<HashMap><database>biostudies-literature</database><scores/><additional><submitter>Ren Y</submitter><funding>Special Research Assistant Program of Chinese Academy of Sciences</funding><funding>Shandong Postdoctoral Innovative Talent Support Program</funding><funding>Natural Science Foundation of Shandong Province</funding><funding>Shandong Energy Institute</funding><funding>National Natural Science Foundation of China</funding><funding>Taishan Scholar Foundation of Shandong Province</funding><funding>Postdoctoral Fellowship Program of CPSF</funding><pagination>e2401702</pagination><full_dataset_link>https://www.ebi.ac.uk/biostudies/studies/S-EPMC11220719</full_dataset_link><repository>biostudies-literature</repository><omics_type>Unknown</omics_type><volume>11(25)</volume><pubmed_abstract>Direct seawater splitting (DSS) offers an aspirational route toward green hydrogen (H&lt;sub>2&lt;/sub>) production but remains challenging when operating in a practically continuous manner, mainly due to the difficulty in establishing the water supply-consumption balance under the interference from impurity ions. A DSS system is reported for continuous ampere-level H&lt;sub>2&lt;/sub> production by coupling a dual-cation exchange membrane (CEM) three-compartment architecture with a circulatory electrolyte design. Monovalent-selective CEMs decouple the transmembrane water migration from interferences of Mg&lt;sup>2+&lt;/sup>, Ca&lt;sup>2+&lt;/sup>, and Cl&lt;sup>-&lt;/sup> ions while maintaining ionic neutrality during electrolysis; the self-loop concentrated alkaline electrolyte ensures the constant gradient of water chemical potential, allowing a specific water supply-consumption balance relationship in a seawater-electrolyte-H&lt;sub>2&lt;/sub> sequence to be built among an expanded current range. Even paired with commercialized Ni foams, this electrolyzer (model size: 2 × 2 cm&lt;sup>2&lt;/sup>) continuously produces H&lt;sub>2&lt;/sub> from flowing seawater with a rate of 7.5 mL min&lt;sup>-1&lt;/sup> at an industrially relevant current of 1.0 A over 100 h. More importantly, the energy consumption can be further reduced by coupling more efficient NiMo/NiFe foams (≈6.2 kWh Nm&lt;sup>-3&lt;/sup> H&lt;sub>2&lt;/sub> at 1.0 A), demonstrating the potential to further optimize the continuous DSS electrolyzer for practical applications.</pubmed_abstract><journal>Advanced science (Weinheim, Baden-Wurttemberg, Germany)</journal><pubmed_title>A Dual-Cation Exchange Membrane Electrolyzer for Continuous H&lt;sub>2&lt;/sub> Production from Seawater.</pubmed_title><pmcid>PMC11220719</pmcid><funding_grant_id>21975271</funding_grant_id><funding_grant_id>2023000042</funding_grant_id><funding_grant_id>SDBX2022032</funding_grant_id><funding_grant_id>ZR2020ZD07</funding_grant_id><funding_grant_id>GZB20230789</funding_grant_id><funding_grant_id>ZR2023QB004</funding_grant_id><funding_grant_id>SEI I202127</funding_grant_id><funding_grant_id>tsqn202211277</funding_grant_id><pubmed_authors>Fan F</pubmed_authors><pubmed_authors>Li J</pubmed_authors><pubmed_authors>Zhang Y</pubmed_authors><pubmed_authors>Ren Y</pubmed_authors><pubmed_authors>Chen L</pubmed_authors><pubmed_authors>Cui G</pubmed_authors><pubmed_authors>Tang B</pubmed_authors><pubmed_authors>Wang Z</pubmed_authors><pubmed_authors>Zhao J</pubmed_authors></additional><is_claimable>false</is_claimable><name>A Dual-Cation Exchange Membrane Electrolyzer for Continuous H&lt;sub>2&lt;/sub> Production from Seawater.</name><description>Direct seawater splitting (DSS) offers an aspirational route toward green hydrogen (H&lt;sub>2&lt;/sub>) production but remains challenging when operating in a practically continuous manner, mainly due to the difficulty in establishing the water supply-consumption balance under the interference from impurity ions. A DSS system is reported for continuous ampere-level H&lt;sub>2&lt;/sub> production by coupling a dual-cation exchange membrane (CEM) three-compartment architecture with a circulatory electrolyte design. Monovalent-selective CEMs decouple the transmembrane water migration from interferences of Mg&lt;sup>2+&lt;/sup>, Ca&lt;sup>2+&lt;/sup>, and Cl&lt;sup>-&lt;/sup> ions while maintaining ionic neutrality during electrolysis; the self-loop concentrated alkaline electrolyte ensures the constant gradient of water chemical potential, allowing a specific water supply-consumption balance relationship in a seawater-electrolyte-H&lt;sub>2&lt;/sub> sequence to be built among an expanded current range. Even paired with commercialized Ni foams, this electrolyzer (model size: 2 × 2 cm&lt;sup>2&lt;/sup>) continuously produces H&lt;sub>2&lt;/sub> from flowing seawater with a rate of 7.5 mL min&lt;sup>-1&lt;/sup> at an industrially relevant current of 1.0 A over 100 h. More importantly, the energy consumption can be further reduced by coupling more efficient NiMo/NiFe foams (≈6.2 kWh Nm&lt;sup>-3&lt;/sup> H&lt;sub>2&lt;/sub> at 1.0 A), demonstrating the potential to further optimize the continuous DSS electrolyzer for practical applications.</description><dates><release>2024-01-01T00:00:00Z</release><publication>2024 Jul</publication><modification>2025-04-04T23:54:42.752Z</modification><creation>2025-04-04T23:54:42.752Z</creation></dates><accession>S-EPMC11220719</accession><cross_references><pubmed>38569463</pubmed><doi>10.1002/advs.202401702</doi></cross_references></HashMap>