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Alright @iain/hsm here's the thread.
This thread is specific to a pair of Rix SA6's that I'm building.
A few important notes and history
Things that I want Iain's opinions on.
This thread is specific to a pair of Rix SA6's that I'm building.
A few important notes and history
- These are older military compressors that were in bad shape and I'm fully rebuilding.
- Both compressors are going to be slowed WAY down. I have bank bottles, so I have no need for it to run at 6cfm to directly fill bottles. Slower speeds also means less power consumption when travelling or modifying the garage power supply.
- Compressor #1 is going to be run with a 1.5hp, 220vac 3p motor using an inverter VFD to be able to run off of a standard 110v power outlet in the US.
- Compressor #2 is going to be run with a 3hp, 220vac, 3p motor using a standard VFD to run off of a standard 220v dryer outlet.
- Both VFD's are going to be set in constant current mode so they will slow down as the pressure goes up to keep stable power consumption when travelling.
- Both compressors will have their stock fans removed and replaced with electric fans. This will provide continuous cooling at full speed since they are running considerably slower than their design parameters and since heat buildup is of serious concern since they are officially only rated for 30mins duty cycle.
- Both compressors will have nitrox sticks using 2" Koflo static mixers part number 2-40C-4-12-2. Shutoff solenoids will be tied to the VFD.
- Both compressors will have auxiliary filtration both for coalescing and filtration. The military didn't care about dew point since they were using AL bottles, but these are going into steel banks and steel bottles, so the condensers on the stock pumps are woefully inadequate. Not knowing the age and history of the condensers, I'm just not going to use them. Will replace with new units from Parker to get to Grade D air, then put a hyperfilter on there for CO to CO2 conversion and CO2 removal.
- 2nd and 3rd stage will have Water Separators with auto-drains
- After the 3rd stage WS, there will be a 1um coalescer, then a pair of .01um coalscers, then an adsorber.
- After all of that will be a hyperfilter to convert any CO that's in the area to CO2 then scrub it. I know the Rix won't generate any CO, but you never know what's in the air around you.
Things that I want Iain's opinions on.
- Intake filter
- I was planning on using a Solberg since they're readily available and about the only option for aftermarket silencer/filter combo's. You don't seem to like them since they're metal, but for indoor environment how much of a risk is there?
- Modifications to make this reliable at 3000-4500psi.
- The engineers at Rix seem to have a 30 minute duty cycle in their mind and that the sales guys only increased the OPV pressures when they increased the pressures from 3000 to 5000. I am pretty sure there should be something done for balancing to get it to behave that high.
- Want to run at 3000 minimum since that's what the banks are going to be run at, but more importantly I want the coalescer PMV at 3000psi minimum for dew point since it is going to be filling steel bank bottles. Since the original pressure was 1500psi, it leads me to believe that the balance pressure is lower than 3000. I understand it's more work to keep it at that pressure, but the filters are happier, coalescers are happier, and my bottles will be happier with drier air.
- Cylinder temperature and pressure monitoring.
- Want to have interstage pressure monitoring to be able to cut the compressor off if any stage goes above setpoint. Per Rix, at 4500psi outlet pressure, that's 100psi on the first stage and 620 on the second stage. Likely set a 120/650psi cutoff. Final output obviously being the 4500psi that the banks are going to be filled to. May lower that to 4000psi or so if there is any good reason to.
- Rix recommended 450f temperature cutoff. We consider 400f the max operating temperature for PTFE in industrial applications since that is where initial degradation occurs. I will likely set the cylinder temperature cutoff around 370f. I will likely have air temp monitoring in all cylinders by replacing the plug with a T so I can get pressure and temperature at the heads, and then since I have a 4th input on the controller, I'll put a surface probe near the bearings to keep the grease from getting too hot and running out.
- EAN50 pumping
- Since this is going to be used for technical diving, it would be ideal if it could pump EAN50. I know you've modified these things for oxygen use, and that would be ideal, but what should be done with a max speed of 800rpm to pump EAN50?