Your browser doesn't support javascript.
loading
Pure-Water-Fed Forward-Bias Bipolar Membrane CO2 Electrolyzer.
Heßelmann, Matthias; Lee, Jason Keonhag; Chae, Sudong; Tricker, Andrew; Keller, Robert Gregor; Wessling, Matthias; Su, Ji; Kushner, Douglas; Weber, Adam Z; Peng, Xiong.
Afiliação
  • Heßelmann M; Energy Technologies Area, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
  • Lee JK; Chemical Process Engineering, RWTH Aachen University, Forckenbeckstr. 51, 52074 Aachen, Germany.
  • Chae S; Energy Technologies Area, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
  • Tricker A; Energy Technologies Area, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
  • Keller RG; Energy Technologies Area, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
  • Wessling M; Chemical Process Engineering, RWTH Aachen University, Forckenbeckstr. 51, 52074 Aachen, Germany.
  • Su J; Chemical Process Engineering, RWTH Aachen University, Forckenbeckstr. 51, 52074 Aachen, Germany.
  • Kushner D; DWI Leibniz-Institute for Interactive Materials, Forckenbeckstr. 50, 52074 Aachen, Germany.
  • Weber AZ; Energy Technologies Area, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
  • Peng X; Energy Technologies Area, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
ACS Appl Mater Interfaces ; 16(19): 24649-24659, 2024 May 15.
Article em En | MEDLINE | ID: mdl-38711294
ABSTRACT
Coupling renewable electricity to reduce carbon dioxide (CO2) electrochemically into carbon feedstocks offers a promising pathway to produce chemical fuels sustainably. While there has been success in developing materials and theory for CO2 reduction, the widespread deployment of CO2 electrolyzers has been hindered by challenges in the reactor design and operational stability due to CO2 crossover and (bi)carbonate salt precipitation. Herein, we design asymmetrical bipolar membranes assembled into a zero-gap CO2 electrolyzer fed with pure water, solving both challenges. By investigating and optimizing the anion-exchange-layer thickness, cathode differential pressure, and cell temperature, the forward-bias bipolar membrane CO2 electrolyzer achieves a CO faradic efficiency over 80% with a partial current density over 200 mA cm-2 at less than 3.0 V with negligible CO2 crossover. In addition, this electrolyzer achieves 0.61 and 2.1 mV h-1 decay rates at 150 and 300 mA cm-2 for 200 and 100 h, respectively. Postmortem analysis indicates that the deterioration of catalyst/polymer-electrolyte interfaces resulted from catalyst structural change, and ionomer degradation at reductive potential shows the decay mechanism. All these results point to the future research direction and show a promising pathway to deploy CO2 electrolyzers at scale for industrial applications.
Palavras-chave

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Idioma: En Ano de publicação: 2024 Tipo de documento: Article

Texto completo: 1 Coleções: 01-internacional Base de dados: MEDLINE Idioma: En Ano de publicação: 2024 Tipo de documento: Article