Derivation of the Continuity Equation (Section 9-2, Çengel and Cimbala) We Summarize the Second Derivation in the Text –

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Derivation of the Continuity Equation (Section 9-2, Çengel and Cimbala) We summarize the second derivation in the text – the one that uses a differential control volume. First, we approximate the mass flow rate into or out of each of the six surfaces of the control volume, using Taylor series expansions around the center point, where the velocity components and density are u, v, w, and . For example, at the right face, Ignore terms higher than order dx. The mass flow rate through each face is equal to times the normal component of velocity through the face times the area of the face. We show the mass flow rate through all six faces in the diagram below (Figure 9-5 in the text): Infinitesimal control volume of dimensions dx, dy, dz. Area of right face = dydz. Mass flow rate through the right face of the control volume. Next, we add up all the mass flow rates through all six faces of the control volume in order to generate the general (unsteady, incompressible) continuity equation: all the positive mass flow rates (into CV) all the negative mass flow rates (out of CV) We plug these into the integral conservation of mass equation for our control volume: This term is approximated at the center of the tiny control volume, i.e., The conservation of mass equation (Eq. 9-2) thus becomes Dividing through by the volume of the control volume, dxdydz, yields Finally, we apply the definition of the divergence of a vector, i.e., GGxzGy GGGGG where , , and x ,yz , xyz xyz Letting GV in the above equation, where Vuvw ,, , Eq. 9-8 is re-written as .

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