SlideShare a Scribd company logo
1 of 15
Download to read offline
DISTILLATION
“It is defined as separation of components of liquid mixture by process involving vaporization &
then condensation at another place.”
It involves two steps:
01). Converting a liquid into vapour.
02). Transferring the vapour to another place & recovering the liquid by condensation.
The feed liquid is knowns as “Distillation” and the condensate liquid is called “Distillate or
Condensate”.
APPLICATIONS
- Separation of volatile oil.
- Purification of organic solvents.
- Manufacturing of official preparation.
- Refineries of petroleum products.
- Recovery of solvents.
- Separation of drugs obtained from plant & animals.
- Purification of drugs obtained from chemical process.
IDEAL SOLUTION
“Ideal solutions are defined as the one which there is no change in the properties of the
components other that dilution when they are mixed to form a solution.”
Example: Methanol & water.
DALTON’S LAW
“Daltons law of partial pressure states that pressure extract by a mixture of gases is equal to
sum of partial vapour pressure exerted by each gas.”
RAOULT’S LAW
“It states that partial vapor pressure of each volatile components is equal to vapour pressure of
pure components multiplied by its mole fraction in the solution at a given temperature. “
SIMPLE DISTILLATION
It is the process of a converting single constituents for liquid (mixture) into its vapour,
transferring the vapour to another place & recovering the liquid by condensing the vapour.
Usually by allowing it to coming contact with cold surface.
PRINCIPLE
Liquid boil when its vapour pressure is equal to atmospheric pressure. Simple distillation
conducted at its boiling point.
The higher the relative volatility of liquid the better the separation. Heat is supplied to liquid so
that it boils & resulting vapour condensed.
CONSTRUCTION
It consists of a distillation flask with a side arm sloping
downwards. A condenser if fitted into the side arm by means of a cork.
The condenser is usually is water condenser.
The condenser is connected to receiver flask by means of adaptor.
`
PROCEDURE
The liquid is to be distilled its filled into the flask. A thermometer is inserted in to the cork &
fixed to the flask. The water is circulated through jacket of condenser. The heat is supplied &
content is heated & boiled after some time. The vapour rises up & passes down the side arm
into the condenser the temperature rises rapidly & reaches a constant value the temperature is
equal to the boiling point of liquid finally the vapour form are condense & collected in to
receiver.
APPLICATIONS
→ It is used for preparation distilled water & water for injection.
→ Volatile & aromatic water are prepared.
→ Nonvolatile solid are separated from volatile liquid.
FLASH DISTILLATION
It is defined as the process in which the enter liquid is suddenly vaporized by passing it term
high pressure zone to low.
PRINCIPLE
When a hot liquid mixture is allowed to enter form high pressure zone to vaporized suddenly
during this process the chamber get cooled the individual vapour. Vapour phase molecule of
high boiling fraction get condensed, while low boiling fraction remain as vapour. This process
requires for the equilibrium to reach & therefore the liquid & vapour are held in contact with
each other for some period of time & then are separated.
The vapour are further condensed & collected.
CONSTRUCTION
It consists of a pump, which is connected to a feed reservoir.
Pump helps in pumping the feed into heating chamber which consists of suitable heating
mechanism.
The other end of the pipe is directly introduced into the vapour-liquid separator through a
reducing valve. The vapour outlet is provide at the top of the separator & liquid outlet is
provided at the bottom.
WORKING
The feed is pumped through a heater at a certain pressure. The liquids get heated, which enters
the vapour-liquid separator through a pressure reducing valve. Due to the drop-in pressure the
liquid flashes, which further enhances the vaporization process.
Suddenly vaporization induces cooling. The individual vapour phase molecules of high boiling
fraction get condensed while the low boiling fraction remains as vapour.
The mixture is allowed for a sufficient time, so that vapour & liquid portions separate & achieve
equilibrium.
USES
It is used for separating components, which boils at widely different temperatures.
It is widely used in petroleum industry.
ADVANTAGES
→ It is used for obtaining multi-components.
→ It can be used in continuous mode.
DISADVANTAGES
❑ It is not suitable for two components systems.
❑ It is not suitable if the separated components are needed in pure quality.
It is the type of distillation process which involve separation of mixable liquids. The process
involves repeated distillation & condensation & the mixture I usually separated into
components parts; the separation happens when the mixture is heated at a certain
temperature. Where fraction of the mixture starts to vaporized.
PRINCIPLE
The basic principle of this type of distillation is that differ boil & evaporates at different
temperature so when the mixture is heated, substance with power boiling point start to boil
first & convert in to vapour.
CONSTRUCTION
It consists of a fractionating column, distillation flask, condenser,
receiver & heat source. The fractionating column is inserted between the still & condenser at
the top of column, a condenser is provided & heat is supplied at the bottom of the column.
FRACTIONAL DISTILLATION
WORKING
The mixture to be distilled is feed to the boiler & heated. A mixture of two mixable liquids A &
B is taken where A have more volatility then B.
The solution is added into the flask, heat is applied & the mixture starts to boil the vapour are
formed having large amount of vapour from liquid A. these vapour moves through the
fractalizing column into the condenser where it is cool down to form a liquid which is collected
into the receiver. Vaporization & condensation takes place throughout the process until two
mixtures are separated completely.
USES
Use for purification of water as well as separating water & acetone.
Use in several industries like oil binaries & chemical plants for purification &
separation of organic compounds.
ADVANTAGES
It is used for separating large amount of mixable liquid according to their boiling point.
Example: acetone & water.
DISADVANTAGES
This method cannot be used to separate mixable liquid from azeotropic mixture.
DISTILLATION UNDER REDUCE PRESSURE
it is defined as a process in which liquids is distilled at a temperature lower than its boiling point
by applications of vacuum.
PRINCIPLE
Liquid boil when its vapour pressure is equal to atmospheric pressure. If the
external pressure is reduced by applications of vacuum, the boiling point of liquid decreases
therefore the liquid boils at lower temperature.
CONSTRUCTION
Distillation under reduced pressure or vacuum is carried out in a specially designed glass
apparatus. A to necked ‘Claisen’s flask’ is used, the main neck of which is fitted with along
capillary tube (capillary tubes avoids bumping) & the side neck being fitted with a
thermometer.
The side tube is connected to a condenser carrying a receiver at the other end. The receiver is
attached to a vacuum pump to reduce the pressure. The pressure is measured with the help of
a manometer.
WORKING
The liquid to be distilled is filled into the flask. The reducing vacuum applied
and content or heated gradually. The temperature rises & get vaporized rapidly due to vacuum.
the vapour passes through the condenser & conduced is collected into the receiver.
The temperature is noted which is less than the boiling point of the liquids.
ADVANTAGES
This method is used for the compound which degraded or higher temperature.
Example: Enzymes, vitamins & alkaloids etc.
DISADVANTAGES
❑ In vacuum distillation persistent foaming occurs.
❑ Not suitable for preparation of semi-solids or solid extracts.
STEAM DISTILLATION
PRINCIPLE
Steam distillation is a method of distillation carried out with the help of steam & used for
separation of high boiling substance from non-volatile impurities.
A mixture of immixible liquids begainst to boil when the some of their vapour pressure, is equal
to atmospheric pressure.
For volatile- substance which are mixable with water steam distillation involve the principle of
fractional distillation.
CONSTRUCTIONS
It consists of steam can with a cork having two holes in one-hole
safety tube is attached & through another hole a vent tube is pumped, the other the bent tube
is connected to the flask, containing non-aqueous liquids.
A delivery tube is insulted is the second flask which connect flask & condenser.
WORKING
The non-aqueous liquid is placed in the flask. The small quantity of water is added to it. Steam
can be filled with water; the flask & steam can are heated simentionally. This steam carries the
volatile oil & passes in to the condenser which is cooled in to the receiver the process is
continued until all the non-aqueous liquid has been distilled.
In the receiver water & organic liquid forms two separate dyes which can be easily separated.
APPLICATION
❑ It is used of separation of immixible liquids.
Example: Toluene & water.
❑ It is used for extraction of most of the volatile oil like clobe like.
❑ Camphor is also distilled by this method.
ADVANTAGES
→ Volatile oil can be separated at lower temperature is steam distillation, without loss of
aroma.
→ It is useful in purification li liquids with high boiling points.
→ Provided molecular weight.
DISADVANTAGES
Not suitable when immixible liquids & water reacts with each other.
MOLECULAR DISTILLATION
A process in which each molecule in the vapour phase travels the mean free path & gets
condensed individually without intermolecular collisions on application of vacuum.
PRINCIPLE
The substance to be distilled have very low vapour pressure i.e. viscous
liquid, oils, waxy material & high molecular weight substance. These boils at very high
temperature in order to decrease boiling point of liquid high vacuum is applied.
The mean free path of a molecule is defined as average distance through
which a molecule can move without coming in to collision with each other. Its express as-
 =  3/p
Where p = vapour pressure.
 = density.
The mean free path can be increase by desecrating the viscosity.
REQUIRMENT FOR MOLECULAR DISTILLATION
01). The evaporating surface must bee closed to condensing surface this insure the molecular to
come in contact with the condenser a soon as they leave the evaporating surface.
02). The liquid surface area must be large as possible, because the vapour is evoled from the
surface of the molecule.
03). The molecular collision should be minimizing because the change of direction path of
molecules.
❑ More frequently used in the refining of fixed oils.
❑ Vitamin A is separated from fish liver oil.
❑ Purification of chemicals, “tricresyl phosphate”.
APPLICATION
FALLING FILM MOLECULAR STILL
PRINCIPLE
In this method vaporization occurs from the film of liquid flowing down a heated surface under
high vacuum. The vapors travel short distance & strike condenser.
Each molecule is condensed= individually & distillate is collected.
CONSTRUCTION
It consists of a vessel of diameter 1m, the wall of the vessel is provided with jacket.
Wipers are provided to the vessel wall which are connected to rotating head to motor &
condenser are arranged very closed to wall of vessel.
Vacuum pump is also connected to the vessel.
WORKING
The vessel is heated & vacuum is applied at the center. Wipers are allowed to rotate and it is
entered as the liquid flow down it spread o from a film by wipers, which are moving at a speed
of 3m/sec.
Since the moving at an already heated, the liquid films evaporate directly. Vapour travel its
mean free path & strike the condenser, the condensate is collected in vessels.
It is used purification chemicals such a di-methyl thalate.
Vitamin A is separated from oil.
ADVANTAGES
Short residence time of the feed.
Significantly lower temperature is required due to high vacuum.
DISADVANTAGES
This is not used for azeotropic mixture.
USES

More Related Content

Similar to distillation-191227021008.pdf

MP5040 Lecture 5.pdf- Process engineering
MP5040 Lecture 5.pdf- Process engineeringMP5040 Lecture 5.pdf- Process engineering
MP5040 Lecture 5.pdf- Process engineering
akalankar
 

Similar to distillation-191227021008.pdf (20)

Evaporation.pptx
Evaporation.pptxEvaporation.pptx
Evaporation.pptx
 
Distillation
Distillation Distillation
Distillation
 
DISTILLATION
DISTILLATIONDISTILLATION
DISTILLATION
 
Distillation pdf srd
Distillation pdf srdDistillation pdf srd
Distillation pdf srd
 
Distillation processes ,Types of Distillation, Types of Water
Distillation processes ,Types of Distillation, Types of WaterDistillation processes ,Types of Distillation, Types of Water
Distillation processes ,Types of Distillation, Types of Water
 
Distillation.pptx
Distillation.pptxDistillation.pptx
Distillation.pptx
 
Mechanism of Distillation,simple distillation steam &fractional distillation...
 Mechanism of Distillation,simple distillation steam &fractional distillation... Mechanism of Distillation,simple distillation steam &fractional distillation...
Mechanism of Distillation,simple distillation steam &fractional distillation...
 
Evaporation by ankita yagnik
Evaporation by ankita yagnikEvaporation by ankita yagnik
Evaporation by ankita yagnik
 
Distillation and Evaporation
Distillation and EvaporationDistillation and Evaporation
Distillation and Evaporation
 
evaporation.pdf
evaporation.pdfevaporation.pdf
evaporation.pdf
 
Evaporation - Pharmaceutical Engineering 1st
Evaporation - Pharmaceutical Engineering 1stEvaporation - Pharmaceutical Engineering 1st
Evaporation - Pharmaceutical Engineering 1st
 
Distillation
DistillationDistillation
Distillation
 
Distillation.pptx
Distillation.pptxDistillation.pptx
Distillation.pptx
 
Distillation main
Distillation mainDistillation main
Distillation main
 
Distillation
DistillationDistillation
Distillation
 
Desuperheater selection guide
Desuperheater selection guideDesuperheater selection guide
Desuperheater selection guide
 
MP5040 Lecture 5.pdf- Process engineering
MP5040 Lecture 5.pdf- Process engineeringMP5040 Lecture 5.pdf- Process engineering
MP5040 Lecture 5.pdf- Process engineering
 
Evaporation by ankita yagnik
Evaporation by ankita yagnikEvaporation by ankita yagnik
Evaporation by ankita yagnik
 
Evaporation MSG.ppt Pharmaceutical Engineering SEM-III
Evaporation MSG.ppt Pharmaceutical Engineering SEM-IIIEvaporation MSG.ppt Pharmaceutical Engineering SEM-III
Evaporation MSG.ppt Pharmaceutical Engineering SEM-III
 
distillation
distillationdistillation
distillation
 

More from SaqibShaik2

distillationbyankitayagnik-180430073733.pdf
distillationbyankitayagnik-180430073733.pdfdistillationbyankitayagnik-180430073733.pdf
distillationbyankitayagnik-180430073733.pdf
SaqibShaik2
 

More from SaqibShaik2 (20)

microbiology 1 units.pdf
microbiology 1 units.pdfmicrobiology 1 units.pdf
microbiology 1 units.pdf
 
microbiology 3 unit.pdf
microbiology 3 unit.pdfmicrobiology 3 unit.pdf
microbiology 3 unit.pdf
 
unit 4 microbiology.pdf
unit 4 microbiology.pdfunit 4 microbiology.pdf
unit 4 microbiology.pdf
 
Endocrine System.pdf
Endocrine System.pdfEndocrine System.pdf
Endocrine System.pdf
 
Urinary System.pdf
Urinary System.pdfUrinary System.pdf
Urinary System.pdf
 
Aromatic acid
Aromatic acid Aromatic acid
Aromatic acid
 
PP-UNIT-5_pH and buffers .pdf
PP-UNIT-5_pH and buffers .pdfPP-UNIT-5_pH and buffers .pdf
PP-UNIT-5_pH and buffers .pdf
 
surface-and-interfacial-phenomenon.pptx
surface-and-interfacial-phenomenon.pptxsurface-and-interfacial-phenomenon.pptx
surface-and-interfacial-phenomenon.pptx
 
complexation-and-protein-binding.pptx
complexation-and-protein-binding.pptxcomplexation-and-protein-binding.pptx
complexation-and-protein-binding.pptx
 
poc unit-2 Basicity of amines .pdf
poc unit-2 Basicity of amines .pdfpoc unit-2 Basicity of amines .pdf
poc unit-2 Basicity of amines .pdf
 
Reaction of anthracene
Reaction of anthracene Reaction of anthracene
Reaction of anthracene
 
Semi solid dosage forms
Semi solid dosage formsSemi solid dosage forms
Semi solid dosage forms
 
POC-UNIT-2 Acidity of phenols .pdf
POC-UNIT-2 Acidity of phenols .pdfPOC-UNIT-2 Acidity of phenols .pdf
POC-UNIT-2 Acidity of phenols .pdf
 
complexation-110223092.pptx
complexation-110223092.pptxcomplexation-110223092.pptx
complexation-110223092.pptx
 
PP- Phenol-Water System .pdf
PP- Phenol-Water System .pdfPP- Phenol-Water System .pdf
PP- Phenol-Water System .pdf
 
drying-210615034632.pdf
drying-210615034632.pdfdrying-210615034632.pdf
drying-210615034632.pdf
 
Aromaticity and Huckels rule .pdf
Aromaticity and Huckels rule .pdfAromaticity and Huckels rule .pdf
Aromaticity and Huckels rule .pdf
 
PP- Buffer action mechanism .pdf
PP- Buffer action mechanism .pdfPP- Buffer action mechanism .pdf
PP- Buffer action mechanism .pdf
 
PP- Buffer equation .pdf
PP- Buffer equation .pdfPP- Buffer equation .pdf
PP- Buffer equation .pdf
 
distillationbyankitayagnik-180430073733.pdf
distillationbyankitayagnik-180430073733.pdfdistillationbyankitayagnik-180430073733.pdf
distillationbyankitayagnik-180430073733.pdf
 

Recently uploaded

Gardella_Mateo_IntellectualProperty.pdf.
Gardella_Mateo_IntellectualProperty.pdf.Gardella_Mateo_IntellectualProperty.pdf.
Gardella_Mateo_IntellectualProperty.pdf.
MateoGardella
 
Beyond the EU: DORA and NIS 2 Directive's Global Impact
Beyond the EU: DORA and NIS 2 Directive's Global ImpactBeyond the EU: DORA and NIS 2 Directive's Global Impact
Beyond the EU: DORA and NIS 2 Directive's Global Impact
PECB
 
1029 - Danh muc Sach Giao Khoa 10 . pdf
1029 -  Danh muc Sach Giao Khoa 10 . pdf1029 -  Danh muc Sach Giao Khoa 10 . pdf
1029 - Danh muc Sach Giao Khoa 10 . pdf
QucHHunhnh
 
Activity 01 - Artificial Culture (1).pdf
Activity 01 - Artificial Culture (1).pdfActivity 01 - Artificial Culture (1).pdf
Activity 01 - Artificial Culture (1).pdf
ciinovamais
 
Making and Justifying Mathematical Decisions.pdf
Making and Justifying Mathematical Decisions.pdfMaking and Justifying Mathematical Decisions.pdf
Making and Justifying Mathematical Decisions.pdf
Chris Hunter
 

Recently uploaded (20)

Key note speaker Neum_Admir Softic_ENG.pdf
Key note speaker Neum_Admir Softic_ENG.pdfKey note speaker Neum_Admir Softic_ENG.pdf
Key note speaker Neum_Admir Softic_ENG.pdf
 
Gardella_Mateo_IntellectualProperty.pdf.
Gardella_Mateo_IntellectualProperty.pdf.Gardella_Mateo_IntellectualProperty.pdf.
Gardella_Mateo_IntellectualProperty.pdf.
 
Accessible design: Minimum effort, maximum impact
Accessible design: Minimum effort, maximum impactAccessible design: Minimum effort, maximum impact
Accessible design: Minimum effort, maximum impact
 
Measures of Dispersion and Variability: Range, QD, AD and SD
Measures of Dispersion and Variability: Range, QD, AD and SDMeasures of Dispersion and Variability: Range, QD, AD and SD
Measures of Dispersion and Variability: Range, QD, AD and SD
 
Class 11th Physics NEET formula sheet pdf
Class 11th Physics NEET formula sheet pdfClass 11th Physics NEET formula sheet pdf
Class 11th Physics NEET formula sheet pdf
 
Beyond the EU: DORA and NIS 2 Directive's Global Impact
Beyond the EU: DORA and NIS 2 Directive's Global ImpactBeyond the EU: DORA and NIS 2 Directive's Global Impact
Beyond the EU: DORA and NIS 2 Directive's Global Impact
 
1029 - Danh muc Sach Giao Khoa 10 . pdf
1029 -  Danh muc Sach Giao Khoa 10 . pdf1029 -  Danh muc Sach Giao Khoa 10 . pdf
1029 - Danh muc Sach Giao Khoa 10 . pdf
 
Activity 01 - Artificial Culture (1).pdf
Activity 01 - Artificial Culture (1).pdfActivity 01 - Artificial Culture (1).pdf
Activity 01 - Artificial Culture (1).pdf
 
Paris 2024 Olympic Geographies - an activity
Paris 2024 Olympic Geographies - an activityParis 2024 Olympic Geographies - an activity
Paris 2024 Olympic Geographies - an activity
 
Basic Civil Engineering first year Notes- Chapter 4 Building.pptx
Basic Civil Engineering first year Notes- Chapter 4 Building.pptxBasic Civil Engineering first year Notes- Chapter 4 Building.pptx
Basic Civil Engineering first year Notes- Chapter 4 Building.pptx
 
psychiatric nursing HISTORY COLLECTION .docx
psychiatric  nursing HISTORY  COLLECTION  .docxpsychiatric  nursing HISTORY  COLLECTION  .docx
psychiatric nursing HISTORY COLLECTION .docx
 
How to Give a Domain for a Field in Odoo 17
How to Give a Domain for a Field in Odoo 17How to Give a Domain for a Field in Odoo 17
How to Give a Domain for a Field in Odoo 17
 
Introduction to Nonprofit Accounting: The Basics
Introduction to Nonprofit Accounting: The BasicsIntroduction to Nonprofit Accounting: The Basics
Introduction to Nonprofit Accounting: The Basics
 
PROCESS RECORDING FORMAT.docx
PROCESS      RECORDING        FORMAT.docxPROCESS      RECORDING        FORMAT.docx
PROCESS RECORDING FORMAT.docx
 
Mattingly "AI & Prompt Design: The Basics of Prompt Design"
Mattingly "AI & Prompt Design: The Basics of Prompt Design"Mattingly "AI & Prompt Design: The Basics of Prompt Design"
Mattingly "AI & Prompt Design: The Basics of Prompt Design"
 
APM Welcome, APM North West Network Conference, Synergies Across Sectors
APM Welcome, APM North West Network Conference, Synergies Across SectorsAPM Welcome, APM North West Network Conference, Synergies Across Sectors
APM Welcome, APM North West Network Conference, Synergies Across Sectors
 
Web & Social Media Analytics Previous Year Question Paper.pdf
Web & Social Media Analytics Previous Year Question Paper.pdfWeb & Social Media Analytics Previous Year Question Paper.pdf
Web & Social Media Analytics Previous Year Question Paper.pdf
 
Ecological Succession. ( ECOSYSTEM, B. Pharmacy, 1st Year, Sem-II, Environmen...
Ecological Succession. ( ECOSYSTEM, B. Pharmacy, 1st Year, Sem-II, Environmen...Ecological Succession. ( ECOSYSTEM, B. Pharmacy, 1st Year, Sem-II, Environmen...
Ecological Succession. ( ECOSYSTEM, B. Pharmacy, 1st Year, Sem-II, Environmen...
 
SOCIAL AND HISTORICAL CONTEXT - LFTVD.pptx
SOCIAL AND HISTORICAL CONTEXT - LFTVD.pptxSOCIAL AND HISTORICAL CONTEXT - LFTVD.pptx
SOCIAL AND HISTORICAL CONTEXT - LFTVD.pptx
 
Making and Justifying Mathematical Decisions.pdf
Making and Justifying Mathematical Decisions.pdfMaking and Justifying Mathematical Decisions.pdf
Making and Justifying Mathematical Decisions.pdf
 

distillation-191227021008.pdf

  • 1. DISTILLATION “It is defined as separation of components of liquid mixture by process involving vaporization & then condensation at another place.” It involves two steps: 01). Converting a liquid into vapour. 02). Transferring the vapour to another place & recovering the liquid by condensation. The feed liquid is knowns as “Distillation” and the condensate liquid is called “Distillate or Condensate”. APPLICATIONS - Separation of volatile oil. - Purification of organic solvents. - Manufacturing of official preparation. - Refineries of petroleum products. - Recovery of solvents. - Separation of drugs obtained from plant & animals. - Purification of drugs obtained from chemical process. IDEAL SOLUTION “Ideal solutions are defined as the one which there is no change in the properties of the components other that dilution when they are mixed to form a solution.” Example: Methanol & water. DALTON’S LAW “Daltons law of partial pressure states that pressure extract by a mixture of gases is equal to sum of partial vapour pressure exerted by each gas.” RAOULT’S LAW “It states that partial vapor pressure of each volatile components is equal to vapour pressure of pure components multiplied by its mole fraction in the solution at a given temperature. “
  • 2. SIMPLE DISTILLATION It is the process of a converting single constituents for liquid (mixture) into its vapour, transferring the vapour to another place & recovering the liquid by condensing the vapour. Usually by allowing it to coming contact with cold surface. PRINCIPLE Liquid boil when its vapour pressure is equal to atmospheric pressure. Simple distillation conducted at its boiling point. The higher the relative volatility of liquid the better the separation. Heat is supplied to liquid so that it boils & resulting vapour condensed. CONSTRUCTION It consists of a distillation flask with a side arm sloping downwards. A condenser if fitted into the side arm by means of a cork. The condenser is usually is water condenser. The condenser is connected to receiver flask by means of adaptor. `
  • 3. PROCEDURE The liquid is to be distilled its filled into the flask. A thermometer is inserted in to the cork & fixed to the flask. The water is circulated through jacket of condenser. The heat is supplied & content is heated & boiled after some time. The vapour rises up & passes down the side arm into the condenser the temperature rises rapidly & reaches a constant value the temperature is equal to the boiling point of liquid finally the vapour form are condense & collected in to receiver. APPLICATIONS → It is used for preparation distilled water & water for injection. → Volatile & aromatic water are prepared. → Nonvolatile solid are separated from volatile liquid.
  • 4. FLASH DISTILLATION It is defined as the process in which the enter liquid is suddenly vaporized by passing it term high pressure zone to low. PRINCIPLE When a hot liquid mixture is allowed to enter form high pressure zone to vaporized suddenly during this process the chamber get cooled the individual vapour. Vapour phase molecule of high boiling fraction get condensed, while low boiling fraction remain as vapour. This process requires for the equilibrium to reach & therefore the liquid & vapour are held in contact with each other for some period of time & then are separated. The vapour are further condensed & collected. CONSTRUCTION It consists of a pump, which is connected to a feed reservoir. Pump helps in pumping the feed into heating chamber which consists of suitable heating mechanism. The other end of the pipe is directly introduced into the vapour-liquid separator through a reducing valve. The vapour outlet is provide at the top of the separator & liquid outlet is provided at the bottom.
  • 5. WORKING The feed is pumped through a heater at a certain pressure. The liquids get heated, which enters the vapour-liquid separator through a pressure reducing valve. Due to the drop-in pressure the liquid flashes, which further enhances the vaporization process. Suddenly vaporization induces cooling. The individual vapour phase molecules of high boiling fraction get condensed while the low boiling fraction remains as vapour. The mixture is allowed for a sufficient time, so that vapour & liquid portions separate & achieve equilibrium. USES It is used for separating components, which boils at widely different temperatures. It is widely used in petroleum industry. ADVANTAGES → It is used for obtaining multi-components. → It can be used in continuous mode. DISADVANTAGES ❑ It is not suitable for two components systems. ❑ It is not suitable if the separated components are needed in pure quality.
  • 6. It is the type of distillation process which involve separation of mixable liquids. The process involves repeated distillation & condensation & the mixture I usually separated into components parts; the separation happens when the mixture is heated at a certain temperature. Where fraction of the mixture starts to vaporized. PRINCIPLE The basic principle of this type of distillation is that differ boil & evaporates at different temperature so when the mixture is heated, substance with power boiling point start to boil first & convert in to vapour. CONSTRUCTION It consists of a fractionating column, distillation flask, condenser, receiver & heat source. The fractionating column is inserted between the still & condenser at the top of column, a condenser is provided & heat is supplied at the bottom of the column. FRACTIONAL DISTILLATION
  • 7. WORKING The mixture to be distilled is feed to the boiler & heated. A mixture of two mixable liquids A & B is taken where A have more volatility then B. The solution is added into the flask, heat is applied & the mixture starts to boil the vapour are formed having large amount of vapour from liquid A. these vapour moves through the fractalizing column into the condenser where it is cool down to form a liquid which is collected into the receiver. Vaporization & condensation takes place throughout the process until two mixtures are separated completely. USES Use for purification of water as well as separating water & acetone. Use in several industries like oil binaries & chemical plants for purification & separation of organic compounds. ADVANTAGES It is used for separating large amount of mixable liquid according to their boiling point. Example: acetone & water. DISADVANTAGES This method cannot be used to separate mixable liquid from azeotropic mixture.
  • 8. DISTILLATION UNDER REDUCE PRESSURE it is defined as a process in which liquids is distilled at a temperature lower than its boiling point by applications of vacuum. PRINCIPLE Liquid boil when its vapour pressure is equal to atmospheric pressure. If the external pressure is reduced by applications of vacuum, the boiling point of liquid decreases therefore the liquid boils at lower temperature. CONSTRUCTION Distillation under reduced pressure or vacuum is carried out in a specially designed glass apparatus. A to necked ‘Claisen’s flask’ is used, the main neck of which is fitted with along capillary tube (capillary tubes avoids bumping) & the side neck being fitted with a thermometer. The side tube is connected to a condenser carrying a receiver at the other end. The receiver is attached to a vacuum pump to reduce the pressure. The pressure is measured with the help of a manometer.
  • 9. WORKING The liquid to be distilled is filled into the flask. The reducing vacuum applied and content or heated gradually. The temperature rises & get vaporized rapidly due to vacuum. the vapour passes through the condenser & conduced is collected into the receiver. The temperature is noted which is less than the boiling point of the liquids. ADVANTAGES This method is used for the compound which degraded or higher temperature. Example: Enzymes, vitamins & alkaloids etc. DISADVANTAGES ❑ In vacuum distillation persistent foaming occurs. ❑ Not suitable for preparation of semi-solids or solid extracts.
  • 10. STEAM DISTILLATION PRINCIPLE Steam distillation is a method of distillation carried out with the help of steam & used for separation of high boiling substance from non-volatile impurities. A mixture of immixible liquids begainst to boil when the some of their vapour pressure, is equal to atmospheric pressure. For volatile- substance which are mixable with water steam distillation involve the principle of fractional distillation. CONSTRUCTIONS It consists of steam can with a cork having two holes in one-hole safety tube is attached & through another hole a vent tube is pumped, the other the bent tube is connected to the flask, containing non-aqueous liquids. A delivery tube is insulted is the second flask which connect flask & condenser.
  • 11. WORKING The non-aqueous liquid is placed in the flask. The small quantity of water is added to it. Steam can be filled with water; the flask & steam can are heated simentionally. This steam carries the volatile oil & passes in to the condenser which is cooled in to the receiver the process is continued until all the non-aqueous liquid has been distilled. In the receiver water & organic liquid forms two separate dyes which can be easily separated. APPLICATION ❑ It is used of separation of immixible liquids. Example: Toluene & water. ❑ It is used for extraction of most of the volatile oil like clobe like. ❑ Camphor is also distilled by this method. ADVANTAGES → Volatile oil can be separated at lower temperature is steam distillation, without loss of aroma. → It is useful in purification li liquids with high boiling points. → Provided molecular weight. DISADVANTAGES Not suitable when immixible liquids & water reacts with each other.
  • 12. MOLECULAR DISTILLATION A process in which each molecule in the vapour phase travels the mean free path & gets condensed individually without intermolecular collisions on application of vacuum. PRINCIPLE The substance to be distilled have very low vapour pressure i.e. viscous liquid, oils, waxy material & high molecular weight substance. These boils at very high temperature in order to decrease boiling point of liquid high vacuum is applied. The mean free path of a molecule is defined as average distance through which a molecule can move without coming in to collision with each other. Its express as-  =  3/p Where p = vapour pressure.  = density. The mean free path can be increase by desecrating the viscosity. REQUIRMENT FOR MOLECULAR DISTILLATION 01). The evaporating surface must bee closed to condensing surface this insure the molecular to come in contact with the condenser a soon as they leave the evaporating surface. 02). The liquid surface area must be large as possible, because the vapour is evoled from the surface of the molecule. 03). The molecular collision should be minimizing because the change of direction path of molecules.
  • 13. ❑ More frequently used in the refining of fixed oils. ❑ Vitamin A is separated from fish liver oil. ❑ Purification of chemicals, “tricresyl phosphate”. APPLICATION
  • 14. FALLING FILM MOLECULAR STILL PRINCIPLE In this method vaporization occurs from the film of liquid flowing down a heated surface under high vacuum. The vapors travel short distance & strike condenser. Each molecule is condensed= individually & distillate is collected. CONSTRUCTION It consists of a vessel of diameter 1m, the wall of the vessel is provided with jacket. Wipers are provided to the vessel wall which are connected to rotating head to motor & condenser are arranged very closed to wall of vessel. Vacuum pump is also connected to the vessel.
  • 15. WORKING The vessel is heated & vacuum is applied at the center. Wipers are allowed to rotate and it is entered as the liquid flow down it spread o from a film by wipers, which are moving at a speed of 3m/sec. Since the moving at an already heated, the liquid films evaporate directly. Vapour travel its mean free path & strike the condenser, the condensate is collected in vessels. It is used purification chemicals such a di-methyl thalate. Vitamin A is separated from oil. ADVANTAGES Short residence time of the feed. Significantly lower temperature is required due to high vacuum. DISADVANTAGES This is not used for azeotropic mixture. USES