CHAPTER 5 and 6
CHAPTER 5 and 6
CHAPTER 5 and 6
conditioning
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Refrigeration
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Introduction
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Principle of Refrigeration
SURROUNDING
SYSTEM
• Ammonia.
• Freon.
• Methyl Chloride.
• Carbon Dioxide.
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Parts of a Refrigerator
• Evaporator.
• Condenser.
• Expansion Device.
• Circulating System
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Parts of a Refrigerator
• Evaporator.
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Parts of a Refrigerator
• Condenser.
• Expansion device.
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Parts of a Refrigerator
• Circulating system
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Vapor Compression Refrigeration
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Vapor Compression Refrigeration
Wall or Window 16
Properties of a Good Refrigerant:
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Properties of a Good Refrigerant:
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Properties of a Good Refrigerant:
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PERFORMANCE CHARACTERISTICS OF
REFRIGERATION SYSTEM
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Refrigeration Effect
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Capacity of Refrigeration
• The capacity of refrigeration is expressed in terms of tons of
refrigeration which is the unit of refrigeration.
A ton of refrigeration is defined as the quantity of heat
absorbed in order to form one ton of ice in 24 hrs when the initial
temperature is 0⁰C.
One (American) ton = 2000 pounds
In SI System,
1 ton of Refrigeration = 210 kJ/min
= 3.5 kW
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Ice Making Capacity
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Coefficient of Performance
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Relative Coefficient of Performance
𝐴𝑐𝑡𝑢𝑎𝑙 𝐶𝑂𝑃
𝑅𝑒𝑙𝑎𝑡𝑖𝑣𝑒 𝐶𝑂𝑃 =
𝑇ℎ𝑒𝑜𝑟𝑒𝑡𝑖𝑐𝑎𝑙 𝐶𝑂𝑃
27
Chapter 6 – Thermal Systems Applications
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Definition
A pump is a device that moves fluids (liquids
or gases), or sometimes slurries, by
mechanical action, typically converted from
electrical energy into Hydraulic energy.
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PUMPS
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The purpose of a pump is to add energy to
a fluid, resulting in an increase in fluid
pressure, not necessarily an increase of
fluid speed across the pump.
A blower is a gas pump with relatively moderate to high pressure rise and
moderate to high flow rate. Examples include centrifugal blowers and
squirrel cage blowers in automobile ventilation systems, furnaces, and
leaf blowers.
ΔP = Rise in pressure
V = Discharge rate
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Pumps and turbines in which energy is supplied or extracted by a
rotating shaft are properly called turbo machines or dynamic
machines. In dynamic machines, there is no closed volume;
instead, rotating blades supply or extract energy to or from the
fluid.
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In positive-displacement machines, fluid is directed into a closed volume.
Energy transfer to the fluid is accomplished by movement of the
boundary of the closed volume, causing the volume to expand or
contract, thereby sucking fluid in or squeezing fluid out, respectively.
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Positive Displacement Pumps
Lobe Pump
Source: https://www.youtube.com/watch?v=mEF3qh-hH-I
Source: https://gfycat.com/decimalsoftcanvasback
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Gear Pump
Source: http://bestanimations.com/Science/Gears/Gears4.html
Source: http://processprinciples.com/2012/07/gear-pumps/
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Scroll Pump
Source:
http://www.gentecsys.com/Knowledge/KB04_comp_tec
Source: https://gfycat.com/discover/compresor-gifs
h.htm
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Screw Pump or Cavity pump
Source:
https://en.wikipedia.org/wiki/Archimed
es%27_screw Source: https://empoweringpumps.com/leistritz-screw-
pump-applications-in-pipelines-refineries-and-chemical-
plants/
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Vane pump
Source: https://en.wikipedia.org/wiki/Rotary_vane_pump
Source: https://makeagif.com/gif/rotary-
vane-pump-animation-FwVfPQ
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Dynamic machines:
Input
Centrifugal pump
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Source: https://gfycat.com/fataleducatedcolt
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CENTRIFUGAL PUMP
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CENTRIFUGAL COMPRESSOR
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Chapter 5. Thermal Engineering-2
Chapter 5:
Turbines and Internal combustion engines are power developing thermal
systems where as Refrigeration, air conditioning systems , pumps, blowers
and compressors are power consuming devices.
______________________________________________________________
Pumps:
There are two broad categories of turbomachinery, pumps and turbines. The
word pump is a general term for any fluid machine that adds energy to a
fluid. Some authors call pumps energy absorbing devices since energy is
supplied to them, and they transfer most of that energy to the fluid, usually
via a rotating shaft (Fig. 5.1a). The increase in fluid energy is usually felt as
an increase in the pressure of the fluid. Turbines, on the other hand, are
energy producing devices—they extract energy from the fluid and transfer
most of that energy to some form of mechanical energy output, typically in
the form of a rotating shaft (Fig.5.1b).
Figure 5.1: (a) A pump supplies energy to a fluid, while (b) a turbine extracts energy
from a fluid.
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The fluid at the outlet of a turbine suffers an energy loss, typically in the
form of a loss of pressure. An ordinary person may think that the energy
supplied to a pump increases the speed of fluid passing through the pump
and that a turbine extracts energy from the fluid by slowing it down. This is
not necessarily the case. Consider a control volume surrounding a pump
(Fig. 5.2).
Figure 5.2 : For the case of steady flow, conservation of mass requies that the mass
flow rate out of the pump must equal the mass flow rate into the pump; for
incompressible flow with equal inlet and outlet cross-secional areas (Dout = Din) , we
conclude that Vout =Vin , Pout >Pin.
We assume steady conditions. By this we mean that neither the mass flow
rate nor the rotational speed of the rotating blades changes with time. (The
detailed flow field near the rotating blades inside the pump is not steady of
course, but control volume analysis is not concerned with details inside the
control volume.) By conservation of mass, we know that the mass flow rate
into the pump must equal the mass flow rate out of the pump. If the flow is
incompressible, the volume flow rates at the inlet and outlet must be equal
as well. Furthermore, if the diameter of the outlet is the same as that of the
inlet, conservation of mass requires that the average speed across the outlet
must be identical to the average speed across the inlet. In other words, the
pump does not necessarily increase the speed of the fluid passing through
it; rather, it increases the pressure of the fluid. Of course, if the pump were
turned off, there might be no flow at all. So, the pump does increase fluid
speed compared to the case of no pump in the system. However, in terms of
changes from the inlet to the outlet across the pump, fluid speed is not
necessarily increased. (The output speed may even be lower than the input
speed if the outlet diameter is larger than that of the inlet.)
Fluid machines that move liquids are called pumps, but there are several
other names for machines that move gases (Fig. 5.3).
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A fan is a gas pump with relatively low pressure rise and high flow rate.
Examples include ceiling fans, house fans, and propellers.
A blower is a gas pump with relatively moderate to high pressure rise and
moderate to high flow rate. Examples include centrifugal blowers and
squirrel cage blowers in automobile ventilation systems, furnaces, and leaf
blowers.
A compressor is a gas pump designed to deliver a very high pressure rise,
typically at low to moderate flow rates. Examples include air compressors
that run pneumatic tools and inflate tires at automobile service stations,
and refrigerant compressors used in heat pumps, refrigerators, and air
conditioners.
Figure 5.3: When used with gases, pumps are called fans, blowers or compressors,
depending on the relative values of pressure rise and volume flow rate.
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Figure 5.4: Not all pumps have a rotating shaft; (a) energy is supplied to this manual
tyre pump by the up and down motion of a person’s arm to pump air; (b) a similar
mechanism is used to pump water with an old –fashioned well pump.
Figure 5.5: (a) The human heart is an example of a positive displacement pump;
blood is pumped by expansion and contraction of heart chambers called ventricles.
(b) The common water meter in your house is an example of a positive displacement
turbine; water fills and exits a chamber of known volume for each revolution of the
output shaft.
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enclosed turbines, such as the hydroturbine that extracts energy from water
in a hydroelectric dam, and open turbines such as the wind turbine that
extracts energy from the wind (Fig. 5.6).
Figure 5.6: A wind turbine is a good example of a dynamic machine of the open type;
air turns the blades, and the output shaft drives an electric generator.
Lobe pump, gear pump, scroll pump, cavity pump/ conveyor, Peristaltic
Pump, Reciprocating pump,
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Figure 5.8: Lobe pump Figure 5.9: Gear pump
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Figure 5.14: Piston Pump and plunger pump
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the volute. The volute is a region that expands in cross-sectional area as it
wraps around the pump casing. The purpose of the volute is to collect the
liquid discharged from the periphery of the impeller at high velocity and
gradually cause a reduction in fluid velocity by increasing the flow area. This
converts the velocity head to static pressure. The fluid is then discharged
from the pump through the discharge connection.
Compressors:
Air compressor:
The purpose of an air compressor is to provide a continuous
supply of pressurized air.
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utilized by the centrifugal pump. The air particles enter the eye of the
impeller, designated D in Figure 15.17. As the impeller rotates, air is thrown
against the casing of the compressor. The air becomes compressed as more
and more air is thrown out to the casing by the impeller blades. The air is
pushed along the path designated A, B, and C in Figure 5.17. The pressure
of the air is increased as it is pushed along this path. Note in Figure 5.17
that the impeller blades curve forward, which is opposite to the backward
curve used in typical centrifugal liquid pumps. Centrifugal compressors can
use a variety of blade orientation including both forward and backward
curves as well as other designs.
Refrigeration system:
Refrigeration Systems:
Introduction:
One of the major application area of thermodynamics is refrigeration, which
is the transfer of heat from a lower temperature region to a higher
temperature region. Devices that produce refrigeration are called
refrigerators, and the cycles on which they operate are called refrigeration
cycles. The most frequently used refrigeration cycle is the vapor-compression
refrigeration cycle in which the refrigerant is vaporized and condensed
alternately and is compressed in the vapor phase. For large scale cooling
needs, the more economical and desirable system is vapour-absorption
refrigeration system where the thermal energy can be directly used as a
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source of energy instead of using electrical energy as a major source of
energy.
Refrigerators and heat pumps are essentially the same devices; they differ in
their objectives only. The objective of a refrigerator is to maintain the
refrigerated space at a low temperature by removing heat from it.
Discharging this heat to a higher-temperature medium is merely a necessary
part of the operation, not the purpose. The objective of a heat pump,
however, is to maintain a heated space at a high temperature. This is
accomplished by absorbing heat from a low-temperature source, such as
well water or cold outside air in winter, and supplying this heat to a warmer
medium such as a house (Fig. 1 b).
Thus,
Coefficient of performance of refrigeration system is defined as a ratio of
refrigerating effect to the input work required to produce the effect.
These relations can also be expressed in the rate form by replacing the
. . .
quantities QL, QH, and Wnet,in by Q L , Q H and W net .in , respectively. Notice that
both COPR and COPHP can be greater than 1.
COP HP = COPR + 1
for fixed values of QL and QH. This relation implies that COPHP >1 since COPR
is a positive quantity.
The cooling load of a typical 200-m2 residence is in the 3-ton (10-kW) range.
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Relative COP: It is defined as the ratio of actual COP to the theoretical COP.
Fig: Schematic and T-s diagram for the ideal vapor-compression refrigeration cycle.
The refrigerant at low temperature and low pressure passing through the
evaporator coils absorbs the latent heat of evaporation from the substances
to be cooled and gets evaporated. Thus the temperature of the freezing
chamber gets lowered. The evaporated low pressure refrigerant is drawn by
compressor and compresses it to high pressure, so that corresponding to
that high pressure, the saturation temperature of the refrigerant is higher
than the temperature of the cooling medium (ambient air or water) in the
condenser. Thus the high-temperature and high pressure vapour rejects
heat to the cooling medium and gets condensed to saturated liquid in the
condenser. At the exit of the condenser the saturated liquid refrigerant is
ready to expand to low pressure and temperature. The high pressure,
approximately room temperature liquid refrigerant flows to the throttle valve
(expansion valve or a capillary tube) in which it expands to a low pressure
and then ducted to the evaporator to repeat the cycle.
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The expansion valve lowers the pressure
and temperature of the refrigerant, at
the same time evaporates the refrigerant
partly. Thus the refrigerant entering the
evaporator will be a wet vapour and at a
very low temperature of around -20°C.
To maintain the evaporator temperature
with the desired limits, the motor driving
the compressor is controlled by a
thermostat switch.
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c) Corrosiveness
d) Chemical Stability
4) Other properties
a) COP
b) Odour
c) Leak
d) Action with Lubricating Oil
2) Freezing point: An ideal refrigerant must have a very low freezing point
because the refrigerant should not freeze at low evaporator
temperatures.
6) Specific heat of liquid and vapour: A good refrigerant must have low
specific heat when it is in liquid state and high specific heat when it is
vaporised. The low specific heat of the refrigerant helps in sub-cooling
of the liquid and high specific heat of the vapour helps in decreasing
the superheating of the vapour. Both these desirable properties
increase the refrigeration effect.
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11) Coefficient of Performance: The coefficient of performance of a
refrigerant must be high so that the energy spent in refrigeration will
be less.
13) Leakage tests: The refrigerant must be such that any leakage can be
detected by simple tests.
14) Action with lubricating oil: A good refrigerant must not react with the
lubricating oil used in lubricating the parts of the compressor.
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