GASES AND VAPOUR MIXTURES 419
dharm
\M-therm\Th9-1.pm5
Fig. 9.4
Applying steady-flow energy equation to the mixing section (neglecting changes in kinetic
and potential energy), we get
mh&&AA 11 +mhBB+ Q = mh&&AA 22 +mhBB+ W
In case of adiabatic flow : Q = 0, and also W = 0 in this case
∴ mh&&AA 11 +mhBB = mh&&AA 22 +mhBB
Also h = cpT, hence,
mc T&&ApAA+mc TBpBB = mc T mc T&&ApAB+ pB
For any number of gases this becomes
Σ mc T&ipii = T Σ mc&ipi
i.e., T =
Σ
Σ
mc T
mc
i pii
i pi
...(9.28)
Also, Cp = Mcp and M = m/n
∴ nCp = mcp
Hence, T =
Σ
Σ
nC T
nC
i pii
i pi
...(9.29)
Eqns. (9.28) and (9.29) represent one condition which must be satisfied in an adiabatic mixing
process of perfect gas in steady flow. In a particular problem some other information must be known
(e.g., specific volume or the final pressure) before a complete solution is possible.
9.7. Gas and Vapour Mixtures
Fig. 9.5 (i) shows a vessel of fixed volume which is maintained at a constant temperature. The
vessel is evacuated and the absolute pressure is therefore zero.
p=0
T
Vessel
(evocuated)
p
T
patTg
T
(1–x)kg
water
xkg
Vapour
(i)(ii)(iii)
Fig. 9.5