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energy efficiency analysis, performance evaluation and

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Figure 1.1 Schematic of a typical flow-by capacitive deionization with ion exchange.
Figure 1.2 Illustration of constant voltage charging and constant current charging. (A) Constant voltage (CV) charging and zero voltage discharge, effluent concentration profile and current responses
Figure 2.2 Graphical illustration of a batch-mode and thermodynamically reversible CDI process
Figure 2.3 Relationship between cell voltage and micropore charge density, and that between the micropore and bulk concentrations
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High TEE in (some) CDI processes with intercalation materials Materials and Methods Conclusions Excess voltage and excess energy Dynamic transport modeling Experimental results and model validation Conclusions

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