18. PROCEDURE:
The liquid to be distilled is filled into the flask to one-half to two-
third of its volume
Bumping is avoided by adding small pieces of porcelain before
distillation
A thermometer inserted into the cork and fixed to the flask below the
level of the side arm.
Water is circulated through the condenser.
The contents are heated gradually. The liquids begin to boil after
sometime.
The vapour begin to rise up and passes down the side arm into the
condenser.
The temp rises gradually and reaches constant value.
The temperature of the distillate is noted down, which is equal to the
boiling point of the liquid.
The vapour is condensed and collected into the receiver.
Distillation is continued until a small volume of liquid remaining in
the flask.
19.
20.
21.
22. Working:
The feed is pumped through a heater at a certain
pressure.
The liquid get heated, which enters the vapour-
liquid separator through a pressure reducing valve.
Due to drop in pressure, the hot liquid flashes,
which further enhancing the vaporization
process.
The sudden vapourization induce cooling.
The individual vapour phase molecules of high
boiling fraction get condensed, while low boiling
fraction remains as vapour.
The mixure is allowed for sufficient time, so that
liquid and vapour portions separate and attain
equilibrium.
The vapour is separated through a pipe from above
and liquid is collected from the bottom of the
separator.
23.
24.
25.
26. Working:
The mixture to be distilled is fed to the
boiler and heated.
Fractionating column is inserted between
still and the condenser.
Consider a mixture of two miscible liquids
A and B containing 20% of A and 80% of
B.
Liquid A is more volatile component
having a lower boiling point .
Liquid B is less volatile component having
a higher boiling point.
When the boiling point of the mixture
reached, the vapour composition curves
are drawn.
27. These curves indicate that the vapour contains 60%
of A.
When this vapour is condensed, the resulting liquid
is again heated to boiling, this vapour gives the
composition containing 90% of A (second pair of
curve from the bottom).
This vapour impinging on a cool surface and get
condensed.
This fraction is revapourised by heating to its
boiling point. This boiling point curve of this
distillate indicates 98% of A. (third pair of curve
from the bottom)
This fraction of vapour impinges on a cooling
surface. This gives 4th pair of curves. Now this
vapour contains higher proportion of A.
The vapour moves to a condenser at the top of the
column and get condensed
Thus repetition of these processes yield pure A.
28. DISTILLATION UNDER REDUCED PRESSURE
It is defined as a distillation process in which the liquid is distilled at a
temperature lower than its boiling point by the application of vacuum.
Principle:
Liquid boils when vapour pressure is equal to the atmospheric pressure.
If the external pressure is reduced by applying vaccum, the boiling point of
the liquid decreases.
Therefore the liquid boils at a lower temperature.
Example:
Water bolis at 100°c at an atmospheric pressure 101.31kPa (760mmHg)
Vapour pressure of the water is 9.33kPa (70mm Hg) at 40°c.
Hence external pressure is reduced to 9.33kPa (70mm Hg) where water boils
at 40°c.
This results is an increase in the rate of mass transfer into vapour.
29. Application:
Changing physical form:
Preventing degradation of active constituent:
During extraction, concentration and processing at higher temp, the active
constituents may undergo decomposition. Hence extraction and
concentration should be done at a lower temp under reduced pressure.
Disadvantages
Not suitable for the preparation of semisolid or solid extract.
In vaccum distillation, persistant foaming occurs. This may be overcome by
adding capryl slcohol to the liquid.
30. PROCEDURE:
The liquid to be distilled is filled into the
flask to one-half to two-third of its
volume
Bumping is avoided by adding small
pieces of porcelain before distillation.
The capillary tube and thermometer are
kept in place in the flask.
The required vaccum is applied.
The contents are heated gradually. the
temp rises and liquid gets vaporized
rapidly due to vacuum.
The vapour passes through the condenser.
The condensate is collected in the receiver.
The temperature is noted down, which
would be less than the boiling point of the
liquid.
31.
32.
33.
34. working:
• The flask is filled with non aqueous
liquid.
• A small amount of water is added to it.
water is filled in the steam can.
• Both the flask and the steam can be
heated simultaneously to maintain a
uniform flow od steam through the
boiling mixture.
• The mixture heats up and steam carries
the volatile oil into the condenser where
the oil gets cooled by the cold water.
• The condensed immiscible liquid is
collected in the receiver.
• It is continues till all the non aqueous
liquid distils off.
• Water and organic liquid collects in the
receiver as two distinct laters which are
separated usind a separating flask.
35.
36.
37.
38.
39.
40.
41. Centrifugal molecular still:
• Vaccum is applied at the center of the
vessel.
• The buket shaped vessel allowed to rotate
at high speed.
• The feed is introduced from the center of
the vessel.
• Due to the centrifugal action of the rotating
bucket, liquid moves outward over the
surface of the vessel and forms a film.
• since, the radiant heater heat the surface,
the liquid evaporates directly from the film.
• The vapour travels its mean free path and
strikes the condenser.
• The condensate is collected into another
vessel.
• The residue is collected from the bottom of
the vessel and is recirculated through the
feed port for further distillation.
42. Wiped film molecular still:
• The vessel is heated by suitable means.
• Vaccum is applied at the center of the vessel
and wipers are allowed to rotate.
• The feed is entered through the inlet of the
vessel.
• As the liquid flows down the wall, it is spread
to form s film by PTFE (poly tetra fluoro
ethylene) wipers, which are moving at arate of
3meters per second.
• The velocity of the film evaporates directly.
• The vapour travels its mean free path anf
strikes the condenser.
• The condensate is collected into a vessel.
• The residue is collected from the bottom of the
vessel and re circulated through the feed port
for further distillation.
• Capacity is about 1000litre per unit.