Feed gas: 150m3/h,200C;1.1bar⟹G1=150∗293273∗1.0131.1∗22.41
Inlet SO2 conc,y1=0.03∗Gs=6.775(1−0.03)=6.572hkmol
= 0.1930 kmol/ k ; SO2 leaving = 0.0102 kmol/h
⟹y2=0.0102+6.5720.0102=0.00155Liquid rate=1.4kmol/h=Ls=L2x1=0.1930+1.40.1930=0.1212;x2=0(feed liquid SO2−free))
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