# Convective Heat Transfer

Heat energy transferred between a surface and a moving fluid with different temperatures - is known as **convection**.

In reality this is a combination of diffusion and bulk motion of molecules. Near the surface the fluid velocity is low, and diffusion dominates. At distance from the surface, bulk motion increases the influence and dominates.

Convective heat transfer can be

**forced**or**assisted**convection**natural**or**free**convection

### Forced or Assisted Convection

Forced convection occurs when a fluid flow is induced by an external force, such as a pump, fan or a mixer.

### Natural or Free Convection

Natural convection is caused by buoyancy forces due to dens ity differences caused by temperature variations in the fluid. At heating the density change in the boundary layer will cause the fluid to rise and be replaced by cooler fluid that also will heat and rise. This continues phenomena is called free or natural convection.

Boiling or condensing processes are also referred to as a convective heat transfer processes.

- The heat transfer per unit surface through convection was first described by Newton and the relation is known as the
**Newton's Law of Cooling**.

The equation for convection can be expressed as:

q = h_{c}A dT(1)

where

q= heat transferred per unit time (W, Btu/hr)

A= heat transfer area of the surface (m^{2}, ft^{2})

h_{c }= convective heat transfer coefficient of the process (W/(m^{2o}C,Btu/(ft)^{2}h^{o}F)

dT= temperature difference between the surface and the bulk fluid (^{o}C, F)

### Heat Transfer Coefficients - Units

*1 W/(m*^{2}K) = 0.85984 kcal/(h m^{2}^{o}C) = 0.1761 Btu/(ft^{2}h^{o}F)*1 Btu/(ft*^{2}h^{o}F) = 5.678 W/(m^{2}K) = 4.882 kcal/(h m^{2}^{o}C)*1 kcal/(h m*^{2}^{o}C) = 1.163 W/(m^{2}K) = 0.205 Btu/(ft^{2}h^{o}F)

### Convective Heat Transfer Coefficients

Convective heat transfer coefficients - *h _{c}*

*-*depends on type of media, if its gas or liquid, and flow properties such as velocity, viscosity and other flow and temperature dependent properties.

Typical convective heat transfer coefficients for some common fluid flow applications:

Free Convection - air, gases and dry vapors : 0.5 - 1000 (W/(m^{2}K))Free Convection - water and liquids: 50 - 3000(W/(m^{2}K))Forced Convection - air, gases and dry vapors:10 - 1000 (W/(m^{2}K))Forced Convection - water and liquids:50 - 10000 (W/(m^{2}K))Forced Convection - liquid metals:5000 - 40000 (W/(m^{2}K))Boiling Water : 3.000 - 100.000 (W/(m^{2}K))Condensing Water Vapor: 5.000 - 100.000 (W/(m^{2}K))

#### Convective Heat Transfer Coefficient for Air

The convective heat transfer coefficient for **air** flow can be approximated to

*h _{c} = 10.45 - v + 10 v^{1/2} (2)*

*where *

*h _{c} = heat transfer coefficient (kCal/m^{2}h°C) *

*v = relative speed between object surface and air (m/s)*

Since* *

*1 kcal/m ^{2}h°C = 1.16 W/m^{2}°C*

- (2) can be modified to

*h _{cW} = 12.12 - 1.16 v + 11.6 v^{1/2} (2b)*

*where *

*h _{cW} = heat transfer coefficient (W/m^{2}°C) *

Note! - this is an empirical equation and can be used for velocities *2* to *20 m/s*.

### Example - Convective Heat Transfer

A fluid flows over a plane surface *1 m by 1 m.* The surface temperature is *50*^{o}*C*, the fluid temperature is *20*^{o}*C* and the convective heat transfer coefficient is *2000 W/m*^{2o}*C*. The convective heat transfer between the hotter surface and the colder air can be calculated as

q= (2000 W/(m^{2o}C)) ((1 m) (1 m)) ((50^{o}C) - (20^{o}C))

= 60000 (W)

= 60 (kW)

### Convective Heat Transfer Calculator

*A - surface area (m ^{2})*

*t _{surface} - surface temperature (^{o}C)*

*t _{air}*

*- air temperature (*

^{o}C) *h _{c}*

*- convective heat transfer coefficient (W/(m*

^{2}K))

Heat Transfer = (*W*)

### Convective Heat Transfer Chart

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