If you are doing suction line pressure drop calcs for the purpose of getting a value for NPSHa, the term "suction line" starts at the location where the liquid last equilibrated with a vapor space - this would also mean the liquid residence time in this equipment is sufficient for the liquid to reach equilibrium with the vapor. If the liquid has flashed out some vapor in this vessel, the residence time and liquid level must also be adequate to minimise vapor phase carryunder into the pump suction line.