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laws:hypofe2 [2025/09/10 14:33] arthur [Real parameters] |
laws:hypofe2 [2025/09/10 14:39] (current) arthur [Number of state variables] |
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^ Line 1 (3I10,2G10.0) ^^ | ^ Line 1 (3I10,2G10.0) ^^ | ||
|NLAWFEM2|Number of constitutive laws at the subscale| | |NLAWFEM2|Number of constitutive laws at the subscale| | ||
- | |KFLU|Number of DOF: 1=Pw, 2=Pw+C, 3=Pw+Pg, 4=Pw+C+Pg with C the concentration in pollutant| | + | |KFLU|Number of DOF at the microscale: 1 = $P_w$, 2 = $P_w+C$, 3 = $P_w+P_g$, 4 = $P_w+C+P_g$ with $C$ the concentration in pollutant| |
|MITER|Maximum number of iterations at the subscale| | |MITER|Maximum number of iterations at the subscale| | ||
|CNORM|Norm for the solver of the subscale| | |CNORM|Norm for the solver of the subscale| | ||
- | |FACONV|Units of conversion of the RVE (it has a size of 1[-])| | + | |FACONV|Units of conversion of the RVE (it has a size of 1*FACONV[-])| |
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|SIG(16)|Advective flow of dissolved gas along $x$ (unused)| | |SIG(16)|Advective flow of dissolved gas along $x$ (unused)| | ||
|SIG(17)|Advective flow of dissolved gas along $y$ (unused)| | |SIG(17)|Advective flow of dissolved gas along $y$ (unused)| | ||
- | |SIG(18)|Unused| | + | |SIG(18)|Vapour flow along $x$ $(=f_{vx})$| |
- | |SIG(19)|Unused| | + | |SIG(19)|Vapour flow along $y$ $(=f_{vy})$| |
- | |SIG(20)|Unused| | + | |SIG(20)|Vapour flow stored $(=f_{ve})$| |
|SIG(21)|Unused| | |SIG(21)|Unused| | ||
|SIG(22)|Unused| | |SIG(22)|Unused| | ||
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===== State variables ===== | ===== State variables ===== | ||
==== Number of state variables ==== | ==== Number of state variables ==== | ||
- | 10 + 5*(Number of Subscale Nodes)\\ | + | 11 + 5*(Number of Subscale Nodes)\\ |
- | /!\ The state variables vector also contains the following information for each subscale node: X,Y,Pw,C,Pg | + | /!\ The state variables vector also contains the following information for each subscale node: $X$, $Y$, $P_w$, $C$, $P_g$ |
==== List of state variables ==== | ==== List of state variables ==== | ||
|Q(1)|Liquid water mass at the RVE| | |Q(1)|Liquid water mass at the RVE| | ||
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|Q(7)|Homogenised gas relative permeability| | |Q(7)|Homogenised gas relative permeability| | ||
|Q(8)|Homogenised macroscale tortuosity| | |Q(8)|Homogenised macroscale tortuosity| | ||
- | |Q(9)|Vapour mass at the RVE (unused)| | + | |Q(9)|Vapour mass at the RVE| |
- | |Q(10)|Homogenised succion| | + | |Q(10)|Homogenised total suction $(= p_g - p_w + osmotic)$| |
- | |Q(11 + (i-1)*5)|$X_i$| | + | |Q(11)|Homogenised osmotic suction $(= osmotic)$| |
- | |Q(11 + (i-1)*5 +1)|$Y_i$| | + | |Q(12 + (i-1)*5)|$X_i$| |
- | |Q(11 + (i-1)*5 +2)|$P_{w,i}$| | + | |Q(12 + (i-1)*5 +1)|$Y_i$| |
- | |Q(11 + (i-1)*5 +3)|$C_i$| | + | |Q(12 + (i-1)*5 +2)|$P_{w,i}$| |
- | |Q(11 + (i-1)*5 +4)|$P_{g,i}$| | + | |Q(12 + (i-1)*5 +3)|$C_i$| |
+ | |Q(12 + (i-1)*5 +4)|$P_{g,i}$| | ||