Theory part:
What are the conditions under which a surge analysis of a
piping becomes necessary? What is the basis of surge analysis? What are we
checking and trying to achieve by doing surge analysis of a piping section or a
piping system?
Coming to the practical case:
There is an existing fire water piping network in the plant.
We are installing new equipments as part of the plant expansion and the new
equipment also needs fire protection piping with spray nozzles all around. For
this we are taking a tapping out of existing fire water header pipe and
installing a deluge valve skid and with some butterfly valves, installing the
spray nozzles. Valves will be in open position and the line will always be in
pressurized condition. Does this line require a surge analysis and why?
Piping Material: GRP
Test Pressure: 27 Barg
We are not installing any pumps or surge vessels and any
other pulsating equipment to foresee any surge problems. Does this typically
falls under a piping engineer's scope or a process engineer need to look at
this?
Thanks for bearing with my long questions.