By combining the above derived relations and the momentum equation on the form given by (3.95), we can get an expression where the friction force is a function of Mach number only
For convenience equation (3.95) is written again here
From equation (4.198) we can get a relation that expresses the pressure derivative term, dp/p, in terms of Mach number and d(u2)/u2. Inserting this in (4.201) gives
In analogy with the heat addition process discussed in the previous section, one-dimensional flow with heat addition is a continuous process. We will derive the differential relations for one-dimensional flow with friction, which will lead to trends for supersonic and supersonic flow with friction.
Figure 4.28:Change in flow quantities due to the addition of an infinitesimal pipe segment with the length dx
Eqns. (4.206) - (4.215) are expressed as functions of du and in order to get a direct relation to the addition of friction caused by the increase in pipe length dx, the equations are rewritten so that all variable changes are functions of the entropy increase ds.
Using the differential relations above, we can get a good picture of the development of flow variables as friction is continuously added to the flow (see Figures Figure 4.29 and Figure 4.30).
Figure 4.29:Change in flow variables as friction is continuously added to a subsonic flow
Figure 4.30:Change in flow variables as friction is continuously added to a supersonic flow
Figure 4.31:The Fanno flow process illustrated in a Ts-diagram. The dashed line shows the critical temperature, T∗, the blue line is the Fanno flow process, subsonic above T∗ and supersonic below T∗. The gray lines are isobars.
Figure Figure 4.31 shows the Fanno flow process in a Ts-diagram. The dashed line represents the sonic temperature, which means that the flow states along the process line above the dashed line are subsonic flow states and the part of the line below the dashed line represents supersonic flow states. In both subsonic and supersonic flow addition of friction leads to a change in temperature in the direction towards the sonic temperature, i.e. the flow approaches sonic conditions (M=1). When the length of the pipe through which the fluid flows is equal to the length at which the flow is sonic, the flow is choked (friction choking) and further pipe length cannot be added without a change in the flow conditions. For an initially subsonic flow, a pipe longer than L∗, the change in flow conditions is analogous to the what happens for addition of heat to a subsonic flow that has reached sonic state discussed in the previous section. The inlet conditions will change such that the massflow is reduced without changing the inlet total conditions such as the pipe length is equal to L∗ for the new inlet conditions.
Figure 4.32:For friction-choked subsonic flow, further increase of the length of the pipe/duct will lead to an update of the inlet static conditions such that the massflow per unit area is changed and the length corresponding to friction choking L∗ is increased.
Figure 4.33:change of the inlet static conditions on subsonic over choking (close up)
Figure 4.34:For friction-choked supersonic flow, further increase of the length of the pipe/duct may lead to the generation of a shock inside of the pipe. The location of the shock will be such that L∗ downstream of the shock equals the remaining length of the pipe at the shock location.
For a choked supersonic flow, addition of more friction (increasing the length of the pipe such that L>L∗) may lead to the generation of a shock inside the pipe. In contrast to the one-dimensional flow with heat addition where a shock does not change q∗, L∗ is increased over a shock. The internal shock will be generated in an axial location such that L∗ downstream of the shock equals the remaining pipe length at the shock location (see Figure Figure 4.34. As more length is added to the pipe, the shock will move further and further upstream in the pipe until it stands at the pipe entrance. If the pipe is longer than L∗ after o shock standing at the inlet, the shock will move to the upstream system and the pipe flow will be subsonic and the massflow will be adjusted such that L=L∗ according to the process described for subsonic choking above.
From prvevious derivations, we know that L∗ is a function of mach number according to
by dividing both the numerator and denominator in the fractions by M2 it is easy to see that the choking length (Figure Figure 4.35) approaches a finite length for great Mach numbers and thus the upper limit for the choking length L1∗ is given by
Figure 4.35:L∗ as a function of Mach number. For high supersonic Mach numbers, the choking length approaches a finite value.
From the normal shock relations we know that the downstream Mach number approaches the finite value (γ−1)/2γ large Mach numbers and thus the choking length downstream the shock is limited to
Figure Figure 4.36 shows the development of choking length L1∗ in a supersonic flow as a function of Mach number in relation to the corresponding choking length L2∗ downstream of a normal shock generated at the same Mach number. As can be seen from the figure, a normal shock will always increase the choking length.
Figure 4.36:L∗ as a function of M1 (Mach number in station 1) for initially supersonic flow. L1∗ is the choking length corresponding to M1 and L2∗ the choking length downstream of a normal shock at station 1. A normal shock will always increase the choking length.