YungPlantEng
Chemical
- Jan 19, 2022
- 95
I have a 4” pumped condensate line tying into a 8” valve controlled condensate header with each at different temperatures. I wanted to understand if there were any heuristics or practices that allowed one to state if the cyclic thermal stresses would need to be considered based off the deltaT between the two streams. Consider both as pressurized to where the flow is single phase. See sketch for example.
Keep in mind we’ve already observed fatigue related failures in a slightly different piping arrangement under these temperature conditions. This new arrangement would tie in such that the temperature differential is greatly reduced but I wanted to see if any standards or practices would help formalize this as a solution. Couldn’t find much on thermal stresses specific to mixing points.
Keep in mind we’ve already observed fatigue related failures in a slightly different piping arrangement under these temperature conditions. This new arrangement would tie in such that the temperature differential is greatly reduced but I wanted to see if any standards or practices would help formalize this as a solution. Couldn’t find much on thermal stresses specific to mixing points.