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CAREER POINT UNIVERSITY
MAJOR ASSIGNMENT
ON
ABSORPTION REFRIGERATION TECHNOLOGY
SUBMITTED TO
MR. ADITYA MISHRA
DEPT.OF (M.E.)
SUBMITTED BY
Deepak Nagar
KID-K10880
B.Tech. (M.E.)
6th Semester
TABLE OF CONTENT
 HISTORY
 INTRODUCTION
 PRINCIPAL OF OPERATION
 PROPERTY OF WORKING FLUID
 FLUID FOR REFERIGERATION SYSTEM
 ADVANTAGES
 CONCLUSION
HISTORY
 The early development of an absorption cycle dates back to the
1700’s. It was known that ice could be produced by an
evaporation of pure water from a vessel contained within an
evacuated container in the presence of sulfuric acid.
 In1810, ice could be made from water in a vessel, which was
connected to another vessel containing sulfuric acid.
 As the acid absorbed water vapor, causing a reduction of
temperature, layers of ice were formed on the water surface.
 The major problems of this system were corrosion and leakage of
air into the vacuum vessel. In 1859,Ferdinand Carre introduced a
novel machine using water/ammonia as the working fuel.
 In the 1950’s, a system using lithium bromide/water as the
working fluid was introduced for industrial applications.
INTRODUCTION
 Most of industrial process uses a lot of thermal energy by
burning fossil fuel to produce steam or heat for the purpose.
 After the processes, heat is rejected to the surrounding as waste.
 This waste heat can be converted to a useful refrigeration by
using a heat operated refrigeration system, such as an absorption
refrigeration cycle.
 Electricity purchased from utility companies for conventional
vapor compression refrigerators can be reduced.
 The use of heat operated refrigeration systems help reduce
problems related to global environmental, such as the so called
greenhouse effect from CO2 emission from the combustion of
fossil fuels in utility power plants.
PRINCIPAL OF OPERATION
 The working fluid in an absorption refrigeration system is a
binary solution consisting of refrigerant and absorbent.
 Two evacuated vessels are connected to each other. The left
vessel contains liquid refrigerant while the right vessel contains a
binary solution of absorbent/refrigerant.
 The solution in the right vessel will absorb refrigerantvapor
from the left vessel causing pressure to reduce.
 While the refrigerant vapor is being absorbed, the temperature
of the remaining refrigerant will reduce as a result of its
vaporization.
 This causes a refrigeration effect to occur inside the left vessel. At
the same time, solution inside the right vessel becomes more
dilute because of the higher content of refrigerant absorbed. This
is called the “absorption process”.
 Normally, the absorption process is an exothermic process,
therefore, it must reject heat out to the surrounding in order to
maintain its absorption capability.
 Whenever the solution cannot continue with the absorption
process because of saturation of the refrigerant, the refrigerant
must be separated out from the diluted solution.
 Heat is normally the key for this separation process. It is applied
to the right vessel in order to dry the refrigerant from the
solution.
 The refrigerant vapor will be condensed by transferring heat to
the surroundings.
 With these processes, the refrigeration effect can be produced
by using heat energy.
 However, the cooling effect cannot be produced continuously as
the process cannot be done simultaneously.
PROPERTIES OF WORKING FLUID
FOR ABSORTIPON REFERIGERATION
SYSTEM
In addition to these requirements, the following are desirable :
 The elevation of boiling (the difference in boiling point
between the pure refrigerant and the mixture at the same
pressure) should be as large as possible.
 Refrigerant should have high heat of vaporization and high
concentration within the absorbent in order to maintain low
circulation rate between the generator and the absorber per
unit of cooling capacity.
 Both refrigerant and absorbent should be non-corrosive,
environmental friendly,and low-cost.
WORKING FLUID FOR
ABSORTIPON REFERIGERATION
SYSTEM
 Most common working fluids are Water/NH3 and LiBr/water.
 Since the invention of an absorption refrigeration system, water
NH3 has been widely used for both cooling and heating purposes.
 Both NH3 (refrigerant) and water (absorbent) are highly stable for
a wide range of operating temperature and pressure.
 NH3 has a high latent heat of vaporization, which is necessary for
efficient performance of the system. It can be used for low
temperature applications, as the freezing point of NH3 is 77°C.
 The use of LiBr/water for absorption refrigeration systems began
around 1930.
 Two outstanding features of LiBr/water are non-volatility
absorbent of LiBr and extremely high heat of vaporization of water
(refrigerant).
ADVANTAGES
 Most vapor compression systems commonly use
chlorofluorocarbon refrigerants (CFCs), because of their
thermo physical properties.
 It is through the restricted use of CFCs, due to depletion
of the ozone layer that will make absorption systems
more prominent.
 However, although absorption systems seem to provide
many advantages, vapor compression systems still
dominate all market sectors.
 In order to promote the use of absorption systems,
further development is required to improve their
performance and reduce cost.
CONCLUSION
 Current research and development efforts on multi-
effect cycles show considerable promise for future
application. A combined ejector-absorption system [92]
is another possible option. This system can provide COP
as high as a double-effect system with little increase in
system complexity.
 A diffusion absorption refrigeration system is the only
true heat-operated refrigeration cycle. This system has
been widely used as a domestic refrigerator. However, it
is only available with small cooling capacity and its COP
is low (0.1 to 0.2). Many attempts have been made to
improve its performance.
THANK YOU

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K10880 deepaknagar vapour absorption technology

  • 1. CAREER POINT UNIVERSITY MAJOR ASSIGNMENT ON ABSORPTION REFRIGERATION TECHNOLOGY SUBMITTED TO MR. ADITYA MISHRA DEPT.OF (M.E.) SUBMITTED BY Deepak Nagar KID-K10880 B.Tech. (M.E.) 6th Semester
  • 2. TABLE OF CONTENT  HISTORY  INTRODUCTION  PRINCIPAL OF OPERATION  PROPERTY OF WORKING FLUID  FLUID FOR REFERIGERATION SYSTEM  ADVANTAGES  CONCLUSION
  • 3. HISTORY  The early development of an absorption cycle dates back to the 1700’s. It was known that ice could be produced by an evaporation of pure water from a vessel contained within an evacuated container in the presence of sulfuric acid.  In1810, ice could be made from water in a vessel, which was connected to another vessel containing sulfuric acid.  As the acid absorbed water vapor, causing a reduction of temperature, layers of ice were formed on the water surface.  The major problems of this system were corrosion and leakage of air into the vacuum vessel. In 1859,Ferdinand Carre introduced a novel machine using water/ammonia as the working fuel.  In the 1950’s, a system using lithium bromide/water as the working fluid was introduced for industrial applications.
  • 4. INTRODUCTION  Most of industrial process uses a lot of thermal energy by burning fossil fuel to produce steam or heat for the purpose.  After the processes, heat is rejected to the surrounding as waste.  This waste heat can be converted to a useful refrigeration by using a heat operated refrigeration system, such as an absorption refrigeration cycle.  Electricity purchased from utility companies for conventional vapor compression refrigerators can be reduced.  The use of heat operated refrigeration systems help reduce problems related to global environmental, such as the so called greenhouse effect from CO2 emission from the combustion of fossil fuels in utility power plants.
  • 5. PRINCIPAL OF OPERATION  The working fluid in an absorption refrigeration system is a binary solution consisting of refrigerant and absorbent.  Two evacuated vessels are connected to each other. The left vessel contains liquid refrigerant while the right vessel contains a binary solution of absorbent/refrigerant.  The solution in the right vessel will absorb refrigerantvapor from the left vessel causing pressure to reduce.  While the refrigerant vapor is being absorbed, the temperature of the remaining refrigerant will reduce as a result of its vaporization.  This causes a refrigeration effect to occur inside the left vessel. At the same time, solution inside the right vessel becomes more dilute because of the higher content of refrigerant absorbed. This is called the “absorption process”.
  • 6.  Normally, the absorption process is an exothermic process, therefore, it must reject heat out to the surrounding in order to maintain its absorption capability.  Whenever the solution cannot continue with the absorption process because of saturation of the refrigerant, the refrigerant must be separated out from the diluted solution.  Heat is normally the key for this separation process. It is applied to the right vessel in order to dry the refrigerant from the solution.  The refrigerant vapor will be condensed by transferring heat to the surroundings.  With these processes, the refrigeration effect can be produced by using heat energy.  However, the cooling effect cannot be produced continuously as the process cannot be done simultaneously.
  • 7. PROPERTIES OF WORKING FLUID FOR ABSORTIPON REFERIGERATION SYSTEM In addition to these requirements, the following are desirable :  The elevation of boiling (the difference in boiling point between the pure refrigerant and the mixture at the same pressure) should be as large as possible.  Refrigerant should have high heat of vaporization and high concentration within the absorbent in order to maintain low circulation rate between the generator and the absorber per unit of cooling capacity.  Both refrigerant and absorbent should be non-corrosive, environmental friendly,and low-cost.
  • 8. WORKING FLUID FOR ABSORTIPON REFERIGERATION SYSTEM  Most common working fluids are Water/NH3 and LiBr/water.  Since the invention of an absorption refrigeration system, water NH3 has been widely used for both cooling and heating purposes.  Both NH3 (refrigerant) and water (absorbent) are highly stable for a wide range of operating temperature and pressure.  NH3 has a high latent heat of vaporization, which is necessary for efficient performance of the system. It can be used for low temperature applications, as the freezing point of NH3 is 77°C.  The use of LiBr/water for absorption refrigeration systems began around 1930.  Two outstanding features of LiBr/water are non-volatility absorbent of LiBr and extremely high heat of vaporization of water (refrigerant).
  • 9. ADVANTAGES  Most vapor compression systems commonly use chlorofluorocarbon refrigerants (CFCs), because of their thermo physical properties.  It is through the restricted use of CFCs, due to depletion of the ozone layer that will make absorption systems more prominent.  However, although absorption systems seem to provide many advantages, vapor compression systems still dominate all market sectors.  In order to promote the use of absorption systems, further development is required to improve their performance and reduce cost.
  • 10. CONCLUSION  Current research and development efforts on multi- effect cycles show considerable promise for future application. A combined ejector-absorption system [92] is another possible option. This system can provide COP as high as a double-effect system with little increase in system complexity.  A diffusion absorption refrigeration system is the only true heat-operated refrigeration cycle. This system has been widely used as a domestic refrigerator. However, it is only available with small cooling capacity and its COP is low (0.1 to 0.2). Many attempts have been made to improve its performance.