Italic written matter is from book written by Norman Liberman sir, Effect of Lighter components on Overhead Composition control. I have doubt in it. Can Someone guide me.
Effect of Lighter Components on Overhead Composition
Control
I noticed on my depropanizer in Texas City that the butane content of my
propane product was erratic, even though the tower top pressure and
temperature were constant. However, when I studied the lab data closely, I
noticed an interesting trend. When the ethane content of the propane
product was high, so was the butane. As the ethane content of the
depropanizer feed became erratic, so did the butane content of the propane.
But why?
The vapor leaving the top of a tower is at its dew-point temperature and
pressure. As the ethane content of a propane vapor stream flowing at its dew
point goes up, the dew-point temperature will decrease. The ethane makes
the propane more volatile. If the reflux rate is on tower-top temperature
control, the lower dew-point temperature will reduce the reflux to restore the
temperature set point. The reduced reflux flow permits more butane to be
distilled overhead.
The resulting variable butane content of the overhead product reflects not so
much a malfunction of the temperature control, but a natural variation in the
overhead ethane content. What I eventually did on my depropanizer was to
integrate the online gas chromatograph (GC) to reset the tower-top
temperature set point for ethane and butane composition. Now, with
advances in computer control, this technique has become common.
It is very clear, when the Ethane content increases in top vapor containing Propane, it is obvious that dew point temperature decreases.
Keeping top temperature of the column set value as same as before, firstly why does reflux flow gets reduced as mentioned in the paragraph, when ethane content in top vapor increases?
Can Someone help me to understand? Thank you.