You're right - most of it is beyond the capabilities of most posting in this forum. Does that mean it can't be done? Hardly. Will the results achieved using my methodology be exactly correct? Certainly not. They're based on correlations, which have errors inherent to them. Will it give a reasonable approximation? Yes - that's the entire point. Will entrance effects be really as important as you make them out to be? No, because the system is turbulent. If the flow were laminar (which we've both agreed that it should not be in such systems), then the entrance effects would be significant.
Simply put, if you want an exact temperature profile everywhere within the waterblock, you can use CFD. However, since I doubt the guy asking the question has access to such software (nor do 99.9% of the other people in this forum), this is irrelevant. What I have stated is correct, whether you would care to acknowledge it or not: increasing the flow velocity will increase the heat transfer coefficient and decrease core temperatures to an asymptotic limit. If you would care to dispute this simple argument, please feel free to do so, but this time using real words, not 'dynameter', 'turbulating', and other thomfoolery. I find it extremely hard to accept criticism from someone claiming to be a fluid mechanics engineer who can't even come close to the proper spelling of the word 'diameter'. As I said, I've already performed said calculations and supplied a link in the previous thread on this subject in this forum. The provided solution is not given for a perpendicular-impinging waterblock, but for a parallel flow configuration as that is the simpler case. Since no one expressed interest, I didn't waste my time solving the more complex case for perpendicular flow.