Thanks Steve, are you implying that an impact toughness spec typically results in a heat treatment of the base metal to achieve the desired toughness value?
I think this may be the gap in my understanding. Heat treatment is only mentioned sparingly in paragraphs relating to low temperature service.
Thanks GD2, I understand MDMT selection and the purpose of Fig. 323.2.2-1. What I'm struggling with is the fundamentals of specifying a material that requires impact testing.
Why would we expect an impact-tested material to perform any better than the same material that has not been impact...
Thanks for the response.
I read that toughness testing is typically required as a part of material specs but additional testing per Table 323.2.2-1 is required to use the material below its line in Fig 323.2.2-1. What happens in this instance? Are we just *hoping* the material comes back...
I've always specified materials that don't require impact testing but I don't have a great understanding of what the practical implications would be if the testing is required (for instance if A53B is specified for use below its curve in Fig 323.2.2-1 of B31.3).
In a general sense...
Does it...
I was attempting to compare visual examination acceptance criteria between B31.1 and B31.3 and am getting tripped up by the different terminology used by each code. B31.3 seems to favor the term groove weld in Table 341.2-1 while B31.1 uses butt weld in Table 136.4.1-1.
In my experience, large...
Thanks, Table 6 was indeed helpful and we will stick with the client spec since Class W will not meet their requirements.
Just to confirm "starting material manufacturer" = "starting pipe manufacturer" = "mill" =/= "fitting manufacturer"?
We have a client specifying A403 Class WX or WU fittings and I'm trying to understand the practical difference between these options and Class W, which is what our standard spec calls out. Based upon my reading of 5.4, 5.5, and 5.6, my understanding is that:
Class W requires radiographic...
We'll be pumping ~67% emulsified sulfur from one tank into another. I've been told the viscosity can be as high as 10,000 cP however, I need the flow behavior index (n, unitless) to accurately model it in our hydraulic software.
Absent that information, are there any general guidelines (e.g...
Thanks for the responses all, unfortunately we do not have maintenance requirements or data for existing equipment. This is a conceptual life-cycle cost estimate activity. Likely the best approach will be to just apply a uniform percentage of ~5% across all equipment types, similar to the rule...
Does anyone have a good reference with rules of thumb for estimating maintenance cost requirements of various types of process equipment compared to capital cost? I have a copy of Plant Design and Economics already but I am looking for something more granular based on the type of equipment. I...
I have seen 24" listed as the maximum size for A234 WPB (seamless) fittings; beyond that they are welded (WPB-W).
Is there a standard that actually specifies this as as the breakpoint?
Additionally, their pressure ratings should both be equivalent to seamless pipe if built to B16.9 (para 2.1)...
Thanks a bunch Steve, very helpful.
I assume DWTT also produces energy values? Equations 1 and 2 in para 841.1.2 of B31.8 note the calculated CVN values as being "full size Charpy V-notch absorbed energy". That would indicate to me that these are in fact DWTT, not charpy tests. Annex G also...
I am reviewing a specification for a gas pipeline (material API 5L PSL2) with a minimum temperature of -50F. According to B31.8, this triggers Annex G of API 5L. I am really struggling to sort the actual requirements of CVN and/or DWT testing.
- My understanding is that shear area is calculated...