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easier to control corrosion as compared to MED. However, due to the indirect heat transfer, MSF has a lower performance and consumes more energy than MED (Van der Bruggen and Vandecasteele, 2002). Figure 2–4: Principle of MSF Furthermore, considering the low-grade nature of heat from the potato crisps processing plant under investigation, this technology will not be economic for a wastewater purification application. MD is a relatively new technology. It is an evaporative process, using a porous hydrophobic membrane, which physically separates the aqueous liquid feed from the gaseous permeate based on the vapour pressure gradient (Wirth and Corinne, 2002). A typical flow diagram of an MD process is shown in Figure 2-5. The feed stream is sent to a heat exchanger where it is preheated using the heat from the vaporized permeate. The heated feed stream is then pumped through a heater where it is vaporized. The vaporized (permeate) part of the feed stream is drawn through the hydrophobic membrane using a vacuum pump. The permeate is then used to preheat the feed stream in the heat exchanger before being passed through a cooler 54PDF Image | OPTIMISING THERMAL ENERGY RECOVERY
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