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CASE STUDY OF LIQUID SUCTION
HEAT EXCHANGER IN MECHANICAL
REFRIGERATION SYSTEM USING
ALTERNATIVE REFRIGERANTS.
PRESENTED BY: COORDINATED BY:
Samir Ghorasainee Keshav Acharya
Sampanna Dhakal Teaching Assistant
Sanam Sapkota Purwanchal Campus,
Sanchita Sapkota Dharan
Mechanical Refrigeration System
 Mechanical refrigeration, often referred to as refrigeration or air
conditioning, is a process by which heat is removed from a location
using a human-made heat exchange system.
 As the refrigerant circulates through the system, it is alternately
compressed and expanded, changing its state from a liquid to a
vapor.
Components of
Refrigeration Cycle
Evaporator : It absorbs heat from
refrigerating space.
Compressor : It increases the pressure
and temperature of refrigerant through
compression.
Condenser : It releases the heat into
surrounding.
Expansion Valve : It decreases the
pressure of the refrigerant.
Modification of the System
 Many studies have been done to
modify and enhance the performance
and energy consumption of the
mechanical refrigeration system.
 Using heat exchanger in the mechanical
refrigeration system is one of the
effective technique that can be used to
improve the energy performance of the
system.
 A LSHX is a counterflow heat
exchanger in which the warm
refrigerant liquid from the condenser
exchanges heat with the cool refrigerant
vapor from the evaporator.
Modification of the System
 Refrigerant type can also influence the
system performance, so it is a big
challenge to obtain matching between the
system modification and refrigerant type.
 The performances of the alternative
refrigerants R600a, R134a and R22 while
using liquid suction heat exchanger are
studied.
R600a R22
R134a
Model Development
 The liquid-suction heat exchanger is installed across the suction and
liquid lines.
Model Development
The Liquid Suction Heat Exchanger allows:
 Subcooling for the condensed refrigerant.
 Reducing the flash gas in the liquid line to ensure maximum capacity for the
thermostatic expansion valve.
 Superheating liquid of refrigerant which is located in the suction line.
 Prevention of liquid refrigerant entering the reciprocating compressor.
Thermodynamics Analysis of Subcooling
Fig: P-h diagram of Subcooling Fig: T-s diagram of Subcooling
Thermodynamics Analysis of Subcooling
 Subcooling reduces the flash gas in the liquid line to ensure maximum capacity for the
thermostatic expansion valve, which eventually increases the refrigeration effect.
 It increases the amount of heat rejection from the condenser.
 It also increases the enthalpy of refrigerant entering the evaporator from 4 to 4’ , which
increases the refrigeration effect.
 The work to be done in the Compressor remains unchanged.
 Since subcooling increases the refrigeration effect without changing the compressor input,
COP of the system can be increased significantly.
Thermodynamics Analysis of Subcooling
 Increases Refrigeration effect
 Doesn’t change the work input
 More refrigeration with same work
input
Thermodynamic Analysis for Superheating
 Superheating saves compressor from damage by preventing refrigerant liquid
droplets that may be flown with the gas from entering the suction line.
 If superheating of refrigerant takes place due to heat transfer with the refrigerated
space then it is called as useful superheating as it increases the refrigeration effect.
 On the other hand, it is possible for the refrigerant vapor to become superheated
by exchanging heat with the surroundings as it flows through the connecting
pipelines, which is called as useless superheating.
Thermodynamic Analysis for Superheating
Fig: P-h diagram of superheating Fig: T-s diagram of superheating
Thermodynamic Analysis for Superheating
 Superheating increases the refrigeration effect of the system.
 It also increases the work to be supplied to the compressor.
 Thus, although increasing the refrigeration effect of the system it may
or may not increase the COP.
 The change in COP depends upon the refrigerant used.
Results & Conclusion
 Multiple simulations were run for wide range of conditions.
 Refrigerants R600a, R134a and R22 were used in the system.
 Two systems : Non-Modified and Modified with LSHX were examined.
 All the results were obtained through Engineering Equation Solver.
Effects of Subcooling
 The liquid-suction heat exchanger
improves the sub-cooling for three
types of refrigerants; R22, R134a and
R600a.
 However, higher value of the sub-cool
temperature was achieved by R600a.
Fig : Effect of Liquid-Suction Heat Exchanger on Superheating at
Different Condenser Pressure and Different Refrigerants
Effects of Superheating
 The LSHX effectively increased the
superheat temperature in the suction
line.
 The figure also shows that the higher
value of the super heat temperature
was achieved by R600a and achieved
better performance. Fig : Effect of Liquid-Suction Heat Exchanger on Superheating
at Different Condenser Pressure and Different Refrigerants
Comparison between non-modified and
modified system
Non-Modified System Modified system
The following comparison shows the refrigerant effect at different Condenser pressure
and different refrigerants :
Comparison between non-modified and
modified system
Non-Modified System
 R600a achieved highest value of
refrigerant effect
 Refrigerant Effect: about 250kJ/kg
when the condenser pressure was
350 kPa
Modified System
 R600a achieved highest value of
refrigerant effect
 Refrigeration Effect: about 350
kJ/kg when the condenser
pressure was 350 kPa
Comparison of COP
Result & Conclusion
 The Figure shows that the highest value of COP was achieved by the modified
system using R134a.
 Which is about 7% and 12% higher than that of R600a and R22 respectively.
 The COP can be improved and enhanced up to 20% based on the refrigerant type
and operating conditions while using LSHX.
 The R600a is good replacement for other refrigerants but it has lower COP
compared with R134a due to its thermodynamic properties.
Acknowledgement
 We thank Raid Ahmed Mahmood, School of Mechanical and
Electrical Engineering, University of Southern Queensland,
Australia for the research.
We thank you all for your time and coordination.
CASE-STUDY-OF-LIQUID-SUCTION-HEAT-EXCHANGER-IN.pptx
CASE-STUDY-OF-LIQUID-SUCTION-HEAT-EXCHANGER-IN.pptx

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CASE-STUDY-OF-LIQUID-SUCTION-HEAT-EXCHANGER-IN.pptx

  • 1. CASE STUDY OF LIQUID SUCTION HEAT EXCHANGER IN MECHANICAL REFRIGERATION SYSTEM USING ALTERNATIVE REFRIGERANTS. PRESENTED BY: COORDINATED BY: Samir Ghorasainee Keshav Acharya Sampanna Dhakal Teaching Assistant Sanam Sapkota Purwanchal Campus, Sanchita Sapkota Dharan
  • 2. Mechanical Refrigeration System  Mechanical refrigeration, often referred to as refrigeration or air conditioning, is a process by which heat is removed from a location using a human-made heat exchange system.  As the refrigerant circulates through the system, it is alternately compressed and expanded, changing its state from a liquid to a vapor.
  • 3. Components of Refrigeration Cycle Evaporator : It absorbs heat from refrigerating space. Compressor : It increases the pressure and temperature of refrigerant through compression. Condenser : It releases the heat into surrounding. Expansion Valve : It decreases the pressure of the refrigerant.
  • 4. Modification of the System  Many studies have been done to modify and enhance the performance and energy consumption of the mechanical refrigeration system.  Using heat exchanger in the mechanical refrigeration system is one of the effective technique that can be used to improve the energy performance of the system.  A LSHX is a counterflow heat exchanger in which the warm refrigerant liquid from the condenser exchanges heat with the cool refrigerant vapor from the evaporator.
  • 5. Modification of the System  Refrigerant type can also influence the system performance, so it is a big challenge to obtain matching between the system modification and refrigerant type.  The performances of the alternative refrigerants R600a, R134a and R22 while using liquid suction heat exchanger are studied. R600a R22 R134a
  • 6. Model Development  The liquid-suction heat exchanger is installed across the suction and liquid lines.
  • 7. Model Development The Liquid Suction Heat Exchanger allows:  Subcooling for the condensed refrigerant.  Reducing the flash gas in the liquid line to ensure maximum capacity for the thermostatic expansion valve.  Superheating liquid of refrigerant which is located in the suction line.  Prevention of liquid refrigerant entering the reciprocating compressor.
  • 8. Thermodynamics Analysis of Subcooling Fig: P-h diagram of Subcooling Fig: T-s diagram of Subcooling
  • 9. Thermodynamics Analysis of Subcooling  Subcooling reduces the flash gas in the liquid line to ensure maximum capacity for the thermostatic expansion valve, which eventually increases the refrigeration effect.  It increases the amount of heat rejection from the condenser.  It also increases the enthalpy of refrigerant entering the evaporator from 4 to 4’ , which increases the refrigeration effect.  The work to be done in the Compressor remains unchanged.  Since subcooling increases the refrigeration effect without changing the compressor input, COP of the system can be increased significantly.
  • 10. Thermodynamics Analysis of Subcooling  Increases Refrigeration effect  Doesn’t change the work input  More refrigeration with same work input
  • 11. Thermodynamic Analysis for Superheating  Superheating saves compressor from damage by preventing refrigerant liquid droplets that may be flown with the gas from entering the suction line.  If superheating of refrigerant takes place due to heat transfer with the refrigerated space then it is called as useful superheating as it increases the refrigeration effect.  On the other hand, it is possible for the refrigerant vapor to become superheated by exchanging heat with the surroundings as it flows through the connecting pipelines, which is called as useless superheating.
  • 12. Thermodynamic Analysis for Superheating Fig: P-h diagram of superheating Fig: T-s diagram of superheating
  • 13. Thermodynamic Analysis for Superheating  Superheating increases the refrigeration effect of the system.  It also increases the work to be supplied to the compressor.  Thus, although increasing the refrigeration effect of the system it may or may not increase the COP.  The change in COP depends upon the refrigerant used.
  • 14. Results & Conclusion  Multiple simulations were run for wide range of conditions.  Refrigerants R600a, R134a and R22 were used in the system.  Two systems : Non-Modified and Modified with LSHX were examined.  All the results were obtained through Engineering Equation Solver.
  • 15. Effects of Subcooling  The liquid-suction heat exchanger improves the sub-cooling for three types of refrigerants; R22, R134a and R600a.  However, higher value of the sub-cool temperature was achieved by R600a. Fig : Effect of Liquid-Suction Heat Exchanger on Superheating at Different Condenser Pressure and Different Refrigerants
  • 16. Effects of Superheating  The LSHX effectively increased the superheat temperature in the suction line.  The figure also shows that the higher value of the super heat temperature was achieved by R600a and achieved better performance. Fig : Effect of Liquid-Suction Heat Exchanger on Superheating at Different Condenser Pressure and Different Refrigerants
  • 17. Comparison between non-modified and modified system Non-Modified System Modified system The following comparison shows the refrigerant effect at different Condenser pressure and different refrigerants :
  • 18. Comparison between non-modified and modified system Non-Modified System  R600a achieved highest value of refrigerant effect  Refrigerant Effect: about 250kJ/kg when the condenser pressure was 350 kPa Modified System  R600a achieved highest value of refrigerant effect  Refrigeration Effect: about 350 kJ/kg when the condenser pressure was 350 kPa
  • 20. Result & Conclusion  The Figure shows that the highest value of COP was achieved by the modified system using R134a.  Which is about 7% and 12% higher than that of R600a and R22 respectively.  The COP can be improved and enhanced up to 20% based on the refrigerant type and operating conditions while using LSHX.  The R600a is good replacement for other refrigerants but it has lower COP compared with R134a due to its thermodynamic properties.
  • 21. Acknowledgement  We thank Raid Ahmed Mahmood, School of Mechanical and Electrical Engineering, University of Southern Queensland, Australia for the research.
  • 22. We thank you all for your time and coordination.