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152 3. Heterogeneous Processes and Reactor Analysis
4
3
2
p
Pe
1
Edwards-Richardson
Hiby
0
0.01 0.1 1 10 100 1000
Re p * Sc
Figure 3.36 Edwards–Richardson versus Hiby’s correlation (for 0.45 and Sc 1).
10
p
1
Pe
Kubo
Edwards-Richardson
0.1
0.1 1 10 100 1000
Re p
Figure 3.37 Comparison of Edwards–Richardson and Kubo correlations (for 0.45, for liquid
Sc 1000 and for gas Sc 1).
