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ENH: Uptodate of tutorials
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@ -37,7 +37,7 @@ boundaryField
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burner
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{
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type flowRateInletVelocity;
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flowRate 0.001294; //60kW C3H8
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flowRate constant 0.001294; //60kW C3H8
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value uniform (0 0 0);
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}
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@ -71,6 +71,7 @@ solvers
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nCellsInCoarsestLevel 10;
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agglomerator faceAreaPair;
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mergeLevels 1;
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maxIter 20;
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}
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G
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@ -99,7 +100,7 @@ relaxationFactors
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equations
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{
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"(U|k).*" 1;
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"(C3H8|O2|H2O|CO2|hs).*" 0.9;
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"(CH4|O2|H2O|CO2|hs).*" 0.9;
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}
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}
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@ -31,6 +31,7 @@ divSchemes
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div(U,p) Gauss linear;
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div(phi,h) Gauss upwind;
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div(phi,k) Gauss upwind;
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div(phi,K) Gauss upwind;
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div(phi,epsilon) Gauss upwind;
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div(phi,R) Gauss upwind;
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div(R) Gauss linear;
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@ -31,6 +31,7 @@ divSchemes
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div(U,p) Gauss linear;
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div(phi,h) Gauss upwind;
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div(phi,k) Gauss upwind;
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div(phi,K) Gauss upwind;
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div(phi,epsilon) Gauss upwind;
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div(phi,R) Gauss upwind;
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div(R) Gauss linear;
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@ -31,6 +31,7 @@ divSchemes
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div(U,p) Gauss linear;
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div(phi,h) Gauss upwind;
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div(phi,k) Gauss upwind;
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div(phi,K) Gauss upwind;
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div(phi,epsilon) Gauss upwind;
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div(phi,R) Gauss upwind;
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div(R) Gauss linear;
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@ -31,6 +31,7 @@ divSchemes
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div(U,p) Gauss linear;
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div(phi,h) Gauss upwind;
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div(phi,k) Gauss upwind;
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div(phi,K) Gauss upwind;
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div(phi,epsilon) Gauss upwind;
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div(phi,R) Gauss upwind;
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div(R) Gauss linear;
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