jtk921
Chemical
- May 10, 2005
- 18
I have a new heat exchanger with both shell and tubes 304L and rated at 150 psi @ 350 F, water on tube side, steam on shell side (ASME Section VIII, Div 1). Does the MAWP change if the operating temperature is 160 F? How can I calculate it? Is there a graph or equation? Steam will be regulated through a control valve, but max. upstream pressure is 160 psig. Would I need a PSV on the steam side if the exchanger were blocked in? If I size a PSV for thermal expansion on the tube side, would I use the saturation temperature at 150 psi?