Those steps represent the theoretical plates ( or equilibrium stages ).
2.
Close boiling mixtures may require many equilibrium stages to separate the key components.
3.
It is simply a hypothetical equilibrium stage.
4.
Hence, a distillation column needs more plates than the number of theoretical vapor liquid equilibrium stages.
5.
Hence, a distillation column needs more plates than the required number of theoretical vapor liquid equilibrium stages.
6.
The efficiency of a tray or plate is typically lower than that of a theoretical 100 % efficient equilibrium stage.
7.
The graph passes through three stages : an equilibrium stage, a single-spike stage, and a limit cycle stage.
8.
Hence, a fractionating column almost always needs more actual, physical plates than the required number of theoretical vapor liquid equilibrium stages.
9.
Equilibrium stages are ideal steps where compositions achieve vapor liquid equilibrium, repeating the separation process and allowing better separation given a reflux ratio.
10.
Just as in gas-liquid absorption, the adoption of reflux at the top of the column can engender multiple equilibrium stages within the column.
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