Hello all,
I am having a heat exchager with fluid on tube side at lower pressure than the fluid on shell side.
The fuild on the shell side is at 22 barg and tube is 9 barg.
For tube ruture scenario, I would like to have a ruture disk on tube side fluid outlet.
Is there any thumb rule by which we can decide to have a rupure disk for tube rupture in a heat exchanger.
Thanks in advance.
|
Rupture Disc On Heat Exchager For Tube Rupture
Started by prasad54, Apr 09 2009 06:31 AM
1 reply to this topic
Share this topic:
#1
Posted 09 April 2009 - 06:31 AM
#2
Posted 09 April 2009 - 06:59 AM
QUOTE (prasad54 @ Apr 9 2009, 03:31 AM) <{POST_SNAPBACK}>
Is there any thumb rule by which we can decide to have a rupure disk for tube rupture in a heat exchanger.
prasad,
I'm not sure precisely what you are asking. If you are meaning, "Would a rupture disk be an effective pressure relieving device (i.e. compared to a PSV)?", then I would say the answer is "yes". In fact, I think RD's are even more effective than PSV's because they are quicker acting - important in cases such as tube ruptures.
The situation you envision does present a problem, however. If we imagine a full single tube rupture occuring near the tube fluid inlet, then I can imagine that the inlet side of the channel would develop excessive pressure. It would be isolated from the RD or PSV by a reservoir of 22 barg fluid, so there could be a problem that the RD or PSV would not fully address. Perhaps other forum members more familiar with this scenario could offer additional assistance, since I don't really know how to address this issue.
Good luck,
Doug
Similar Topics
Simulating A Single Tube Heat Exchanger In Aspen HysysStarted by Guest_catia_* , Today, 07:53 AM |
|
|
||
Rate Of Heat Transfer Vs VelocityStarted by Guest_golegolegole_* , 30 Apr 2024 |
|
|
||
Overall Heat Transfer CoefficientStarted by Guest_T_bag_* , 16 Apr 2024 |
|
|
||
Rupture Disc DesignStarted by Guest_chaupradip_* , 13 Apr 2024 |
|
|
||
Specific Heat DatabaseStarted by Guest_bckesim_* , 08 Apr 2024 |
|
|