ANSYS Fluent 19.0 CFD with laminar flow, porous media and Langmuir kinetic UDFs
Zn-HHTP-H CFD porous-media model · Model
N2/NH3 gas model, 2.5 um x 2.5 um x 1.5 um domain, inlet velocity 100 um s-1, Kbulk = 2e-15 m2, room conditions.
| Property | Reported value | Normalised value | Uncertainty | Origin and quality | Source |
|---|---|---|---|---|---|
| Hollow volume ratio beta Zn-HHTP-B | beta = 0 | — | — | Text Exact Reported | 4 · Numerical simulations · Fig. 4c |
| Hollow volume ratio beta Zn-HHTP-HMarked as a best value within this paper | beta = 0.76 | — | — | Text Exact Reported | 4 · Numerical simulations · Fig. 4c |
| Hollow volume ratio beta Zn-HHTP-HS | beta = 0.43 | — | — | Text Exact Reported | 4 · Numerical simulations · Fig. 4c |
| Simulated Khollow/Kbulk Zn-HHTP-HMarked as a best value within this paper | 8.81 | — | — | SI Table Exact Reported | S64 · Supplementary Table 4 · Supplementary Table 4 |
| Simulated Khollow/Kbulk Zn-HHTP-HS | 1.84 | — | — | SI Table Exact Reported | S64 · Supplementary Table 4 · Supplementary Table 4 |
| Average surface velocity Us Zn-HHTP-B | 4.87 x 10-6 m/s | — | — | Text Exact Reported | 4 · Numerical simulations · Fig. 4c |
| Average surface velocity Us Zn-HHTP-HMarked as a best value within this paper | 3.94 x 10-5 m/s | — | — | Text Exact Reported | 4 · Numerical simulations · Fig. 4c |
| Average surface velocity Us Zn-HHTP-HS | 1.43 x 10-5 m/s | — | — | Text Exact Reported | 4 · Numerical simulations · Fig. 4c |