Module 3: Transport phenomena in furnaces
  Lecture 29: Refractory Design in furnaces
 

The expression   is known as logarithmic mean area. Consider a thin walled pipe or a duct with a wall thickness less than inside diameter , the area ratio  is less than 2 and the logarithmic mean area is substantially equal to the arithmetic mean area . However, if  is greater than 2 which could be a thick-walled pipe or thick insulation of small pipes or tube furnaces, use of arithmetic mean area would predict higher heat losses than the logarithmic mean area.

Figure 4 is the construction of a composite cylindrical wall having radius  and  measured from the centre of the cylinder of radius  such that  and . The thermal conductivity of the refractory material of thicknesses  and  is  and  respectively.  The length of the cylinder is . As in the case of flat wall  and  are the heat transfer coefficients that determine surface temperatures  and . The composite wall is placed in between furnace temperature  and environment temperature .


Figure 29.4:

  Temperature distribution in a composite cylindrical wall of different diameters at steady state.

As no heat is produced in the composite wall, steady state heat flow for the length of the cylinder  is

(9)

Adding thermal resistance in series



(10)

The equation 10 determines the heat flow in a composite wall. The temperature profile is as shown in the figure by the solid line.