cheapsx said:
Seems as most diaphragm type tanks accept about 65% of their total volume. If you use a non diaphragm type tank does the same hold true for acceptance volume for that type of tank or is there a rule of thumb for using that type of tank?.
Most references distinguish between diaphragm tanks and simple closed tanks by assuming that the simple closed tank will start out a 0 psig and the diaphragm tank will start out at some pre-charged pressure equal to the static water column pressure at the elevation of the tank plus at least 4 or 5 psi, which is the minimum system pressure at the elevation of the expansion tank.
So the diaphragm tank won't start accepting any water until there is some heat expansion because it is already pre-charged at the minimum system pressure. But the simple closed tank will accept water until the air inside is compressed to the minimum system pressure, and only then can it begin to accept operational expansion.
If the simple closed tank starts out at 0 psig, the required tank size can be much larger than a membrane tank that is pre-charged, especially if the tank elevation is low in a tall system.
However what the old-timers taught me was that you want to pre-charge a simple closed tank by filling the system and then pumping air into the tank and bleed off water until the water level in the tank is down near the bottom. From then on you just need to keep an eye on it, and the tank needs to be isolated with a valve if opening the system could allow air in the tank to blow back through the system. Thus the minimum size of a pre-charged simple closed tank can approach that of a diaphragm tank.
But this kind of fussing about is from an era where getting the expansion tank charge just right and then keeping an eye on it was just one more task in tending to heating systems that generally required more on-going maintenance, and may not be worth it these days of hands-off trouble-free operation if simply getting a bigger tank is doable.
The only rule of thumb is that the most expansion you can see from 40 or 50 degF up to 210 degF or so is 4% of system volume. Otherwise the size of the tank depends on pre-charge pressure, system height, tank elevation, and maximum pressure at the boiler. The formulas aren't hard, but you need to have all the parameters for a given situation:
(broken link removed to http://www.amtrol.com/enginhandbook.htm)
Also other than height affecting pressure does it matter where the tank is connected to the system? Is it better to do it at the storage or the boiler? In my set up at the boiler would be better so all pumps are pumping away from the expansion tank
For a membrane tank you want the tank connection to be strictly downhill and below the point where it connects to the system such that no air from the system can accumulate below the diaphragm and cause corrosion inside. The tank can still be at any elevation in the system, it's just that the pipe that tees off to the tank needs to run vertically and/or downhill so air bubbles won't travel into the tank.
For a simple closed tank the traditional systems provide a way of insuring that all dissolved gases released by the post-boiler separator are fed to the top of the expansion tank, and therefore the expansion tank is normally above where the line tees off to it.
Notwithstanding all the dire warnings you will encounter as regards 'pumping away', if the storage is adjacent to the boiler, and if the pipes 1.25" or so such that there's only three of four feet of head across the pump, and if the system pressure is 15 psig or so at the boiler, if you ask me it doesn't much matter where the expansion tank is connected in the boiler-to-storage-and-back circuit, but most will tell you it is impossible for this to be correct.
YMMV --ewd