ABSTRACT
Owing to the rapidly growing world population and the alarming effects of global warming, there appears to be an ever-increasing demand for freshwater almost everywhere. For this reason, considerable effort has been devoted in recent years to develop an efficient and sustainable desalination technology. Among various alternatives, the air gap membrane distillation (AGMD) is widely considered as a promising candidate since the energy consumed per unit of water generated by this method is the lowest (Cabassud and Wirth, 2003; Ben Bacha et al., 2007; Bui et al., 2010). Many researchers have already constructed rigorous mathematical models to simulate and analyze the underlying transport phenomena so as to identify the key variables affecting the water flux in an AGMD module (Koschikowski et al., 2003; Meindersma et al., 2006; Ben Bacha et al., 2007; Chang et al., 2010). Particularly, Ben Bacha et al. (2007) and Chang et al. (2010, 2012) have built models of all units embedded in a solar-driven membrane distillation desalination system (SMDDS), that is, (1) the solar absorber, (2) the thermal storage tank, (3) the counter-flow shelland-tube heat exchanger, (4) the AGMD modules, and (5) the distillate tank, and then discussed various operational and control issues accordingly. The process flow diagram of a typical SMDDS design can be found in Figure 10.1. Gálvez et al. (2009) meanwhile designed a 50 m3/day desalination setup with an innovative solar-powered membrane, and Guillen-Burrieza et al. (2011) also assembled a solar-driven AGMD pilot plant. These two studies were performed with the common goal of minimizing energy consumption per unit of distillate produced. Note that SMDDS should be operated in batch mode since the solar energy can only be supplied intermittently and periodically. Furthermore, the freshwater demand of SMDDS is assumed to be time variant, thus the traditional continuous operation is almost out of the question in this study.
