Where I come from (hydrocarbon processing industry), definition of design conditions is fundamental to the discipline and goes hand-in-hand with process flow and mass & energy balance development.
That's why the data on the left hand side of a line list or line designation table is "owned" by the process engineer.
To arrive at the key data, the determination of the design pressure / temperature needs to be developed. I'm not about to set out such basic principles long hand here. However, you would do well to review chapter 4 of this reference:
https://www.pdhonlin...esign P-001.pdf
that I found by web search.
If you're lucky, you can find the data in a line list or project basis of design. If not, it's possibly a case of get down to basics, understand the mechanical limitations and operating potential of the equipment involved in your process (e.g. pumps, compressors, heaters, reactors) and marry that detail together with piping standards to arrive at a sensible end point. Another port of call for guidance is API STD 521 - take a look at (7th Edition) B.3 Procedure to Calculate the Design Pressure or MAWP of Equipment Components for guidance. This could be a substantial piece of work. Difficult to offer better guidance over the web.
If anyone can offer better guidance, I'd appreciate an alternate perspective.
Edited by astro, 26 October 2020 - 04:02 AM.