Electrochemical CO2 reduction in membrane-electrode assemblies

Chem ◽  
2022 ◽  
Author(s):  
Lei Ge ◽  
Hesamoddin Rabiee ◽  
Mengran Li ◽  
Siddhartha Subramanian ◽  
Yao Zheng ◽  
...  
2019 ◽  
Vol 12 (6) ◽  
pp. 1950-1968 ◽  
Author(s):  
Lien-Chun Weng ◽  
Alexis T. Bell ◽  
Adam Z. Weber

This work presents a multiphysics model simulating membrane-electrode assemblies for CO2 reduction.


2020 ◽  
Vol 13 (10) ◽  
pp. 3592-3606
Author(s):  
Lien-Chun Weng ◽  
Alexis T. Bell ◽  
Adam Z. Weber

A multiphysics model is presented to study potential losses in Cu-MEAs and how various physical phenomena impact the product distribution of CO2 reduction.


2013 ◽  
Vol 10 (1) ◽  
Author(s):  
Toshiro Kobayashi ◽  
Etsuro Hirai ◽  
Hideki Itou ◽  
Takuya Moriga

This paper describes the development of mass-production technology for membrane-electrode assemblies (MEA) with a radical capturing layer and verifies its performance. Some of the authors of this paper previously developed an MEA with a radical capturing layer along the boundaries between the electrode catalyst layer and the polymer membrane to realize an endurance time of 20,000 h in accelerated daily start and daily stop (DSS) deterioration tests. Commercialization of these MEAs requires a production technology that suits mass production lines and provides reasonable cost performance. After developing a water-based slurry and selecting a gas diffusion layer (GDL), a catalyst layer forming technology uses a rotary screen method for electrode formation. Studies confirmed continuous formation of the catalyst layer, obtaining an anode/cathode thickness of 55 μm (+10/−20)/50 μm (+10/−20) by optimizing the opening ratio and thickness of the screen plate. A layer-forming technology developed for the radical capturing layer uses a two-fluid spraying method. Continuous formation of an 8 μm thick (±3 μm) radical capturing layer proved feasible by determining the appropriate slurry viscosity, spray head selection, and optimization of spraying conditions.


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