Abstract
Liquid-solid fluidisation is frequently encountered in drinking water treatment processes, for instance in seeded crystallisation softening processes. For modest superficial fluid velocities, liquid–solid fluidisation systems are generally considered to be homogeneous, as reported in literature. However, during fluidisation experiments with calcite grains, open spaces of water can be observed between the fluidised particles, even at relatively low fluid velocities. Moreover, significant heterogeneous particle–fluid patterns are detected at higher fluid velocities. Such heterogeneous behaviour can beneficially or adversely affect the chemical crystallisation efficiency. To obtain information about voids in bulk regions, complementary Computational Fluid Dynamics - Discrete Element Method (CFD-DEM) simulations were performed and compared with the experimental results for validation. Simulations were performed using different water inlet velocities and fractionised calcite granules obtained from full-scale reactors. Here, the results are analysed using the bed height, voidage and pressure drop of the system. Furthermore, images of the experiments and simulations are visually compared for the formation of voids. The simulations showed distinct differences in void fraction in the cross-section of the column. It is shown that throughout the range of considered water velocities, heterogeneous behaviour exists and cannot be neglected. The heterogeneity and onset of fluidisation behaviour obtained from the simulations and experimental observations were compared and found to agree reasonably well.
Highlights
Fluidisation characteristics were measured for calcite pellets
liquid–solid fluidised (LSF) systems are often considered to be homogeneous at modest velocities
In the experiments with calcite grains, local voids were observed at relatively low fluid velocities and significant heterogeneous particle–fluid patterns at higher fluid velocities
Summary
In the Netherlands, more than 400 million m3 water is softened annually in drinking water treatment plants employing fluidised bed pellet reactors (Hofman et al, 2007). Pellets are extracted from the reactor when a defined grain size threshold is exceeded. Larger particles will migrate to the lower region of the reactor bed and, depending on the flow conditions, a stratified bed with a certain particle size profile will evolve. In these softening reactors, sand is generally used as seeding material and calcite pellets are produced as a by-product (van Dijk and Wilms, 1991). Pure calcite can be used as seeding material, while fullgrown calcite pellets, extracted from the reactor, can be dried, grained and sieved and re-used as seeding material (Schetters et al, 2015)
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