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G H PATEL COLLEGE OF ENGINEERING
AND TECHNOLOGY
PREPARED BY: 180110105001-HONEY AGRAWAL
180110105002-ZANKRUIT AMIN
180110105003-ANNAN PATEL
180110105004-BAPODARA PRAKASH
OUTLINES
• Introduction
• Applications
• Distillation principles
• Concept of relative volatility
• Vapour liquid equilibria
• P-x-y ,T-x-y diagram
• effect of P & T on equilibrium data
• References
INTRODUCTION
DEFINITION:
o “Distillation is an unit operation which
involves separation of a vaporizable
component from a multi-component
system and subsequent condensation of
vapours”.
o “Distillation is a process of separating the
component substances from a liquid
mixture by the selective evaporation and
condensation”.
o “Distillation ids defined as the separation
of the components of a liquid mixture by
a process involves vaporization and
subsequent condensation at another
place.”
APPLICATIONS
INTRO TO
BINARY
MIXTURE
DISTILLATION
PRINCIPLES
• Separation of components from a liquid mixture via distillation
depends on the differences in boiling points of the individual
components.
• Also, depending on the concentrations of the components
present, the liquid mixture will have different boiling point
characteristics.
• Therefore, distillation processes depends on the vapor
pressure characteristics of liquid mixtures.
VAPOUR
PRESSURE
AND
BOILING
The vapor pressure of a liquid at a particular temperature is the equilibrium
pressure exerted by molecules leaving and entering the liquid surface. Here are some
important points regarding vapor pressure:
energy input raises vapour pressure
vapor pressure is related to boiling
a liquid is said to ‘boil’ when its vapor pressure equals the surrounding pressure
the ease with which a liquid boils depends on its volatility
liquids with high vapor pressures (volatile liquids) will boil at lower temperatures
the vapor pressure and hence the boiling point of a liquid mixture depends on the
relative amounts of the components in the mixture
distillation occurs because of the differences in the volatility of the components in the
liquid mixture
Relative
Volatility
• Relative volatility is a measure of the differences in
volatility between 2 components, and hence their boiling
points. It indicates how easy or difficult a particular
separation will be. The relative volatility of component ‘I’
with respect to component ‘j’ is defined as
• Yi = mole fraction of component ‘I’ in the vapor
• xi = mole fraction of component ‘I’ in the liquid
• Thus, if the relative volatility between 2 components is
very close to one, it is an indication that they have very
similar vapor pressure characteristics. This means that
they have very similar boiling points and therefore, it will
be difficult to separate the two components via
distillation.
VAPOR LIQUID EQUILLIBRIA
Constant pressure VLE data is obtained from boiling
point diagrams. The VLE plot expresses the bubble-
point and the dew-point of a binary mixture at
constant pressure. The curved line is called
the equilibrium. The next two VLE plots below on the
other hand, shows non-ideal systems which will present
more difficult separations.
CONTINUED
The most intriguing VLE curves are generated by azeotropic
systems. An azeotrope is a liquid mixture which when
vaporized, produces the same composition as the liquid. The
two VLE plots below, show two different azeotropic systems,
one with a minimum boiling point and one with a maximum
boiling point. In both plots, the equilibrium curves cross the
diagonal lines, and this are azeotropic points where the
azeotropes occur. In other words, azeotropic systems give rise
to VLE plots where the equilibrium curves crosses the
diagonals.
CONTINUED
• Note the shapes of the respective equilibrium lines in relation to the diagonal lines that bisect
the VLE plots.
• Both plots are however, obtained from homogenous azeotropic systems. An azeotrope that
contains one liquid phase in contact with vapor is called a homogenous azeotrope.
• A homogenous azeotrope cannot be separated by conventional distillation.
• However, vacuum distillation may be used as the lower pressures can shift the azeotropic
point.
• Alternatively, an additional substance may add to shift the azeotropic point to a more
‘favorable’ position.
When this additional component appears in appreciable amounts at the top of the column, the
operation is called azeotropic distillation.
When the additional component appears mostly at the bottom of the column, the operation is
called extractive distillation
The VLE curve on the left is also generated by an azeotropic system, in this case a heterogenous
azeotrope. Heterogenous azeotropes can be identified by the ‘flat’ portion on the equilibrium
diagram. They may be separated in 2 distillation columns since these substances usually form
two liquid phases with widely differing compositions. The phases may be separated using settling
tanks under appropriate conditions.
P-X-Y AND T-X-Y
DIAGRAM
EFFECT OF
PRESSURE AND
TEMPERATURE ON
EQUILIBRIUM
DIAGRAM
References
1. “Unit operation of chemical
engineering” Mc cabe Smith warren
halley Vol.5
2. R.E. Treybal “MASS TRANSFER
OPERATIONS”
3. BINAY K DUTTA “MASS TRANSFER
OPERATIONS”
4. Advantages and Disadvantages of
Distillation - BIOTECH
(biotechwater.com)

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MASS TRANSFER OPERATION-DISTILLATION

  • 1. G H PATEL COLLEGE OF ENGINEERING AND TECHNOLOGY PREPARED BY: 180110105001-HONEY AGRAWAL 180110105002-ZANKRUIT AMIN 180110105003-ANNAN PATEL 180110105004-BAPODARA PRAKASH
  • 2. OUTLINES • Introduction • Applications • Distillation principles • Concept of relative volatility • Vapour liquid equilibria • P-x-y ,T-x-y diagram • effect of P & T on equilibrium data • References
  • 3. INTRODUCTION DEFINITION: o “Distillation is an unit operation which involves separation of a vaporizable component from a multi-component system and subsequent condensation of vapours”. o “Distillation is a process of separating the component substances from a liquid mixture by the selective evaporation and condensation”. o “Distillation ids defined as the separation of the components of a liquid mixture by a process involves vaporization and subsequent condensation at another place.”
  • 6. DISTILLATION PRINCIPLES • Separation of components from a liquid mixture via distillation depends on the differences in boiling points of the individual components. • Also, depending on the concentrations of the components present, the liquid mixture will have different boiling point characteristics. • Therefore, distillation processes depends on the vapor pressure characteristics of liquid mixtures.
  • 7. VAPOUR PRESSURE AND BOILING The vapor pressure of a liquid at a particular temperature is the equilibrium pressure exerted by molecules leaving and entering the liquid surface. Here are some important points regarding vapor pressure: energy input raises vapour pressure vapor pressure is related to boiling a liquid is said to ‘boil’ when its vapor pressure equals the surrounding pressure the ease with which a liquid boils depends on its volatility liquids with high vapor pressures (volatile liquids) will boil at lower temperatures the vapor pressure and hence the boiling point of a liquid mixture depends on the relative amounts of the components in the mixture distillation occurs because of the differences in the volatility of the components in the liquid mixture
  • 8. Relative Volatility • Relative volatility is a measure of the differences in volatility between 2 components, and hence their boiling points. It indicates how easy or difficult a particular separation will be. The relative volatility of component ‘I’ with respect to component ‘j’ is defined as • Yi = mole fraction of component ‘I’ in the vapor • xi = mole fraction of component ‘I’ in the liquid • Thus, if the relative volatility between 2 components is very close to one, it is an indication that they have very similar vapor pressure characteristics. This means that they have very similar boiling points and therefore, it will be difficult to separate the two components via distillation.
  • 9. VAPOR LIQUID EQUILLIBRIA Constant pressure VLE data is obtained from boiling point diagrams. The VLE plot expresses the bubble- point and the dew-point of a binary mixture at constant pressure. The curved line is called the equilibrium. The next two VLE plots below on the other hand, shows non-ideal systems which will present more difficult separations.
  • 10. CONTINUED The most intriguing VLE curves are generated by azeotropic systems. An azeotrope is a liquid mixture which when vaporized, produces the same composition as the liquid. The two VLE plots below, show two different azeotropic systems, one with a minimum boiling point and one with a maximum boiling point. In both plots, the equilibrium curves cross the diagonal lines, and this are azeotropic points where the azeotropes occur. In other words, azeotropic systems give rise to VLE plots where the equilibrium curves crosses the diagonals.
  • 11. CONTINUED • Note the shapes of the respective equilibrium lines in relation to the diagonal lines that bisect the VLE plots. • Both plots are however, obtained from homogenous azeotropic systems. An azeotrope that contains one liquid phase in contact with vapor is called a homogenous azeotrope. • A homogenous azeotrope cannot be separated by conventional distillation. • However, vacuum distillation may be used as the lower pressures can shift the azeotropic point. • Alternatively, an additional substance may add to shift the azeotropic point to a more ‘favorable’ position. When this additional component appears in appreciable amounts at the top of the column, the operation is called azeotropic distillation. When the additional component appears mostly at the bottom of the column, the operation is called extractive distillation The VLE curve on the left is also generated by an azeotropic system, in this case a heterogenous azeotrope. Heterogenous azeotropes can be identified by the ‘flat’ portion on the equilibrium diagram. They may be separated in 2 distillation columns since these substances usually form two liquid phases with widely differing compositions. The phases may be separated using settling tanks under appropriate conditions.
  • 13. EFFECT OF PRESSURE AND TEMPERATURE ON EQUILIBRIUM DIAGRAM
  • 14. References 1. “Unit operation of chemical engineering” Mc cabe Smith warren halley Vol.5 2. R.E. Treybal “MASS TRANSFER OPERATIONS” 3. BINAY K DUTTA “MASS TRANSFER OPERATIONS” 4. Advantages and Disadvantages of Distillation - BIOTECH (biotechwater.com)