Abstract
Our study focuses on an experimental demonstration of a novel method for CO2 removal from ocean water that combines H2 and redox salt looping to induce pH swings
in electrochemical flow cells. Model-driven design optimization guides 3-D printed electrolyte flow channel designs to alleviate mass-transfer limitations. A ridged flow
channel with 1 mm thick fins protruding at an angle of 30◦ from the base reduces ferri-/ferro-cyanide redox salt diffusion boundary layer thickness by up to 41% while
restricting pressure drop to less than 138 Pa. A notable feature of this work is the experimental validation of the intrinsic in-situ cleaning capabilities enabled by the
reversible looping process, eliminating what would otherwise be process down time. Over 4 acidification/basification cycles, 86% removal of fouling from electrode surfaces is demonstrated, while distinctly maintaining a constant electrochemical energy intensity.
The lab-scale, proof-of-concept experimental demonstration show promising results, which are interpreted to provide insights and guidelines towards further enhancing
scalability and efficiency of oceanic carbon removal and utilization processes.
Supplementary materials
Title
Supplementary Materials
Description
Nomenclature, 3-D Model Set-Up, Cell Assembly, Calibration, Resistance Standardization, Validation of 0-D Model, Output pH, Image Processing Technique, Cleaning, DIC measurement calibration
Actions



![Author ORCID: We display the ORCID iD icon alongside authors names on our website to acknowledge that the ORCiD has been authenticated when entered by the user. To view the users ORCiD record click the icon. [opens in a new tab]](https://www.cambridge.org/engage/assets/public/coe/logo/orcid.png)