Principle issues regarding the liquid level in the upper part of the tower
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This post was last edited by sxf1028102800 on 2026-3-19 11:01. A humble question: For the liquid level in the upper part of a gasoline distillation tower, if this level is currently at 50%, how can it be increased to 70%, or decreased from 50% to 20%? What factors determine these changes in the liquid level? Does the change in liquid level have an impact on others? I’m not quite understanding the principle of the liquid level at the top of the tower. Could everyone please explain it? Thank you, looking forward to your input as shown in the diagram
This is a process operation issue; change the reflux flow rate and adjust the tower temperature
There is also a liquid-receiving tray at the top of the tower, which can be used to measure the liquid level
Does the liquid level in the receiver tank affect the operation of the tower?
Is the tray a fully extracted tray or a partially extracted tray?