View Full Version : Ammonia Piping Specification
Volnei
23-03-2002, 07:35 PM
I just want to know what kind of pipes you have been using for Ammonia plants with low temperatures over there. I also would like to know what's the filler welding specification that you use for welding those pipes.
It's too hard to find ASTM 333 pipes here in Brazil.
Best regards.
SIVAKUMAR
24-03-2002, 03:51 PM
ASTM 106 GRADE pipes are suitable and availble widely. Try them
Regards,
R.Sivakumar
C. Noseworthy
29-03-2002, 03:20 PM
ASTM A53 is also commonly used.
Michael Bellstedt
02-01-2003, 09:36 PM
Carefull: A 106 and A53 should not be used at low temperatures, unless sample testing to prove ductility have been done. I know that these materials are widely used for low temp nonetheless, but the practice should not be recommended. A333 is hard to come by and expensive, but for low temp work you really should be using it.
Regards
Michael
Hi, Michael:)
got me thinking when you mentioned ASTM A333 looking at our standard specs we would only us it if there was a combination of low temperature and high pressures (below -29 deg c and 4 bar pressure) otherwise either ASTM A 106 grade B or ERW API5L would be used dependant on availability and cost.
On the CO2 jobs we have been using some for of stainless steel, in this case you have very low temperatures coupled with high pressures.
My thought is we could be using stainless on more jobs as the cost isn't that great, especially on NH3 where the pipework enters areas where personell are present ie. drops into room evaporators.
regards. Andy
Michael Bellstedt
02-01-2003, 11:37 PM
Hi Andy,
yup, your approach is industry standard. But, unless my memory fails me, the pressure codes are quite explicit on this, and A333 is the preferred way to go for low temp. In Australia most contractors use Sched 80 A106 or A53 for low temp as a rule, but I have never heard of anyone actually complying with the code and doing the ductility tests that are formally required. You can get away with it, I am sure, but in this day and age of "duty of care", what would a jury say in the event of an accident that may have been the result of taking a shortcut in material selection? In my position as consultant, I make the client well aware of the implications of using lower grade steels for low temp (generally they accept the risk and go for A106, I should add).
In a way this industry approach is self fulfilling or catch 22: No one uses A333, so it is hard to come by and expensive. Therefore no one uses A333......
But I agree fully with your comments re stainless steel, especially with regard to CO2 installations.
cheers
Michael
TRONG BACH
11-04-2006, 11:46 AM
Dear Mr. Andy,
Could you give me address of website which I can download literature (documents) of guides of caculation and choise NH3 piping?
Do you have them? Pls give me?
Best Regards,
Trong Bach.
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US Iceman
11-04-2006, 04:44 PM
Here is one link where you can purchase the US version of the refrigerantion piping calculations.
http://catalog.asme.org/Codes/PrintBook/B315_2001_Refrigeration.cfm
There are others from the UK and Germany also.
The version of piping code you want to use is determined by your local code enforcement office or governmental legislation.
Any of these may show you how to determine the piping calculations, but they are not free.
Dear Mr. Andy,
Could you give me address of website which I can download literature (documents) of guides of caculation and choise NH3 piping?
Do you have them? Pls give me?
Best Regards,
Trong Bach.
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Hi Trong Bach:)
Danfoss have a program DirCal that used to be a free download, you can still get it free, but you need to email Danfoss and they post you a copy.
Its under http://ie.refrignet.danfoss.com/SW/IERA_Registration/en/index.htm?click=i_{5C40F534-276F-43EF-8FEA-4AE739C04C94}
Kind Regards. Andy:)
US Iceman
11-04-2006, 08:16 PM
I thought he was looking for pipe stress calculations? :o
Oh well, he has both now.
I thought he was looking for pipe stress calculations? :o
Oh well, he has both now.
Iceman you could be right, to be honest this is something I have not calculated in any job I have been involved with the design of. I would follow the guidlines given in BSEN378 and for ammonia the IOR guidance booklet.
Kind Regards. Andy:)
Ponca Dave
04-02-2008, 11:49 AM
A333 was talked about and introduced by Mr. Bob Berdeck in 1985 at an IIAR convention and adopted into many codes for systems below -20 F.
Since the pipe and fittings seem to be made of "unobtanium" it's hard to get a project done on time.
The alternative is to do a finite stress analysis on the system.
This is a tedious math quest. (believe me)
But software is available from Algor
It's easy to use and simple for refrig. systems.
The software is about $6,000 but well worth it.
packie81
11-02-2008, 05:41 PM
You can use A53 and A106 below -20°F as long as you "de-rate" the allowable stress in the pipe.
An example would be:
Allowable stress in A106 @ -20°F is 15,000psi
Allowable stress in A106 @ -40°F is 12,000psi
This is determined from ASME B31.5.
I use a very detailed spreadsheet to calculate the stress in the pipe caused by internal pressure, wind and earthquake.
If you can't find A333 and can't use de-rated A106/A53, try stainless steel.
Steve
hendry
15-02-2008, 07:35 PM
Hola pals, normally i would proceed to SCHEDULE pipes seamless.
BSI standards and others could provide better details.
cheers.
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