Thank you, Brutus. That is super useful. I also saw your previous post, which answered a lot of my questions.
My idea is to fabricate a removable glass fibre tank that will fit in the forward part of the boat under the deck to collect the overflow from the condenser tank. I'll create a "take off" point near the top of the tank using a union fitting and plumb copper tube back into the fabricated collection tank.
I already have the non-return valve on order, so I will still fit it in the line to the tank.
https://www.youtube.com/watch?v=WJJe1eHWLmwIf you pause this vid at 00:15, you can see how I solved it. Better yet, scroll to 10:25~10:30, better visibility.
I replaced the "emptying cap" of the condenser/oilseparator with a teflon plug, pierced by a piece of 2 mm OD, 1 mm ID copper tubing, that runs all the way to the bottom of the condenser/oilseparator. This way, you leave the oil separator body undamaged.
There is quite a bit of velocity in that condenser, and having any significant level in there only reduces its inner working and necessitates the emptying after the run (if you don't, then the next cold start, producing between 10 and 20 ml of condensate in mere seconds, will overflow the condenser)
The thread used for that plug is M8 x 1,25 if I am not mistaken. Not a common bolt thread, but pretty good availlable as dies and taps nonetheless.
You can without a problem extend the draintube with some 2 mm ID silicon tubing to get the discharge to a tank at some distance.
There are no issues fitting a non-return valve in the feedline, but with a single feedline and no bypassvalve, it also serves no function.
If your TX allows, use a speedcontroller for the feedpump, and control it via a slave channel and a programmable curve to the steam throttle.
Assuming constant boiler pressure, the feed quantity is proportional to the throttle position. This will save you the trouble of setting up a boiler level detection system and either manually or automatically starting/stopping the pump.
A continuous feed is also better for the boiler (thermal stresses are more constant) and steam production ( no "shots" of cold water intermittently entering).
Setting up the curve is relatively easy: all it takes is 4 separate 10~15 minute runs at steady throttle position (1/4th, 1/2, 3/4th and full), and this works well enough for me to never have seen the need for a better system in 120 runhours.
I mean, if you want to adhere to the KISS principle, direct feedpump speedcontrol is AS simple as it gets... No additional servo, no additional bypass valve, no alarms or detection, all you need is the possibility for a visible confirmation of the pump functioning.