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Update Inc_Combustion.md (#186)
remove density from source term in description of transport equations
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_tutorials/incompressible_flow/Inc_Combustion/Inc_Combustion.md

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@@ -48,7 +48,7 @@ The `CSpeciesSolver` object in SU2 solves the controlling variables and passive
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$$
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\begin{equation}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(\rho D\nabla\mathcal{Y}\right) = \rho\dot{\omega}_\mathcal{Y}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(\rho D\nabla\mathcal{Y}\right) = \dot{\omega}_\mathcal{Y}
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\end{equation}
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$$
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@@ -60,15 +60,15 @@ $$
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$$
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\begin{equation}
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\frac{\partial \rho Y_j}{\partial t} + \nabla\cdot(\rho\vec{u}Y_j) - \nabla\cdot\left(\rho D\nabla Y_j\right) = \rho\dot{\omega}^+ + \rho\dot{\omega}^- Y_j
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\frac{\partial \rho Y_j}{\partial t} + \nabla\cdot(\rho\vec{u}Y_j) - \nabla\cdot\left(\rho D\nabla Y_j\right) = \dot{\omega}^+ + \dot{\omega}^- Y_j
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\end{equation}
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$$
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2. partially or non-premixed, no preferential diffusion:
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$$
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\begin{equation}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(\rho D\nabla\mathcal{Y}\right) = \rho\dot{\omega}_\mathcal{Y}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(\rho D\nabla\mathcal{Y}\right) = \dot{\omega}_\mathcal{Y}
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\end{equation}
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$$
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@@ -80,21 +80,21 @@ $$
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$$
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\begin{equation}
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\frac{\partial \rho Z}{\partial t} + \nabla\cdot(\rho\vec{u}Z) - \nabla\cdot\left(\rho D\nabla Z\right) = \rho\dot{\omega}_\mathcal{Y}
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\frac{\partial \rho Z}{\partial t} + \nabla\cdot(\rho\vec{u}Z) - \nabla\cdot\left(\rho D\nabla Z\right) = \dot{\omega}_\mathcal{Y}
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\end{equation}
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$$
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$$
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\begin{equation}
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\frac{\partial \rho Y_j}{\partial t} + \nabla\cdot(\rho\vec{u}Y_j) - \nabla\cdot\left(\rho D\nabla Y_j\right) = \rho\dot{\omega}^+ + \rho\dot{\omega}^- Y_j
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\frac{\partial \rho Y_j}{\partial t} + \nabla\cdot(\rho\vec{u}Y_j) - \nabla\cdot\left(\rho D\nabla Y_j\right) = \dot{\omega}^+ + \dot{\omega}^- Y_j
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\end{equation}
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$$
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3. pre-mixed, partially pre-mixed, non-premixed, with preferential diffusion:
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$$
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\begin{equation}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(\rho D\nabla\beta_\mathcal{Y}\right) = \rho\dot{\omega}_\mathcal{Y}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(\rho D\nabla\beta_\mathcal{Y}\right) = \dot{\omega}_\mathcal{Y}
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\end{equation}
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$$
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@@ -112,7 +112,7 @@ $$
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$$
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\begin{equation}
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\frac{\partial \rho Y_j}{\partial t} + \nabla\cdot(\rho\vec{u}Y_j) - \nabla\cdot\left(\rho D\nabla Y_j\right) = \rho\dot{\omega}^+ + \rho\dot{\omega}^- Y_j
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\frac{\partial \rho Y_j}{\partial t} + \nabla\cdot(\rho\vec{u}Y_j) - \nabla\cdot\left(\rho D\nabla Y_j\right) = \dot{\omega}^+ + \dot{\omega}^- Y_j
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\end{equation}
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$$
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@@ -175,7 +175,7 @@ Pre-mixed combustion of reactants with high hydrogen content at lean conditions
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$$
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\begin{equation}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(D\nabla\beta_\mathcal{Y}\right) = \rho\dot{\omega}_\mathcal{Y}
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\frac{\partial \rho \mathcal{Y}}{\partial t} + \nabla\cdot(\rho\vec{u}\mathcal{Y}) - \nabla\cdot\left(D\nabla\beta_\mathcal{Y}\right) = \dot{\omega}_\mathcal{Y}
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\end{equation}
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$$
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