thermodynamic calculations of two-stage vapor compression

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Thermodynamic Calculations of Two-Stage Vapor Compression Refrigeration Cycle with Flash Chamber and Separate Vapor Mixing Intercooler Author: Volodymyr Voloshchuk [email protected] Introduction In the event that a high COP of a refrigeration cycle is of greater importance compared to other factors, it is possible to significantly increase the COP of a basic cycle through the use of a multistage vapor compression cycle. This is especially true when the pressure ratio between the heat rejection and heat absorption pressures is large 5 or more. Multistaging involves one or more intermediate pressures between the heat rejection and heat absorption pressures, and a series of compressors operating between successive pressure intervals. One type of multi-compressor vapor compression cycle includes a mixing chamber where saturated vapor from the flash chamber mixes with the vapor leaving the low pressure stage compressor. This vapor-mixing chamber acts as a regenerative intercooler since it cools the superheated vapor leaving the low-pressure stage compressor using lower temperature saturated workin fluid, mixing the two prior to the next stage of compression. This type of refrigeration cycle is analysed in the following calculation.

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Page 1: Thermodynamic Calculations of Two-Stage Vapor Compression

Thermodynamic Calculations of Two-StageVapor Compression Refrigeration Cycle

with Flash Chamber and Separate Vapor Mixing Intercooler

Author: Volodymyr Voloshchuk

[email protected]

IntroductionIn the event that a high COP of a refrigeration cycle is of greater importance compared to other factors, it is possible to significantly increase the COP of a basic cycle through the use of a multistage vapor compression cycle. This is especially true when the pressure ratio between the heat rejection and heat absorption pressures is large 5 or more.Multistaging involves one or more intermediate pressures between the heat rejection and heat absorption pressures, and a series of compressors operating between successive pressure intervals.One type of multi-compressor vapor compression cycle includes a mixing chamber where saturated vapor from the flash chamber mixes with the vapor leaving the low pressure stage compressor. This vapor-mixing chamber acts as a regenerative intercooler since it cools the superheated vapor leaving the low-pressure stage compressor using lower temperature saturated workin fluid, mixing the two prior to the next stage of compression.This type of refrigeration cycle is analysed in the following calculation.

Page 2: Thermodynamic Calculations of Two-Stage Vapor Compression

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Creation functions on properties and processes of working fluids

Vapor pressure on the saturated line as a function of temperature

Liquid pressure on the saturated line as a function of temperature

Liquid temperature on the saturated line as a function of pressure

Vapor temperature on the saturated line as a function of pressure

Liquid specific enthalpy on the saturated line as a function of temperature

Vapor specific enthalpy on the saturated line as a function of temperature

Liquid specific enthalpy on the saturated line as a function of pressure

Page 3: Thermodynamic Calculations of Two-Stage Vapor Compression

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(3.1)(3.1)

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(3.2)(3.2)

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Vapor specific enthalpy on the saturated line as a function of pressure

Liquid specific entropy on the saturated line as a function of temperature

Vapor specific entropy on the saturated line as a function of temperature

Liquid specific entropy on the saturated line as a function of pressure

Vapor specific entropy on the saturated line as a function of pressure

Temperature as a function of pressure and specific entropy

Temperature as a function of pressure and specific enthalpy

Specific enthalpy as a function of pressure and temperature

Specific entropy as a function of pressure and temperature

Input DataTemperature of heat source

Temperature of heat consumption

Temperature difference in the evaporator

Page 4: Thermodynamic Calculations of Two-Stage Vapor Compression

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(3.5)(3.5)

(3.7)(3.7)

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(4.7)(4.7)

(4.4)(4.4)

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(3.3)(3.3)

(3.6)(3.6)

(4.3)(4.3)

(4.6)(4.6)

(3.4)(3.4)

(4.5)(4.5)

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(4.2)(4.2)

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Temperature difference in the condenser

Isentropic efficiency of the compressor

Pressure increase in compressor 1

Working fluid

CalculationsTemperature of the working fluid at the evaporator outlet

Pressure of the working fluid at the evaporator outlet

Specific enthalpy of the working fluid at the evaporator outlet

Specific entropy of the working fluid at the evaporator outlet

Pressure of the working fluid at the flash intercooler outlet

Pressure of the working fluid at the flash intercooler outlet

Temperature of the working fluid at the flash intercooler outlet

Specific enthalpy of the working fluid at the flash intercooler outlet

Page 5: Thermodynamic Calculations of Two-Stage Vapor Compression

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(4.14)(4.14)

(4.9)(4.9)

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(4.17)(4.17)

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(4.16)(4.16)

(4.19)(4.19)

(4.15)(4.15)

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(4.8)(4.8)

(3.3)(3.3)

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(4.10)(4.10)

(4.12)(4.12)

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(4.18)(4.18)

(4.11)(4.11)

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(4.13)(4.13)

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Specific enthalpy of the working fluid at the flash intercooler outlet

Pressure of the working fluid at the evaporator intlet

Specific enthalpy of the working fluid at the evaporator intlet

Temperature of the working fluid at the evaporator intlet

Specific enthalpy of saturated liquid of the working fluid at the evaporator inlet

Quality of the working fluid at the evaporator intlet

Specific entropy of saturated liquid of the working fluid at the evaporator inlet

Specific entropy of the working fluid at the evaporator inlet

Specific entropy of the working fluid at the compressor 1 outlet after isentropic compression

Temperature of the working fluid at the compressor 1 outlet after isentropic compression

Specific enthalpy of the working fluid at the compressor 1 outlet after isentropic compression

Page 6: Thermodynamic Calculations of Two-Stage Vapor Compression

(4.27)(4.27)

(4.28)(4.28)

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(4.29)(4.29)

(4.22)(4.22)

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(4.8)(4.8)

(3.3)(3.3)

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(4.25)(4.25)

(4.30)(4.30)

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(4.21)(4.21)

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(4.23)(4.23)

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Enhtalpy change in the compressor after isentropic compression

Enhtalpy change in the compressor 1 after actual compression

Specific enthalpy of the working fluid at the compressor 1 outlet after actual compression

Specific enthalpy of the working fluid at the compressor 1 outlet after actual compression

Specific entropy of the working fluid at the compressor 1 outlet after actual compression

Pressure of the working fluid at the vapor mixing intercooler inlet

Temperature of the working fluid at the vapor mixing intercooler inlet

Specific enthalpy of the working fluid at the vapor mixing intercooler inlet

Specific entropy of the working fluid at the vapor mixing intercooler inlet

Temperature of the working fluid at the condenser outlet

Pressure of the working fluid at the condenser outlet

Page 7: Thermodynamic Calculations of Two-Stage Vapor Compression

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(4.38)(4.38)

(4.40)(4.40)

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(4.32)(4.32)

(4.19)(4.19)

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(4.36)(4.36)

(4.8)(4.8)

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(3.3)(3.3)

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Specific enthalpy of the working fluid at the condenser outlet

Specific entropy of the working fluid at the condenser outlet

Pressure of the working fluid at the compressor 2 outlet

Pressure of the working fluid at the compressor 2 inlet

Pressure increase in the compressor 2

Specific enthalpy of the working fluid at the flash chamber intlet

Pressure of the working fluid at the flash chamber intlet

Temperature of the working fluid at the flash chamber intlet

Specific enthalpy of saturated liquid of the working fluid at the flash chamber inlet

Specific enthalpy of saturated vapor of the working fluid at the flash chamber inlet

Quality of the working fluid at the flash chamber intlet

Specific entropy of saturated liquid of the working fluid at the flash chamber inlet

Page 8: Thermodynamic Calculations of Two-Stage Vapor Compression

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(4.50)(4.50)

(4.48)(4.48)

(4.43)(4.43)

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(4.49)(4.49)

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(4.19)(4.19)

(4.44)(4.44)

(4.51)(4.51)

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(4.8)(4.8)

(3.3)(3.3)

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(4.52)(4.52)

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(4.46)(4.46)

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Specific entropy of saturated liquid of the working fluid at the flash chamber inlet

Specific entropy of the working fluid at the flash chamber inlet

Ratio of mass flow rates between the high pressure circuit and that of the low pressure circuit

Specific enthalpy of the working fluid at the compressor 2 intlet

Temperature of the working fluid at the compressor 2 intlet

Specific entropy of the working fluid at the compressor 2 intlet

Specific entropy of the working fluid at the compressor 2 outlet after isentropic compression

Temperature of the working fluid at the compressor 2 outlet after isentropic compression

Specific enthalpy of the working fluid at the compressor 2 outlet after isentropic compression

Enhtalpy change in the compressor 2 after isentropic compression

Enhtalpy change in the compressor 2 after actual compression

Page 9: Thermodynamic Calculations of Two-Stage Vapor Compression

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(4.19)(4.19)

(4.59)(4.59)

(4.58)(4.58)

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(4.53)(4.53)

(4.8)(4.8)

(3.3)(3.3)

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(4.61)(4.61)

(4.60)(4.60)

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(4.42)(4.42)

(4.55)(4.55)

Specific enthalpy of the working fluid at the compressor 2 outlet after actual compression

Specific enthalpy of the working fluid at the compressor 2 outlet after actual compression

Specific entropy of the working fluid at the compressor 2 outlet after actual compression

Heat rejection in the condenser referred to 1 kg of refrigerant in the low pressure circuit

Heat addition in the evaporator referred to 1 kg of refrigerant in the low pressure circuit

The total work of compressors referred to 1 kg of the working fluid in the low pressure circuit

Coefficent of performance of a refrigerator

Coefficent of performance of a heat pump

Plot the Refrigeration Cycle on a P-h-T Chart

Page 10: Thermodynamic Calculations of Two-Stage Vapor Compression

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(4.19)(4.19)

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(4.42)(4.42)

(4.53)(4.53)

(4.8)(4.8)

(3.3)(3.3)

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