Hello betty,
Thanks for providing a drawing (this makes it MUCH easier to answer your question).
I have some foolish assumptions before I answer your question:
1) I assume the priority of this project is propylene liquid production
2) I assume the cooling water supply is pumping at a rate to meet the thermal demands of propylene condensation
I would place the temperature controller just barely above the condensed liquid in the recycled gas condenser. This value MUST be lower than the vapour point that you wish to keep. If the temperature approaches equilibrium or is higher than the vapour point, you are now producing vapour from the liquid.
I hope this helps. Do you have any other suggestions for a different position?
Eugene