Boilup Ratio

Also known as boilup ratio · boil up ratio · V over B · reboil ratio · vapour to bottoms ratio · reboiler boilup

VB=VBV_B = \frac{V}{B}

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The boilup ratio is the reflux ratio's counterpart at the bottom of the column: vapour raised by the reboiler divided by bottoms product drawn off beneath it. It sets the slope of the stripping operating line the way reflux sets the slope of the rectifying one, and it governs how thoroughly the light component is chased out of the liquid on its way down.

It is also where distillation's energy goes. Reflux is returned by a condenser, which rejects heat; boilup is raised by a reboiler, which supplies it, and that is the steam, the hot oil or the fired duty on the utility invoice. Distillation is commonly estimated to account for something like a tenth of global industrial energy use, and the vapour rate VV is the term responsible for essentially all of it. Anything that reduces boilup at constant separation — better feed placement, feed preheat where it helps, heat integration between columns, higher-efficiency internals — goes straight to the operating cost.

An important structural point: in a simple two-product column, boilup and reflux are not independent. Fix the feed, the feed condition, the split and the reflux, and the boilup follows from the balance around the feed stage, Vˉ=(R+1)D(1q)F\bar{V} = (R+1)D - (1-q)F. Specifying both by hand over-determines the column, and a design that does so has an inconsistency hidden in it somewhere. What is genuinely a choice is which of the two an operator manipulates: a column whose tighter specification is on the bottoms usually controls on boilup, and one whose tighter specification is overhead usually controls on reflux.

There is a hard ceiling on boilup that has nothing to do with cost. Tray hydraulics — flooding, entrainment, weeping — are governed by vapour velocity, so the vapour rate sets the column diameter and the column diameter sets the maximum vapour rate. Push a column past its flood point and separation does not merely get expensive, it collapses: liquid is carried up the column instead of flowing down, and the composition profile disappears. The operating window between weeping at the bottom end and flooding at the top is what turndown means, and it is why a column designed for one throughput may not work well at half of it.

Boilup Ratio
VB=VBV_B = \frac{V}{B}
VB
Where
  • VBV_B= Boilup ratio
  • VV= Vapour boilup rate (kg/h)
  • BB= Bottoms flow rate (kg/h)