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Stagnation properties

Up until this point, we have exclusively referred to static properties, which are measured as though we are moving along with the fluid.

A useful concept is the stagnation state, which is a reference state associated with the fluid being brought to rest and at zero potential, isentropically, and with no work done. This means that there is no energy exchange with surroundings (Q=W=0Q = W = 0, and dSe=0dS_e = 0), there are no losses (dSi=0dS_i = 0).

Stagnation enthalpy

We can apply the energy equation from any point in the flow a to the stagnation reference point b:

ha+Va22+gza+q=hb+Vb22+gzb+wshb=ha+Va22+gza\begin{gather*} h_a + \frac{V_a^2}{2} + g z_a + q = h_b + \frac{V_b^2}{2} + g z_b + w_s \\ \rightarrow h_b = h_a + \frac{V_a^2}{2} + g z_a \end{gather*}

and thus we can define the stagnation enthlapy, or total enthalpy, as

ht=h+V22+gz  .h_t = h + \frac{V^2}{2} + g z \;.

The one-dimensional steady energy equation can then be written as

ht1+q=ht2+ws  ,h_{t1} + q = h_{t2} + w_s \;,

or δq=δws+dht\delta q = \delta w_s + d h_t.

Stagnation pressure

We can also consider a stagnation pressure, which is the pressure at the stagnation state. Applying our property relationship to the stagnation state:

Tds=dhvdpTtdst=dhtvtdpt  ,\begin{gather*} T \, ds = dh - v \, dp \\ \rightarrow T_t \, ds_t = d h_t - v_t \, d p_t \;, \end{gather*}

where dst=ds=dse+dsid s_t = ds = ds_e + ds_i, since the stagnation process is isentropic. We can combine this with the (stagnation) energy equation:

Tt(dse+dsi)=dhtvtdptδq=δws+dhtδq=δws+Tt(dse+dsi)+vtdptdptρt+dse(TtT)+Ttdsi+δws=0  ,\begin{gather*} T_t \left( ds_e + ds_i \right) = dh_t - v_t \, dp_t \\ \delta q = \delta w_s + d h_t \\ \delta q = \delta w_s + T_t \left( ds_e + ds_i \right) + v_t \, dp_t \\ \rightarrow \frac{dp_t}{\rho_t} + ds_e (T_t - T) + T_t \, ds_i + \delta w_s = 0 \;, \end{gather*}

which is the stagnation pressure-energy equation.

This looks complicated, but tells us something useful. If we consider a process with no shaft work (δws=0\delta w_s = 0), no heat transfer (δq=0\delta q = 0), and no losses (dsi=0ds_i = 0), then

dptρt=0=dpt  ,\frac{d p_t}{\rho_t} = 0 = d p_t \;,

or stagnation pressure is constant.

Losses will be present in most real systems, and so the more realistic version of this equation is

dptρt+Ttdsi=0\frac{d p_t}{\rho_t} + T_t \, ds_i = 0 \,

which shows us that losses cause the stagnation pressure to decrease (since dsi>0ds_i > 0).