Dimensionless numbers in fluid mechanics
Dimensionless numbers (or characteristic numbers) have an important role in analyzing the behavior of fluids and their flow as well as in other transport phenomena.[1] They include the Reynolds and the Mach numbers, which describe as ratios the relative magnitude of fluid and physical system characteristics, such as density, viscosity, speed of sound, and flow speed. To compare a real situation (e.g. an aircraft) with a small-scale model it is necessary to keep the important characteristic numbers the same. Names and formulation of these numbers were standardized in ISO 31-12 and in ISO 80000-11.
Diffusive numbers in transport phenomena
vs. | Inertial | Viscous | Thermal | Mass |
---|---|---|---|---|
Inertial | vd | Re | Pe | PeAB |
Viscous | Re−1 | μ/ρ, ν | Pr | Sc |
Thermal | Pe−1 | Pr−1 | α | Le |
Mass | PeAB−1 | Sc−1 | Le−1 | D |
As a general example of how dimensionless numbers arise in fluid mechanics, the classical numbers in transport phenomena of mass, momentum, and energy are principally analyzed by the ratio of effective diffusivities in each transport mechanism. The six dimensionless numbers give the relative strengths of the different phenomena of inertia, viscosity, conductive heat transport, and diffusive mass transport. (In the table, the diagonals give common symbols for the quantities, and the given dimensionless number is the ratio of the left column quantity over top row quantity; e.g. Re = inertial force/viscous force = vd/ν.) These same quantities may alternatively be expressed as ratios of characteristic time, length, or energy scales. Such forms are less commonly used in practice, but can provide insight into particular applications.
Droplet formation
vs. | Momentum | Viscosity | Surface tension | Gravity | Kinetic energy |
---|---|---|---|---|---|
Momentum | ρvd | Re | Fr | ||
Viscosity | Re−1 | ρν, μ | Oh, Ca, La−1 | Ga−1 | |
Surface tension | Oh−1, Ca−1, La | σ | Bo−1 | We−1 | |
Gravity | Fr−1 | Ga | Bo | g | |
Kinetic energy | We | ρv2d |
Droplet formation mostly depends on momentum, viscosity and surface tension.[2] In inkjet printing for example, an ink with a too high Ohnesorge number would not jet properly, and an ink with a too low Ohnesorge number would be jetted with many satellite drops.[3] Not all of the quantity ratios are explicitly named, though each of the unnamed ratios could be expressed as a product of two other named dimensionless numbers.
List
All numbers are dimensionless quantities. See other article for extensive list of dimensionless quantities. Certain dimensionless quantities of some importance to fluid mechanics are given below:
References
- "ISO 80000-1:2009". International Organization for Standardization. Retrieved 2019-09-15.
- Dijksman, J. Frits; Pierik, Anke (2012). "Dynamics of Piezoelectric Print-Heads". In Hutchings, Ian M.; Martin, Graham D. (eds.). Inkjet Technology for Digital Fabrication. John Wiley & Sons. pp. 45–86. doi:10.1002/9781118452943.ch3. ISBN 9780470681985.
- Derby, Brian (2010). "Inkjet Printing of Functional and Structural Materials: Fluid Property Requirements, Feature Stability, and Resolution" (PDF). Annual Review of Materials Research. 40 (1): 395–414. Bibcode:2010AnRMS..40..395D. doi:10.1146/annurev-matsci-070909-104502. ISSN 1531-7331. S2CID 138001742.
- Bhattacharje, Subrata; Grosshandler, William L. (1988). Jacobs, Harold R. (ed.). The formation of wall jet near a high temperature wall under microgravity environment. National Heat Transfer Conference. Vol. 1. Houston, TX: American Society of Mechanical Engineers. pp. 711–716. Bibcode:1988nht.....1..711B.
- "Table of Dimensionless Numbers" (PDF). Retrieved 2009-11-05.
- Mahajan, Milind P.; Tsige, Mesfin; Zhang, Shiyong; Alexander, J. Iwan D.; Taylor, P. L.; Rosenblatt, Charles (10 January 2000). "Collapse Dynamics of Liquid Bridges Investigated by Time-Varying Magnetic Levitation" (PDF). Physical Review Letters. 84 (2): 338–341. Bibcode:2000PhRvL..84..338M. doi:10.1103/PhysRevLett.84.338. PMID 11015905. Archived from the original (PDF) on 5 March 2012.
- "Home". OnePetro. 2015-05-04. Retrieved 2015-05-08.
- Schetz, Joseph A. (1993). Boundary Layer Analysis. Englewood Cliffs, NJ: Prentice-Hall, Inc. pp. 132–134. ISBN 0-13-086885-X.
- "Fanning friction factor". Archived from the original on 2013-12-20. Retrieved 2015-06-25.
- Tan, R. B. H.; Sundar, R. (2001). "On the froth–spray transition at multiple orifices". Chemical Engineering Science. 56 (21–22): 6337. Bibcode:2001ChEnS..56.6337T. doi:10.1016/S0009-2509(01)00247-0.
- Stewart, David (February 2003). "The Evaluation of Wet Gas Metering Technologies for Offshore Applications, Part 1 – Differential Pressure Meters" (PDF). Flow Measurement Guidance Note. Glasgow, UK: National Engineering Laboratory. 40. Archived from the original (PDF) on 17 November 2006.
- Richardson number Archived 2015-03-02 at the Wayback Machine
- Schmidt number Archived 2010-01-24 at the Wayback Machine
- Ekerfors, Lars O. (1985). Boundary lubrication in screw-nut transmissions (PDF) (PhD). Luleå University of Technology. ISSN 0348-8373.
- Petritsch, G.; Mewes, D. (1999). "Experimental investigations of the flow patterns in the hot leg of a pressurized water reactor". Nuclear Engineering and Design. 188: 75–84. doi:10.1016/S0029-5493(99)00005-9.
- Smith, Douglas E.; Babcock, Hazen P.; Chu, Steven (12 March 1999). "Single-Polymer Dynamics in Steady Shear Flow" (PDF). Science. American Association for the Advancement of Science. 283 (5408): 1724–1727. Bibcode:1999Sci...283.1724S. doi:10.1126/science.283.5408.1724. PMID 10073935. Archived from the original (PDF) on 1 November 2006.
- Bookbinder; Engler; Hong; Miller (May 2001). "Comparison of Flow Measure Techniques during Continuous and Pulsatile Flow". 2001 BE Undergraduate Projects. Department of Bioengineering, University of Pennsylvania.
- Tropea, C.; Yarin, A.L.; Foss, J.F. (2007). Springer Handbook of Experimental Fluid Mechanics. Springer-Verlag.