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Distillation and Alcohol
Production Application
Distillation and Alcohol
Production Application
Distillation and Alcohol
Production Application
 Distillation process
 Types of distillation
 Distillation equipment & properties of them
 Alcohol production
 Distillation of alcohol
 Types of alcohol distillation
Distillation
 Distillation is a kind of separation technique of two or more
volatile liquid compounds by using the difference in boiling
points and relative volatility.
 The process takes place in a column, and two heat
exchangers.
 In the column two phases, liquid and gas, are distributed to
enrich the vapor in more volatile compounds and enrich the
liquid phase on less volatile compounds.
 Mass transfer is the key to a successful distillation.
Advantages & Disadvantages
Advantages
 It has simple flowsheet, low
capital investment, and low
risk. If components to be
separated have a high
relative volatility difference
and are thermally stable,
distillation is hard to beat.
Disadvantages
 Distillation has a low energy
efficiency and requires thermal
stability of compounds at their
boiling points. It may not be
attractive when azeotropes are
involved or when it is necessary
to separate high boiling
components, present in small
concentrations, from large
volumes of a carrier, such as
water.
Types of Distillation
 Continuous Distillation
 Batch Distillation
 Semi-Batch Distillation
Continuous Distillation
 The mixture which is to be
separated is fed to column at
one or more points.
 Liquid mixture runs down the
column while vapor goes up.
 Vapor is produced by partial
vaporisation of the mixture
which is heated in reboiler.
 Then vapor is partially
condensed to earn back the
less volatile compounds to the
column to separate as bottom
product. (reflux)
Batch Distillation
 The oldest operation used
for separation of liquid
mixtures.
 Feed is fed from bottom,
where includes reboiler, to
be processed.
 Numbers of accumulator
tanks are connected to
collect the main and the
intermediate distillate
fractions.
Semi-batch Distillation
 Semi-batch distillation is
very similar to batch
distillation.
 Feed is introduced to
column in a continuous or
semi-continuous mode.
 It is suitable for extractive
and reactive distillations.
Comparison of Distillation Types
 For batch distillation, it is
enough to use only one
column to separate
multicomponent liquid
mixture.
 One sequence of
operation is enough to
separate all the
components in a mixture.
 For continuous distillation,
to separate multi-
component liquid mixtures,
more than one columns are
necessary to be used.
 One column is dedicated to
separate a specific mixture
and specific operation.
Equipment Designs
 Plate Columns (Tray Columns)
 Packed Beds
Plate Columns (Tray Columns)
 It is the most widely used kind of distillation
column.
 Trays are shaped to maximize the liquid-
vapor contact and increase the mass
transfer area.
 Tray types include sieve, valve & bubble
cap.
Advantages & Disadvantages
Advantages
 Least expensive column for
diameters greater than 0.6m
 The liquid-vapor contact in the
cross-flow of plate columns is
more effective than counter-
current-flow in packed columns.
 Cooling coils can be easily added
to the plate column
 Can handle high liquid flow rates.
Disadvantages
 Higher pressure drops than packed
columns
 Foaming can occur because the
liquid is agitated by the vapor
flowing up through it.
Packed Beds
 Packings can be provided either as dumped or
stacked.
 Dumped packing constitutes of bulk inert
materials.
 Stacked packing is includes meshwork which has
the same diameter with the column.
 Important criteria for packings are efficient
contact (liquid-vapor), resistance to flow, flow
capacity, resistance of packing against corrosion.
Advantages & Disadvantages
 When the diameter is less
than 0.6m it is less
expensive than the plate
column.
 Packing is able to handle
corrosive materials.
 Lower pressure drop than
in plate columns.
 Good for thermally sensitive
liquids.
 Can break during installation
or due to thermal expansion.
 Not cost efficient for high
liquid flow rates.
 Contact efficiencies are
decreased when the liquid
flow rate is too low.
Making of Alcohol
 Alcohols, generally can be
created by reduction of aldehydes
or twice reduction of ketones.
 Ethanol (C2H5OH) can produced
by fermentation of molasses.
 Fermentations is done in a tank
and it is cleaned and sterilized
before the fermentation begins.
 Molasses have strong concentration of sugar which
doesn't provide the adequate conditions for
fermentation. Consequently it must be diluted to
concentration of %17 sugar.
 Optimum environmental pH range is between 4.0
and 5.0; and optimum temperature is 76°F (25°C).
 Fermented molasses is called beer and it contains
%6.5 to %11 alcohol by volume.
Making of Alcohol
Distillation of Alcohol
 Under 1 atmosphere pressure
boiling points of water and alcohol
are 100°C and 78.3°C.
• Water and ethyl alcohol mixture forms an azeotrope in
atmospheric pressure at a mole fraction of %89.4 of ethyl alcohol
which means that by simple distillation of ethyl alcohol, it cannot
be purified more than %95.6 w.
• As distillation equipment, bubble cap trays and tray columns are
mostly used in alcohol distillation.(Figure on left)
Pot Distillation Process (Batch
Distillation)
 Entire batch of beer is
heated in a large container
and alcohol/water vapours
are channelled into a
distillation column.
 After all the boiling and
reflux operations, when
almost all alcohol is boiled,
process is stopped and
stillage is removed.
 The basic advantage of pot distillation is its
simplicity. It has simple equipment system.
Fermentation and boiling for distillation can take
place at the same pot, which makes it more
practical
 The disadvantage of the pot distillation is low
distillation efficiency. It requires about three times
more energy comparing to continuous distillation.
Pot Distillation Process (Batch
Distillation)
Continuous-Feed Distillation
Process
 Typically it is also known as
continuous distillation.
 Alcohol/liquid mixture is fed to
column and it flows.
 Flow rate is decreased by trays.
 Mixture boils up in the reboiler and
goes up of the column to
condenser as it contacts with the
condensed liquid.
 The vapor with high alcohol
percent leaves the condenser to
be collected in accumulator.
 The advantage of the continuous feed distillation
process is it's high energy efficiency comparing to
the pot distillation process. Eventually amount of
energy required for per litre of alcohol is less than
in pot distillation. On the other hand it can operate
for long hours (almost 8000 hours per annum)
 The disadvantage of continuous feed distillation is
it needs a little more complicated equipment
system comparing to the batch distillation.
Continuous-Feed Distillation
Process
Vacuum Distillation
 Low temperature allows us to
achieve higher alcohol
concentrations.
 At a pressure below 0.1
atmosphere azeotrope
disappears and enables to
distillate to almost 100 percent
alcohol.
 Because of the high
operation and
installation costs, low
energy efficiency,
vacuum distillation
appears to be
uneconomical in the
commercial
applications.
Vacuum Distillation
Azeotropic Distillation
 This type of distillation is used for processes that produce almost
100% alcohol with help of an organic solvent and two additional
distillations.
 A solvent (pentane, gasoline etc.) is added to distillation product
coming out of the usual distillation column.
 Mixture is fed to another distillation column which separates it into a
top product and a bottom product.
 Distillate of this column is fed to a third column which distils out the
solvent leaving the mixture of alcohol-water.
 Solvent is recycled and never gets out.
 System is hard to design and it is more complicated comparing to
ordinary distillation system.

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Distillation and Alcohol Production Application.ppt

  • 1. Distillation and Alcohol Production Application Distillation and Alcohol Production Application
  • 2. Distillation and Alcohol Production Application  Distillation process  Types of distillation  Distillation equipment & properties of them  Alcohol production  Distillation of alcohol  Types of alcohol distillation
  • 3. Distillation  Distillation is a kind of separation technique of two or more volatile liquid compounds by using the difference in boiling points and relative volatility.  The process takes place in a column, and two heat exchangers.  In the column two phases, liquid and gas, are distributed to enrich the vapor in more volatile compounds and enrich the liquid phase on less volatile compounds.  Mass transfer is the key to a successful distillation.
  • 4.
  • 5. Advantages & Disadvantages Advantages  It has simple flowsheet, low capital investment, and low risk. If components to be separated have a high relative volatility difference and are thermally stable, distillation is hard to beat. Disadvantages  Distillation has a low energy efficiency and requires thermal stability of compounds at their boiling points. It may not be attractive when azeotropes are involved or when it is necessary to separate high boiling components, present in small concentrations, from large volumes of a carrier, such as water.
  • 6. Types of Distillation  Continuous Distillation  Batch Distillation  Semi-Batch Distillation
  • 7. Continuous Distillation  The mixture which is to be separated is fed to column at one or more points.  Liquid mixture runs down the column while vapor goes up.  Vapor is produced by partial vaporisation of the mixture which is heated in reboiler.  Then vapor is partially condensed to earn back the less volatile compounds to the column to separate as bottom product. (reflux)
  • 8. Batch Distillation  The oldest operation used for separation of liquid mixtures.  Feed is fed from bottom, where includes reboiler, to be processed.  Numbers of accumulator tanks are connected to collect the main and the intermediate distillate fractions.
  • 9. Semi-batch Distillation  Semi-batch distillation is very similar to batch distillation.  Feed is introduced to column in a continuous or semi-continuous mode.  It is suitable for extractive and reactive distillations.
  • 10. Comparison of Distillation Types  For batch distillation, it is enough to use only one column to separate multicomponent liquid mixture.  One sequence of operation is enough to separate all the components in a mixture.  For continuous distillation, to separate multi- component liquid mixtures, more than one columns are necessary to be used.  One column is dedicated to separate a specific mixture and specific operation.
  • 11. Equipment Designs  Plate Columns (Tray Columns)  Packed Beds
  • 12. Plate Columns (Tray Columns)  It is the most widely used kind of distillation column.  Trays are shaped to maximize the liquid- vapor contact and increase the mass transfer area.  Tray types include sieve, valve & bubble cap.
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  • 23. Advantages & Disadvantages Advantages  Least expensive column for diameters greater than 0.6m  The liquid-vapor contact in the cross-flow of plate columns is more effective than counter- current-flow in packed columns.  Cooling coils can be easily added to the plate column  Can handle high liquid flow rates. Disadvantages  Higher pressure drops than packed columns  Foaming can occur because the liquid is agitated by the vapor flowing up through it.
  • 24. Packed Beds  Packings can be provided either as dumped or stacked.  Dumped packing constitutes of bulk inert materials.  Stacked packing is includes meshwork which has the same diameter with the column.  Important criteria for packings are efficient contact (liquid-vapor), resistance to flow, flow capacity, resistance of packing against corrosion.
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  • 32. Advantages & Disadvantages  When the diameter is less than 0.6m it is less expensive than the plate column.  Packing is able to handle corrosive materials.  Lower pressure drop than in plate columns.  Good for thermally sensitive liquids.  Can break during installation or due to thermal expansion.  Not cost efficient for high liquid flow rates.  Contact efficiencies are decreased when the liquid flow rate is too low.
  • 33. Making of Alcohol  Alcohols, generally can be created by reduction of aldehydes or twice reduction of ketones.  Ethanol (C2H5OH) can produced by fermentation of molasses.  Fermentations is done in a tank and it is cleaned and sterilized before the fermentation begins.
  • 34.  Molasses have strong concentration of sugar which doesn't provide the adequate conditions for fermentation. Consequently it must be diluted to concentration of %17 sugar.  Optimum environmental pH range is between 4.0 and 5.0; and optimum temperature is 76°F (25°C).  Fermented molasses is called beer and it contains %6.5 to %11 alcohol by volume. Making of Alcohol
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  • 36. Distillation of Alcohol  Under 1 atmosphere pressure boiling points of water and alcohol are 100°C and 78.3°C. • Water and ethyl alcohol mixture forms an azeotrope in atmospheric pressure at a mole fraction of %89.4 of ethyl alcohol which means that by simple distillation of ethyl alcohol, it cannot be purified more than %95.6 w. • As distillation equipment, bubble cap trays and tray columns are mostly used in alcohol distillation.(Figure on left)
  • 37. Pot Distillation Process (Batch Distillation)  Entire batch of beer is heated in a large container and alcohol/water vapours are channelled into a distillation column.  After all the boiling and reflux operations, when almost all alcohol is boiled, process is stopped and stillage is removed.
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  • 40.  The basic advantage of pot distillation is its simplicity. It has simple equipment system. Fermentation and boiling for distillation can take place at the same pot, which makes it more practical  The disadvantage of the pot distillation is low distillation efficiency. It requires about three times more energy comparing to continuous distillation. Pot Distillation Process (Batch Distillation)
  • 41. Continuous-Feed Distillation Process  Typically it is also known as continuous distillation.  Alcohol/liquid mixture is fed to column and it flows.  Flow rate is decreased by trays.  Mixture boils up in the reboiler and goes up of the column to condenser as it contacts with the condensed liquid.  The vapor with high alcohol percent leaves the condenser to be collected in accumulator.
  • 42.  The advantage of the continuous feed distillation process is it's high energy efficiency comparing to the pot distillation process. Eventually amount of energy required for per litre of alcohol is less than in pot distillation. On the other hand it can operate for long hours (almost 8000 hours per annum)  The disadvantage of continuous feed distillation is it needs a little more complicated equipment system comparing to the batch distillation. Continuous-Feed Distillation Process
  • 43. Vacuum Distillation  Low temperature allows us to achieve higher alcohol concentrations.  At a pressure below 0.1 atmosphere azeotrope disappears and enables to distillate to almost 100 percent alcohol.
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  • 45.  Because of the high operation and installation costs, low energy efficiency, vacuum distillation appears to be uneconomical in the commercial applications. Vacuum Distillation
  • 46. Azeotropic Distillation  This type of distillation is used for processes that produce almost 100% alcohol with help of an organic solvent and two additional distillations.  A solvent (pentane, gasoline etc.) is added to distillation product coming out of the usual distillation column.  Mixture is fed to another distillation column which separates it into a top product and a bottom product.  Distillate of this column is fed to a third column which distils out the solvent leaving the mixture of alcohol-water.  Solvent is recycled and never gets out.  System is hard to design and it is more complicated comparing to ordinary distillation system.
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