Hi Friends,
In earlier posts, we have already discussed about the Desilication in Bayer process and Design of agitators for Pre-desilication tanks. Thus, It is essential to have the fair idea about the particle size distribution, percentage solids, density of particle and viscosity of ground Bauxite slurry as product of grinding circuit. Such process and operating data may not be available in any published documents. As such the granulometry of Bauxite slurry varies widely for different Alumina refineries but given data are adequate for taking up initial design work of the plant
Previously, we have already discussed in detail the methodology to work out the motor rating of agitator for a typical pre-desilication tank. In present post, we are presenting the typical granulometry of bauxite particles in slurry fed to desilication tanks as given below-
Particle size distribution as percentage in slurry on weight basis
Particle size distribution as percentage in slurry on weight basis
Mesh Size (BS)
|
Typical
|
Range
|
+10 Mesh
|
1
|
0-2
|
-10 + 12 Mesh
|
2
|
1-3
|
-12 + 14 Mesh
|
2
|
1-3
|
-14 + 16 Mesh
|
6
|
5-7
|
-16 + 30 Mesh
|
18
|
16-20
|
-30 + 85 Mesh
|
13
|
10-15
|
-85 + 100 Mesh
|
3
|
2-5
|
-100 + 200 Mesh
|
12
|
10-15
|
-200 Mesh
|
43
|
41-45
|
Such reliable data / information are rarely available in any published literature as it has been presented as outcome of personal experience in the related field.
Trust, all concerned individuals will find this information very useful for design of agitator for Desilication tanks and meeting related process requirements for selection of slurry transfer pumps. Please put your views / suggestions / remarks / comments, if any.
Regards.
Kunwar Rajendra
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