|

How To Size A Thermal Relief Valve
Started by Plumbercs, Sep 18 2008 02:07 AM
31 replies to this topic
Share this topic:
#26
Posted 31 March 2010 - 03:52 AM
JoeWong:
It is included in own API 521 5th Edition,not in its Addendum.
It is included in own API 521 5th Edition,not in its Addendum.
#27
Posted 31 March 2010 - 10:43 AM
fallah:
But is is included in the API STD 521 5th Edition, Jan 2007 Addendum May 2008 which is published as a single document where joe is referring to.
But is is included in the API STD 521 5th Edition, Jan 2007 Addendum May 2008 which is published as a single document where joe is referring to.
#28
Posted 31 March 2010 - 12:03 PM
fallah:
Dear,
You and Joe both may be right in a way that probably the mode of access onto API site could be varying i.e. as a member or free subscriber.
As a free subscriber access could be somewhat restricted as I found early on.
Hope this helps in clarifying the issue& slightly prolonged discussion here above.
Dear,
You and Joe both may be right in a way that probably the mode of access onto API site could be varying i.e. as a member or free subscriber.
As a free subscriber access could be somewhat restricted as I found early on.
Hope this helps in clarifying the issue& slightly prolonged discussion here above.
#29
Posted 01 April 2010 - 02:17 AM
Qalander:
Contrary to your thinking, there is no problem regarding the access to standard and,...., therefore discussion to be done for better clarification...
Contrary to your thinking, there is no problem regarding the access to standard and,...., therefore discussion to be done for better clarification...
#30
Posted 01 April 2010 - 02:32 AM
fallah:
OK,
Dear fallah Thanks (I withdraw from my envisaged scenario as you clarify). Whereas I do appreciate your update & still wait for Joe's response;if any!
So that I and other forum colleagues get better/ more accurate awareness on the issue.
OK,
Dear fallah Thanks (I withdraw from my envisaged scenario as you clarify). Whereas I do appreciate your update & still wait for Joe's response;if any!
So that I and other forum colleagues get better/ more accurate awareness on the issue.
#31
Posted 26 June 2012 - 09:35 AM
Hi Guys,
I am checking if a thermal relief valve is required on the cold side of a new exchanger in case of the blocked-in condition. Isolating block valves are to be installed on the inlet & outlet lines of the cold stream to/from the exchmage. The following are the operating conditions:
Hot Side:
Cold Side:
The design pressures are based on the maximum shut-off pressure of the pumps.
My analysis is that, a thermal relief valve is not necessary because, for the cold-side pressure to reach the design pressure of 1,448 KPag during blocked-in condition, the Recycle Water must attain a temperature of 200 C. Since the Inhibited Water temperature (heating medium) is only 85 C, it is not possible for the Recycle Water to have a temperature of 200 C.
Is my analysis proper? Please comment.
Thanks.
I am checking if a thermal relief valve is required on the cold side of a new exchanger in case of the blocked-in condition. Isolating block valves are to be installed on the inlet & outlet lines of the cold stream to/from the exchmage. The following are the operating conditions:
Hot Side:
Fluid: Inhibited Water
Inlet Temperature: 85 C
Outlet Temperature: 33 C
Inlet Pressure: 370 Kpag
Design Pressure: 1,380 Kpag
Cold Side:
Fluid:Recycle Water
Inlet Temperature: 22 C
Outlet Temperature: 79 C
Inlet Pressure: 720 KPag
Design Pressure: 1,448 KPag
The design pressures are based on the maximum shut-off pressure of the pumps.
My analysis is that, a thermal relief valve is not necessary because, for the cold-side pressure to reach the design pressure of 1,448 KPag during blocked-in condition, the Recycle Water must attain a temperature of 200 C. Since the Inhibited Water temperature (heating medium) is only 85 C, it is not possible for the Recycle Water to have a temperature of 200 C.
Is my analysis proper? Please comment.
Thanks.
#32
Posted 26 June 2012 - 01:55 PM
Pinoycan:
This is an old thread that you are skyjacking. Rather than extend this thread longer than 2 pages, please cut and paste your query into a NEW THREAD on this Forum. Otherwise, this thread get confused and members find it difficult to determine who is answering what and to whom.
I will delete this post after a couple of days, giving you time to start your own new thread.
This is an old thread that you are skyjacking. Rather than extend this thread longer than 2 pages, please cut and paste your query into a NEW THREAD on this Forum. Otherwise, this thread get confused and members find it difficult to determine who is answering what and to whom.
I will delete this post after a couple of days, giving you time to start your own new thread.
Similar Topics
Check Valve FailureStarted by Guest_Falah_* , 26 Mar 2025 |
|
![]() |
||
Multiport Selector Valve (Msv)Started by Guest__1angelia23_* , 12 Mar 2025 |
|
![]() |
||
![]() Valve Cavity - Pressure Relief ValveStarted by Guest_CS10_* , 20 Feb 2025 |
|
![]() |
||
![]() Valve Cv InputsStarted by Guest_QuantumEng_* , 01 Apr 2024 |
|
![]() |
||
![]() Tube Rupture ReliefStarted by Guest_felderosfelder101021_* , 16 Jan 2025 |
|
![]() |