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¢ Turbulent flow is desired in most mass-
transfer operations:
1. to increase the rate of transfer per unit
area
2. to help disperse one fluid in another
3. to create more interfacial area
¢ Mass transfer to a fluid interface is often
unsteady-state type.
Mass Transfer Theories
Page 2


¢ Turbulent flow is desired in most mass-
transfer operations:
1. to increase the rate of transfer per unit
area
2. to help disperse one fluid in another
3. to create more interfacial area
¢ Mass transfer to a fluid interface is often
unsteady-state type.
Mass Transfer Theories
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢ Is defined as rate of mass transfer per unit area per
unit conc. difference.
¢k
c
is molar flux divided by conc. difference
¢k
c
has a unit of velocity in cm/s, m/s
¢ Concentration, c in moles/volume
Page 3


¢ Turbulent flow is desired in most mass-
transfer operations:
1. to increase the rate of transfer per unit
area
2. to help disperse one fluid in another
3. to create more interfacial area
¢ Mass transfer to a fluid interface is often
unsteady-state type.
Mass Transfer Theories
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢ Is defined as rate of mass transfer per unit area per
unit conc. difference.
¢k
c
is molar flux divided by conc. difference
¢k
c
has a unit of velocity in cm/s, m/s
¢ Concentration, c in moles/volume
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢k
y
in mol/area.time (mol/m
2
.s)
¢y or x are mole fractions in the vapor or liquid phase.
Page 4


¢ Turbulent flow is desired in most mass-
transfer operations:
1. to increase the rate of transfer per unit
area
2. to help disperse one fluid in another
3. to create more interfacial area
¢ Mass transfer to a fluid interface is often
unsteady-state type.
Mass Transfer Theories
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢ Is defined as rate of mass transfer per unit area per
unit conc. difference.
¢k
c
is molar flux divided by conc. difference
¢k
c
has a unit of velocity in cm/s, m/s
¢ Concentration, c in moles/volume
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢k
y
in mol/area.time (mol/m
2
.s)
¢y or x are mole fractions in the vapor or liquid phase.
Gas phase coefficient, k
g
Page 5


¢ Turbulent flow is desired in most mass-
transfer operations:
1. to increase the rate of transfer per unit
area
2. to help disperse one fluid in another
3. to create more interfacial area
¢ Mass transfer to a fluid interface is often
unsteady-state type.
Mass Transfer Theories
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢ Is defined as rate of mass transfer per unit area per
unit conc. difference.
¢k
c
is molar flux divided by conc. difference
¢k
c
has a unit of velocity in cm/s, m/s
¢ Concentration, c in moles/volume
MASSTRANSFERTHEORIES
Mass transfer coefficient, k
¢k
y
in mol/area.time (mol/m
2
.s)
¢y or x are mole fractions in the vapor or liquid phase.
Gas phase coefficient, k
g
MASS TRANSFER THEORIES MASS TRANSFER THEORIES
There are three types of theories in mass transfer
coefficients.
1) Film theories
2) Penetration theories
3) Surface –renewal theories
Read More
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FAQs on PPT - Mass Transfer Theories - Mass Transfer - Chemical Engineering

1. What are the different mass transfer theories in chemical engineering?
Ans. The different mass transfer theories in chemical engineering include diffusion, convection, and dispersion. Diffusion refers to the movement of molecules from an area of high concentration to an area of low concentration. Convection involves the transfer of mass by the movement of a fluid, such as through convection currents. Dispersion refers to the spreading out of a substance due to mechanical mixing or turbulence.
2. How does diffusion affect mass transfer in chemical engineering?
Ans. Diffusion plays a crucial role in mass transfer in chemical engineering. It is the primary mechanism by which molecules are transported from one location to another. Diffusion occurs due to the random motion of molecules and is influenced by factors such as concentration gradients, temperature, and the size of the molecules involved. Understanding diffusion is essential for designing efficient separation processes in chemical engineering.
3. What is the significance of convection in mass transfer?
Ans. Convection is significant in mass transfer as it enhances the rate of transfer by providing bulk movement of the fluid. It is particularly important in situations where the concentration gradients are small or when the diffusivity is low. Convection can occur through natural (e.g., buoyancy-driven) or forced (e.g., pumping) means. By combining convection with diffusion, engineers can achieve faster and more efficient mass transfer processes.
4. How does dispersion impact mass transfer efficiency?
Ans. Dispersion has a significant impact on mass transfer efficiency in chemical engineering. It refers to the spreading out or mixing of a substance due to mechanical mixing or turbulence. In mass transfer processes, dispersion can lead to increased contact between phases, facilitating mass transfer. However, excessive dispersion can also result in lower efficiency, as it may cause the undesired mixing of components or dilution of the desired product.
5. How can mass transfer theories be applied in practical applications?
Ans. Mass transfer theories find wide application in various practical scenarios in chemical engineering. They are employed in the design and optimization of separation processes such as distillation, absorption, and extraction. Mass transfer theories also play a crucial role in understanding and controlling chemical reactions, as they determine the rate at which reactants come into contact and react. Additionally, they are used in the design of reactors, membranes, and other equipment involved in mass transfer processes.
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