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Basics of Fluid Mechanics, 2014a

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8.2. MASS CONSERVATION 229<br />

The first term in equation (8.3) for the infinitesimal volume is expressed, neglecting<br />

higher order derivatives, as<br />

∫<br />

V<br />

dρ dρ<br />

dV =<br />

dt dt<br />

dV<br />

{ }} {<br />

dx dy dz +<br />

The second term in the LHS <strong>of</strong> equation (8.2) is expressed 2 as<br />

∼0<br />

{ ( }} {<br />

d 2 )<br />

ρ<br />

f<br />

dt 2 + ··· (8.4)<br />

∫<br />

A<br />

U rn ρdA=<br />

dA xz<br />

{ }} {<br />

dx dz<br />

dA yz<br />

{ }} {<br />

dy dz [ (ρU x )| x<br />

− (ρU x )| x+dx<br />

]<br />

+<br />

dA xz<br />

] { }} {<br />

[(ρU y )| y<br />

− (ρU y )| y+dy<br />

+ dx dy [ ]<br />

(ρU z )| z<br />

− (ρU z )| z+dz<br />

(8.5)<br />

The difference between point x and x + dx can be obtained by developing Taylor series<br />

as<br />

(ρU x )| x+dx<br />

=(ρU x )| x<br />

+ ∂ (ρU x)<br />

∂x ∣ dx (8.6)<br />

x<br />

The same can be said for the y and z coordinates. It also can be noticed that, for<br />

example, the operation, in the x coordinate, produces additional dx thus a infinitesimal<br />

volume element dV is obtained for all directions. The combination can be divided by<br />

dx dy dz and simplified by using the definition <strong>of</strong> the partial derivative in the regular<br />

process to be<br />

∫<br />

[ ∂(ρUx )<br />

U rn ρdA= − + ∂(ρU y)<br />

+ ∂(ρU ]<br />

z)<br />

(8.7)<br />

∂x ∂y ∂z<br />

A<br />

Combining the first term with the second term results in the continuity equation<br />

in Cartesian coordinates as<br />

Continuity in Cartesian Coordinates<br />

∂ρ<br />

∂t + ∂ρU x<br />

∂x<br />

+ ∂ρU y<br />

+ ∂ρU z<br />

=0<br />

∂y ∂z<br />

(8.8)<br />

Cylindrical Coordinates<br />

The same equation can be derived in cylindrical coordinates.<br />

change, as depicted in Figure 8.2, in the control volume is<br />

The net mass<br />

2 Note that sometime the notation dA yz also refers to dA x .<br />

d ṁ = ∂ρ<br />

dv<br />

{ }} {<br />

dr dz r dθ (8.9)<br />

∂t

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