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Figure 1

Principle of operation of the centrifugal air classifier
Principle of operation of the centrifugal air classifier

Figure 2

Sampling with a spoon [after 7].
Sampling with a spoon [after 7].

Figure 3

Dissolution, filtration and drying of material.
Dissolution, filtration and drying of material.

Figure 4

Sulphur and mass content for different samples.
Sulphur and mass content for different samples.

Results of an attempt to remove sulphur from filter ash by the wet procedure

Sample 5 (S5)Mass (g)Mass per cent (%)Sulphur content (%)
108.4100.03.38
Insoluble material (5I)72.566.90.56
Soluble material (5S)35.933.18.39

Classification at a cut size of 20 μm

Sample 2 (S2)Mass (g)Mass per cent (%)Sulphur content (%)
251.7100.03.38
Fine fraction (2F)128.951.23.30
Coarse fraction (2C)122.848.83.44

Classification at a cut size of 30 μm

Sample 3 (S3)Mass (g)Mass per cent (%)Sulphur content (%)
260.2100.03.38
Fine fraction (3F)195.475.13.71
Coarse fraction (3C)64.824.92.32

Classification at a cut size of 10 μm

Sample 1 (S1)Mass (g)Mass per cent (%)Sulphur content (%)
258.4100.03.38
Fine fraction (1F)56.321.80.55
Coarse fraction (1C)202.178.24.19

Density measurements with a pycnometer

Test no.Density (kg/m3)
12,445.8
22,579.5
32,539.5

Classification at a cut size of 40 μm

Sample 4 (S4)Mass (g)Mass per cent (%)Sulphur content (%)
254.0100.03.38
Fine fraction (4F)198.878.33.49
Coarse fraction (4C)55.221.72.81

Determination of operating conditions for the centrifugal air classifier using the operating diagram of the classifier

Cut size dTV (mm)RPM n (min−1)Airflow Q (m3/h)
108,90046.1
205,20049.8
304,10050.9
403,50051.5