0
$\begingroup$

I am studying a particular throttling process (https://en.m.wikipedia.org/wiki/Isenthalpic_process, https://en.m.wikipedia.org/wiki/Joule%E2%80%93Thomson_effect): cryogenic flow going through an orifice (please see below)

enter image description here

Experimental measurements of both static upstream and downstream pressures $p_1$ and $p_2$ yield a pressure drop $\Delta P_{12} = p_1 - p_2 >0$. Same occurs with upstream and downstream temperatures $T_1$ and $T_2$ (so $\Delta T_{12} = T_1 - T_2 >0$).

I want to explain the temperature drop $\Delta T$ based on just classical thermodynamics, using the concept of enthalpy.

Taking a control volume way upstream and another downstream we have $H_u = U_u + P_uV_u$ and $H_d = U_d + P_dV_d$ respectively. Besides, I made the assumption that the volume upstream and downstream is the same given that the expansion caused by the formation of bubbles is negligible way downstream

Enthalpy is conserved so it follows that

\begin{equation*} H_1 = U_1 + P_1 V = U_2 + P_2 V = H_2 \end{equation*}

\begin{equation*} \Rightarrow \Delta U_{21} = \Delta P_{12} V \neq 0 \end{equation*}

At this stage I made another assumption: the internal energy is a function only of temperature. Hence

\begin{equation*} \Delta U_{21} = \Delta P_{12} V \neq 0 \Rightarrow \Delta T_{12} \neq 0 \end{equation*}

But here's the problem: $\Delta P_{12} V > 0$ so $\Delta U_{21} > 0$. But this cannot be, as it implies $T_{12} >0$ rather than $T_{12} < 0$.

What am I missing?

I am not taking into account the kinetic energy due to the flow, this might need to be incorporated.

$\endgroup$
5
  • 1
    $\begingroup$ You should be using a single control volume encompassing the orifice disc. The change in H from inlet to outlet of the cv should be zero for the stream. $\endgroup$ Commented Jun 30, 2022 at 13:17
  • $\begingroup$ Hi Chester. I arrived essentially at the same equation, $\Delta U_{21} = \Delta P_{12} V \neq 0$, but now 1 and 2 mean inlet and outlet of the new cv. $\endgroup$
    – JD_PM
    Commented Jun 30, 2022 at 13:43
  • $\begingroup$ U is not just a function of temperature; there is a phase change. $\endgroup$ Commented Jun 30, 2022 at 13:54
  • $\begingroup$ Let me look at $\Delta U_{21}$ in more detail. The equation I derived, $\Delta U_{21} = \Delta P_{12} V = W$ is the first law of thermodynamics for the system (given that $Q = 0$). $W$ is the work done on the cv inlet minus the work done on the cv outlet $\endgroup$
    – JD_PM
    Commented Jun 30, 2022 at 14:55
  • $\begingroup$ In other words, how can we incorporate phase change contribution to $\Delta U_{21}$ ? Latent heat? $\endgroup$
    – JD_PM
    Commented Jun 30, 2022 at 14:55

1 Answer 1

0
$\begingroup$

To analyze this change, you should work directly with enthalpy. For the exit liquid, $H_L=C_P(T_2-T_1)$. For the exit vapor, $H_V=C_P(T_2-T_1)+\lambda (P_2)$ where $\lambda$ is the heat of vaporization at P2. These are the exit enthalpies per unit mass.

So if X represents the final mass fraction vapor, $$(1-X)H_L+XH_V=0$$,together with $$T_2=T_2(P_2)$$, where $P_2$ is the equilibrium vapor pressure at temperature $T_2$.

$\endgroup$

Your Answer

By clicking “Post Your Answer”, you agree to our terms of service and acknowledge you have read our privacy policy.

Not the answer you're looking for? Browse other questions tagged or ask your own question.