Direct heat exchange is, therefore, not possible. In our example, we will buffer the heat so that the available heat is not lost. The temperature difference is the driving force for heating or cooling. It is, therefore, essential to keep the hot buffer as warm as possible and the cold buffer as cool as possible. A batch is often heated or cooled by pumping the contents around through a heat exchanger. However, this has a negative effect on heat recovery because the pumping also produces an average temperature; the return temperature is low at the beginning of the heating process and high at the end. So, a better approach would be to heat the raw materials feeding into the reactor and cool the product stream coming out. This method would ensure the hot buffer is kept at the highest possible temperature and the cold buffer at the lowest possible temperature.
Low temperature loss due to heating and cooling product streams
To compensate for the temperature drop in the hot buffer (caused by heating the product), the hot buffer needs heating; electrically with a heater. But because we heat the raw materials feeding into the reactor rather than pumping the product around, the temperature loss is relatively low; a favourable effect. By applying a heat buffer, the heating time range is also lengthened, resulting in much lower peak power than direct heating. By cooling the product, the cold buffer becomes warmer and needs cooling. The required cooling capacity is minimised by cooling the product stream leaving the reactor rather than pumping the product through a heat exchanger. The concept described above minimises peak electrical power and maximises heat recovery.