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m_w = m_{Ww}


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m_o = \rho_O \cdot q_{Oo} + \rho_G \cdot q_{Go}



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m_g = \rho_G \cdot q_{Gg} + \rho_O \cdot q_{Og}



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m_w = \rho_W \cdot q_{Ww}



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m_o = \rho_O \cdot q_{Oo} + \rho_G \cdot R_s \, q_{Oo}



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m_g = \rho_G \cdot q_{Gg} + \rho_O \cdot R_v \, q_{Gg}



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m_w = \rho_W \cdot q_{Ww}



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m_o = (\rho_O + \rho_G \cdot R_s) \cdot q_{Oo}



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m_g = (\rho_G + \rho_O \cdot R_v) \cdot q_{Gg}



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m_w = \rho_W \cdot q_{Ww}



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m_o = (\rho_O + \rho_G \cdot R_s) \cdot \frac{q_o}{B_o}



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m_g = (\rho_G + \rho_O \cdot R_v) \cdot \frac{q_g}{B_g}



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m_w = \rho_W \cdot \frac{q_w}{B_w}



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\rho_o = \frac{\rho_O + \rho_G \cdot R_s}{B_o}



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m_g = \frac{\rho_G + \rho_O \cdot R_v}{B_g}



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m_w = \frac{\rho_W}{B_w}



Now it's easy to show that The total mass flow of fluid phases is the same as the total mass of fluid componentsall phases:

\dot m = \dot m_o + \dot m_g + \dot m_w = \dot m_O + \dot m_G + \dot m_W
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Here is the breakdown:

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\dot m = \dot m_o + \dot m_g + \dot m_w =  (\rho_O + \rho_G \cdot R_s) \cdot \frac{q_o}{B_o} + (\rho_G + \rho_O \cdot R_v) \cdot \frac{q_g}{B_g} + \rho_W \cdot \frac{q_w}{B_w}

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\dot m = (\rho_O + \rho_G \cdot R_s) \cdot \frac{q_O - R_v \, q_G}{1-R_v \, R_s} + (\rho_G + \rho_O \cdot R_v) \cdot \frac{q_G - R_s \, q_O}{1- R_v \, R_s} + \rho_W \cdot q_W

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\dot m = \frac{ (\rho_O + \rho_G \cdot R_s)\cdot (q_O - R_v \, q_G) +  (\rho_G + \rho_O \cdot R_v) \cdot (q_G - R_s \, q_O) }{1-R_v \, R_s} + \rho_W \cdot \frac{q_w}{B_w}

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\dot m = \dot m_o + \dot m_g + \dot m_w = \dot m_O + \dot m_G + \dot m_W