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## Overview

## Problem Description

## Results

This scenario describes the transport of two solutes (Snythetica and Syntheticb) through a saturated media. Both solutes react to Productd according to $\text{Product d}=\text{Synthetic a}+0.5~\text{Synthetic b}$. The speed of the reaction is described with a first–order relationship $\frac{dc}{dt}=U(\frac{c_{\text{Synthetic a}}}{K_m+c_{\text{Synthetic b}}})$. The coupling of OGS-6 and IPhreeqc used for simulation requires to simulate the transport of $H^+$–ions, additionally. This is required to adjust the compulsory charge balance computation executed by Phreeqc. The solution by OGS-6–IPhreeqc will be compared to the solution by a coupling of OGS-5–IPhreeqc.

**1d scenario:**
The 1d–model domain is 0.5 m long and discretized into 200 line elements.
The domain is saturated at start–up ($p(t=0)=$ 1.0e-5 Pa).
A constant pressure is defined at the left side boundary ($g_{D,\text{upstream}}^p$) and a Neumann BC for the water mass out-flux at the right side ($g_{N,\text{downstream}}^p$).
Both solutes, Synthetic a and Synthetic b are present at simulation start–up at concentrations of $c_{\text{Synthetic a}}(t=0)=c_{\text{Synthetic b}}(t=0)= 0.5~\textrm{mol kg}^{-1}~\textrm{water}$, the influent concentration is $0.5~\textrm{mol kg}^{-1}~\textrm{water}$ as well.
Product d is not present at start–up ($c_{\text{Productd}}(t=0)=0$); neither in the influent.
The initial concentration of $\text{H}^+$–ions is $1.0e\textrm{-}7~\textrm{mol kg}^{-1}~\textrm{water}$; the concentration at the influent point is the same.
Respective material properties, initial and boundary conditions are listed in the tables below.

**2d scenario:**
The 2d–scenario only differs in the domain geometry and assignment of the boundary conditions.
The horizontal domain is 0.5 m in x and 0.5 m in y direction, and, discretized into 10374 quadratic elemtents with an edge size of 0.0025 m.

Parameter | Description | Value | Unit |
---|---|---|---|

$\phi$ | Porosity | 1.0 | |

$\kappa$ | Permeability | 1.157e-12 | $\textrm{m}^2$ |

$S$ | Storage | 0.0 | |

$a_L$ | long. Dispersion length | 0.0 | m |

$a_T$ | transv. Dispersion length | 0.0 | m |

$\rho_w$ | Fluid density | 1.0e+3 | $\textrm{kg m}^{-3}$ |

$\mu_w$ | Fluid viscosity | 1.0e-3 | Pa s |

$D_{\text{H}^+}$ | Diffusion coef. for $\text{H}^+$ | 1.0e-7 | m$^2$ s |

$D_{solutes}$ | Diffusion coef. for Synthetica, Syntheticb and Productd | 1.0e-12 | m$^2$ s |

$U$ | Reaction speed constant | 1.0e-3 | h$^{-1}$ |

$K_m$ | Half–saturation constant | 10 | mol kg$^{-1}$ water |

Table: Media, material and component properties

Parameter | Description | Value | Unit |
---|---|---|---|

$p(t=0)$ | Initial pressure | 1.0e+5 | Pa |

$g_{N,downstream}^p$ | Water outflow mass flux | -1.685e-02 | mol kg$^{-1}$ water |

$g_{D,upstream}^p$ | Pressure at inlet | 1.0e+5 | Pa |

$c_{Synthetica}(t=0)$ | Initial concentration of Synthetica | 0.5 | mol kg$^{-1}$ water |

$c_{Syntheticb}(t=0)$ | Initial concentration of Syntheticb | 0.5 | mol kg$^{-1}$ water |

$c_{Productd}(t=0)$ | Initial concentration of Productd | 0 | mol kg${^-1}$ water |

$c_{\text{H}^+}(t=0)$ | Initial concentration of $\text{H}^+$ | 1.0e-7 | mol kg$^{-1}$ water |

$g_{D,upstream}^{Synthetica_c}$ | Concentration of Synthetica | 0.5 | mol kg$^{-1}$ water |

$g_{D,upstream}^{Syntheticb_c}$ | Concentration of Syntheticb | 0.5 | mol kg$^{-1}$ water |

$g_{D,upstream}^{Productd}$ | Concentration of Productd | 0.0 | mol kg$^{-1}$ water |

$g_{D,upstream}^{\text{H}^+}$ | Concentration of $\text{H}^+$ | 1.0e-7 | mol kg$^{-1}$ water |

Table: Initial and boundary conditions

The kinetic reaction results in the expected decline of the concentration of Synthetic a and Synthetic b, which is super-positioned by the influx of these two educts through the left side. By contrast, the concentration of Product d increases in the domain. Over time, opposed concentration fronts for educts and Product d evolve. Both, OGS-6 and OGS-5 simulations yield the same results in the 1d as well as 2d scenario. For instance, the difference between the OGS-6 and the OGS-5 computation for the concentration of Product d expressed as root mean squared error is 1.76e-7 mol kg$^{-1}$ water (over all time steps and mesh nodes, 1d scenario); the corresponding median absolute error is 1.0e-7 mol kg$^{-1}$ water. This verifies the implementation of OGS-6–IPhreeqc.

This article was written by Johannes Boog. If you are missing something or you find an error please let us know.
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Commit: explanation stress concentration and running model 5c94789
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