1. The BPR regulator you purchased I guess was done online and you were given no advice. This is bad.
2. The model type is ideal for a specific application but has a known internal leak rate or 0.05 SCFM
3. Now your Coltri primary chemical filter tower needs also to have a check valve on its inlet side. This is essential both in having a check valve and in its position. before the chemical tower.
4. This way after switching off you can drain the water/oil separators fully and even leave them open without draining the chemical tower of its essential pressure
5. Now you know that the BPR you have chosen will continue to drain the chemical tower at the rate of 0.05 SCFM
5. Calculate or measure the internal diameter and length of the chemical tower internals to get litres volume (say 0.5 Ltrs) times this by the BPR 1800 psig pressure setting in BARG 125 Barg Then divide by the 0.05 SCFM in Litres per minute around 1.416 LPM
So 0.5 litres water capacity x 125 bar is 62.5 litres of dry gas leaking out at a rate of 1.416 Litres per minute is 46 minutes assuming P1 is at a constant 125 bar and its not so do the calculation again at all the failing P1 pressures for flow or take it a read its emptied out overnight.
Clear as mud maybe but your going to need a bigger diameter filter tower with a much larger internal diameter if your think dwell time can be confused with flow rate.
Yes that open-to-atmosphere DIN is how I received the compressor. That just wouldn't do, and is at least an external fix. As far as calculating canister size, I don't need to calculate that, I simply timed it and it drains out WAY faster than overnight. I essentially bought a useless new compressor, and am trying to meet my deadline with essential modifications to make it usable. I never expected to be able to hold pressure in the filters overnight, but from the check I added to the tanks it will. I only need it to hold for a relatively brief cooldown period. Sure, I have 3 sizes of Swagelok benders, but do I really want to disassemble a new compressor to be able to re-tube it and insert check valves where they didn't design in enough space for them the first place? Not really. These upgrades will have to be external. And yes I used the terms loosely, but the model 1310 does "maintain" backpressure.
Doing away with the manifold is not an option. That is one of my criteria, to not make and break connections at different intervals based on varying tank sizes. I don't plan to run the compressor the entire 2 to 2.5 hours at one time to fill the multiple tanks, I just want to be able to switch off the compressor
before the recommended 100 minutes, wait the 30 minute cool down period or more, then switch it back on (after unloading) without bleeding & re-charging manifold & hoses, switching out tanks, valving off tanks, etc. That is the LAST thing I'm going to do with this compressor.
I have 4 or 5 more Microbore hoses & DIN-to-#4 JIC fittings on hand, but am considering fitting each hose permanently with more of the same on/off bleed valve DINs, just without the gauges, and leave them permanently attached to those manifold fittings I capped.
There is only so much expense I'm willing to endure in order to save a few $42 media cartridges per season. I think I'm close to the point of diminishing return, if not already passed it. My order of priority though is safety, then convenience, then expense. If this compressor proves unreliable or not cost effective, I'm not against considering another model, or even another make in the future. I've said for many years, "I've never thought about my wallet when on the bottom of the ocean".