What do you call a volumetric pump? is it a positive-displacement type pump?
If so (i.e. pump curve quasi-vertical), then safety valve should be installed at the pump discharge.
This is because in case of blocked outlet scenario (no flow = no frictionnal pressure drop), the pump developped pressure will increase until it overcomes the pressure drop for which it has been designed. Indeed, this type of pump is not dead-headed like a centrifugal pump.
I propose:
- Set pressure = 10 barg
- Relieving floware can be assumed equal to the rated flowrate of the pump.
"We don't believe things because they are true, things are true because we believe them."