Book contents
- Frontmatter
- Contents
- Preface
- 1 The Global Perspective on Environmental Transport and Fate
- 2 The Diffusion Equation
- 3 Diffusion Coefficients
- 4 Mass, Heat, and Momentum Transport Analogies
- 5 Turbulent Diffusion
- 6 Reactor Mixing Assumptions
- 7 Computational Mass Transport
- 8 Interfacial Mass Transfer
- 9 Air–Water Mass Transfer in the Field
- APPENDIXES
- References
- Subject Index
- Index to Example Solutions
5 - Turbulent Diffusion
Published online by Cambridge University Press: 05 June 2012
- Frontmatter
- Contents
- Preface
- 1 The Global Perspective on Environmental Transport and Fate
- 2 The Diffusion Equation
- 3 Diffusion Coefficients
- 4 Mass, Heat, and Momentum Transport Analogies
- 5 Turbulent Diffusion
- 6 Reactor Mixing Assumptions
- 7 Computational Mass Transport
- 8 Interfacial Mass Transfer
- 9 Air–Water Mass Transfer in the Field
- APPENDIXES
- References
- Subject Index
- Index to Example Solutions
Summary
Turbulent diffusion is not really diffusion but the mixing of chemicals through turbulent eddies created by convection. Turbulent diffusion is thus a form of convection. Although it has the appearance of diffusion in the end (i.e., random mixing similar to diffusion), the causes of diffusion and turbulent diffusion are very different. Since the end products are similar, diffusion coefficients and turbulent diffusion coefficients are often simply added together. This process will be discussed in this chapter.
Background on Turbulent Flow
It is fairly safe to state that, except for flow through porous media, the environment experiences turbulent flow. The reason that we have not used a river, lake, or the atmosphere as an application in an example in Chapter 2 is that these flows are always turbulent. The example simply would not have been realistic. To emphasize this point, we will consider the constriction of a water or air flow that would be required to have the other option, laminar flow.
An experimentally based rule-of-thumb is that laminar flow often occurs when the pipe Reynolds number, Vd/ν, is less than 2,000, or when an open channel Reynolds number, Vh/ν, is less than 500, where V is the cross-sectional mean velocity, d is the pipe diameter, ν is the kinematic viscosity of the fluid, and h is the channel depth. The diameter or depth that would not be exceeded to have laminar flow by these experimental criteria is given in Table 5.1.
- Type
- Chapter
- Information
- Introduction to Chemical Transport in the Environment , pp. 97 - 120Publisher: Cambridge University PressPrint publication year: 2007