LOCAL MEASUREMENTS OF FLUID AND PARTICLE VELOCITIES IN A STIRRED SUSPENSION

Citation
P. Guiraud et al., LOCAL MEASUREMENTS OF FLUID AND PARTICLE VELOCITIES IN A STIRRED SUSPENSION, Chemical engineering journal, 68(2-3), 1997, pp. 75-86
Citations number
29
Volume
68
Issue
2-3
Year of publication
1997
Pages
75 - 86
Database
ISI
SICI code
Abstract
An experimental approach is proposed for the measurement of the local behaviour of continuous and dispersed phases in a stirred suspension a t low particle concentrations (0.5 vol.%). The basic principle involve s the simultaneous measurement of the local velocity and particle size with a phase Doppler velocimeter and the separation of the data obtai ned from large particles (representing the dispersed phase) and very s mall particles (representing the motion of the continuous liquid phase ). This technique was applied to the investigation of a fully baffled cylindrical vessel, with a flat bottom, stirred by an industrial axial propeller. The diameters of the vessel and the propeller and the vert ical clearance were 0.3 m, 0.14 m and 0.1 m respectively. The liquid w as water and spherical glass particles were used as the dispersed phas e. In the absence of particles, the circulation pattern created by the propeller in the middle plane between two baffles revealed a major ci rculation loop in the lower part of the vessel and a minor contra-rota tive loop in the wall surface corner. The calculated pumping coefficie nt, circulation flow number, non-dimensional time of renewal and circu lation time were 0.62, 0.89, 11.76 and 8.15 respectively. The tangenti al velocities remained at values of less than 15% of the impeller tip velocity in the plane of the measurements. Axial, radial and tangentia l mean and root-mean-square velocities for the carrier liquid phase an d particles were measured in the two-phase flow, using particles with a mean diameter of 253 mu m. These measurements showed that the partic les lagged behind the liquid phase in the upward parts of the flow fie ld, but were ahead in some downward parts. The root-mean-square axial velocities obtained for the particles were always greater than these o btained for the continuous phase. Non-homogeneities in the suspension were observed by the local mean diameter field. The effects of the sti rring rate and size of the particles were also checked in tile upward part of the flow in the vessel. (C) 1997 Elsevier Science S.A.