LH2 Cryogenic SS Pressure Vessel Question
LH2 Cryogenic SS Pressure Vessel Question
(OP)
I am running code calculations on Compress Software and have a set MDMT by the customer of -423 deg F. I set the Charpy test temperature at -300F and all of the components pass calculations, except nozzle piping. Nozzle piping is being limited to -300F according to the code and I can't figure out how to reduce piping MDMT. Does anybody have any ideas how I can reduce the nozzle piping to the required -423F MDMT?
Thanks
Thanks





RE: LH2 Cryogenic SS Pressure Vessel Question
Second, after having done that, if you still need help here, post a detailed question containing such things as Code of construction, alloy(s) involved, product forms, etc. etc.
Your last question? Impact test is an option.
Regards,
Mike
The problem with sloppy work is that the supply FAR EXCEEDS the demand