Fig. 2: BPM electrodialysis performance characteristics.
From: A direct coupled electrochemical system for capture and conversion of CO2 from oceanwater

a Simulated BPM voltage vs. total current density (black line) as well as partial current density carried by major ions, including proton and hydroxide for water dissociation (blue line), Na+ (green line) and Cl− (purple line), in the synthetic oceanwater. Black dots indicate the experimentally measured BPM voltage as a function of the applied current density, corrected for the ohmic resistance in the oceanwater. b Fractional current carried by H+ \(\left( {j_{{\mathrm{H}}^ + }}/j_{\mathrm{total}} \right)\), OH− \(\left( {j_{{\mathrm{OH}}^ - }} /j_{\mathrm{total}}\right)\), Na+ \(\left( {j_{{\mathrm{Na}}^ + }} /j_{\mathrm{total}}\right)\) and Cl− \(\left( {j_{{\mathrm{Cl}}^ - }} /j_{\mathrm{total}} \right)\) across the BPM as a function of the total current density (jtotal). c Experimentally measured voltage-current density characteristics of the BPM electrodialysis cell using 0.5 M Na2SO4 electrode solution at a flow rate of 40 ml min−1 (red dots), 0.4 M K3/K4[Fe(CN)6] at a flow rate of 40 ml min−1 (black dots) and 20 ml min−1 (blue dots), 0.2 M K3/K4[Fe(CN)6] at a flow rate of 40 ml min−1 (green dots) and 20 ml min−1 (purple dots). Dashed lines are used to guide the eye. d Experimentally measured (black dots) and calculated (lines) pH of the acidified stream as a function of applied current density for BPM electrodialysis cell with an electrode and membrane active area of 64 cm2.