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The Compleat Distiller

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THE COMPLEAT DISTILLER 111<br />

2)<br />

Vapor now reaching condenser is N - (Nd - rd) = N - Nd + rd<br />

Cooled distillate reaching buffer is N - Nd + rd - r<br />

Rising vapor condensed in buffer is (N - Nd + rd - r)d<br />

Reflux ratio R = [(N - Nd + rd - r) + (Nd - Nd 2 + rd 2 - rd)] / N<br />

= [N - r - Nd 2 + rd 2 ] / N<br />

= [N - r ]÷N - [(N - r)d 2 ] / N<br />

3)<br />

Vapor now reaching condenser is N - (N - Nd + rd - r)d = N - Nd + Nd 2 - rd 2 + rd<br />

Cooled distillate reaching buffer is N - Nd + Nd 2 - rd 2 + rd - r<br />

Amount condensed by this is (N - Nd + Nd 2 - rd 2 + rd - r)d<br />

Reflux ratio R = [N - Nd + Nd 2 - rd 2 + rd - r] + [Nd - Nd 2 + Nd 3 - rd 3 + rd 2 - rd]<br />

= [N - r +Nd 3 - rd 3 ] / N<br />

= [N - r]÷N + [(N - r)d 3 ] / N<br />

etc etc etc<br />

Summary:<br />

Reflux ratio is<br />

1. [N - r]÷N + [(N - r)d] / N<br />

2. [N - r ]÷N - [(N - r)d 2 ] / N<br />

3. [N - r ]÷N + [(N - r)d 3 ] / N<br />

........................<br />

n. [N - r ]÷N - (-1) n [(N - r)d n ] / N<br />

Once again, since d < 1, then this is a converging series with limit [N - r] / N<br />

<strong>The</strong> reflux oscillates around a mean of [N - r], and this is a rapidly damped oscillation and stable as<br />

before.<br />

This shows that the system exhibits damped oscillation should a sudden change in cooling be imposed,<br />

but rapidly settles down to the "default" reflux ratio that would exist should no cooling occur. It also<br />

shows that this occurs no matter how severe the initial cooling may be, large oscillations taking only a<br />

little more time to damp out.<br />

<strong>The</strong>y were wrong!<br />

A compound column is inherently stable in respect of the temperature of the reflux returned by the<br />

head condenser, so no special precautions need be taken to control the flow of coolant in that<br />

condenser, other than keeping it steady at a rate that ensures complete condensation of all vapor<br />

reaching it. Many people have spent needless hours worrying and struggling to design systems that<br />

avoid cooling the condensate, and all the time they were pursuing the wrong goal. Some time spent up<br />

front studying theory can save many hours of fruitless toil.<br />

(If you’re using Cooling or Vapor Management (Chapter 4) to control reflux, then of course you don’t<br />

want complete condensation, but the key point is that the stability of the system ensures that whatever<br />

reflux ratio you do impose will remain constant.

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