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. 2019 Mar 22;7:146. doi: 10.3389/fchem.2019.00146

Figure 4.

Figure 4

Evaluation of the contribution of membrane adsorption to NO3-N removal in FCDI: (A) Change of the effluent NO3-N concentration and (B) mass balance of NO3-N removal. The red lines indicate the results of pseudo-first-order kinetic modeling. The system was operated in single-pass mode at i = 0 A m−2. Experimental conditions: influent NO3-N concentration = 10 mg L−1 and HRT = 0.98 min.