This material has been suggested for a valve body to service at -40F. ASME B16.34 will be used and it does not give pressure ratings below -20 F.
Does anyone know the mechanicals at -40F or have any other information on its capabilities and how to rate it at that temperature?
Thanks!!
I am designing a rectangular vessel according to App.13(in my case it is actually square). It has a flat integral head with an central round opening greater than 1/2 the shortest span. Reference to UG-39-(c)-(1) requires the head to be designed to App.14.
App.14 does not recognize the...
I have Sec II Part D 2004 and do not find Inconel 718 (N07718) nor x750 (N07750) both of which would be SB637. I am interested in bar stock.
Is this in the later editions? What I need is allowable stress at 100F and also the max temp.
Any help will really be appreciated.
Paul
In B16.34-2009 there are several Mandatory Appendices that deal with examination of castings, etc.
The only reference, in the body of the standard, to these in in paragraph 8 (Special Class Valves). However, the appendicies do not reference this and their titles contain the word, "Mandatory"...
The subject has come up about placing a flange on a valve or fitting wherein the flange has a higher class rating than the valve or fitting body.
My position is simply that this is not to be done. However, I thought that I had once seen this published in a standard, but I do not see it in...
I am considering using a disc of SB271 C95400 M02 that will require a shaft perpendicular to the disc. This is a valve application and will be the poppet or internal closure element. ASME Sec II D listed.
I can cast the entire part. Alternatively I could consider using a barstock piece to join...
What is the difference in ASTM A395 vs A536 60-45-12?
Specifically I am interested in why one over the other (irregardless of the small increase in strength). My interest is in valve or fittings. I know that A395 is very commonly used and elevated temp data is also available, but not so for...
I have compressible flow thru a 2" x 200ft pipeline,air inlet at 25 to 30 psig, outlet 2 psig.
In using the complete isothermal equation, with this DP ratio, I believe it is appropriate to use the average specific volume in the equation. (Using Crane TP410 Eq. 1-6)
Comments appreciated...