3. HW. Use the same equilibrium data as in (Q1). However use and film coefficients ky=1.5103kgmolA/sm2. mol fraction and kx=2103kgmolA/s.mol fraction. Use the bulk concentration of yAG=0.3 and xAL=0.1 to calculate the interface concentrations yAi and xAi and flux NA. 4. HW. Using the same data as in (Q3), calculate the overall mass-transfer coefficient Kx and Kx, the flux, and the percent resistance in the gas film. One More Problem 5. In the absorption of component A from an air stream into an aqueous stream, the bulk composition of the two adjacent streams were analyzed to be pA,G=0.1atm and cA,L=0.25lb mole/ /ft3. The Henry's constant for this system is 0.265atm/lb mole A/ft3 of solution). The overall gas coefficient, KG=0.055lb mole A/(hft2 atm). If 57% of the total resistance of mass transfer is encountered in the gas film, determine a. The mass flux of A. b. The concentration on the liquid side of the interface cA,6 c. The gas-film coefficient kG d. The liquid-film coefficient, kL. 3. HW. Use the same equilibrium data as in (Q1). However use and film coefficients ky=1.5103kgmolA/sm2. mol fraction and kx=2103kgmolA/s.mol fraction. Use the bulk concentration of yAG=0.3 and xAL=0.1 to calculate the interface concentrations yAi and xAi and flux NA. 4. HW. Using the same data as in (Q3), calculate the overall mass-transfer coefficient Kx and Kx, the flux, and the percent resistance in the gas film. One More Problem 5. In the absorption of component A from an air stream into an aqueous stream, the bulk composition of the two adjacent streams were analyzed to be pA,G=0.1atm and cA,L=0.25lb mole/ /ft3. The Henry's constant for this system is 0.265atm/lb mole A/ft3 of solution). The overall gas coefficient, KG=0.055lb mole A/(hft2 atm). If 57% of the total resistance of mass transfer is encountered in the gas film, determine a. The mass flux of A. b. The concentration on the liquid side of the interface cA,6 c. The gas-film coefficient kG d. The liquid-film coefficient, kL