The last question must be some kind of hint, to compensate for the opaque and tricky statement of the problem.
My understanding is that the heat rate (W) does not change, as it is determined by the chemical reaction.
Therefore, no heat transfer coefficient is needed, neither convective in air, nor conductive in the foam.
It is only the outer diameter that matters.
It must be such that the heat flow (W/m²) is reduced from hcv(200-25) to hcv(40-25).
Therefore the surface must increase by a factor 11.66 .
Therefore, the diameter must be sqrt(11.66) = 3.41 larger, which gives the thickness of the foam = 2.41/2 = 1.2 .
Question:
Would it be possible to replace the foam by a shell around the tank, with no convective heat transfer, but mainly radiation?