Ok, I had find a solution for this.
Your mean will run if you've only one heat exchager. The problem here is that we've not the number of heat exchanger of shell&tube class in series needed, and this number must be fixed. So, one method can be readed in the Heat Exchanger Design Handbook...
Hi, I need to design a system of heat exchangers for a steady-state process. I have inlet temperatures of the fluids, the amount of heat that must be exchanged, the max flow ratio and other data. The objective is to reach the exchange area and the length of the shell. My problem is that I have...