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Figure

Figure 1(A) Sieve ray with downcomer in a 30 cm diametercolumn. (B) Dual-flow tray in a 30 cm diameter column.
Figure 2Tray layouts.
Figure 3Tray operation schematic diagram.
Figure 2). However, shorter liquid S Sow path and pos-sible maldistribution of liquid and vapour streams in

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