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Published on: June 12, 2016
Empirical correlations for axial dispersion coefficient and Peclet number in fixed-bed columns
Seyed Omid Rastegar1, Tingyue Gu2
1Department of Engineering, Chemical Engineering Group, University of Kurdistan, Sanandaj, Iran.
A new correlation for axial dispersion coefficient in fixed-bed columns was developed. This comprehensive model incorporates molecular diffusion and bed voidage, improving accuracy over existing correlations.
Area of Science:
- Chemical Engineering
- Fluid Dynamics
- Mass Transfer
Background:
- Axial dispersion is a key parameter in fixed-bed reactors, influencing process efficiency.
- Existing correlations like Chung and Wen and De Ligny have limitations, omitting molecular diffusion or bed voidage.
- Accurate modeling of axial dispersion is crucial for optimizing packed-bed column design and operation.
Purpose of the Study:
- To develop a new, more comprehensive, and accurate correlation for the axial dispersion coefficient in fixed-bed columns.
- To address the limitations of existing empirical correlations by including molecular diffusion and bed voidage.
- To provide an improved basis for calculating the Peclet number in packed-bed systems.
Main Methods:
- Compilation and analysis of experimental data on axial dispersion from existing literature.
- Development of a new empirical correlation for the axial dispersion coefficient.
- Validation of the new correlation against experimental data and comparison with established correlations.
- Derivation of a new Peclet number correlation based on the developed axial dispersion coefficient correlation.
Main Results:
- A novel correlation for the axial dispersion coefficient was established, incorporating both molecular diffusion and bed voidage.
- The new correlation demonstrates improved accuracy and comprehensiveness compared to Chung and Wen and De Ligny correlations.
- The derived Peclet number correlation results in an average of 12% lower values than the Chung and Wen correlation.
- Significant reductions in Peclet number values were observed compared to the De Ligny correlation in many cases.
Conclusions:
- The newly developed axial dispersion coefficient correlation offers a more accurate representation of transport phenomena in fixed-bed columns.
- Incorporating molecular diffusion and bed voidage leads to a superior predictive model for packed-bed reactors.
- The findings provide enhanced tools for engineers to optimize the design and performance of fixed-bed systems.
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