H2S is being absorbed in a gas absorber unit. The height of the transfer
unit based on the overall mass transfer coefficient on the gas side is 0.4 m.
The equilibrium data is given by, y = 1.5 x. The bulk concentration of H2S
has to be reduced from 0.05 to 0.001 mole fraction in the gas side. The
height of the tower (in metres) corresponding to an operating line given by,
y = 5x + 0.001 is
(A) 2.0
(B) 1.56
(C) 1.0