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I am trying to calculate the increase in pressure caused by liquid nitrogen at the moment it changes from liquid to vapor within a closed, constant volume at atmospheric pressure. Do I need to include the heat of vaporization? How can this be done?

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    $\begingroup$ What exactly are the initial conditions? Is the volume 100% full of liquid N2 or is there some liquid N2 and some gas and is the gas all N2 or a mixture of N2 and something else? Whatever, nothing is going to change unless you supply some heat to vaporize more of the N2. $\endgroup$ – alephzero Aug 8 '18 at 8:21
  • $\begingroup$ Volume is 100% full. Gas is all LN2. Heat is supplied to vaporize the LN2. $\endgroup$ – astroball Aug 8 '18 at 14:48
  • $\begingroup$ Welcome to engineering stack exchange! Kind of inconsistent here - either you're at closed volume, or you're at atmospheric pressure. Note, it's not an easy situation. $\endgroup$ – Mark Aug 8 '18 at 22:31
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Assume ideal gas conditions in a container at constant $T_o, V_o$. The change in pressure by adding an amount $\Delta n$ of gas is $\Delta p = \Delta n R T_o / V_o$.

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  • $\begingroup$ For delta n, would I use the density of LN2 as liquid for the initial condition, and density of LN2 as gas for the final? $\endgroup$ – astroball Aug 8 '18 at 14:52
  • $\begingroup$ No. You would use the amount of gas that evaporates. Do you know how to get that amount, or is that also an unknown? $\endgroup$ – Jeffrey J Weimer Aug 9 '18 at 14:25
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You have some assumptions, so it's important to clarify the mechanism you are describing. I'll be assuming that you are describing a container filled with LN2 at the boiling point of LN2 under 1 atmosphere of pressure. Then this container is then left out in a room temperature environment while sealed off. The end result is - your container explodes. Proving it is complicated, but you wind up at pressures that far exceed most container's withholding pressure. While I know some thermodynamics, it's not my strongest area, so this may not be technically correct, but it gets a good ballpark estimate.

We begin by considering the phase diagram of nitrogen:

Phase Diagram of Nitrogen showing critical point at 5 MPa and -150C ST Diagram of LN2

Link here and here because images are broken as I write this.

We would begin our journey at point "g" on the ST diagram. The two phases can be considered by considering a fraction x at point "h" on the diagram, at gas phase. We put a permeable barrier between the two phases and begin a set amount of heat flow into the system.

As the internal energy increases, some portion at "g" crosses the barrier into "h". The result increases in pressure and entropy. As such, we move further up the dark red lines, since each phase can cross the barrier. After enough energy, the system reaches the critical point, at top of the dark red peak. I'm not sure how to write the equations to calculate how much energy or what the time it would take, but once we reach this point, we've reached supercritical nitrogen between 20-50 bars. This difficulty is resolved easily in practical engineering via the use of a steam drum, a piece of process equipment that safely separates the phases while preventing bumping. However, advanced techniques today allow the resolution of multi-phase flow and multi-phase heat transfer.

From this point, the process would follow an isochoric process. While hard to describe using a TS diagram, a similar diagram for steam will confirm that isochoric processes gain relatively little entropy compared to the pressure they gain with a rise in temperature. Doubling the temperature nearly has a 10-fold increase in pressure. With such a significant rise, the only conclusion I can arrive at is that you would be at a pressure that would be best measured in units of GigaPascals (GPa). In short, this would most likely destroy your container.

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