Product sampling during transient continuous countercurrent hydrolysis of canola oil and development of a kinetic model
KAUST DepartmentClean Combustion Research Center
Mechanical Engineering Program
Physical Science and Engineering (PSE) Division
high-pressure combustion (HPC) Research Group
Permanent link to this recordhttp://hdl.handle.net/10754/563056
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AbstractA chemical kinetic model has been developed for the transient stage of the continuous countercurrent hydrolysis of triglycerides to free fatty acids and glycerol. Departure functions and group contribution methods were applied to determine the equilibrium constants of the four reversible reactions in the kinetic model. Continuous countercurrent hydrolysis of canola oil in subcritical water was conducted experimentally in a lab-scale reactor over a range of temperatures and the concentrations of all neutral components were quantified. Several of the rate constants in the model were obtained by modeling this experimental data, with the remaining determined from calculated equilibrium constants. Some reactions not included in the present, or previous, hydrolysis modeling efforts were identified from glycerolysis kinetic studies and may explain the slight discrepancy between model and experiment. The rate constants determined in this paper indicate that diglycerides in the feedstock accelerate the transition from "emulsive hydrolysis" to "rapid hydrolysis". © 2013 Elsevier Ltd.
CitationWang, W.-C., Natelson, R. H., Stikeleather, L. F., & Roberts, W. L. (2013). Product sampling during transient continuous countercurrent hydrolysis of canola oil and development of a kinetic model. Computers & Chemical Engineering, 58, 144–155. doi:10.1016/j.compchemeng.2013.06.003
SponsorsThis material is based upon work supported by the National Science Foundation EFRI program under Grant EFRI-093772.
JournalComputers & Chemical Engineering