refrigeration system (mech 324)
DESCRIPTION
TRANSCRIPT
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REFRIGERATION SYSTEMBy: Engr. Yuri G. Melliza
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Refrigeration : Is that area of engineering that deals with the different mechanism involved in maintaining a temperature of a space or material below that of the immediate surroundings.
Uses of Refrigeration:1. Ice making2. Cold Storage3. Air conditioning4. Food preservation5. Other industrial processes that uses refrigeration
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Carnot Cycle:A.Carnot EngineProcesses:
1 to 2 - Heat Addition (T = C)2 to 3 - Expansion (S = C)3 to 4 - Heat Rejection (T = C)4 to 1 - Compression (S = C)
T
S
1 2
34
TH
TL
QA
QR
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Heat Added (T = C)
QA = TH(S2 - S1) 1S2 - S1 = S3 – S4 = SQA = TH S 2Heat Rejected (T =
C)QR = TL(S3 – S4) 3S2 - S1 = S3 – S4 = SQR = TL S 4
Net WorkW = Q ; W = QA - QR W = S (TH – TL) 4
Where:TH – high temperature, KTL – low temperature, K
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Thermal Efficiency
100% x QW
eA
100% x Q
Q-Qe
A
RA
100% x QQ
eA
R
1
100% x T
T-Te
H
LH
100% x TT
eH
L
1
5
6
7
9
8
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B. Carnot RefrigeratorProcesses
1 to 2 - Compression (S = C) 2 to 3 - Heat Rejection (T = C)3 to 4 - Expansion (S = C)4 to 1 - Heat Addition (T = C)TH
T
TL
S1
23
4QA
QR
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Heat Added (T = C)
QA = TL(S1 – S4) 10S2 – S3 = S1 – S4 = SQA = TL S 11Heat Rejected (T =
C)QR = TH(S2 – S3) 12S2 – S3 = S1 – S4 = SQR = TH S 13
Net WorkW = Q ; W = QR - QA W = S (TH – TL) 14
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Coefficient of Performance: It is the ratio of the refrigerating capacity to the net cycle work.
WQ
COP A
Q-Q
QCOP
AR
A
T-T
TCOP
LH
L
15
16
17
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C. Carnot Heat Pump: A heat pump uses the same components as the refrigerator but its main purpose is to reject heat at high thermal energy level.Heat Added (T = C)
QA = TL(S1 – S4) 20S2 – S3 = S1 – S4 = SQA = TL S 21Heat Rejected (T =
C)QR = TH(S2 – S3) 22S2 – S3 = S1 – S4 = SQR = TH S 23
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Performance Factor
Net Work
W = Q ; W = QR - QA W = S (TH – TL) 24
WQ
PF R
Q-Q
QPF
AR
R
T-T
TPF
LH
H
1COPPF
25
26
27
28
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Vapor Compression Cycle
Processes:1 to 2 - Compression (S = C) 2 to 3 - Heat Rejection (P = C)3 to 4 - Expansion (h = C)4 to 1 - Heat Addition (P = C)
Basic Components:1. Gas Compressor 2. Condenser3. Expansion Valve4. Evaporator
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Schematic Diagram
Evaporator
Condenser
4 1
23
QA (Heat Added)
QR (Heat Rejected)
W (Work)
Compressor
Expansion Valve
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Ph and TS Diagram
1
23
4
S = C
P
h
1
2
3
4
h = C
T
S
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CompressorW = m(h2 – h1) KWFor Isentropic Compression (PVk = C)
k1k
1
2
1
2
PP
TT
1PP
1kkmRT1
Wk
1k
1
2
P1V1’ = mRT1
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Where:m – mass flow rate in kg/secV1’ – volume flow rate in m3/secP1 – suction pressure in KPaP2 – discharge pressure in KPaT1 – suction temp. in KT2 – discharge temp. in K
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100% x PP
c- c 1η
100% x VV
η
k1k
1
2v
D
1'v
Volumetric Efficiency:
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Where:V1’ - volume flow rate measured at intake,m3/secVD -displacement volume, m3/secDisplacement Volume:a. For Single acting
m3/sec 4(60)
Nn'LD=V2
Dπ
b. For Double acting (without considering piston rod)
m3/sec 4(60)
Nn'LD2=V2
Dπ
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c. For Double acting (considering piston rod)
[ ]m3/sec d-2D 4(60)LNn'=V 22
Dπ
Piston Speed:PS = 2LN m/min
Where:L - length of stroke, m
D - diameter of bore, md - piston rod diameter, mN - no. of RPMn’ no. of cylinders
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Compressor Efficiencies:
100% x Work Indicated
Work Ideal cn
a. Compression Efficiency
100% x WorkShaft or Brake
Work Indicated m
b. Mechanical Efficiency
100% x WorkShaft or Brake
Work Ideal c
mcnc
c. Compressor Efficiency
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Condenser: QR = m(h2 – h3) KJ/sec
For an air cooled condenserQR = m(h2 – h3) = mCPa(ta2 – ta1) KJ/sec
For water cooled condenserQR = m(h2 – h3) = mwCPw(tw2 – tw1)
KJ/secWhere:
a – refers to airw – refers to water1 – inlet condition2 – exit condtitionCpa = 1.0045 KJ/kg-°CCPw = 4.187 KJ/kg- -°C
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Expansion Valve:
h3 = h4
% 100 x h
hhx
fg4
f444
Where: x - quality
Evaporator:QA = m(h1 – h4) KJ/sec or KW
QA = 60 m(h1 – h4) KJ/min
1 TR = 211 KJ/minTR – tons of refrigeration
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Coefficient of Performance
WQ
COP A
whereQA – refrigerating effect or
Refrigerating capacity, KW
W – compressor work, KW
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Wet compression
11
2
2
33
44
P
h S
T
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Subcooling the refrigerant
11
2
2
33
44
P
h S
T
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Superheating the suction vapor
11
2
2
33
44
P
h S
T
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Effects of Operating ConditionsEffects of Increasing the vaporizing temperature:
a. The refrigerating effect per unit mass increases.
b. The mass flow rate per ton decreases
c. The volume flow rate per ton decreases.
d. The COP increases.e. The work per ton decreases.f. The heat rejected at the condenser
per ton decreases.
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Effects of Increasing the condensing temperature:
a. The refrigerating effect per unit mass
decreases.b. The mass flow rate per ton increasesc. The volume flow rate per ton
increases.d. The COP decreases.e. The work per ton increases.f. The heat rejected at the condenser
per ton increases.
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Effects of superheating the suction vaporA. When superheating produces useful
cooling: a. The refrigerating effect per unit mass
increases.
b. The mass flow rate per ton decreasesc. The volume flow rate per ton decreases.d. The COP increases.e. The work per ton decreases.
B. When superheating occurs without useful cooling:
a. The refrigerating effect per unit mass
remains the same.b. The mass flow rate per ton remains the same.c. The volume flow rate per ton increases.d. The COP decreases.
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e. The work per ton decreases.f. The heat rejected at the condenser
per ton increases.Effects of subcooling the liquid:
a. The refrigerating effect per unit mass increases.
b. The mass flow rate per ton decreases
c. The volume flow rate per ton decreases.
d. The COP increases.e. The work per ton decreases.f. The heat rejected at the condenser
per ton decreases.
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Liquid – Suction Heat Exchanger
The function of the heat exchanger are:1. To ensure that no liquid enter the compressor2. To subcool the liquid from the condenser to prevent bubbles of vapor from impeding the flow of refrigerant through the expansion valve.
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Actual vapor compression cycle:As the refrigerant flows through the
system there will be pressure drops in the condenser, evaporator and piping. Heat loses or heat gains will occur depending on the temperature difference between the refrigerant and the surroundings. Compression will be polytropic with friction and heat transfer instead of isentropic.
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Condenser
Compressor
Evaporator
Heat exchanger
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Multipressure System
A multipressure system is a refrigeration system thathas two or more low-side pressure. The low-side Pressure is the pressure of the refrigerant between the expansion valve and the intake of the compressor.
Removal of Flash gas:The flash gas that develops during the throttling process between the condenser and evaporator wasremoved and recompressed before complete expansion.With flash gas removal a savings in power requirementwill occur.
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IntercoolingIntercooling between two stages of compression redu-ces the work of compression per kg of vapor. Intercoo-ling in a refrigeration system can be accomplished witha watercooled heat exchanger or by using refrigerant.The watercooled intercooler may be satisfactory for twostage air compression, but for refrigerant compressionThe water is not cold enough. The alternate methoduses liquid refrigerant from the condenser to do theintercooling. Discharge gas from the low stage com-pressor bubbles through the liquid in the intercooler.Refrigerant leaves the intercooler as saturated vaporat the intercooler pressure.
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Two evaporators and one compressor
1
23
4 5 6
7 8
compressor
Pressure-reducing valve
condenser
HP evaporator
LP evaporator
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condenser
evaporator
Flash tank and Intercooler
LP compressor
HP compressor
Two compressors and one evaporator
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condenser
LP evaporator
Flash tank and Intercooler
LP compressor
HP evaporator
Two compressors and two evaporators
HP compressor
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Optimum Intercooler or Inter-stage pressure
41i PPP Where:
Pi – optimum interstage or intercooler pressure in KPa
P1 – suction pressure of LP compressor, KPaP4 – discharge pressure of HP compressor, KPa
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Cascade System
Condenser
CascadeCondenser
Evaporator
HP Compressor
LP Compressor
A. Closed cascade condenser
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Condenser
CascadeCondenser
Evaporator
HP Compressor
LP Compressor
B. Direct Contact type cascade condenser
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Air Cycle RefrigerationA. Closed or Dense - Air System
Cooler
Expander Compressor
Refrigerator
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Cooler
Expander Compressor
Refrigerator
B. Open - Air SystemP
V
1
23
4
T
S
1
2
3
4
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Compressor Work:
111
k1k
1
21C
mRTVP
1PP
1kkmRT
W
Cooler:
)T(TmCQ 32pR Expander:
333
k1k
3
43E
mRTVP
1PP
1kkmRT
W
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Refrigerator:
)T(TmCQ 41pA
Network
W = Wc – WE
W = QR - QA
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PRODUCT LOADProduct Load – is the total amount of heat removed from a product in a refrigerated space.
m m m
t1 t2tf
Q1 Q2
Q3
Q = Q1 + Q2 + Q3 + Q4
CP1 CP2
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Where:Q1 – sensible heat in cooling the
productfrom t1 to tf
Q2 – latent heat of fusion (freezing) of the
product at tf
Q3 – sensible heat in cooling further the
product from tf to the final temperature t2
Q4 – heat losses or other heat gains from the products Q1 = mCP1(t1 – tf) KJ/hr
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Q2 = m(hL) KJ/hrQ3 = mCP2(tf – t2)Q4 = Q – (Q1 + Q2 + Q3)
Where:m – mass of product, kg/hrCp1 – specific heat of product below
freezing, KJ/kg-C or KJ/kg-KCp2 - specific heat of product above
freezing, KJ/kg- °C or KJ/kg- °Kt1 – initial temperature, °Ctf – freezing point temperature, °Ct2 – final temperature, °ChL – latent heat of freezing, KJ/kg