I think as many people who find this website, I started out by looking for variable speed controls for my well pump. I am very intrigued by the use of this valve. If it performs as advertised, it would be an acceptable, simpler, and lower cost alternative to the electronic speed controls.
My questions deal with the positioning and configuration of the CSV and associated piping.
My first question, which I think I have already answered for myself is, does the valve need to be in any "up" orientation or can it be placed in any direction? It looks to me like any direction should work since the valves can be placed in the vertical well piping or in a horizontal pipe run in the house. Am I correct?
My second question is about the statement that there can not be any water uses/outlets before this valve. Is this because the valve will be damaged by reverse flow, or because the valve will not function properly in reverse flow, or because any outlet before the valve would not have the benefit of the constant pressure? I ask this because I live on a farmette and the water in the barn is run from the same well and pressure tank that the house is and the split in the line is out in the yard, probably just outside the pitless connection on the well casing. I would rather have the valve in the house so I can easily adjust it and control the pressure in the house and let the barn pressure be whatever it will be since all I use that water for is filling stock tanks for the horses and chickens. It seems to me that a simple arrangement of a bypass loop with a reverse direction check valve in it would allow the water to flow at high volumes to the barn from the house like it does now, but would allow the CSV to control the pressure in the house when water is being used in the house. If damage to the valve occurs in the reverse flow condition, a check valve before the CSV would prevent any water from flowing backward through the CSV and allow all of the reverse flow to go around the CSV through the reverse check valve in the bypass loop. There would be no issues with negative pressures anywhere in the line since once the flow stops the pressure would equalize on both sides of any or all check valves in this configuration.
Thirdly, other than the bypass loop mentioned above, would it be a good idea to install a bypass loop around and isolation valves before and after the CSV in case a problem does arise where the CSV needs to be serviced or removed so that the system does not need to be depressurized and drained to do so?
Sorry, I'm a process engineer and this is just how my mind works. I hope I didn't cause any brain trauma.
Thanks