I perhaps should have worded my initial post better. I was hoping to find written documentation or an example from someone of a fracture control program already implemented.
The fluid is propane (C3) that is to be transferred between plants at a design pressure of 35 Bar.
There is a redundant...
Hi guys
Thanks for the responses.
The minimum design temperature for the line is -5C. However there is the risk when de-energising the line of adiabatic flash.
I'm familiar with the methods and requirements of testing, it was the term "fracture control program" that bothered me as I...
Hi
I'm writing a report to reinstate a redundant pipeline.. During process studies it has been concluded that the material could experience a minimum design temperature of -42C if the piping is subject to adiabatic flash at atmospheric pressure, this is the fluid boiling at atmospheric pressure...