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How To Size A Thermal Relief Valve


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#26 fallah

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Posted 31 March 2010 - 03:52 AM

JoeWong:

It is included in own API 521 5th Edition,not in its Addendum.

#27 CMA010

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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.

#28 Qalander (Chem)

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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.

#29 fallah

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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...

#30 Qalander (Chem)

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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.

#31 PinoyCan

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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:


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 Art Montemayor

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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.




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