Chapter 9 Refrigeration and Liquefaction Introduction n Refrigeration

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Chapter 9. Refrigeration and Liquefaction (냉동과 액화) 고려대학교 화공생명공학과

Chapter 9. Refrigeration and Liquefaction (냉동과 액화) 고려대학교 화공생명공학과

Introduction n Refrigeration n n n Air conditioning of building Preservation of foods and

Introduction n Refrigeration n n n Air conditioning of building Preservation of foods and beverages Manufacture of ice Dehydration of gases Purifications , separations Low temperature reactions Liquefaction n n Propane gases in cylinders Liquid oxygen for rockets LNG (Liquid Natural Gas) Separation of air

9. 1 The Carnot Refrigeration n Reversed heat-engine cycle n n n Heat is

9. 1 The Carnot Refrigeration n Reversed heat-engine cycle n n n Heat is absorbed at low T Heat is rejected at high T Requires external source of energy : W Coefficient of Performance (COP)

9. 2 Vapor-Compression Cycle 4 3 Condenser Const. H throttling process 3 3’ Throttling

9. 2 Vapor-Compression Cycle 4 3 Condenser Const. H throttling process 3 3’ Throttling Valve 1 Compressor Evaporator 4 1 2 Coefficient of Performance 2 Rate of circulation of refrigerant

A Typical Compressor

A Typical Compressor

Vapor-compression refrigeration cycle on P-H diagram ln P Const. S 4 3’ 1 3

Vapor-compression refrigeration cycle on P-H diagram ln P Const. S 4 3’ 1 3 2 H P-H diagrams are more commonly used in refrigeration cycle than TS diagrams.

Example 9. 1 n A refrigerated space is maintained at 10 (o. F) and

Example 9. 1 n A refrigerated space is maintained at 10 (o. F) and cooling water is available at 70 (o. F). Refrigeration capacity is 12, 000 Btu/h. The evaporator condenser are of sufficient size that a 10 (o. F) minimum temperature difference for heat transfer can be realized in each. The refrigerant is tetrafluoroethane (HCF-134 a), for which data are given in Table 9. 1 and Fig. G. 2 (App. G). (a) Whate is the value of COP for a Carnot Refrigerator ? (b) Cacluate COP and m for the vapor-compression cycle of Fig. 9. 1 if the compressor efficiency is 0. 80

Solution (a) 10 o F Minimum temperature difference : Tc = 0 o. F

Solution (a) 10 o F Minimum temperature difference : Tc = 0 o. F Th = 80 o. F

Solution (b) H 1, H 2, H 3, H 4 값을 알면 모든 답을

Solution (b) H 1, H 2, H 3, H 4 값을 알면 모든 답을 구할 수 있다. State 2 ln P H 1 = H 4 Const. S 4 3’ 1 2 3 0 o. F, saturation condition (V) P = 21. 162 psia H 2 = 103. 015 Btu/lbm S 2 = 0. 22525 Btu/lbm. F State 4 80 o. F, saturation condition (L) P = 101. 37 psia H 2 = 37. 987 Btu/lbm State 3’ Read H from Fig. G. 2. P = 101. 37 psia, S=0. 22525 H 3’ = 117 Btu /lbm H

Solution (b) n Compressor efficiency is 0. 8

Solution (b) n Compressor efficiency is 0. 8

Solution (b) n COP n Refrigerant Circulation Rate

Solution (b) n COP n Refrigerant Circulation Rate

9. 3 The Choice of Refrigerant In principle, COP of Carnot refrigerator is independent

9. 3 The Choice of Refrigerant In principle, COP of Carnot refrigerator is independent of the refrigerant. n Irreversibility in the refrigerator cause the COP to depend on the choice of refrigerant. n

The Choice of Refrigerant n Main characteristics n n n Vapor pressure of the

The Choice of Refrigerant n Main characteristics n n n Vapor pressure of the refrigerant at evaporation T should be greater than 1 atm Vapor pressure condenser T should not be high. Additional characteristics n n n Toxicity Flammability Cost Corrosion properties Environmental consideration

Choice of Refrigerant Ammonia, Methyl chloride, Carbon Dioxide, Propane and other hydrocarbons n Halogenated

Choice of Refrigerant Ammonia, Methyl chloride, Carbon Dioxide, Propane and other hydrocarbons n Halogenated Hydrogcarons (CFC, HCFC) n n n CCl 3 F (CFC-11), CCl 2 F 2 (CFC-12) Replacement n CHCl 2 CF 3 (HCF-123), CF 3 CH 2 F(HCF-134 a), CHF 2 CF 3 (HCF-125)

Cascade refrigeration systems n To overcome the limit of operation… n n Tc fixed

Cascade refrigeration systems n To overcome the limit of operation… n n Tc fixed : environments Two or more refrigeration cycle employing different refrigerant

9. 4 Absorption Refrigeration Condenser Throttling Valve Compressor Evaporator This part can be replaced

9. 4 Absorption Refrigeration Condenser Throttling Valve Compressor Evaporator This part can be replaced by heat engine – a work producing device W

Schematic Diagram of an Absorption-Refrigeration Unit QH at TH Heat discarded at TS Condenser

Schematic Diagram of an Absorption-Refrigeration Unit QH at TH Heat discarded at TS Condenser Regenerator Throttling Valve Heat Exchanger Evaporator Absorber Pump QC at TC Heat discarded at TS Li. Br Solution + Water + Ammonia

Ammonia Absorption Refrigeration Unit

Ammonia Absorption Refrigeration Unit

Analysis Work required for the refrigeration cycle Heat required for the production of the

Analysis Work required for the refrigeration cycle Heat required for the production of the work.

9. 5 The Heat Pump n Dual-purpose reversed heat engine n n Winter :

9. 5 The Heat Pump n Dual-purpose reversed heat engine n n Winter : Heating Summer : Cooling If COP = 4, five times work has to be done to the compressor n Economic advantage depends on the cost of electricity vs. oil and natural gases. n

9. 6 Liquefaction Processes n Liquefaction processes n By heat exchange at const. P

9. 6 Liquefaction Processes n Liquefaction processes n By heat exchange at const. P n By an expansion process from which work is obtained (Adiabatic expansion) T n By a throttling process S

Liquefaction Processes For small-scale commercial liquefaction plant, throttling process is commonly employed. n Sufficiently

Liquefaction Processes For small-scale commercial liquefaction plant, throttling process is commonly employed. n Sufficiently low T and high P desired. n

Linde Liquefaction Process 4 3 7 Throttle Cooler Exchanger 8 10 Win 15 2

Linde Liquefaction Process 4 3 7 Throttle Cooler Exchanger 8 10 Win 15 2 1 9 Liquid Gas Feed

Linde Liquefaction Process

Linde Liquefaction Process

Congratulations ! This is the end !

Congratulations ! This is the end !