“…The charging activity of the particle was maximum near the current collecting boundary. The model also show inactivity of charging in the centers of the flow channels [49,54] in terms of uncha when moving away from the current-collector (CC) boundary. Figure 12 shows the charge distributions in the flow channel for the three geometries.…”
Section: Comparison Between Simulations and Experimental Resultsmentioning
confidence: 98%
“…The charging particle was maximum near the current collecting boundary. The m inactivity of charging in the centers of the flow channels [49,54] in when moving away from the current-collector (CC) boundary.…”
Section: Comparison Between Simulations and Experimental Resultsmentioning
confidence: 99%
“…where k B is the Boltzmann constant, and T 0 = 273 K is the temperature in Kelvin. The total mass of superparticles was equal to the total mass of spherical carbon particles in the experimental slurry [49,54]. The motion of superparticles was responsible for the physical charge redistribution, which occurred in two ways.…”
Section: Theoretical Model Descriptionmentioning
confidence: 99%
“…The model described above is implemented for three specific channel geometries: circular, box-shaped with a linear current collector, and box-shaped with an extended current collector, as shown in Figure 5 [54]. Each geometrical design allows the different direct contact rate between the electrode phase and the CC.…”
Section: Geometrical Designmentioning
confidence: 99%
“…With the flow channels 5 mm wide and 120 mm long, the contact area for circular flow channel geometry is approximately 1884 mm 2 . The contact area is reduced to 600 mm 2 and 1800 mm 2 for the box-shaped geometry with linear and extended CC, respectively [54]. The circular-shaped channel geometry resembles the prototype used for experimental analysis and later used for the model optimization and sensitivity testing of modeling parameters.…”
Aqueous electrochemical flow capacitors (EFCs) have demonstrated high-power capabilities and safety at low cost, making them promising energy storage devices for grid applications. A primary performance metric of an EFC is the steady-state electrical current density it can accept or deliver. Performance prediction, design improvements, and up-scaling are areas in which modeling can be useful. In this paper, a novel stochastic superparticle (SP) modeling approach was developed and applied to study the charging of carbon electrodes in the EFC system, using computational superparticles representing real carbon particles. The model estimated the exact values of significant operating parameters of an EFC, such as the number of particles in the flow channel and the number of electrolytic ions per carbon particle. Optimized model parameters were applied to three geometrical designs of an EFC to estimate their performance. The modeling approach allowed study of the charge per carbon particle to form the electric double-layer structure. The linear relationship between the concentration of SPs and the ionic charge was observed when optimized at a constant voltage of 0.75 V. The simulation results are in excellent agreement with experimental data, providing a deep insight into the performance of an EFC and identifying limiting parameters for both engineers and material scientists to consider.
“…The charging activity of the particle was maximum near the current collecting boundary. The model also show inactivity of charging in the centers of the flow channels [49,54] in terms of uncha when moving away from the current-collector (CC) boundary. Figure 12 shows the charge distributions in the flow channel for the three geometries.…”
Section: Comparison Between Simulations and Experimental Resultsmentioning
confidence: 98%
“…The charging particle was maximum near the current collecting boundary. The m inactivity of charging in the centers of the flow channels [49,54] in when moving away from the current-collector (CC) boundary.…”
Section: Comparison Between Simulations and Experimental Resultsmentioning
confidence: 99%
“…where k B is the Boltzmann constant, and T 0 = 273 K is the temperature in Kelvin. The total mass of superparticles was equal to the total mass of spherical carbon particles in the experimental slurry [49,54]. The motion of superparticles was responsible for the physical charge redistribution, which occurred in two ways.…”
Section: Theoretical Model Descriptionmentioning
confidence: 99%
“…The model described above is implemented for three specific channel geometries: circular, box-shaped with a linear current collector, and box-shaped with an extended current collector, as shown in Figure 5 [54]. Each geometrical design allows the different direct contact rate between the electrode phase and the CC.…”
Section: Geometrical Designmentioning
confidence: 99%
“…With the flow channels 5 mm wide and 120 mm long, the contact area for circular flow channel geometry is approximately 1884 mm 2 . The contact area is reduced to 600 mm 2 and 1800 mm 2 for the box-shaped geometry with linear and extended CC, respectively [54]. The circular-shaped channel geometry resembles the prototype used for experimental analysis and later used for the model optimization and sensitivity testing of modeling parameters.…”
Aqueous electrochemical flow capacitors (EFCs) have demonstrated high-power capabilities and safety at low cost, making them promising energy storage devices for grid applications. A primary performance metric of an EFC is the steady-state electrical current density it can accept or deliver. Performance prediction, design improvements, and up-scaling are areas in which modeling can be useful. In this paper, a novel stochastic superparticle (SP) modeling approach was developed and applied to study the charging of carbon electrodes in the EFC system, using computational superparticles representing real carbon particles. The model estimated the exact values of significant operating parameters of an EFC, such as the number of particles in the flow channel and the number of electrolytic ions per carbon particle. Optimized model parameters were applied to three geometrical designs of an EFC to estimate their performance. The modeling approach allowed study of the charge per carbon particle to form the electric double-layer structure. The linear relationship between the concentration of SPs and the ionic charge was observed when optimized at a constant voltage of 0.75 V. The simulation results are in excellent agreement with experimental data, providing a deep insight into the performance of an EFC and identifying limiting parameters for both engineers and material scientists to consider.
CO2 conversion is an important part of the transition towards clean fuels and chemicals. However, low solubility of CO2 in water and its slow diffusion cause mass transfer limitations in...
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