Problem of calculated pressure drop in LNG liquefaction cryogenic tank process
Thread Content
When performing calculations for the LNG liquefaction cryogenic tank process, how should the pressure drop be set? What factors need to be considered when determining the magnitude of this pressure drop? I see that for the designs we’ve done here, there are those with a high-pressure section of 30 kPa, and those with 15 kPa. I would appreciate the advice from those who are more experienced!
In my opinion, the pressure drop is related to the medium and channel resistance~