stanm,
I already separate every pipe to each other. Temperature is not elevated (Design temp=150ºC)
CodeJackal,
sorry about "esquematic" some times I think in spanish.
CodeJackal,
I reviewed 1-10 but said:
"(d) Caution to the Designer. Appendix 1-7(b) design
methods are particularly applicable to large bolted flanged
nozzles in relatively thin (Di /t > 100) vessels when the
vessel nozzle flange is located close to the nozzle/shell
intersection."
So, I have to...
Hi CodeJackal,
Thank you for your comments, I found the rules 1-10 I will review it.
stanm, sorry about my explaination you are rigth it is a header (run Pipe) or in term of Section VIII it is a shell (vessel) I think is more a vessel than a header. I am not designing from the beginning, I am...
Hi everybody!
I have a case where I do not know how treat it, a reinforcement branch in piping or a reinforcement nozzle in pressure vessel?
It has a Head of 60" where go in 6 pipes (36",26",12",26", 12" and 26") and go out two pipes of 36", this head is 10 mts long.
If I use ASME 31.3, is not...
Somebody can help me, recommending an ebook, website or textbook where I can find information about this topic.
I am interested in cogeneration conected to gas turbines.
Regards,
Kenyi
If I have two identical performance pumps (same capacity, pressure, etc) only difference is one has vertical shaft and other one has horizontal shaft. If my system have enough NPSHa to satisfy NPSHr for both pumps, what other consideration I have do to select one of these pumps?
Regards
A SKF Microlog CMVA 60 is powerfull tool, you can use it but you have to make measures with sincronous time technics to separate vibrations from the ground and filter the vibration machine. Of course you must utilize a kit phase.
