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DISTILLATION
Presented By
Ms. Ruchita Tale
Lecturer
Nagpur College Of Pharmacy,
Nagpur 1
Definition
Raoult’s Law
Equipment
Classification
Steam Distillation
Azeotropic & Extractive Distillation
Application
CONTENTS
3
 “Distillation is an unit operation which involves separation of a vaporizable
component from a multi-component system and subsequent condensation of
vapours.”
 “Distillation is a process of separating the component substances from a liquid
mixture by selective evaporation and condensation.”
 “Distillation is defined as the separation of the components of a liquid mixture by
a process involving vaporization and subsequent condensation at another place.”
DEFINITION
4
 Binary Fisson :-
When two liquids mixed together, they may be miscible with each other in
all proportion, such miscible liquid are known as binary mixtures of
liquid.
Example:
 Ethanol + Water
 Acetone + Water
 Benzene + Carbon tetrachloride
TERMINOLOGY
 Ideal Solution (Perfect solution)
Ideal solution is defined as the one in which there is no change in the
properties of components other than dilution, when they mixed to form a
solution.
 Property of ideal solution
 Total volume of solution is equal to sum of volumes of each component.
 No heat absorbed and No heat evolved
 No Chemical reaction in-between
 Final volume of solution represents additive property of individual
components.
 Follow Raoult’s low
4
TERMINOLOGY
 Real Solution
Most system shows varying degree of deviation from raoult’s law, depending
on nature of liquids and temperature. These solution are known as real
solution.
Property of Real solution
 Heat may absorbed or evolved
 Chemical reaction occurs in-between
 Final volume of solution represents additive property of individual
components
 Don’t Follow Raoult’s low
Example
 Carbon tetra-chloride + Cyclohexane
 Choroform +Acetone 5
TERMINOLOGY
7
 It express a quantitative relationship between the
concentration and vapour pressure.
 It states that partial vapour pressure of each volatile
constituent is equal to vapour pressure of the pure
constituent multiplied by its mole fraction in the solution at a
given temperature.
RAOULT’S LAW
 Suppose Homogeneous mixture of liquid A and B
Partial vapour pressure of component A in Mixture
= PA = P°A*XA
Mole fraction of A in solution = XA Vapour pressure
of A in pure state =P°A
Partial vapour pressure of component B in Mixture = PB = P°B *XB
Mole fraction of B in solution = XB Vapour pressure
of A in pure state =P°B
 Total Vapor pressure of Mixture
PT = PA+ PB
PT = P°A *XA + P°B*XB 7
RAOULT’S LAW
9
 Separation of volatile oils - cloves(Eugenol comprises 72-
90%, Vanilin, acetyl eugenol).
 Separation of drugs obtained from plant and animal
sources- Vit. A from fish liveroil.
 Purification of organic solvents - absolute alcohol (100%).
 Purification of drugs obtained from chemical process.
 Manufacture of official preparations -sprit of nitrous ether, sprit of ammonia,
D.water and water for inj.
 Quality control methods- Alcohol content in elixir(4-40%).
 Refining of petroleum products- Petroleum ether 60,80.
 Recovery of solvents - synthesis.
APPLICATIONS:
10
DISTILLATION ASSEMBLY
11
STILL :
 It is a vaporizing chamber and used to place the material to
be distilled.
 The still is heated by a suitable means for vaporization of the
volatile constituents.
 On laboratory scale round bottom flasks made of glass are
used so that the progress of the distillation can be noticed.
 A condenser is attached to the still using appropriate
joints. A trap is inserted between distillation flask and
condenser.
GENERAL EQUIPMENT FOR
DISTILLATION:
CONDENSER :
 Used to condense the vapor
 It is kept cold by circulating water/air through jacket. Types:
 Single-surface condensers
 Straight Tube
 Bulb type
 Spiral
 Coiled type
 Double-surface condensers
 Multi-tubular condensers
The condenser is connected to a receiver through a suitable
adapter.
11
GENERAL EQUIPMENT FOR
DISTILLATION:
CONDENSER :
Bulb type
Straight
Tube
type
Spiral type Coiled type Cold finger,
Spiral type
Lucas’s
Double Surface
12
GENERAL EQUIPMENT FOR
DISTILLATION:
14
RECEIVER :
 It is used to collect the distillate.
 It may be a simple flask.
 It immersed in ice-bath to minimize loss of volatile
matter.
 Florentine receivers are used for the separation of oil
and water.
Types of Florentine receivers :
 Type-I :- for separation of oil heavier than water.
 Type-II :- for separation of oil lighter than water.
GENERAL EQUIPMENT FOR DISTILLATION:
15
RECEIVER :
GENERAL EQUIPMENT FOR DISTILLATION:
I. Simple Distillation (Differential distillation)
II. Flash Distillation (Equilibrium distillation)
III. Vacuum distillation (distillation under reduced pressure)
IV. Molecular Distillation (Evaporation distillation or short path distillation.)
V. Fractional Distillation (Rectification)
VI. Aezotropic and extractive Distillation
VII. Steam Distillation
VIII. Destructive Distillation
IX. Compression Distillation
15
CLASSIFICATION OF DISTILLATION
METHODS
 Steam distillation is method of distillation carried out with aid
of steam.
 It is used to separate High boiling substances from non-volatile
impurities-Separate immiscible liquids
17
STEAM DISTILLATION
18
Principle:
A mixture of immiscible liquids begins to boil when sum of
their vapour pressure is equal to atmospheric pressure.
In case of mixture of water and turpentine, mixture boils
below the boiling point of pure water, though the turpentine
boils at a much higher temperature than that of water.
STEAM DISTILLATION
19
STEAM DISTILLATION
STEAM DISTILLATION
19
20
Example:
Boiling point of Turpentine = 160 °C
Boiling point of Water + Turpentine Mixture = 95.6
°C
At this temperature Vapour pressure of :-
Water
Turpentine
= 86.245 kPa (647 mmHg)
= 15.06 kPa (113 mmHg)
Sum of vapour pressure = 101.31 kPa (760 mmHg)
Which is normal atmospheric pressure and thus high boiling liquid may
be distilled with water at a temperature much below its boiling point.
STEAM DISTILLATION
22
.
Construction of assembly:
 Metallic steam can fitted with cork having two holes.
 Safety tube inserted up to bottom through one hole to maintain pressure
in side stem can, more over when steam comes out from safety tube
indicates that can is empty.
 Through other hole band tube is passed and other end of this tube is connected
to flask containing non-aqueous liquid in which tube is dipped.
 Flask and condenser is connected with delivery tube.
 Condenser is connected to receiver with help of adopter.
 Provision are made to heat both steam can and flask separately
STEAM DISTILLATION
23
Application:
 Used to separate immiscible liquids. Ex- Water + Toluene
Extraction at much lower temperature to protect from
decomposition without loss of aroma
 To extract volatile oils like clove, anise and eucalyptus oils.
 Purification of essential oils like almond oil.
 Camphor is distilled by this method.
 Aromatic water are prepared.
Limitation:
Not suitable when two immiscible liquids reacts with each other.
STEAM DISTILLATION
24
Azeotropic distillation:
 In which azeoptorpic mixture is broken by the addition of third substance,
which forms a new azeotrope with one of the components.
 Azeotropic Distillation refers to process where by new component (called
the entrainer) is added to the original feed mixture to form (or nearly form)
an azeotrope with one or more of the feed components.
 The azeotrope is then removed as either distillate or the bottom.
Azeotropic Mixture(Constant boiling Mixture)
Mixture of special composition giving minimum or maximum boiling
point than individual component with minimum or maximum boiling point
respectively.
AZEOTROPIC & EXTRACTIVE
DISTILLATION
25
AZEOTROPIC & EXTRACTIVE DISTILLATION
Extractive distillation:
 Extractive distillation defined as distillation in the presence of a miscible, high boiling,
relatively non-volatile components, the solvent, that forms no azeotrope with the other
components in the mixture.
 The method of extractive distillation uses a sepration of solvent, which is genrally
nonvolatile, has a boiling point and is misicible with the mixture, but doesn’t from an
azeotropic mixture. The solvent intract differently with the component of the mixture
thereby causing their relative volatilities to change.
 The solvent must alter the relative volatility by a wide enough margin for succesful result.
The quantity,cost,avability of solvent should be consider. The solvent should be easily
seprable from the bottom product and should not react chemically with the component or
the mixture.
AZEOTROPIC & EXTRACTIVE DISTILLATION
Application :-
Absolute alcohol can be prepared by azeotropic distillation.
Petroleum refineries and distilleries use these types of
distillation.
The liquor from fermentation process is a common source of
ethanol and contains approximately 8 to 10%.
AZEOTROPIC & EXTRACTIVE
DISTILLATION
Distillation ppt.pptx

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Distillation ppt.pptx

  • 1. DISTILLATION Presented By Ms. Ruchita Tale Lecturer Nagpur College Of Pharmacy, Nagpur 1
  • 3. 3  “Distillation is an unit operation which involves separation of a vaporizable component from a multi-component system and subsequent condensation of vapours.”  “Distillation is a process of separating the component substances from a liquid mixture by selective evaporation and condensation.”  “Distillation is defined as the separation of the components of a liquid mixture by a process involving vaporization and subsequent condensation at another place.” DEFINITION
  • 4. 4  Binary Fisson :- When two liquids mixed together, they may be miscible with each other in all proportion, such miscible liquid are known as binary mixtures of liquid. Example:  Ethanol + Water  Acetone + Water  Benzene + Carbon tetrachloride TERMINOLOGY
  • 5.  Ideal Solution (Perfect solution) Ideal solution is defined as the one in which there is no change in the properties of components other than dilution, when they mixed to form a solution.  Property of ideal solution  Total volume of solution is equal to sum of volumes of each component.  No heat absorbed and No heat evolved  No Chemical reaction in-between  Final volume of solution represents additive property of individual components.  Follow Raoult’s low 4 TERMINOLOGY
  • 6.  Real Solution Most system shows varying degree of deviation from raoult’s law, depending on nature of liquids and temperature. These solution are known as real solution. Property of Real solution  Heat may absorbed or evolved  Chemical reaction occurs in-between  Final volume of solution represents additive property of individual components  Don’t Follow Raoult’s low Example  Carbon tetra-chloride + Cyclohexane  Choroform +Acetone 5 TERMINOLOGY
  • 7. 7  It express a quantitative relationship between the concentration and vapour pressure.  It states that partial vapour pressure of each volatile constituent is equal to vapour pressure of the pure constituent multiplied by its mole fraction in the solution at a given temperature. RAOULT’S LAW
  • 8.  Suppose Homogeneous mixture of liquid A and B Partial vapour pressure of component A in Mixture = PA = P°A*XA Mole fraction of A in solution = XA Vapour pressure of A in pure state =P°A Partial vapour pressure of component B in Mixture = PB = P°B *XB Mole fraction of B in solution = XB Vapour pressure of A in pure state =P°B  Total Vapor pressure of Mixture PT = PA+ PB PT = P°A *XA + P°B*XB 7 RAOULT’S LAW
  • 9. 9  Separation of volatile oils - cloves(Eugenol comprises 72- 90%, Vanilin, acetyl eugenol).  Separation of drugs obtained from plant and animal sources- Vit. A from fish liveroil.  Purification of organic solvents - absolute alcohol (100%).  Purification of drugs obtained from chemical process.  Manufacture of official preparations -sprit of nitrous ether, sprit of ammonia, D.water and water for inj.  Quality control methods- Alcohol content in elixir(4-40%).  Refining of petroleum products- Petroleum ether 60,80.  Recovery of solvents - synthesis. APPLICATIONS:
  • 11. 11 STILL :  It is a vaporizing chamber and used to place the material to be distilled.  The still is heated by a suitable means for vaporization of the volatile constituents.  On laboratory scale round bottom flasks made of glass are used so that the progress of the distillation can be noticed.  A condenser is attached to the still using appropriate joints. A trap is inserted between distillation flask and condenser. GENERAL EQUIPMENT FOR DISTILLATION:
  • 12. CONDENSER :  Used to condense the vapor  It is kept cold by circulating water/air through jacket. Types:  Single-surface condensers  Straight Tube  Bulb type  Spiral  Coiled type  Double-surface condensers  Multi-tubular condensers The condenser is connected to a receiver through a suitable adapter. 11 GENERAL EQUIPMENT FOR DISTILLATION:
  • 13. CONDENSER : Bulb type Straight Tube type Spiral type Coiled type Cold finger, Spiral type Lucas’s Double Surface 12 GENERAL EQUIPMENT FOR DISTILLATION:
  • 14. 14 RECEIVER :  It is used to collect the distillate.  It may be a simple flask.  It immersed in ice-bath to minimize loss of volatile matter.  Florentine receivers are used for the separation of oil and water. Types of Florentine receivers :  Type-I :- for separation of oil heavier than water.  Type-II :- for separation of oil lighter than water. GENERAL EQUIPMENT FOR DISTILLATION:
  • 15. 15 RECEIVER : GENERAL EQUIPMENT FOR DISTILLATION:
  • 16. I. Simple Distillation (Differential distillation) II. Flash Distillation (Equilibrium distillation) III. Vacuum distillation (distillation under reduced pressure) IV. Molecular Distillation (Evaporation distillation or short path distillation.) V. Fractional Distillation (Rectification) VI. Aezotropic and extractive Distillation VII. Steam Distillation VIII. Destructive Distillation IX. Compression Distillation 15 CLASSIFICATION OF DISTILLATION METHODS
  • 17.  Steam distillation is method of distillation carried out with aid of steam.  It is used to separate High boiling substances from non-volatile impurities-Separate immiscible liquids 17 STEAM DISTILLATION
  • 18. 18 Principle: A mixture of immiscible liquids begins to boil when sum of their vapour pressure is equal to atmospheric pressure. In case of mixture of water and turpentine, mixture boils below the boiling point of pure water, though the turpentine boils at a much higher temperature than that of water. STEAM DISTILLATION
  • 21. 20 Example: Boiling point of Turpentine = 160 °C Boiling point of Water + Turpentine Mixture = 95.6 °C At this temperature Vapour pressure of :- Water Turpentine = 86.245 kPa (647 mmHg) = 15.06 kPa (113 mmHg) Sum of vapour pressure = 101.31 kPa (760 mmHg) Which is normal atmospheric pressure and thus high boiling liquid may be distilled with water at a temperature much below its boiling point. STEAM DISTILLATION
  • 22. 22 . Construction of assembly:  Metallic steam can fitted with cork having two holes.  Safety tube inserted up to bottom through one hole to maintain pressure in side stem can, more over when steam comes out from safety tube indicates that can is empty.  Through other hole band tube is passed and other end of this tube is connected to flask containing non-aqueous liquid in which tube is dipped.  Flask and condenser is connected with delivery tube.  Condenser is connected to receiver with help of adopter.  Provision are made to heat both steam can and flask separately STEAM DISTILLATION
  • 23. 23 Application:  Used to separate immiscible liquids. Ex- Water + Toluene Extraction at much lower temperature to protect from decomposition without loss of aroma  To extract volatile oils like clove, anise and eucalyptus oils.  Purification of essential oils like almond oil.  Camphor is distilled by this method.  Aromatic water are prepared. Limitation: Not suitable when two immiscible liquids reacts with each other. STEAM DISTILLATION
  • 24. 24 Azeotropic distillation:  In which azeoptorpic mixture is broken by the addition of third substance, which forms a new azeotrope with one of the components.  Azeotropic Distillation refers to process where by new component (called the entrainer) is added to the original feed mixture to form (or nearly form) an azeotrope with one or more of the feed components.  The azeotrope is then removed as either distillate or the bottom. Azeotropic Mixture(Constant boiling Mixture) Mixture of special composition giving minimum or maximum boiling point than individual component with minimum or maximum boiling point respectively. AZEOTROPIC & EXTRACTIVE DISTILLATION
  • 25. 25 AZEOTROPIC & EXTRACTIVE DISTILLATION Extractive distillation:  Extractive distillation defined as distillation in the presence of a miscible, high boiling, relatively non-volatile components, the solvent, that forms no azeotrope with the other components in the mixture.  The method of extractive distillation uses a sepration of solvent, which is genrally nonvolatile, has a boiling point and is misicible with the mixture, but doesn’t from an azeotropic mixture. The solvent intract differently with the component of the mixture thereby causing their relative volatilities to change.  The solvent must alter the relative volatility by a wide enough margin for succesful result. The quantity,cost,avability of solvent should be consider. The solvent should be easily seprable from the bottom product and should not react chemically with the component or the mixture.
  • 26. AZEOTROPIC & EXTRACTIVE DISTILLATION
  • 27.
  • 28. Application :- Absolute alcohol can be prepared by azeotropic distillation. Petroleum refineries and distilleries use these types of distillation. The liquor from fermentation process is a common source of ethanol and contains approximately 8 to 10%. AZEOTROPIC & EXTRACTIVE DISTILLATION