Calculation of liquid hydrocarbon pumps
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Recently, the liquid hydrocarbon pump has not been able to deliver the required flow rate. The inlet mixture contains a high proportion of light components, including C2 and C1 compounds. The parameters of the pump are known, as are the inlet pressure and temperature. How can one determine the maximum allowable level of these light components? I would appreciate some guidance from those with experience! Thanks in advance; just give me some ideas.
There’s no problem as long as it doesn’t vaporize at the pump inlet.
The pump inlet is not vaporized; it only has a high carrying capacity