Tahlo 1 I Stroam Nata A Maximum Energy Recovery Heat Exchanger Network (MER HEN), using the Pinch Design method, is to be designed for this chemical process using a minimum approach temperature (TMIN) of 10C. The MER HEN is to be designed in three parts (above the utility pinch, above the process pinch, and below the process pinch). There are three utilities available to provide additional process heating and cooling (Table 1.2). The final developed MER HEN and its component parts (above the utility pinch, above the process pinch, and below the process pinch) are required to be validated and tested for feasibility, by comparing their features with targeted values. Produce a feasible, validated Maximum Energy Recovery Heat Exchanger Network (MER HEN) for the Above Utility Pinch Design region using the Pinch Design method for the chemical process (Table 1.1), using a minimum approach temperature (TMIN) of 10C. In this design region you should be using only hot oil as a utility