Reaction kinetic model for the two-step transesterification in the biodiesel production plant

Hasan, Sulaiman and Hasnan, Khalid and Md Yusof, Mohammad Zainal and Sani, Winardi (2015) Reaction kinetic model for the two-step transesterification in the biodiesel production plant. Other thesis, Universiti Tun Hussein Onn Malaysia.

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Abstract

Crude palm oil (CPO), which is available in abundant in Malaysia, is used as the feedstock in this research work. The work starts with the analysis of the physical and chemical properties of the feedstock and the associated product to obtain the major fatty acid compositions of triglyceride applicable in the crude palm oil. The kinetic models describing the change in the concentrations of the triglycerides, intermediates, alcohol, and the products during the reaction course are formulated through the corresponding kinetic mechanism. By looking at the kinetic mechanisms of the reaction, the chemical reaction is better understood. The ultimately proposed kinetic models of the biodiesel production from crude palm oil and methanol under presence of a base catalyst follow the second order differential equations without a shunt reaction. The emphasis of this research work is on the study of the alcoholysis of the crude palm oil under a base catalyst (transesterification) to produce biodiesel at a high quality and a maximum yield. The concentration profiles of thc rcactants arid the products employed in the transesterification are obtained by solving numerically the associated differential equations with introducing the published reaction rate constants applied in a laboratory scale. The effect of t,he reversible transesterification reaction shows, that each concentration profile of the reactants and the products tends to achieve an equilibrium after a certain reaction time. The simulation results of the kinetics models are implemented in conducting experiments in the pilot plant to produce biodiesel from CPO. Due to impurities such as unwanted gums and pigment, the feedstock must first undergo a physical treatment including degumming and bleaching processes. The high content of water and free fatty acid containing in CPO requires an esterification process. The main objective of this process is to lower that value at a minimum level to avoid the undesired effects such as saponification and inefficiency of the catalyst. Gas chromatography (GC) analysis method was used to determine the methyl ester contents during the reaction progress. Based on these accurate experiment data along with the simulation results, a validation was done. Technical improvements in the plant operation can therefore be deduced towards the best plant performance and a high quality of biodiesel product.

Item Type:Thesis (Other)
Subjects:T Technology > TP Chemical technology > TP315-360 Fuel
ID Code:6908
Deposited By:Normajihan Abd. Rahman
Deposited On:11 May 2015 16:32
Last Modified:11 May 2015 16:32

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