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1. Writing budget equations in flux form

Physical laws for fluds are often most succinctly expressed in Lagrangian form following parcels, e.g.

DADt=SA\frac{DA}{Dt} = S_A

where AA is any scalar tracer per unit mass of fluid, and SAS_A represents sources or sinks of that tracer. When working with budgets of AA averaged in space and time, it is frequently useful to express the conservation equation in flux form, meaning that a divergence of a flux of AA appears in the equation. Therefore, we need to be comfortable with the transformation to flux form. In this exercise you will work through the transformation in a few different ways.

a. Volumetric flux in height coordinates

In height coordinates (e.g. x,y,zx,y,z) we can define the volumetric flux of scalar AA as ρAv⃗\rho A \vec{v} where ρ\rho is the density of the fluid and v⃗\vec{v} is the three dimensional velocity.

In general for any scalar AA, show that the above conservation equation can be written in terms of this volumetric flux as

∂A∂t+∇⋅(ρAv⃗)=ρSA\frac{\partial A}{\partial t} + \nabla \cdot \left( \rho A \vec{v} \right) = \rho S_A

Hints

Make use of the fact that the conservation of mass (continuity equation) is

DρDt+ρ∇⋅v⃗\frac{D\rho}{Dt} + \rho \nabla \cdot \vec{v}

and the material derivative can be expressed in advective form as

D( )Dt=∂( )∂t+v⃗⋅∇( )\frac{D(~)}{Dt} = \frac{\partial (~)}{\partial t} + \vec{v} \cdot \nabla (~)

You may also find these product rule identites helpful:

D(AB)Dt=ADBDt+BDADt\frac{D (AB)}{Dt} = A \frac{DB}{Dt} + B \frac{DA}{Dt}
∇⋅(v⃗B)=v⃗⋅∇B+B∇⋅v⃗\nabla \cdot (\vec{v} B) = \vec{v} \cdot \nabla B + B \nabla \cdot \vec{v}

which are true for any scalars A,BA, B and vector field v⃗\vec{v}

b. Flux in pressure coordinates

In pressure coordinates we have v⃗=(u,v,ω)\vec{v} = (u,v,\omega) and the conservation of mass takes on a simpler form:

∇⋅v⃗=0\nabla \cdot \vec{v} = 0

In this coordinate system, so that the conservation equation for AA can be simply written as

∂A∂t+∇⋅(v⃗A)=SA\frac{\partial A}{\partial t} + \nabla \cdot \left( \vec{v} A \right) = S_A

where v⃗A\vec{v} A is the flux of AA per unit mass.

2. Angular momentum in cylindrical coordinates

When working with the rotating tank in the lab, it is natural to use cylindrical coordinates. Show that the angular momentum of a fluid in cylindrical coordinates is

M=Ωr2+rvM = \Omega r^2 + rv

where Ω\Omega is the rotation rate of the tank, rr is the radius, and vv is the tangential velocity.

3. Conservation of angular momentum in the cylindrical tank

Derive a conservation equation for the angular momentum, i.e., DMDt\frac{DM}{Dt}. The tangential momentum equation is

DvDt=−1ρr∂p∂θ−uvr−2Ωu+Fθ\frac{Dv}{Dt} = -\frac{1}{\rho r} \frac{\partial p}{\partial \theta} - \frac{uv}{r} - 2 \Omega u + F_\theta

where ρ\rho is the density, pp is the pressure, θ\theta is the azimuthal angle, uu is the radial velocity, FθF_\theta is the friction, and the advective form of the total derivative in cylindrical coordinates is:

DDt=∂∂t+u∂∂r+vr∂∂θ+w∂∂z\frac{D}{Dt} = \frac{\partial}{\partial t} + u\frac{\partial}{\partial r} + \frac{v}{r}\frac{\partial}{\partial \theta} + w\frac{\partial}{\partial z}

Qualitatively describe what the terms represent in the conservation equation for the angular momentum.

4. Angular momentum balance in the tank

Convert the advection term into flux form, using the fact that for an incompressible fluid ∇⋅u=0\nabla \cdot \mathbf{u} = 0. Take the zonal and time average of the conservation equation. Assume a steady state and the divergence of the vertical flux of angular momentum is negligible. Under these set of assumptions what is the balance in the zonal and time mean angular momentum budget?

In words, draw an analogy between this budget in the tank and the angular momentum budget we derived for the atmosphere.