Eng-Tips is the largest forum for Engineering Professionals on the Internet.

Members share and learn making Eng-Tips Forums the best source of engineering information on the Internet!

  • Congratulations dmapguru on being selected by the Eng-Tips community for having the most helpful posts in the forums last week. Way to Go!

What should be the Flange Rating for LPG / Caustinc Service ??? 2

Status
Not open for further replies.

massad

Mechanical
Joined
Jul 12, 2006
Messages
27
Location
SA
I am working on a LPG sweetening project in which I am using 2" Sch 80 pipe . The Design pressure is 16.6 barg and temperature is 60C.

My questions are :

1) I am using Carbon Steel A106 pipe . Is carbon steel is suitable for LPG / caustic service ?

2) If carbon steel is acceptaable , then what will be the flange pressure rating . According to ANSI B16.5 150# rating , A105 flange can sustain 18 barg at 60C . Is there any particular requirement that for LPG srvice flange rating should be above 150 # ?

3) Is there will be a problem in welding a 2" Sch 80 pipe with 150 # rating .

Thankyou and Reagrds
Muhammad Assad Ahmed
Mechanical Engineer
 
1.) A106 OK for LPG. Is this for sodium hydroxide or LPG?
2.) ANSI#150 is OK for your design pressure and temperature. If there is a requirement for higher pressure, then you are using an incorrect piping design specification. Apparently your piping design spec covers only systems that will be operating at <= 16.6 Barg and 60ºC. You must find out if your system has a possibility to reach higher pressures.
3.) No problem welding 2" Sch 80 to compatible materials.

Going the Big Inch! [worm]
 
For carbon steel, consider stress relieving all welds to avoig stress corrosion cracking if your NAOH concentration is around or greater than 30% by weight or if you can expect temperatures above 60C with a 30% NAOH Concentration. For lower NAOH concentrations the need to consider stress relieving decreases. For example, at 20% stress relieving should be considered for temperatures at or above 71C. The relationship isn't linear and you should also factor in non-routine temperatures, say steaming out the line for maintenance.

My reference is a Corrosion Data Survey, 5th Edition, compiled by Norman E. Hamner, National Association of Corrosion engineers, Houston, Texas, 1974.
 
Status
Not open for further replies.

Part and Inventory Search

Sponsor

Back
Top