A nuclear explosion can generate a mushroom-shaped thermal plume.

Plume (hydrodynamics)

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## Movement

### Flow and detection

## Types

## Simple plume modeling

## Gaussian plume modelling

## Gallery

## See also

## References

This article uses material from the Wikipedia page available here. It is released under the Creative Commons Attribution-Share-Alike License 3.0.

Plume Hydrodynamics

In hydrodynamics, a **plume** is a column of one fluid moving through another. Several effects control the motion of the fluid, including momentum (inertia), diffusion and buoyancy (density differences). Pure *jets* and pure *plumes* define flows that are driven entirely by momentum and buoyancy effects, respectively. Flows between these two limits are usually described as forced plumes or buoyant jets. "Buoyancy is defined as being positive" when, in the absence of other forces or initial motion, the entering fluid would tend to rise. Situations where the density of the plume fluid is greater than its surroundings (i.e. in still conditions, its natural tendency would be to sink), but the flow has sufficient initial momentum to carry it some distance vertically, are described as being negatively buoyant.^{[1]}

Usually, as a plume moves away from its source, it widens because of entrainment of the surrounding fluid at its edges. Plume shapes can be influenced by flow in the ambient fluid (for example, if local wind blowing in the same direction as the plume results in a co-flowing jet). This usually causes a plume which has initially been 'buoyancy-dominated' to become 'momentum-dominated' (this transition is usually predicted by a dimensionless number called the Richardson number).

A further phenomenon of importance is whether a plume has laminar flow or turbulent flow. Usually there is a transition from laminar to turbulent as the plume moves away from its source. This phenomenon can be clearly seen in the rising column of smoke from a cigarette. When high accuracy is required, computational fluid dynamics (CFD) can be employed to simulate plumes, but the results can be sensitive to the turbulence model chosen. CFD is often undertaken for **rocket plumes**, where condensed phase constituents can be present in addition to gaseous constituents. These types of simulations can become quite complex, including afterburning and thermal radiation, and (for example) ballistic missile launches are often detected by sensing hot rocket plumes. Similarly, spacecraft managers are sometimes concerned with impingement of attitude control system thruster plumes onto sensitive subsystems like solar arrays and star trackers.

Another phenomenon which can also be seen clearly in the flow of smoke from a cigarette is that the leading-edge of the flow, or the starting-plume, is quite often approximately in the shape of a ring-vortex (smoke ring).^{[2]}

Pollutants released to the ground can work their way down into the groundwater, leading to groundwater pollution. The resulting body of polluted water within an aquifer is called a plume, with its migrating edges called plume fronts. Plumes are used to locate, map, and measure water pollution within the aquifer's total body of water, and plume fronts to determine directions and speed of the contamination's spreading in it.^{[3]}

Plumes are of considerable importance in the atmospheric dispersion modelling of air pollution. A classic work on the subject of air pollution plumes is that by Gary Briggs.^{[4]}^{[5]}

A **thermal plume** is one which is generated by gas rising above heat source. The gas rises because thermal expansion makes warm gas less dense than the surrounding cooler gas.

Quite simple modelling will enable many properties of fully developed, turbulent plumes to be investigated.^{[6]}

- It is usually sufficient to assume that the pressure gradient is set by the gradient far from the plume (this approximation is similar to the usual Boussinesq approximation).
- The distribution of density and velocity across the plume are modelled either with simple Gaussian distributions or else are taken as uniform across the plume (the so-called 'top hat' model).
- The rate of entrainment into the plume is proportional to the local velocity.
^{[7]}Though initially thought to be a constant, recent work has shown that the entrainment coefficient varies with the local Richardson number.^{[8]}Typical values for the entrainment coefficient are of about 0.08 for vertical jets and 0.12 for vertical, buoyant plumes whilst for bent-over plumes, the entrainment coefficient is about 0.6. - Conservation equations for mass (including entrainment), and momentum and buoyancy fluxes are sufficient for a complete description of the flow in many cases,
^{[7]}^{[9]}For a simple rising plume these equations predict that the plume will widen at a constant half-angle of about 6 to 15 degrees.

Gaussian plume models can be used in several fluid dynamics scenarios to calculate concentration distribution of solutes such as a smoke stack release or contaminant released in a river. Gaussian distributions are established by Fickian diffusion, and follow a gaussian (bell-shaped) distribution.^{[10]} For calculating the expected concentration of a one dimensional instantaneous point source we consider a mass released at an instantaneous point in time, in a one dimensional domain along . This will give the following equation:^{[11]}

where is the mass released at time and location , and is the diffusivity . This equation makes the following four assumptions:^{[12]}

- The mass is released instantaneously.
- The mass is released in an infinite domain.
- The mass spreads only through diffusion.
- Diffusion does not vary in space.
^{[10]}

Plumes

A nuclear explosion can generate a mushroom-shaped thermal plume.

**^**Turner, J.S. (1979), "Buoyancy effects in fluids", Ch.6, pp.165--&, Cambridge University Press**^**Turner, J. S. (1962).*The Starting Plume in Neutral Surroundings*, J. Fluid Mech. vol 13, pp356-368**^**Fetter, C.W. Jr 1998 Contaminant Hydrogeology**^**Briggs, Gary A. (1975).*Plume Rise Predictions*, Chapter 3 in*Lectures on Air Pollution and Environmental Impact Analysis*, Duanne A. Haugen, editor, Amer. Met. Soc.**^**Beychok, Milton R. (2005).*Fundamentals Of Stack Gas Dispersion*(4th ed.). author-published. ISBN 0-9644588-0-2.**^**Scase, M. M., Caulfield, C. P., Dalziel, S. B. & Hunt, J. C. R. (2006).*Time-dependent plumes and jets with decreasing source strengths*, J. Fluid Mech. vol 563, pp443-461- ^
^{a}^{b}Morton, B. R., Turner, J. S., and Taylor, G.I. (1956),*Turbulent gravitational convection from maintained and instantaneous sources*, P. Roy. Soc. Lond., vol. 234, pp.1--& **^**Kaminski, E. Tait, S. and Carazzo, G. (2005),*Turbulent entrainment in jets with arbitrary buoyancy*, J. Fluid Mech., vol. 526, pp.361--376**^**Woods, A.W. (2010),*Turbulent plumes in nature*, Annu. Rev. Fluid Mech., Vol. 42, pp. 391--412- ^
^{a}^{b}Connolly, Paul. "Gaussian Plume Model".*personalpages.manchester.ac.uk*. Retrieved 2017. **^**Heidi Nepf.*1.061 Transport Processes in the Environment.*Fall 2008. Massachusetts Institute of Technology: MIT OpenCourseWare, https://ocw.mit.edu License: Creative Commons BY-NC-SA.**^**Variano, Evan.*Mass Transport in Environmental Flows*. UC Berkeley.

This article uses material from the Wikipedia page available here. It is released under the Creative Commons Attribution-Share-Alike License 3.0.

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