Heat Transfer Coefficients for Submerged Coils Heat transfer coefficients for steam and hot water coils submerged in oil tanks Sponsored Links
The heat transfer from steam coils with medium pressure, or hot water coils or pipes, submerged in oil or fat can be estimated with the values from the table below.
Heat Transfer Coefficient - natural convection Type of Coil 2o
2 o
(W/m C)
(Btu/hr ft F)
Steam to Light Oil
170
30
Steam to Heavy Oil
85 - 115
15 - 20
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Heat Transfer Coefficient - natural convection Type of Coil 2o
2 o
(W/m C)
(Btu/hr ft F)
Steam to Fat
30 - 60
5 - 10
Hot Water to Oil
60
10
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Heat emission from steam or water pipes submerged in water are indicated in the tables below:
Temperature Difference between the Steam/Water in the Pipe and the Surrounding Water ( o F)
( oC)
Heat Transfer Rate to the Surrounding Water (Btu/ft 2 h o F)
(W/m 2oC)
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For practical applications - the heat transfer rates can roughly be set to:
Type of Application
Heat Transfer Rate to the Surrounding Water (Btu/ft 2 h o F)
(W/m 2oC)
Tank coils with low pressure steam, natural circulation in the tank
100
570
Tank coils with high pressure steam, natural circulation in the tank
200
1100
Tank coils with low pressure steam, forced circulation in the tank
200
1100
Tank coils with high pressure steam, forced circulation in the tank
300
1700
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2o
With low pressure steam and non-assisted circulation we presume the heat transfer rate to be 570 W/m C . The heat transfer from steam to water can then be calculated as: 2o
2
o
o
Q = (570 W/m C) (0.10 m ) (120 C - 20 C) = 5700 W = 5.7 kW
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Properties of Saturated Steam - SI Units A Saturated Steam Table with steam properties as specific volume, density, specific enthalpy and specific entropy Sponsored Links
The steam table below list the properties of steam at varying pressures and temperatures:
Specific Enthalpy of Absolute pressure
Temperature 2
(kPa, kN/m )
o
( C)
Specific Volume 3
(m /kg)
Density - ρ 3
(kg/m )
Specific Entropy of Steam -s-
Liquid - h l l -
Evaporation - h e e -
Steam - h s s -
(kJ/kg)
(kJ/kg)
(kJ/kg)
(kJ/kgK)
0.8
3.8
160
0.00626
15.8
2493
2509
9.058
2.0
17.5
67.0
0.0149
73.5
2460
2534
8.725
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Specific Enthalpy of Absolute pressure
Temperature 2
(kPa, kN/m )
35
o
( C)
72.7
Specific Volume 3
(m /kg)
4.53
Density - ρ 3
(kg/m )
0.221
Specific Entropy of Steam -s-
Liquid - h l l -
Evaporation - h e e -
Steam - h s s -
(kJ/kg)
(kJ/kg)
(kJ/kg)
(kJ/kgK)
304.3
2327
2632
7.717
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Specific Enthalpy of Absolute pressure
Temperature 2
(kPa, kN/m )
110
o
( C)
102.3
Specific Volume 3
(m /kg)
1.55
Density - ρ 3
(kg/m )
0.646
Specific Entropy of Steam -s-
Liquid - h l l -
Evaporation - h e e -
Steam - h s s -
(kJ/kg)
(kJ/kg)
(kJ/kg)
(kJ/kgK)
428.8
2251
2680
7.328
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Specific Enthalpy of Absolute pressure
Temperature 2
(kPa, kN/m )
360
o
( C)
139.9
Specific Volume 3
(m /kg)
0.510
Density - ρ 3
(kg/m )
1.96
Specific Entropy of Steam -s-
Liquid - h l l -
Evaporation - h e e -
Steam - h s s -
(kJ/kg)
(kJ/kg)
(kJ/kg)
(kJ/kgK)
588.5
2144
2733
6.930
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Specific Enthalpy of Absolute pressure
Temperature 2
(kPa, kN/m )
750
o
( C)
167.8
Specific Volume 3
(m /kg)
0.255
Density - ρ 3
(kg/m )
3.915
Specific Entropy of Steam -s-
Liquid - h l l -
Evaporation - h e e -
Steam - h s s -
(kJ/kg)
(kJ/kg)
(kJ/kg)
(kJ/kgK)
709.3
2056
2765
6.682
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Specific Enthalpy of Absolute pressure
Temperature 2
(kPa, kN/m )
1300
o
( C)
191.6
Specific Volume 3
(m /kg)
0.151
Density - ρ 3
(kg/m )
6.62
Specific Entropy of Steam -s-
Liquid - h l l -
Evaporation - h e e -
Steam - h s s -
(kJ/kg)
(kJ/kg)
(kJ/kg)
(kJ/kgK)
815
1971
2785
6.491
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