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The heat transfer coefficient characterizes the intensity of heat exchange between the body surface and the environment, i.e. is the ratio of the heat flux density [W/m2] coming from the body into the medium in contact with it, at a temperature difference between the body under consideration and the medium of one degree [K].
The heat transfer coefficient is calculated by the formula
α = Nu · λ / L
Scheme of the system of nomograms for calculating the heat transfer coefficient |
Designations of parameters in the formula for calculating the heat transfer coefficientNu - Nusselt number; l - coefficient of thermal conductivity, Watt/(m·K) or kkal/(m2·h·ºÑ); L - the characteristic size, mm. For example, for the pipeline is diameter.
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✅ Formulas for calculating the Nusselt number Nu and the system of nomograms for determining the Nusselt number Nu are given on the page "Graph-analytical calculation of the Nusselt number Nu".
Heat transfer coefficient a, kWatt/(m2·K) |
Coefficient of thermal conductivity l, Watt/(m·K) |
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Free convection in gases |
5 ... 30 |
Hydrogen under room conditions |
0,2 |
Free convection waters |
102 ... 103 |
Air |
0,025 |
The compelled convection of gases |
10 ... 500 |
Dioxide of carbon |
0,02 |
The compelled convection of waters |
500 ... 2·104 |
Pure silver and copper |
400 |
Boiling of water |
2·103 ... 4·104 |
Carbon steel |
50 |
Liquid metals |
102 ... 3·104 |
Liquids |
< 1 |
Film-type condensation of water pair |
4·103 ... 104 |
Water |
0,6 |
Dropwise condensation of water pair |
4·104 ... 105 |
Nonmetallic firm materials |
< 10 |
Porous materials (a fuse, cotton wool etc.) |
< 0,25 |
What values can the Nusselt number take?
For example, when water flows inside a heated pipe at a flow rate of 1 m/s, a wall temperature of 100°C, an average water temperature of 40°C, and a pipe inner diameter of 16 mm,
the Nusselt number is 150.
For graphic-analytical calculation of the heat transfer coefficient using a system of nomograms, we accept the range of variation of the Nusselt number: Nu = 0 ... 300..
L=(1.2...8.5)mm Nu=10...70 l=(0.35...0.85)Watt/(K·m) a=(1...7)kWatt/(K·m^2) |
L=(0.9...8.5)mm Nu=2...14 l=(0.09...0.85)Watt/(K·m) a=(0.2...1.4)kWatt/(K·m^2) |
L=(0.1...5.5)mm Nu=0...3 l=(0.01...0.55)Watt/(K·m) a=(0...0.3)kWatt/(K·m^2) |
L=(0.2...8.5)mm Nu=0...3 l=(0.03...0.32)Watt/(K·m) a=(0.01...0.1)kWatt/(K·m^2) |
L=(0.1...6.5)mm Nu=0...0.3 l=(0.07...0.32)Watt/(K·m) a=(0.01...0.04)kWatt/(K·m^2) |
L=(1.2...8.5)mm Nu=10...130 l=(0.35...0.85)Watt/(K·m) a=(3...9)kWatt/(K·m^2) |
L=(1.2...8.5)mm Nu=10...110 l=(0.02...0.24)Watt/(K·m) a=(0.25...1)kWatt/(K·m^2) |
Topic of this section: Heat transfer coefficient. Graph-analytical calculation of the heat transfer coefficient
graphic-analytical systems
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