A packed tower (cross-sectional area: 0.093 m2) is filled with 25.4 mm ceramic rings and it is used for SO2 absorption from air by using pure water inlet. The entering gas contains 20 mol% SO2 and the leaving gas is mandated to contain 2 mol% SO2 before being discharged into the air. The air flow rate is 6.53 x 10-4 kgmol air/s while the water flow rate is 4.2 x 10-2 kgmol water/s. The volumetric film transfer coefficients are given by: k’y a = 0.0594 . Gy0.7 . Gx0.25 (kgmol/s.m3.mol fraction) k’x a = 0.152 . Gx0.82 (kgmol/s.m3.mol fraction) where Gy = kg total gas/s.m2 and Gx = kg total liquid/s.m2 Using the equilibrium data in table A.3-19, calculate the tower height by using K’y a. For numerical integrations, please use 2 points at the y values of 0.08 and 0.15, in addition to the ends of the columns. Please calculate the K’y a values using the approach outlined in Example 10.6.2(c) in your notes (no other approach will be accepted).
A packed tower (cross-sectional area: 0.093 m2) is filled with 25.4 mm ceramic rings and it...
A contaminant (A) is to be removed from air at 293 K and 1.013x10 Pa in a counter current packed tower which has a diameter of 0.6m. Pure water will be used as the absorbent. The inlet gas flow rate is 80 mol.ms. Under these conditions the overall capacity coefficient (K,a) is assumed to be 80 mol.ms.AY. The mole fraction of the contaminant in air should be reduced from 0.071 to 0.004. The tower will operate at 293 K. Determine...
Example The interfacial surface area per unit volume, a, in many types of pack- ing materials used in industrial towers is virtually impossible to measure. Both a and the mass-transfer coefficient depend on the physical geometry of the equipment and on the flow rates of the two contacting, immiscible streams Accordingly, they are normally correlated together as the volumetric mass- transfer coefficient, ka. Empirical equations for the volumetric coefficients must be obtained experimentally for each type of mass-transfer operation. Sherwood...