erbru
Chemical
- May 23, 2015
- 27
Hi all
This is related to my thread on the vacuum pulling due to steam condensation in the atmospheric tanks.
I am trying to quantify all the possible relief scenarios
One of the cases (which I think is not decisive) is a blocked-in vent during the heating up phase (as hot water is added to cold tanks during the sanitsation).
Hot water (85°C) is added to the tank (total volume empty about 43 m3) at a rate of 5.5 m3/h. The tank pressure builds up during this period due to the increase of water in the vapour space and the expansion of the air as well. The tank can probably take only 50-100 mbar of overpressure.
What is the best way of estimating this flow?
Should I take the hot water inflow, convert it to a heat input in kJ/s (total enthalpy of water at this temperature), assume all this heat is used to vapourise water then use the latent heat of water (kJ/kg) to determine the kg/s of water vapour evacuated?
Surely I also need also to account for the increase in air pressure as the tank heats up and evacuate some of the air.
Do I use ideal gas law to calculate the mass of air to evacuate...
But the PSV will be evacuating humid air and not just air or water vapour?
Do I take psychometric charts and look at the specific volume at the start and end temperatures ...but then I need to know the rate at which the temperature is increasing and does the specific volume increase go up at higher rates at higher temperatures (yes).
Do I use empirical data on the tank temperature warming up (available from site) or just the heat input from the hot water stream all converted into increased air enthalpy (conservative).
At 50°C in the tank, without venting, the pressure is already 100 mbar above atmospheric pressure.
This is related to my thread on the vacuum pulling due to steam condensation in the atmospheric tanks.
I am trying to quantify all the possible relief scenarios
One of the cases (which I think is not decisive) is a blocked-in vent during the heating up phase (as hot water is added to cold tanks during the sanitsation).
Hot water (85°C) is added to the tank (total volume empty about 43 m3) at a rate of 5.5 m3/h. The tank pressure builds up during this period due to the increase of water in the vapour space and the expansion of the air as well. The tank can probably take only 50-100 mbar of overpressure.
What is the best way of estimating this flow?
Should I take the hot water inflow, convert it to a heat input in kJ/s (total enthalpy of water at this temperature), assume all this heat is used to vapourise water then use the latent heat of water (kJ/kg) to determine the kg/s of water vapour evacuated?
Surely I also need also to account for the increase in air pressure as the tank heats up and evacuate some of the air.
Do I use ideal gas law to calculate the mass of air to evacuate...
But the PSV will be evacuating humid air and not just air or water vapour?
Do I take psychometric charts and look at the specific volume at the start and end temperatures ...but then I need to know the rate at which the temperature is increasing and does the specific volume increase go up at higher rates at higher temperatures (yes).
Do I use empirical data on the tank temperature warming up (available from site) or just the heat input from the hot water stream all converted into increased air enthalpy (conservative).
At 50°C in the tank, without venting, the pressure is already 100 mbar above atmospheric pressure.