology Thonburi, Bangkok 10140, Thailand
c Department of Applied Chemistry and Biochemistry, Kumamoto University, Kurokami 2-39-1, Kumamoto 860-8555, Japan
d Department of Chemical Engineering, Faculty of Engineering and Industrial Technology, Silpakorn University, Nakorn Pathom 73000, Thailand
Abstract:Sulfated zirconia (SO4-ZrO2) catalysts, prepared with three different sulfur loading contents (0.75%, 1.8% and 2.5%) at two calcination temperatures (500 °C and 700 °C), were tested for use in the transesterification of purified palm oil (PPO) and the esterification of palm fatty acid (PFA) in near-critical and super-critical methanol. Techniques including BET, XRD, NH3- and CO2-TPD revealed that the sulfur content and calcination temperature strongly affects the catalyst base-acid site, specific surface area, average pore size, phase structure, and thus the catalytic reactivity. The most suitable sulfur loading content was found to be 1.8% and the optimum calcination temperature 500 °C. The results show that the use of SO4-ZrO2 reduces esterification reaction times, the amount of methanol necessary and the required reaction temperature. The reactions at 250 °C in the presence of the SO4-ZrO2 catalyst at 0.5 w/w% catalyst to PPO or PFA were found to give the highest FAMEs conversions. Under these conditions, 90% and 75% conversions were achieved within 10 and 1 min from PPO (at 25:1 MeOH:PPO molar ratio) and PFA (at 6:1 MeOH:PFA molar ratio), respectively.
Keywords:Transesterification  Esterification  Super-critical  Sulfated zirconia
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