robsalv
Mechanical
- Aug 8, 2002
- 311
Basically, when reviewing an existing vessel's MDMT / MAT, every part of the vessel construction is reviewed and the warmest determined MDMT sets the vessels MDMT.
That is the level 1 view. This suggests that some parts of the vessel are suitable at lower temperatures. Hold that thought.
Here is a scenario:
- Largeish tower with an inlet nozzle 1/3 the way down. There's a credible contingency where a cool stream (not a shock chill situation) could enter the tower at a few degrees below the tower's listed MDMT. The stream is a small percentage of total tower volume so warms up to general tower temperature quickly. Alarms and procedures are in place to control inlet temperature and avoid breaching MDMT.
Now I haven't done the detailed MDMT review on the tower yet, but I'm confident that the local MDMT around the inlet nozzle can be shown to be below the global MDMT, especially if one applies a level 2 analysis locally.
The fluid only enters while the plant is operational and no contingency can be thought off that the whole tower will be cooled to the inlet fluid temperature.
Sooo, is it outside the codes to set a localised MDMT lower than the global MDMT?
...I was going to put this in the code forum, but this is a practical scenario in managing pressure equipment.
I'd appreciate your time and thoughts. Thanks in advance.
Cheers
Rob
- - - - - - - - - - - - - - -
"Life! No one get's out of it alive."
"The trick is to grow up without growing old..."
That is the level 1 view. This suggests that some parts of the vessel are suitable at lower temperatures. Hold that thought.
Here is a scenario:
- Largeish tower with an inlet nozzle 1/3 the way down. There's a credible contingency where a cool stream (not a shock chill situation) could enter the tower at a few degrees below the tower's listed MDMT. The stream is a small percentage of total tower volume so warms up to general tower temperature quickly. Alarms and procedures are in place to control inlet temperature and avoid breaching MDMT.
Now I haven't done the detailed MDMT review on the tower yet, but I'm confident that the local MDMT around the inlet nozzle can be shown to be below the global MDMT, especially if one applies a level 2 analysis locally.
The fluid only enters while the plant is operational and no contingency can be thought off that the whole tower will be cooled to the inlet fluid temperature.
Sooo, is it outside the codes to set a localised MDMT lower than the global MDMT?
...I was going to put this in the code forum, but this is a practical scenario in managing pressure equipment.
I'd appreciate your time and thoughts. Thanks in advance.
Cheers
Rob
- - - - - - - - - - - - - - -
"Life! No one get's out of it alive."
"The trick is to grow up without growing old..."