An electrolytic cation exchange process has been developed to extract large quantities of carbon dioxide (CO 2 ) from natural seawater where it is in the form of bicarbonate and carbonate, and to simultaneously produce H 2 gas in quantities and ratios (3:1 H 2 to CO 2 ) intended for future synthesis of hydrocarbons. During the early stages of development, optimizing the energy efficiency and CO 2 production efficiency of the process is key to its future practical implementation. Both efficiencies are impacted specifically by the amount of time needed to re-establish equilibrium conditions in the module after a polarity reversal. Three electrolytic cation exchange module (E-CEM) configurations were tested and evaluated to determine the parameters that had the most significant effects on shortening the re-equilibration times after polarity reversal. From these evaluations, a new fourth custom E-CEM was designed, built, and tested that lowered seawater pH 65% faster so that carbonate and bicarbonate in the seawater were re-equilibrated to CO 2 gas for recovery and the electrical resistance was reduced by 31%. These results are important for the future scale-up and implementation of such a process.
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Willauer et al. (2017) studied this question.
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