An absorber is to be designed to remove a VOC pollutant from an exhaust gas stream. Fifteen cubic meters per minute of gas at 289 K and 1.013×105 Pa containing 5.0 mol % VOC is fed to the bottom of the absorption tower. By feeding a VOC-free solvent stream to the top of the tower, the VOC concentration is reduced to 0.3 mol %.
The solvent stream leaves the tower containing 3.65 mol % VOC. With the specified stream flow rates, the overall mass-transfer capacity coefficient, KY a, equals 52.0 mol/ s: m2. DYA. The cross-sectional area of the tower is 0.2 m2.
At 298 K, the equilibrium for the VOC-solvent system may be represented by
YA = 0.8XA.
Determine the hight of the tower.