Design of a stirred batch reactor with scale-up to ensure efficient degumming process at a larger scale
This study investigates the design of a stirred batch reactor with scale-up for the degumming of crude palm oil (CPO) using phosphoric acid (H3PO4). Laboratory-scale experiments were conducted in a triple-neck round vessel, followed by a scale-up to a larger-scale flat-bottom stirred tank reactor....
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Main Authors: | , , , , |
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Format: | Article |
Language: | English English |
Published: |
Elsevier
2024
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Subjects: | |
Online Access: | http://irep.iium.edu.my/115224/7/115224_%20Design%20of%20a%20stirred%20batch%20reactor.pdf http://irep.iium.edu.my/115224/8/115224_%20Design%20of%20a%20stirred%20batch%20reactor_Scopus.pdf http://irep.iium.edu.my/115224/ https://www.sciencedirect.com/science/article/pii/S2590123024008430?via%3Dihub https://doi.org/10.1016/j.rineng.2024.102588 |
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Institution: | Universiti Islam Antarabangsa Malaysia |
Language: | English English |
Summary: | This study investigates the design of a stirred batch reactor with scale-up for the degumming of crude palm oil
(CPO) using phosphoric acid (H3PO4). Laboratory-scale experiments were conducted in a triple-neck round
vessel, followed by a scale-up to a larger-scale flat-bottom stirred tank reactor. Traditional scale-up methods
using geometric similarity criteria are ineffective for reactors with different geometries; hence, this work introduces
an improved approach using degumming efficiency, measured by gum concentration, as the similarity
criterion to design the reactor. Computational Fluid Dynamics (CFD) was employed to model the velocity distribution
and mass transfer processes, predicting gum concentration evolution through gum mass balances in the
oil and aqueous phases. The simulation results showed that maintaining a minimum impeller speed of 93 rpm in
the larger reactor effectively reproduced the best degumming efficiency observed in the laboratory reactor at
500 rpm and 60 ◦C. A strong correlation (R2 = 0.963) was found between the modeled and empirical Sherwood
numbers, indicating successful scale-up. This research demonstrates that degumming efficiency in a laboratory
triple-neck round vessel can be numerically reproduced in a larger flat-bottom stirred tank reactor, providing
valuable insights into the hydrodynamic characteristics unique to each geometry and marking a pivotal step in
reactor scale-up methodologies. |
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