%0 Generic %A Peters, Frank %A Kuipers, Hans %A Munck, de, Martijn %A Dullemond, Mark %D 2023 %T Matlab fig files for the paper 'Experimental gas-fluidized bed drying study on the segregation and mixing dynamics for binary and ternary solids' %U %R 10.4121/b5001ef2-b2f4-4535-92aa-f3988914b22e.v2 %K Fluidized bed drying %K Particle image velocimetry %K Infrared thermography %K Particle temperature distribution %K Solids volume fluxes %K Segregation and mixing %K Machine learning %X

This is a set of Matlab .fig files corresponding to the figures in the paper 'Experimental gas-fluidized bed drying study on the segregation and mixing dynamics for binary and ternary solids' published in Chemical Engineering Journal. In this study, experiments in a pseudo-2D fluidized bed setup were performed to obtain insight in the complex and changing bed hydrodynamics and its interplay with mass and heat transfer. The data was obtained by using a combined Particle Image Velocimetry (PIV), Digital Image Analysis (DIA) and Infrared (IR) technique. Furthermore, a machine learning algorithm was applied in order to determine the segregation and mixing dynamics.


The dataset consists of the following .fig files whereof a short description is given below:


Figure 3: Minimum fluidization velocity determination using the mean pressure drop over the bed. 

Figure 4: Precision-recall analysis


Figure 8: Segregation index based on the average height of the medium and large-sized solids.

Figure 9: Segregation index based on the average height of the medium and large-sized solids.

Figure 10 A, B, C and D: Time-averaged solids volume fluxes for the u0=0.975 m/s drying case at four different times.

Figure 11 A, B, C and D: Time-averaged solids volume fluxes for the u0=1.17 m/s drying case at four different times.

Figure 12 A, B, C and D: Time-averaged solids volume fluxes for the u0=1.365 m/s drying case at four different times.

Figure 13 A and B: Mean particle temperature and standard deviation over time for the three different superficial gas velocities.


Figure 17 A and B: Segregation indices based on the average height of the small, medium and large-sized solids.

Figure 18 A, B, C and D: Time-averaged solids volume fluxes for the u0=0.7875 m/s drying case at four different times.

Figure 19 A, B, C and D: Time-averaged solids volume fluxes for the u0=0.945 m/s drying case at four different times.

Figure 20 A, B, C and D: Time-averaged solids volume fluxes for the u0=1.1025 m/s drying case at four different times.

Figure 21 A and B: Mean particle temperature and standard deviation over time for the three different superficial gas velocities.

%I 4TU.ResearchData