Explanation:
Steady-state conduction with internal heat generation:
dx2d2T+kq˙=0 ......(i)
It is given that the surface of the cylinder is insulated the heat will transfer only in x-direction i.e. 1-D heat transfer.
The temperature will remain the same even if we change the convective heat transfer coefficient.
Proof:

The rate of heat generation is q˙=cosL2πx
To find the temperature profile we will differentiate equation (i) and will use boundary conditions.
dx2d2T=−kq˙
Integrating equation we get,
dxdT=∫−kq˙dx = −k1∫cosL2πxdx
dxdT=−k1×2πL sinL2πx+c1 ....... (a)
substitute boundary condition:
at x = 0 , dT/dx = 0, sin (0) = 0
we get c1 = 0
Integrating again we get
T=−2πkL×2π−L cosL2πx+c2 ........(b)
at x = L
Heat conducted = Heat convected
\(-kA\left(\frac{dT}{dx}\right){x =L} = hA (T{L} - T_{∞})\)
−k(−k1×2πL sinL2πL)=h(TL−T∞)
sin 2π = 0 , LHS = 0 hence
Tx = L = T∞
substituting in equation b
Tx = L = T∞ =−2πkL×2π−L cosL2πL+c2
c2 = T∞−4π2kL2
Hence the equation of temperature is:
T=T∞+2πkL×2πL cosL2πx−4π2kL2
It does not depend on convective heat transfer coefficient h.
Hence on there is no effect on temperature TA if convective heat transfer is increased to 2h.

Confusion Points