REFRIGERATION AND AIR CONDITIONING
Lecture slides by
MR. C K SETHI
ASST. PROFESSOR
GIET, BBSR
REFRIGERATION AND AIR CONDITIONING
Refrigeration
Refrigerators and heat pumps
Refrigerator and Heat pump
Heat Pump
Warm Space
Cold Space
Refrig erator
Work Input
QR
Work Input
QR
Terminologies of Refrigeration
Refrigerating Effect (N): It is defined as the quantity of heat extracted from a cold body or space to be cooled in a given time.
N= Heat extracted from the cold space
Time taken
Specific Heat of water and ice : It is the quantity of heat required to raise or lower the temperature of one kg of water (or ice), through one kelvin or (10
c) in one second.
Specific heat of water, Cpw = 4.19 kJ/kg K Specific heat of ice, Cpice = 2.1 kJ/kg K.
Terminologies of Refrigeration
Capacity of a Refrigeration Unit :
refrigerating machine is ton of refrigeration.
Heat extracted from at 0o c = latent heat of ice
Latent heat of ice = 336 kJ/kg
i.e., 336 kJ of heat should be extracted from one kg of water at 0o C to convert it into ice.
Terminologies of Refrigeration
One ton of refrigeration
One ton of refrigeration
= 336x1000 kJ/24 hrs.
= 336x1000 kJ/min
24x60
= 233.333 kJ/min
= 3.8889 kJ/sec
Terminologies of Refrigeration
Co efficient of Performance: It is defined as the ratio of heat extracted in a given time (refrigerating effect) to the work input.
Co efficient of performance = Heat extracted in evaporator
Co efficient of performance =
Work Input Refrigerating Effect
Co efficient of performance =
Work Input
N W
The COP is always greater than 1 and known as theoretical coefficient of performance.
Refrigerants
Refrigerant: Any substance that absorbs heat through expansion and vaporisation process and loses heat due to condensation is a refrigeration process is called refrigerant.
Some examples of refrigerants are,
Classification of Refrigerants
Refrigerants are classified as,
(a) Primary Refrigerants: It is a working medium which is used for cooling the substance by absorption of latent heat.
E.G Ammonia (NH3), Carbon dioxide (CO2), Sulphur dioxide (SO2), Freon 12, etc.,
(b) Secondary Refrigerants: Secondary refrigerant is a substance already cooled by primary refrigerant and then employed for cooling purposes.
E.g Ice, solid carbon dioxide.
These refrigerants cool the substance by absorption of their sensible heat.
Types of Refrigerators
E.g., Bell Coleman Cycle.
Applications of Refrigeration
the gases.
Properties of Refrigeration
vapourisation.
Vapour Compression Refrigeration System
S – entropy means transformation, increases with increase in temperature and decreases with decrease in temperature
ᵹ Q = T ds
Vapour Compression Refrigeration System - Construction
compressors directly coupled with high speed rotating engines (gas turbine) are used.
Vapour Compression Refrigeration System - Construction
Compressor: For very big plants Centrifugal compressors directly coupled with high speed rotating engines
(gas turbine) are used
Vapour Compression Refrigeration System - Construction
Vapour Compression Refrigeration System -
Working
Working :
evaporator flows into the compressor.
Vapour Compression Refrigeration System
- Working
| | |
Working : | | |
compressor.
air or water.
| ||
Vapour Compression Refrigeration System
- Working
Working :
Vapour Absorption Refrigeration system
In this system compression process of vapour compression cycle is eliminated. Instead of that the following three processes are carried out.
Vapour Absorption Refrigeration system
Vapour Absorption Refrigeration system - Construction
Construction:
Vapour Absorption Refrigeration system – Working
Working:
Vapour Absorption Refrigeration system - Construction
Working:
Vapour Absorption Refrigeration system - Construction
Working:
Vapour Absorption Refrigeration system - Construction
Working:
Vapour Absorption Refrigeration system - Construction
Working:
Vapour Absorption Refrigeration system - Construction
Working:
Applications of refrigeration system
Comparison between Vapour compression & Vapour Absorption refrigeration systems | ||
S.No. | Vapour Compression System | Vapour Absorption System |
1 | This system has more wear and tear and produces more noise due to the moving parts of the compressor. | Only moving part in this system is an aqua pump. Hence the quieter in operation and less wear and tear |
2. | Electric power is needed to drive the system | Waste of exhaust steam may be used. No need of electric power |
3. | COP is more | COP is less |
4. | At partial loads performance is poor. | At partial loads performance is not affected. |
5. | Mechanical energy is supplied through compressor | Heat energy is utilised |
6. | Energy supplied is ¼ to ½ of the refrigerating effect (less) | Energy supplied is about one and half times the refrigerating effect (more) |
Comparison between Vapour compression & Vapour Absorption refrigeration systems
S.No. | Vapour Compression System | Vapour Absorption System |
7. | Charging of the refrigerating to the system is easy | Charging of refrigerant is difficult |
8. | Preventive measure is needed, since liquid refrigerant accumulated in the cylinder may damage to the cylinder | Liquid refrigerant has no bad effect on the system. |
Layout of Domestic Refrigerator
Layout of Domestic refrigerator
Domestic refrigerator……
Domestic refrigerator……
Domestic refrigerator……
condenser coil.
AIR CONDITIONING
AIR CONDITIONING:
Air Conditioning is the process of conditioning the air according to the human comfort, irrespective of external conditions.
AIR CONDITIONING
Applications of Air Conditioning
Air conditioning systems are classified as
CLASSIFICATION OF AIR CONDITIONING
AIR CONDITIONING
Types of Air conditioners
TERMINOLOGIES
TERMINOLOGIES
Humidity: mass of water vapor present in 1kg of dry air
Absolute humidity: mass of water vapor present in 1cu.m of dry air
TERMINOLOGIES
Window Type Air Conditioner
Window Type Air Conditioner
Window Type Air Conditioner
Window Type Air Conditioner - Working
refrigerant.
Window Type Air Conditioner - Working
Window Type Air Conditioner -
Working
ps
controlled by the dampers.
Merits and Demerits of Window type air
conditioner
Merits :
room.
Demerits:
Split Type Air Conditioner - Construction
Split Type Air Conditioner - Layout
Split Type Air Conditioner - Layout
Split Type Air Conditioner - Layout
Split Type Air Conditioner - Working
evaporates in the indoor evaporator coil.
indoor unit air and thus, the room is cooled.
drain pipe.
Split Type Air Conditioner -Working
Merits and Demerits of Split type air
conditioner
Merits :
Merits and Demerits of Split type air
conditioner
DeMerits :
Applications of air conditioning
Vapor-Compression Refrigeration Cycle
control volumes involving these components:
►Evaporator
►Compressor
►Condenser
►Expansion valve
►Most common refrigeration cycle in use today
►There are four principal
All energy transfers by work and heat are taken as positive in the directions of the arrows on the schematic and energy balances are written accordingly.
Two-phase
liquid-vapor mixture
The Vapor-Compression Refrigeration Cycle
work input.
Process 2-3: vapor refrigerant
condenses to liquid through heat
transfer to the cooler surroundings. Process 3-4: liquid refrigerant expands to the evaporator pressure.
►The processes of this cycle are
Process 4-1: two-phase liquid-vapor mixture of refrigerant is evaporated through heat transfer from the refrigerated space.
Process 1-2: vapor refrigerant is compressed to a relatively high temperature and pressure requiring
Two-phase liquid-vapor mixture
The Vapor-Compression Refrigeration Cycle
►Engineering model:
►Each component is analyzed as a control volume at steady state.
►Dry compression is presumed: the refrigerant is a vapor.
►The compressor operates adiabatically.
►The refrigerant expanding through the valve undergoes a throttling process.
►Kinetic and potential energy changes are ignored.
The Vapor-Compression Refrigeration Cycle
Evaporator
(Eq. 10.3)
►Applying mass and energy rate balances
1 4
in
m&
Q& = h − h
►The term Q& is referred to as the
in
refrigeration capacity, expressed in kW in the SI unit system or Btu/h in the English unit system.
►A common alternate unit is the ton of refrigeration which equals 200 Btu/min or about 211 kJ/min.
The Vapor-Compression Refrigeration Cycle
Compressor
Assuming adiabatic compression
Condenser
Expansion valve
Assuming a throttling process
c = h2 − h1
m&
W&
h4 = h3
(Eq. 10.5)
(Eq. 10.6)
(Eq. 10.4)
►Applying mass and energy rate balances
out
= h2 − h3
m&
Q&
�The Vapor-Compression Refrigeration Cycle
►
Coefficient of Performance (COP)
Carnot Coefficient of Performance
This equation represents the maximum theoretical coefficient of performance of any refrigeration cycle operating between cold and hot regions at TC and TH, respectively.
Example 11-1
8
Refrigerant-134a is the working fluid in an ideal compression refrigeration cycle. The refrigerant leaves the evaporator at -20oC and has a condenser pressure of 0.9 MPa. The mass flow rate is 3 kg/min. Find COPR and COPR, Carnot for the same Tmax and Tmin , and the tons of refrigeration.
Using the Refrigerant-134a Tables, we have
1
1
3
3
2s
2s 1
State1
State 2
Compressor exit
kJ kg
kJ kg
kJ
kJ
State 3
⎫
⎫⎧
⎪⎧
⎪⎪h1 = 238.41
h = 278.23
Compressor inlet ⎪⎪
⎪⎪
P2s = P2 = 900 kPa
⎬⎨
⎬⎨
T = −20o C
⎪⎪T
⎪⎪s = 0.9456
1
= 43.79o C
⎪⎩ 2s
kg ⋅ K
s = s = 0.9456
x = 1.0
⎪ ⎩⎪
⎭
kg ⋅ K ⎪⎭
P = 900 kPa
3
4
4 1
3
4
3
x = 0.0
o
State 4
Throttle exit
kJ
kg
kJ
⎫⎧h = 101.61 kJ
⎫
⎧x = 0.358
⎪
Condenser exit ⎪⎪
⎪⎪
⎪⎪
⎬⎨
⎬⎨
s4 = 0.4053
T = T = −20 C
⎪⎪
⎪⎪s = 0.3738
kg ⋅ K
⎪ ⎪
⎪⎩
kg ⋅ K
h = h
⎩
⎭
⎭
= m&(h − h ) = h − h
9
2
1
L 1 4 1 4
R
net ,in 2 1
kg
COP =
(238.41−101.61) kJ
= kg
(278.23 − 238.41) kJ
Q&
W&
m&(h − h ) h − h
min
min
1Ton
kg 211 kJ
= 3 kg (238.41−101.61) kJ
= 1.94Ton
= 3.44
The tons of refrigeration, often called the cooling load or refrigeration effect, are
Q& = m&(h − h )
L 1 4
R, Carnot
COP
=
TL TH − TL
(−20 + 273) K
=
(43.79 − (−20))K
= 3.97
power to the compressor, in horsepower, is required for each ton of cooling.
10
Another measure of the effectiveness of the refrigeration cycle is how much input
The unit conversion is 4.715 hp per ton of cooling.
4.715
net , in
L
R
COP
Ton
=
= 4.715 hp
3.44 Ton
= 1.37 hp
W&
Q&
Features of Actual Vapor-Compression Cycle
►Heat transfers between refrigerant and cold and warm regions are not reversible.
►Refrigerant temperature in evaporator is less than TC.
►Refrigerant temperature in condenser is greater than TH.
►Irreversible heat transfers have negative effect on performance.
Features of Actual Vapor-Compression Cycle
through the condenser is increased relative to the temperature of the warm region, TH.
Trefrigerant ↓
Trefrigerant ↑
Features of Actual Vapor-Compression Cycle
►An increase in specific entropy accompanies an adiabatic irreversible compression process. The work input for compression process 1-2 is greater than for the counterpart isentropic compression process 1-2s.
►Since process 4-1, and thus the refrigeration capacity,
is the same for cycles
1-2-3-4-1and 1-2s-3-4-1, cycle
1-2-3-4-1 has the lower COP.
Isentropic Compressor Efficiency
►The isentropic compressor efficiency is the ratio of the minimum theoretical work input to the actual work input, each per unit of mass flowing:
(Eq. 6.48)
work required in an actual compression from compressor inlet state to exit pressure
work required in an isentropic compression from compressor inlet state to the exit pressure
Actual Vapor-Compression Cycle
Example: The table provides steady-state operating data for a vapor-compression refrigeration cycle using R-134a as the working fluid. For a refrigerant mass flow rate of 0.08 kg/s, determine the
State | 1 | 2s | 2 | 3 | 4 |
h (kJ/kg) | 241.35 | 272.39 | 280.15 | 91.49 | 91.49 |
Actual Vapor-Compression Cycle
(a) The compressor power is
W& = m&(h − h )
c 2 1
⎜
⎝ ⎠
⎟
s kg 1 kJ/s
c
W& = ⎛0.08 kg ⎞ 280.15 − 241.35) kJ 1 kW = 3.1 kW
(
(b) The refrigeration capacity is
Q& = m&(h − h )
in 1 4
⎠
⎜
⎝
1 ton
kg 211 kJ/min min
⎟(241.35 − 91.49) kJ
s
in
Q& = ⎛0.08 kg ⎞
60 s = 3.41 tons
State | 1 | 2s | 2 | 3 | 4 |
h (kJ/kg) | 241.35 | 272.39 | 280.15 | 91.49 | 91.49 |
Actual Vapor-Compression Cycle
(c) The coefficient of performance is
(h2 − h1 )
C.O.P = (h1 − h4 )
(280.15 − 241.35)kJ/kg
C.O.P = (241.35 − 91.49)kJ/kg =
3.86
State | 1 | 2s | 2 | 3 | 4 |
h (kJ/kg) | 241.35 | 272.39 | 280.15 | 91.49 | 91.49 |
Actual Vapor-Compression Cycle
c
c
(h − h )
s = 2s 1
W& / m& (h2 − h1)
(W& / m&)
ηc =
ηc = (272.39 − 241.35)kJ/kg = 0.8 = 80%
(280.15 − 241.35)kJ/kg
State | 1 | 2s | 2 | 3 | 4 |
h (kJ/kg) | 241.35 | 272.39 | 280.15 | 91.49 | 91.49 |
(d) The isentropic compressor
efficiency is
p-h Diagram
►The pressure-enthalpy (p-h) diagram is a thermodynamic property diagram commonly used in the refrigeration field.
Other Refrigeration Cycles
20
Cascade refrigeration systems
Very low temperatures can be achieved by operating two or more vapor-compression systems in series, called cascading. The COP of a refrigeration system also increases as a result of cascading.
21
Multistage compression refrigeration systems
Multipurpose refrigeration systems
22
A refrigerator with a single compressor can provide refrigeration at several
temperatures by throttling the refrigerant in stages.
Liquefaction of gases
23
Another way of improving the performance of a vapor-compression refrigeration system is by using multi•stage compression with regenerative cooling. The vapor- compression refrigeration cycle can also be used to liquefy gases after some modifications.
Selecting Refrigerants
►Refrigerant selection is based on several factors:
►Performance: provides adequate cooling capacity cost-effectively.
►Safety: avoids hazards (i.e., toxicity).
►Environmental impact: minimizes harm to stratospheric ozone layer and reduces negative impact to global climate change.
Refrigerant Types and Characteristics
Global Warming Potential (GWP) is a simplified index that estimates the potential future influence on global warming associated with different gases when released to the atmosphere.
Refrigerant Types and Characteristics
►Chlorofluorocarbons (CFCs) and Hydrochlorofluorocarbons (HCFCs) are early synthetic refrigerants each containing chlorine. Because of the adverse effect of chlorine on Earth’s stratospheric ozone layer, use of these refrigerants is regulated by international agreement.
►Hydrofluorocarbons (HFCs) and HFC blends are chlorine-free refrigerants. Blends combine two or more HFCs. While these chlorine-free refrigerants do not contribute to ozone depletion, with the exception of R-1234yf, they have high GWP levels.
►Natural refrigerants are nonsynthetic, naturally occurring substances which serve as refrigerants. These include carbon dioxide, ammonia, and hydrocarbons. These refrigerants feature low GWP values; still, concerns have been raised over the toxicity of NH3 and the safety of the hydrocarbons.
VAPOUR COMPRESSION CYCLE
COP for Ideal Vapor Absorption Refrigeration System
Practical Vapor – Absorption Refrigeration System
•
Practical vapor – absorption refrigeration system
Generator: The strong solution of ammonia refrigerant and water absorbent are heated by the external source of heat such as steam or hot water. It can also be heated by other sources like natural gas, electric heater, waste exhaust heat etc.
Practical vapor absorption refrigeration system
Generator - Due to heating the refrigerant ammonia gets vaporized and it leaves the generator. However, since water has strong affinity for ammonia and its vaporization point is quite low some water particles also get carried away with ammonia refrigerant, so it is important to pass this refrigerant through analyzer.
Vapour Absorption Refrigeration Systems
Based On Water-Lithium Bromide Pair
VARS based on H2O – LiBr Pair
lithium bromide in water is used as absorbent.
VARS based on H2O – LiBr Pair
Sample Problem in Simple VARS
9. The operating temperatures of a single stage vapour absorption refrigeration system are: generator: 90oC; condenser and absorber: 40oC; evaporator: 0oC. The system has a refrigeration capacity of 100 kW and the heat input to the system is 160 kW. The solution pump work is negligible.
from the system.
Sample Problem in Simple VARS