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Mohammad Zia Ullah
Department of Chemical and Polymer Engineering
University of Engineering and Technology , Lahore(Fsd
Campus)
muhammadzia7272@gmail.com
• To obtain
overall mass transfer coefficient
height of a transfer coefficient
• Based on experimental data obtained from certain
arrangements and then generalized for all systems.
• This experimental data for O2-H2O with ceramic rings
shown in fig.
• Relationship between Hox and Gx(liq mass velocity)
changes with dia of rings
• For ½ inch rings:
Hx α Gxⁿ n=0.4
• For larger rings:
Hx α Gxⁿ n=0.2
• At high mass velocities Hx is nearly proportional to the
Gx.
• The liquid film resistance for other systems can be
calculated by correcting differences in diffusivity and
viscosity.
• The relation is
• Where ‘α’ and ‘n’ are empirical constants
given in literature for different packing types.
• The exponent 0.5 on schmidt number is obtained from
penetration theory.
• ‘n’ varies with packing size and packing type but typical
value is taken 0.3.
• Molecular weight have no net effect on coefficient.
• The coefficient mainly depends upon flow rate, diffusivity
and viscosity.

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Mass transfer coeeficients

  • 1.
  • 2. Mohammad Zia Ullah Department of Chemical and Polymer Engineering University of Engineering and Technology , Lahore(Fsd Campus) muhammadzia7272@gmail.com
  • 3. • To obtain overall mass transfer coefficient height of a transfer coefficient • Based on experimental data obtained from certain arrangements and then generalized for all systems.
  • 4.
  • 5. • This experimental data for O2-H2O with ceramic rings shown in fig. • Relationship between Hox and Gx(liq mass velocity) changes with dia of rings • For ½ inch rings: Hx α Gxⁿ n=0.4 • For larger rings: Hx α Gxⁿ n=0.2
  • 6. • At high mass velocities Hx is nearly proportional to the Gx. • The liquid film resistance for other systems can be calculated by correcting differences in diffusivity and viscosity. • The relation is
  • 7. • Where ‘α’ and ‘n’ are empirical constants given in literature for different packing types. • The exponent 0.5 on schmidt number is obtained from penetration theory. • ‘n’ varies with packing size and packing type but typical value is taken 0.3.
  • 8. • Molecular weight have no net effect on coefficient. • The coefficient mainly depends upon flow rate, diffusivity and viscosity.