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Schmatic ... P-h Diagram of an Ideal Vapor-. Compression Refrigeration Cycle.
10
CHAPTER
Refrigeration Cycles
10-1
Refrigerator and Heat Pump Objectives The objective of a refrigerator is to remove heat (Q L) from the cold medium; the objective of a heat pump is to supply heat (QH) to a warm medium (fig. 10-1)
10-14
Some Basic Definitions • The transfer of heat from lower temperature regions to higher temperature ones is called refrigeration. • Devices that produce refrigeration are called refrigerators, and the cycles on which they operate are called refrigeration cycles. • The working fluids used in refrigerators are called refrigerants. • Refrigerators used for the purpose of heating a space by transferring heat from a cooler medium are called heat pumps.
10-15
Coefficient of Performance • The performance of refrigerators and heat pumps is expressed in terms of coefficient of performance (COP), defined as
The Reversed Carnot Cycle
10-2
10-16
Carnot Refrigerator and Heat Pump • A refrigerator or heat pump that operates on the reversed Carnot cycle is called a Carnot refrigerator or a Carnot heat pump, and their COPs are
10-16
Why not use the reversed Carnot Refrigeration Cycle
• Easier to compress vapor only and not liquid-vapor mixture • Cheaper to have irreversible expansion through an expansion valve
Schmatic and T-s Diagram for Ideal VaporCompression Refrigeration Cycle 10-2
(Fig. 10-3)
10-4
P-h Diagram of an Ideal VaporCompression Refrigeration Cycle (Fig. 10-5)
10-3
Ordinary Household Refrigerator (Fig. 10-4)
Four Processes of the Ideal VaporCompression Refrigeration Cycle
10-17
• The Ideal Vapor-Compression Refrigeration Cycle Process 1-2 2-3 3-4 4-1
Description Isentropic compression Constant pressure heat rejection in the condenser Throttling in an expansion valve Constant pressure heat addition in the evaporator
1st and 2nd Law Analysis of Ideal VaporCompression Refrigeration Cycle • Results of First and Second Law Analysis for SteadyFlow Component
Process
First Law Result
Compressor
s = Const.
W&in = m& (h2 − h1 )
Condenser
P = Const.
Q& H = m& (h2 − h3 )
Throttle Valve
∆s > 0
Evaporator
P = Const.
h4 = h3 Q& L = m& (h1 − h4 )
COP of An Ideal Vapor-Compression Refrigeration Cycle Q& L h1 − h4 COPR = = W&net ,in h2 − h1 Q& H h2 − h3 COPHP = & = Wnet ,in h2 − h1
Schmatic and T-s Diagram for Actual VaporCompression Refrigeration Cycle 10-5
(Fig. 10-7)
10-5
Practice Problem 10.1 Refrigerant-134a is the working fluid in an ideal compression refrigeration cycle. The refrigerant leaves the evaporator 20oC and has a condenser pressure of 0.9 MPa. The mass flow rate is 3 kg/min. Find COP R , COPR, Carnot for same Tmax and Tmin , and the tons of refrigeration. (One ton of refrigeration is equivalent to 12,000 Btu/hr or 211 kJ/min.)
Heat Pump Heats a House in Winter and Cools it in Summer 10-6
(Fig. 10-9)
A Two-Stage Cascade Regrigeration System
10-6
Objecitve: To achieve a larger temperature range (cooler temperautre) without requiring a large pressure range in the compressor
A Two-Stage Cascade Regrigeration System with a flash chamber
10-6
10-7
Schmatic and T-s Diagram for RefrigeratorFreezer Unit with One Compressor
(Fig. 10-14)
Linde-Hampson System for Liquefying Gases 10-8
(Fig. 10-15)
10-9
Simple Gas Refrigeration Cycle (Reversed Brayton Cycle) (Fig. 10-16)
10-20
Objective and COP of Gas Refrigeration Cycle
• Objective: to cool aircraft and to obtain very low (cryogenic) temperatures after it is modified with regeneration. The work output of the turbine can be used to reduce the work input requirements to the compressor.
10-10
Gas Refrigeration Cycle With Regeneration COLD refrigerated space
(Fig. 10-19)
WARM environment
Ammonia Absorption Refrigeration Cycle
10-11
• Useful when inexpensive thermal energy is available at 200 to 200 C • Pump work is typically small because a liquid is being compressed