In HYSYS dynamic simulation, discussions on knowledge related to the tank module are welcome; experts are invited to engage in in-depth discussions

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1) In the Tank model within the TANK module (not Seperator and 3 phase Sep), what impact does the installation height of the nozzle have on the pressure levels of the materials entering and leaving the TANK during dynamic simulations? 2) If the material exported by TNAK is connected to a pump, does the liquid level in the tank affect the pressure at the pump inlet? (In reality, it does have an impact; it’s not clear whether the software can handle this.) 3) A low-temperature medium at atmospheric pressure: in actual production, the space above the tank should be filled with a saturated gas phase, while the liquid at the bottom of the tank is in a supercooled state. When using TANK for dynamic simulation, how are the gas phase pressure and subcooled liquid in the tank head space represented? The above issues arose during the simulation of actual operating conditions; I hope experts can discuss them in depth so that we can gain a better understanding of the software’s functions and make better use of it to conduct simulation calculations for actual production facilities! Thank you all!