In fact, there is a temperature profile within the wall, which you can characterized by both wall surface temperature. Being the heat flux constant across the fluid and wall, one can derive (plane geometry)
h1.A.(T1-Tw1) = k.A/e.(Tw1-Tw2)= h2.A.(Tw2-T2)
Notation seems to be typical....
hence, being
Tw2= h1/h2*(T1-Tw1) + T2,
the expression for Tw1 can be found:
(e/k+1/h2).T1 + T2/h1
Tw1 = ---------------------------
1/h1 + 1/h2 + e/k
So, the wall temperature is higly dependent upon the relative heat transfer coefficient. Here, if the heat transfer coefficient for Side 2 is 100 (water) and 10 for Side 1 (Oil), the wall temperature will be closer to the side 2 Bulk temperature.
Regards