GASES AND VAPOUR MIXTURES 419dharm
\M-therm\Th9-1.pm5Fig. 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&ipii.e., T =Σ
Σmc T
mci pii
i pi...(9.28)
Also, Cp = Mcp and M = m/n
∴ nCp = mcpHence, T =Σ
ΣnC T
nCi 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
TVessel
(evocuated)p
TpatTg
T(1–x)kg
waterxkg
Vapour(i)(ii)(iii)
Fig. 9.5