Abstract
The biodiesel production was performed in stirred tank chemical reactor by numerical simulation. The main results are that the percentage of conversion from triglyceride to biodiesel is approximately of 82 % when the molar flow ratio between triglyceride/alcohol is 1:5. This system displays only one equilibrium point. Since there are imaginary eigenvalues in the Jacobian matrix analysis, the equilibrium point is unstable. The biodiesel production in stirred tank chemical reactor is good because the settling time is short, and has higher conversion.
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Acknowledgment
The author is grateful to Dr. Ever Peralta for his revisions in the text. This work was support in part by COMECYT.
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Appendix
Appendix
The particular model for the case study is governed by the next set of ordinary differential equations.
Where: β i = k o i exp(−E A, i /Rx 9) and γ i = θx i,0
Using the expansion Taylor series the dynamic system governing by (6) can be represented by (7).
Reordering the before equation
In deviation variables \( \underset{\sim }{\xi }=\underset{\sim }{x}-{\underset{\sim }{x}}_e \) (7) have the next form:
For the case study the function Jacobian matrix values are:
The eigenvalues of Jacobian matrix can be find by (11).
The eigenvalues are displays in (12).
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Regalado-Méndez, A., Romero, R.R., Rangel, R.N., Skogestad, S. (2015). Biodiesel Production in Stirred Tank Chemical Reactors: A Numerical Simulation. In: Elleithy, K., Sobh, T. (eds) New Trends in Networking, Computing, E-learning, Systems Sciences, and Engineering. Lecture Notes in Electrical Engineering, vol 312. Springer, Cham. https://doi.org/10.1007/978-3-319-06764-3_14
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