Can any one provide me the information about running of the well heads without the process scale inhibitor pumps for a shorter duration? I need to decide on the SIL level of the system instrumentation. Thanks in advance.
Scale must be due to Ca, Mg, Ba salts in the water phase ?
Any PSVs' on this facility - can they or the PSV inlet lines get blocked with scale ?
Some mitigation possible if you have penultimate high pressure trip protection
Thanks for the reply. Yes we have the PSV facility and also a PSHH trip. But the point is, how fast this system should be started back after rectifying the scale inhibition pumping system ?