Accurate voidage prediction in fluidisation systems for full-scale drinking water pellet softening reactors using data driven models

• Published in: Journal of water process engineering Vol. 37; p. 101481
• Main Authors: Kramer, O.J.I., de Moel, P.J., Padding, J.T., Baars, E.T., Hasadi, Y.M.F. El, Boek, E.S., van der Hoek, J.P.
• Format: Journal Article
• Language: English
• Published: Elsevier Ltd 01.10.2020
• Subjects: Data driven modelling; Drinking water treatment; Fluidised bed reactors; Full-scale water softening; Symbolic computation; Voidage prediction; Drinking water treatment; Full-scale water softening; Voidage prediction; Data driven modelling; Symbolic computation; Fluidised bed reactors
• ISSN: 2214-7144; 2214-7144
• DOI: 10.1016/j.jwpe.2020.101481

[Display omitted] •A new explicit voidage prediction model for liquid-solid fluidised bed is proposed.•Voidage prediction accuracy is improved from 11 % to 2% by combining Reynolds and Froude.•Specific surface area is of major importance in drinking water treatment processes.•Full-scale pellet softening reactors can be optimised by using superficial space velocity. In full-scale drinking water production plants in the Netherlands, central softening is widely used for reasons related to public health, client comfort, and economic and environmental benefits. Almost 500 million cubic meters of water is softened annually through seeded crystallisation in fluidised bed reactors. The societal call for a circular economy has put pressure on this treatment process to become more sustainable. By optimising relevant process conditions, the consumption of chemicals can be reduced, and raw materials reused. Optimal process conditions are feasible if the specific crystallisation surface area in the fluidised bed is large enough to support the performance of the seeded crystallisation process. To determine the specific surface area, crucial variables including voidage and particle size must be known. Numerous models can be found in the literature to estimate the voidage in liquid-solid fluidisation processes. Many of these models are based on semi-empirical porous-media-based drag relations like Ergun or semi-empirical terminal-settling based models such as Richardson-Zaki and fitted for monodisperse, almost perfectly round particles. In this study, we present new voidage prediction models based on accurate data obtained from elaborate pilot plant experiments and non-linear symbolic regression methods. The models were compared with the most popular voidage prediction models using different statistical methods. An explicit model for voidage estimation based on the dimensionless Reynolds and Froude numbers is presented here that can be used for a wide range of particle sizes, fluid velocities and temperatures and that can therefore be directly used in water treatment processes such as drinking water pellet softening. The advantage of this model is that there is no need for applying numerical solutions; therefore, it can be explicitly implemented. The prediction errors for classical models from the literature lie between 2.7 % and 11.4 %. With our new model, the voidage prediction error is reduced to 1.9 %.