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Hydrodynamics and heat transfer of gas–solid two-phase mixtures flowing through packed beds – a review

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TLDR
In this paper, a review of the recent development in the field including both hydrodynamics and heat transfer of gas-solid two-phase mixtures flowing through packed beds is presented.
Abstract
Flow of a gas–solid two-phase mixture through a packed bed is relevant to a number of industrial processes such as heat recovery and filtration of dusty flue gases, iron making in shaft reactors, gas purification, and sorption enhanced reaction processes. In spite of the industrial relevance, little work has been reported in the literature. The limited amount of research work has mainly addressed the macroscopic hydrodynamics in terms of pressure drop and solids hold-ups at the ambient temperature. Very little is done, until fairly recent, on solids motion at the single particle level, hydrodynamics at elevated temperatures and heat transfer. This paper reviews the recent development in the field including both the hydrodynamics and heat transfer of gas–solid two-phase mixtures flowing through packed beds, which is believed to represent the state-of-the-art in the field. The review is not aimed to be exhaustive but rather focused on our own work carried out over the past few years in the Institute of Particle Science & Engineering at the University of Leeds. And some of our results are compared with that of other groups.

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Citations
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Assessment of devolatilization schemes in predicting product yields of biomass fast pyrolysis

TL;DR: In this article, three devolatilization schemes for biomass fast pyrolysis were tested and validated in a numerical model that considered the multiphase hydrodynamics and chemical reactions of biomass fast pyrrithm.
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Experimental study on heat storage and transfer characteristics of supercritical air in a rock bed

TL;DR: In this paper, the authors investigated the heat storage and heat transfer behavior of supercritical air flowing through a rock bed with the working temperature and pressure ranging up to 120°C and 6.55 MPa, respectively.
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Progress in low temperature hydrogen production with simultaneous CO2 abatement

TL;DR: In this article, a new process has been proposed and investigated for low temperature hydrogen production from hydrocarbons with simultaneous CO2 abatement, based on a concept involving simultaneous hydrogen production and CO2 removal, which uses a stationary catalyst phase and a continuously moving adsorbent phase for in situ removal of CO2 and ex situ regeneration of adsorbents.
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A review study of solid-gas sublimation flow for refrigeration: From basic mechanism to applications

TL;DR: The basic mechanisms of sublimation two-phase flows are reviewed and several representative refrigeration systems are introduced and compared in this review study, which may give useful indications for future innovations.
Journal ArticleDOI

Hydrodynamics of a packed bed of non-spherical polydisperse particles: A fully virtual approach validated by experiments

TL;DR: This work presents a numerical workflow to generate a virtual packed bed made of non-spherical polydisperse particles, and subsequently predict its permeability, and opens the door to numerical estimation of bed tortuosity, dispersion coefficients, volumetric heat exchange coefficients, and much more, using the particle size distribution as unique input data.
References
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Journal ArticleDOI

Effect of Surface Morphology on the Flow of Entrained Fine Particles by Ascending Gas through Packed Beds

TL;DR: In this paper, the authors investigated the effect of surface roughness of coal particles on the static and dynamic holdups of fine coal particles in a blast furnace, and found that the fine particles are trapped in the form of static holdup in the isolated narrow spaces bounded with packed particles, and that they remain on the surface of the packed particles which are exposed to the gas flow for only a short period of time.
Journal ArticleDOI

Gas‐solid Two‐phase Mixtures Flowing Upward through a Confined Packed Bed

TL;DR: In this paper, a continuous-based porosity model is used to simulate the flow behavior of a gas-solid two-phase mixture through a confined packed bed and the experimental results show that the model captures the main features of solids behaviour in terms of the radial distributions of the suspended particle concentration and the axial solids velocity.