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Devansh Aneja
Independent Researcher
India
ABSTRACT
Modeling of heat and mass transfer in packed bed reactors is central to optimizing performance in catalytic, adsorption, and reaction processes. This manuscript reviews fundamental transport phenomena governing single-phase and multiphase flows through random and structured packings, presents three industrially relevant case studies from 2000–2014, details a mathematical and numerical methodology rooted in porous-media theory, and reports simulation results validated against experimental data. Emphasis is on diffusion regimes, axial dispersion, effective thermal conductivity, and interphase transfer coefficients using correlations available up to 2014. Conclusions highlight model accuracy, limitations, and recommend directions for improved scale-up. Ten key references, all published by the end of 2014, support the analysis.
KEYWORDS
Packed bed reactors, heat transfer, mass transfer, modeling, porous media
REFERENCES
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