“…As discussed above, the removal of CC from CTBD in CWs could optimize the efficiency of physicochemical desalination processes. Numerous studies report the removal of, example bulk organics (Konnerup, Koottatep, & Brix, 2009;Neralla, Weaver, Lesikar, & Persyn, 2000), nutrients, such as N and P (Lin, Jing, Wang, & Lee, 2002;Vymazal 2007;Zheng et al, 2016), heavy metals (Khan, Ahmad, Shah, Rehman, & Khaliq, 2009;Maine, Sune, Hadad, S anchez, & Bonetto, 2006), petrochemical constituents (Knight, Kadlec, & Ohlendorf, 1999;Toor, Franz, Fedorak, MacKinnon, & Liber, 2013), and emerging contaminants including pharmaceuticals (Hijosa-Valsero et al, 2011;Li, Zhu, Ng, & Tan, 2014;R€ uhmland, Wick, Ternes, & Barjenbruch, 2015;Zhang et al, 2012), personal care products ( Avila, Nivala et al, 2014;Matamoros & Bayona, 2006;Reyes-Contreras, Matamoros, Ruiz, Soto, & Bayona, 2011), endocrine disruptors ( Avila, Nivala et al, 2014;Avila, Bayona, Mart ın, Salas, & Garc ıa, 2015), and pesticides (Budd, O'Geen, Goh, Bondarenko, & Gan, 2009;Moore et al, 2009) in CWs. Examples of water streams treated by CWs are domestic waste water (Ye & Li, 2009;Zhao et al, 2011), industrial waste water (Chen, Kao, Yeh, Chien, & Chao, 2006;Ji et al, 2002), and surface water streams (Schulz & Peall, 2001;Zhou & Hosomi, 2008).…”