or any system that uses a single circ to try to cover various, ever-cheanging loads. like 3 way thermostatics, etc.
With a fixed speed circ you chose the pump that matches your system requirements, typically at design day with all loads calling. You try to select a circ to work on the "knee" or middle third of it's curve. Typically that is the highest efficiency point of the circ.
The red line is the pump curve from the manufacturer. The blue lines are from a system curve overlay sheet, or calculated on the HDS program. where the system curve touches the pump curve is the actual operating point. There is no such thing a a circ with a flat curve.
Now look what happens as zone valves open and close. the pump is running all over the curve. on the high end you get high velocity, noise, and potential erosion corrosion. High pressure can squeeze by the closed zone valves and create ghost flows, overheating or un-controlled output in some zones. possibly inadequate flow through the boiler or heat source. On the low end.... slow flow, poor air removal, possible in-adequate heat distribution, and the pump running 15% or less efficiency.
A differential bypass valve can correct to a degree, but it is a parasitic valve and just sheds away pump head.
As I mentioned before the ECM variable speed delta p pumps will correct this issue, at a cost.
I am a fan of zone valved systems and most of my jobs are ZVs. Design around a flat pump curve pump, keep the loads down to where one pump can handle no more then 4 ZVs or design around a PAB pressure activated bypass.
The graph is from a 2001 article in PM Engineer by John Sigenthaler.
hr
With a fixed speed circ you chose the pump that matches your system requirements, typically at design day with all loads calling. You try to select a circ to work on the "knee" or middle third of it's curve. Typically that is the highest efficiency point of the circ.
The red line is the pump curve from the manufacturer. The blue lines are from a system curve overlay sheet, or calculated on the HDS program. where the system curve touches the pump curve is the actual operating point. There is no such thing a a circ with a flat curve.
Now look what happens as zone valves open and close. the pump is running all over the curve. on the high end you get high velocity, noise, and potential erosion corrosion. High pressure can squeeze by the closed zone valves and create ghost flows, overheating or un-controlled output in some zones. possibly inadequate flow through the boiler or heat source. On the low end.... slow flow, poor air removal, possible in-adequate heat distribution, and the pump running 15% or less efficiency.
A differential bypass valve can correct to a degree, but it is a parasitic valve and just sheds away pump head.
As I mentioned before the ECM variable speed delta p pumps will correct this issue, at a cost.
I am a fan of zone valved systems and most of my jobs are ZVs. Design around a flat pump curve pump, keep the loads down to where one pump can handle no more then 4 ZVs or design around a PAB pressure activated bypass.
The graph is from a 2001 article in PM Engineer by John Sigenthaler.
hr