Our refinery has a FW design coker with top/bottom delta valves and a 90 deg side entry inlet. Our operating procedure states that we are to:
[quote]”…..1) steam purge at 20,000 #/hr for 35 minutes and then 2) reduce our steam quench to 5,000#/hr. 3) Let the quench water flow start into the drum until water hammer starts. When the quench water control valve begins to open start backing out the quench steam. (Water hammer is normal and should not harm anything. It will subside once the quench steam is closed. The two flows must be maintained momentarily to ensure the “blowhole” does not collapse. )…..[/quote]”
The problem I am having is the “normal” water hammer has caused valve bonnet gaskets to fail in our steam quench system.
Questions: 1) Is inducing water hammer really “normal” when performing the steam quench-to-water quench transition. 2) I understand the side entry nozzle causes a non-uniform coke formation in the drum (one of the negatives to our Delta Valve designed drum system). Is this the reason for the loss of a “blowhole” concern or is there another reason? 3) Has anyone else had a similar problem? If so, have you fixed it and how?
Thank you