Answer:
0.0371 kg/s.m
Explanation:
From the given information, let's have an imaginative view of the semi-cylinder; (The image is shown below)
Assuming the base surface of both ends of the cylinder is denoted by:

Thus, using the summation rule, the view factor
and
is as follows:

Let assume the surface (1) is flat, the 
Now:


However, using the reciprocity rule to determine the view factor from the dome-shaped cylinder
to the flat base surface
; we have:

Suppose, we replace DL for
and
=
Then:

Now, we need to employ the use of energy balance formula to the dryer.
i.e.

But, before that; let's find the radian heat exchange occurring among the dome and the flat base surface:

where;



∴

Recall the energy balance formula;

where;

here;
= enthalpy of vaporization
m = the water mass flow rate
∴
