(i) Specific humidity,
W=pt−pv0.622pv=1.0312−0.02520.622×0.0252=0.01586 kg/kg of dry air
(ii) Relative humidity, ϕ=pvspv=0.05630.0252
(pvs=0.0563 bar corresponding to 350C, from steam tables)
=0.447 or 44.7 %
(iii) Vapour density:
using characteristic gas equation , we have
pvVv=mvRvTv
pv=VvmvRvTv=ρvRvTv
where ,ρv= Vapuor density, Rv= Molecular weightofH20Universal gas content=188314.3
0.0252×105=ρv×188314.3×(273+35)
ρv=8314.3×3080.0252×105×18=0.0177kg/m3
(iv)Dew point temperature;tdp: Corresponding to 0.0252 bar, from steam tables(by interpolation)
tdp=21+(22−21)×0.0264−0.02490.0252−0.0249
=21.20C
(v) Enthalpy of mixture per kg of dry air,h:
h=1.005tdb+W(2500+1.88tdb)
=1.005×35+0.01586[2500+1.88×35]
=35.175+40.69
=75.86kJ/kg of dry air
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