Dimensionless variables
| Variable | Description |
|---|---|
| x* = x/L, y* = y/L, z* = z/L | Dimensionless position with respect to the characteristic length L |
| t* = t/(L/u0) | Dimensionless time with respect to the inlet velocity, u0 |
| ut = Ut/u0 | Dimensionless total Darcy flux |
| r = rp/r0 | Dimensionless average pore radius |
| Av = av/a0 | Dimensionless interfacial area |
| κ = K/K0 | Dimensionless permeability |
| cf = Cf /C0, cs = Cs/C0 | Dimensionless concentrations with respect to the inlet concentration of the acid, C0 |
| p = (P − Pout)/(u0L/K0) | Dimensionless pressure with respect to the constant pressure at boundary, Pout |
| Pore-scale Thiele modulus (reaction rate over diffusion rate) with respect to molecular diffusion Dm | |
| Macroscopic Thiele modulus | |
| Da = ksa0L/u0 | Damköhler number |
| Nac = αC0/ρs | Acid capacity number |
| η = 2r0/L | Ratio of average pore diameter to characteristic length |
| Sh = 2kcrp/Dm | Sherwood number (the ratio of the convective mass transfer to the rate of diffusive mass transport) |
| Variable | Description |
|---|---|
| Dimensionless position with respect to the characteristic length | |
| Dimensionless time with respect to the inlet velocity, | |
| Dimensionless total Darcy flux | |
| Dimensionless average pore radius | |
| Dimensionless interfacial area | |
| Dimensionless permeability | |
| Dimensionless concentrations with respect to the inlet concentration of the acid, | |
| Dimensionless pressure with respect to the constant pressure at boundary, | |
| Pore-scale Thiele modulus (reaction rate over diffusion rate) with respect to molecular diffusion | |
| Macroscopic Thiele modulus | |
| Da = | Damköhler number |
| Acid capacity number | |
| Ratio of average pore diameter to characteristic length | |
| Sh = 2 | Sherwood number (the ratio of the convective mass transfer to the rate of diffusive mass transport) |
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