anapaz79
Mechanical
- Nov 21, 2012
- 12
Hi all,
I am currently working on a Thermosolar Plant where a molten salts are the fluid to be heated in order to obtain steam afterwards. This molten salt line goes up through a tower of 250 m, and as the salts solidify at high temperatures, to avoid damage on the flanges face it was decided not to use flanges. This is, the line goes up in zig-zag from the ground level, up to 250 m completely butt welded. The material of the pipe is A312 TP347H, that in order to save material costs was stratified in different schedules, since pressure shall be quite different at the bottom where the molten salts pump is located, than at the top where pressure reduces 85% aprox.
Now, my question is if we can proceed with an Initial Test Service, in lieu of an standard hydrostatic test. As per ASME B31.1 para. 137.7 (code that applies), I kind of understand that I could use this alternative, since I do not have valves or blinds to isolate the line, and obviously temporary closures are unpractical (all site works are quite complicated due to the nature of the layout of the line). Does any one have any experience on this matter? Since I really do not find any limitation in ASME B31.1 to use this testing method, other than it can't be used for Boiler External Piping (not the case).
Design conditions of the line are 40 bar of design pressure at the bottom (pump) and 593ºC.
Any repply or personal experience on this field shall be fully appreciated.
Regards!
I am currently working on a Thermosolar Plant where a molten salts are the fluid to be heated in order to obtain steam afterwards. This molten salt line goes up through a tower of 250 m, and as the salts solidify at high temperatures, to avoid damage on the flanges face it was decided not to use flanges. This is, the line goes up in zig-zag from the ground level, up to 250 m completely butt welded. The material of the pipe is A312 TP347H, that in order to save material costs was stratified in different schedules, since pressure shall be quite different at the bottom where the molten salts pump is located, than at the top where pressure reduces 85% aprox.
Now, my question is if we can proceed with an Initial Test Service, in lieu of an standard hydrostatic test. As per ASME B31.1 para. 137.7 (code that applies), I kind of understand that I could use this alternative, since I do not have valves or blinds to isolate the line, and obviously temporary closures are unpractical (all site works are quite complicated due to the nature of the layout of the line). Does any one have any experience on this matter? Since I really do not find any limitation in ASME B31.1 to use this testing method, other than it can't be used for Boiler External Piping (not the case).
Design conditions of the line are 40 bar of design pressure at the bottom (pump) and 593ºC.
Any repply or personal experience on this field shall be fully appreciated.
Regards!