Gas molecular weight has an impact on compressor surge as when it reduces.
What are the factors which should be considered during an on-going site operation with continuous feed?
A surge may be linked to feed changes?

Why is it recommended to monitor the pump suction pressure during startup and not the discharge pressure?

Many modern compressor control systems include dedicated surge detection based on:
Rapid flow reversals
Pressure oscillations
High-frequency vibration
Characteristic changes in differential pressure
If surge is detected repeatedly or for a defined duration, protective action is initiated, typically ...

What is the reason that the definition of asset Integrity and process safety sometimes is used interchangeably?
In my opinion, they are having distinct funtions.

Some of the old links do not seem to be working anymore.