higher than expected/desired return temps - turns out the loading unit pump was moving water too QUICKLY. So what was happening was that a well defined stream developed in the tank where water was flowing from the supply straight to the return which was screwing up stratification and not doing much mixing either
That would be considered "channeling".....yes?
As in when you have high flow through a resin filtration bed (demineralizer, charcoal media, etc) you can cause a channelling / tunneling effect where the flow takes the path of least resistance and moves through the filter media and does not get cleaned / purified correctly. At my work we have anion / cation resin beds that turn city water into grade A pure water for boiler makeup. Exccessive flow will cause them to die with low throughput. They usually break through on high silica before they hit the high conductivity set point. We now have an RO unit and run the demin beds as polishers. 300 Kgal instead of 30 Kgal throughput before needing a re-generation.
Back to boilers & storage.....besides pumping capacity, what about using a flow diffuser on the tank tappings? Say you have a 1" pipe from the boiler to the tank. Why not insert that pipe into the tank, drill that pipe full of holes and "shower" the top of the tank with little jets instead of a 1" stream. The same could be done with the cold "suction" from the tank to the boiler.
Simple diffuser manifold. My boilers at work:
- Dearating feed water tank is 12 psi and roughly 290 deg F
- The boiler economizer pre heats that to about 400 - ish
- So 400 ish feedwater at 130 gpm is injected to the bottom of a horizontal steam drum via a 4" by 12 foot long diffuser pipe with lots of 1/2" holes
- Steam drum temps are running about 550 and 1000 psi, this is a saturated system 1/2 water, 1/2 steam with cyclonic and chevron moisture separators on the steam outlet. That steam is then superheated to 830 deg F.