|Reynolds number has been listed as a level-4 vital article in Science. If you can improve it, please do. This article has been rated as B-Class.|
|WikiProject Physics / Fluid Dynamics||(Rated B-class, Mid-importance)|
|WikiProject Chemical and Bio Engineering|
|It is requested that a physics diagram or diagrams be included in this article to improve its quality. Specific illustrations, plots or diagrams can be requested at the Graphic Lab.
For more information, refer to discussion on this page and/or the listing at Wikipedia:Requested images.
- 1 Reynolds Numbers Vary as a function of elevation?
- 2 Typical Reynolds Numbers?
- 3 Inertial force?
- 4 Reynolds number boundaries of flow regimes
- 5 vs.
- 6 Euler number used in Similarity of flows section
- 7 Reynold's / Reynolds number
- 8 Effects of Small Reynolds Number
- 9 L
- 10 Engineers
- 11 Viscosity
- 12 Definition
- 13 Dynamic similitude
- 14 Adimensional vs. Non-dimensional vs. Dimensionless
- 15 Why Doesn't Anyone Do the Corrections?
- 16 D
- 17 Article needs diagram showing effects of varying reynolds
- 18 Example of the importance of the Reynolds number
- 19 remarks - geometry of the system; attached vs separated flows
- 20 Lower limit for vortex street?
- 21 Unilluminating (to me) article
- 22 Mathematical formulæ
Reynolds Numbers Vary as a function of elevation?
What on earth does that mean? Elevation? Altitude? I prefer to see the discussion focus on fundamental attributes of the fluid such as pressure, temperature, density or whatever. Saying that the Reynolds numbers are a function of elevation is just wrong. 220.127.116.11 (talk) —Preceding undated comment added 00:43, 21 January 2010 (UTC).
Typical Reynolds Numbers?
I think this is a good concept for a section, but it's a mess. First, there's no units on any of the figures - I'd add them, but the whole section needs a work-over....
First, how can a blue whale have a Reynolds number? The Reynolds number is the property of fluid flow: not a baseball, mammal, or boat. Second, none of these figures have references, although I am not disputing their veracity.
This section needs a good table (with citations) that lists typical fluid flows that Wikipedia users could relate to (for understanding of the concept - like the flow in a garden hose, the flow in an HVAC duct, etc), maybe combined with fluid flows that are of more encyclopedic value (like the fluid flow in the brain).
Strictly speaking, there is no such thing as an "inertial force." Any object (e.g., a fluid particle) possesses inertia, while it is acted upon by forces. I realize that the definition of a Reynolds number as "a ratio of inertial force to viscous force" is used frequently in both textbooks and peer reviewed literature, but I've always considered it to be sloppy.
Additionally, I would like to point out that neither the quantity μ/L nor the quantity vsρ have units of force, so to list them as forces may be very confusing to the general reader. This will not do for an encyclopedia.
In terms of the equations of motion (e.g., Navier-Stokes equations), if one uses a length scale , a time scale , and a velocity scale , the dimension of the inertial term (i.e., the term which represents the time rate of change of momentum per unit volume) is , while the dimension of the viscous term (i.e., the term represented by the divergence of the viscous stress tensor) is . A Reynolds number is properly the ratio of these terms, . Note that the dimension of the terms in the equations of motion have units of force per unit volume, so that, if multiplied by , they will yield forces. If you must define a Reynolds number as a ratio of forces, then, your "inertial force" should be and your viscous force should be .
--18.104.22.168 04:04, 11 June 2007 (UTC)
- How about "inertial effects to viscous effects"? - EndingPop 12:36, 12 June 2007 (UTC)
- I'm really not sure what the best way to define the Reynolds number is, for an encyclopedia entry. The definition should be comprehensible to the general reader, so defining it in terms of a proper scaling of the equations of motion is probably not a good idea. I'll check some of my old textbooks. I seem to recall that there was a nice description in Bird, Stewart, and Lightfoot's Transport Phenomena. This has been the standard undergraduate textbook for chemical engineers studying transport phenomena for the last 50 years, and hence might not be a bad reference for the article. By the way, the "inertial force" in the note above should be .--22.214.171.124 00:07, 13 June 2007 (UTC)
- Another way to define the Reynolds number is in terms of energies, btw. The kinetic energy per unit volume characteristic of a flow is , and the characteristic scale for viscous dissipation per unit volume is . Hence, the Reynolds number is .--126.96.36.199 00:18, 13 June 2007 (UTC)
- However, the first paragraph says, "a measure of the ratio of inertial forces to viscous forces ", so it is explicitly referring to forces, not energies. Consequently, it SHOULD say the inertial forces are , and the viscous forces 27 January 2010 (UTC) —Preceding unsigned comment added by 188.8.131.52 (talk)
- The Reynolds number is the ratio of advection of momentum (velocity transport) to the diffusion of angular momentum (vorticity transport). From a dimensional analysis standpoint, diffusion coefficients have units of . The "diffusion coefficient" for momentum (i.e., velocity transport) is just . The diffusion coefficient for vorticity is just the kinematic viscosity (see the vorticity page). I would suggest that this definition be used since other non-dimensional numbers are defined in terms of a ratio of advection to diffusion of two properties (e.g., see Prandtl Number, ratio of advection to heat diffusion and Schmidt Number, ratio of momentum to mass diffusion). Hope this helps. --Allen314159 18:58, 21 August 2007 (UTC)
imo, you guys are way to picky; the use of ratio inertial/viscous force is widely used in many different communities. I think what you are missing is that an article like this has to function on 3 or 4 layers: for the general audience, without say HS algebra, the ratio of force idea is intuitive; for the HS/college algebra set, and then for people ready to deal with angular momentum imo, as a phd who has written several articles here, you are making a common mistake, writing only for thetopmost level. nothing wrong with that, but as wiki is a general encyclopedia, really need a general article you might, as a learning exercise, study the article at britannica.com; not saying it is right, but it is at the right *level* i'm not trying to be rude: i know that it is *really* hard to write down correctly — Preceding unsigned comment added by 184.108.40.206 (talk) 19:06, 7 October 2013 (UTC)
Reynolds number boundaries of flow regimes
There seems to be some inconsistency about whether laminar flow ends at 2100 or 2300 in this article, as well as about the upper bound of the unknown regime. The page states that it's 3000, but it should be 4000. From Process Fluid Mechanics by Morton M. Denn, 1980, p 34: "Laminar flow usually ends at Re = 2100; between Re = 2100 and about 4000, the flow seems to pulsate between laminar and turbulent portions. Fully developed turbulence begins at Re of about 4000." My fluid mechanics professor (http://www.cheme.cornell.edu/cheme/people/profile/index.cfm?netid=laa25) also confirms this version of the flow regime divisions. --Icefaerie 03:50, 26 February 2007 (UTC)
- If you go ask your fluid mechanics professor, he/she will likely tell you that this is a rule of thumb. It is not a hard and fast rule. That is likely the source of the different numbers. Perhaps the article should express this? - EndingPop 15:21, 26 February 2007 (UTC)
Definitely a rule of thumb. Laminar flow is definitely expected below a Reynolds number of 2000, but there is a transition zone between 2000 and 4000. In my professional judgment it is safe to treat flows as turbulent at Reynold's numbers greater than 3000 in most cases. One interesting thought to illuminate the uncertainty in where laminar flow ends is that in carefully controlled laboratory settings laminar flow has been achieved at Reynold's numbers as high as 100,000. There is a very interesting article on this in the February 2004 issue of Physics Today. —Preceding unsigned comment added by 220.127.116.11 (talk) 03:41, 5 January 2009 (UTC)
In this field dimensionless numbers such as this are known with two letters, no subscript. The page was changed to add a subscript, and I reverted it. -EndingPop 19:02, 15 October 2006 (UTC)
Euler number used in Similarity of flows section
It's a comment to an excellent page named "Reynolds number" (http://en.wikipedia.org/wiki/Reynolds_number).
Under 'The similarity of flows' subsection, it's stated:
In order for two flows to be similar they must have the same geometry and equal Reynolds numbers. When comparing fluid behaviour at homologous points in a model and a full-scale flow, the following holds:
Re*=Re; p*/(rho* v^2*) = p/(rho v^2) [sorry, I couldn't copy the formula here. p=pressure; rho=density; v=velocity]
The latter equation does not represent the Reynolds number. It is the Euler number Eu=p/(rho v^2), which, along with Re, is one of the major fluid dynamics criteria.
--18.104.22.168 23:20, 24 October 2005 (UTC)
I agree. I quote http://www.engineeringtoolbox.com/euler-number-d_579.html and Euler number (physics). Also I question the relevence of a section on flow similarity in an article about the Reynolds' number which although yes is a requirement of similar flows is not the end of the story for flow analysis by a long way, a new article about Similarity of flow or Flow similarity (etc) should be made about using wind tunnels and aqua tanks in lab experiments to model real flows (eg aerofoil in wind tunnel saving on having to send up a real aircraft). For now I have clarified what is the Re and what is Eu, and made a link to Euler number (physics). Fegor 15:06, 17 March 2006 (UTC)
- There are a whole host of dimensionless numbers that are used in similitude analyses. If you add heat transfer to the list, it'll more than double in size (at least in number that are used often). The important thing is that Re is used almost always, along with whatever other dimensionless number is required. Perhaps it would be better to explain this using just Re and then have a list of commonly used dimensionless numbers with their equations. Eu, Fr, Ma, We, then with heat transfer you also have Pr, Nu, Ra, etc. Anyway, my point is that there are many that are useful in their own areas, but Re is the only one that is used in almost every situation. - EndingPop 17:18, 17 March 2006 (UTC)
Reynold's / Reynolds number
Currently Reynold's number redirects to Reynolds number, whilst Reynolds' number does not exist (note the apostrophes). As a matter of grammer and consistency I think the article should be hosted at Reynolds' number (I do not mean Reynold's number), for precedent look at Bernoulli's principle for when apostrophe should go before the s, and Bayes' theorem or Huygens' principle are examples of when it should go after.Fegor 12:46, 9 March 2006 (UTC)
- This is a valid point, The theory was named after Osborne Reynolds and so is his theory. In english the apostrophe indicating possession comes after the name and so in this case the correct name of the number should be Reynolds' number --Cleverbum 15:49, 5 June 2006 (UTC)
- well it's done now. I added them to the actual artical now. change it back if you feel strongly Fegor 22:45, 25 September 2006 (UTC)
- I googled on it. Theres 161,000 "Reynold's number" and over 20,000,000 "Reynolds number". AFAIK Reynolds is a not an uncommon English name, and the evidence is that it was the guy's name, not Reynold. Also one of the first hits is efunda and wolfram, who are likely to correct, and they both used no apostrophe. So I'm inclined to change it back unless there's a violent objection, and rename the article.WolfKeeper 23:10, 25 September 2006 (UTC)
- you seem to be missing the point. we are not debating about his name (which, yes, is Reynolds), but whether his number Reynolds' number should be have an apostrophe after the s or not have one at all. eFunda is a reputable website but I doubt they are hardly an authority on grammar. Fegor 00:10, 26 September 2006 (UTC)
- With all due respect, you are the one missing the point. What major verifiable source do you have that this is correctly or usually spelled with an apostrophe? Incidentally, I also checked Encyclopedia Britannica, no apostrophe.WolfKeeper 00:29, 26 September 2006 (UTC)
- So yes, I violently object, and yes I've moved it all back. When 100x more hits do it one way, and all the major sources do it the same way, IMHO it's a bit of a clue.WolfKeeper 00:45, 26 September 2006 (UTC)
Effects of Small Reynolds Number
I have heard that (due to the effects of small Reynolds numbers), that flying for flies and other small insects is much more like swimming than flying. Is this a correct analogy? If true, would it be useful to add as an example?
- I've not heard about that, so I can't confirm or deny it. The example I heard about in class is bull semen. -EndingPop 11:41, 8 August 2006 (UTC)
- I've heard this enough times that it may be worth addressing here on talk. Reynolds number is "the ratio of inertial (resistant to change of motion) forces to viscous (heavy and gluey) forces." A large airplane has a large amount of inertia behind it, so the gluey, viscous forces of the air do not have much effect. A model airplane, of the exact same type, shape and configuration, will have drastically different flight characteristics because of it's lower Reynolds number. To the model with lower inertia, the viscosity of the air plays a much bigger role.
- To an insect, the very low Reynolds number means that the insect doesn't have the inertial forces to easily overcome the viscous forces. It has no glide potential, and must constantly provide thrust to keep moving against the viscosity. This also means that the flow across the insect is mostly laminar flow, and the large boundary layer produced gives a very large effective area, as opposed to the actual area of the wing. In this way, a comparison to "swimming" through a heavier fluid seems OK, but inadequate. It's a little more like the resistance you'd feel if you tried to run or flap your arms under water.
- That is where the comparison ends. The compressibility and density of the air are not affected by inertia. (Well, at least not when talking about subsonic flow.) The insect is no more buoyant, and so must maintain lift as well as thrust. In this way, the insect is definitely not swimming, but flying. Zaereth (talk) 19:47, 18 May 2011 (UTC)
Rather than putting that it's equal to 2r for circular sections should it be better to put L= 4A/P (A= area, P = perimeter). Would do it myself but I feel I might mess up. Spanish wiki has it this way. --English - Spanish 14:11, 27 November 2006 (UTC)
- Maybe it makes more sense to have a separate section on common characteristic lengths. This could include a discussion on the hydraulic diameter. - EndingPop 18:58, 27 November 2006 (UTC)
"engineers will avoid any pipe configuration that falls within the range of Reynolds numbers from about 2000 to 3000 to ensure that the flow is either laminar or turbulent." What kind of engineers do this and why? Does this apply to pipes in my house? Richard Giuly 12:28, 9 March 2007 (UTC)
- The only reason I can see for doing this is to allow accurate modelling of flow patterns. It is very difficult (if not impossible) to model the transition phase. Of course, you can define the bounds easily enough - one would be a fully turbulent model, the other fully laminar. So long as it doesn't matter where in that region the flow is, there is no reason to avoid the turbulent region - this will generally be true for home piping, however in situations where the magnitude of the pressure drop or the degree of mixing are important the transition phase may be undesirable. It's not always possible to avoid though - certain process engineering applications have a nasty habit of having Re ~2000-4000. Adacore (talk) 16:23, 30 July 2008 (UTC)
I feel that they are often designed well outside of the transition zone because in this region drastic pressure and flow variations can occur making the system difficult to model and design. Most often a civil engineer will design pipelines in cities and homes. —Preceding unsigned comment added by 22.214.171.124 (talk) 03:49, 5 January 2009 (UTC)
Common values for kinematic viscosity do not belong on this page. That section should be removed. 126.96.36.199 05:42, 30 May 2007 (UTC)
Agreed. I removed the "common values" section. There is already a link to the extensive entry about viscosity.Oanjao 16:10, 31 July 2007 (UTC)
I concur. eta is the symbol used for viscosity in my literature (Biological Physics by Philip Nelson, Physics for scientists and engineers 6th ed. Tipler and Mosca, Physical Biology of the Cell by Rob Phillips et. al as examples), in fact I cannot recall having seen mu used for viscosity before, so I must admit I am a little confused as to why it is used here. Shouldn't convention be followed? Who fixes this? Elvegaro (talk) 10:23, 8 October 2011 (UTC)
- I suggest you look at the Wikipedia article on viscosity. Chemical Engineer (talk) 11:20, 8 October 2011 (UTC)
I'm proposing some changes to the definition section, because I think it would be clearer:
Typically it is given as follows:
The main changes I made are removing the units, and replacing the HTML entities with TeX markup, so that they appear the same in the equation as in the explanation. I removed the units, because it doesn't seem like they belong there. Why, for example, should velocity care if it's in meters per second or feet per second? Does it change the equation any? If anything, we could list the dimensions, but that is also probably not necessary, or could be covered by linking to the page in question (i.e., velocity becomes velocity, then the reader can look at that page to discover the dimensions of velocity).
I'd also like to point out that quantities used in other formulas such as in lift coefficient don't list the units of each term.
- The definition is WRONG. It is a common misapprehension (and common on the Internet) that Re = ratio of inertial to viscous forces, though it may be said to be proportional to this ratio (or to effects, rather than forces). This can be seen by the fact that the critical value of Re is different for a pipe, sphere in fluid and stirred tank. The choice of "characteristic dimension" is to some extent arbitrary. For a pipe the radius or diameter would do, giving a possible factor of 2. In a typical stirred tank, using the diameter of the impeller or the vessel gives a factor of 3. For a rotating object such as the impeller in a stirred tank, or a cylinder viscometer, the rotational speed could logically be in radians per second or revolutions per second, giving a factor of 2 pi. (In some conventions the speed in rpm was used with customary values of density and viscosity.) For various geometric arrangements of fluid moving relative to a body, the Reynolds number is defined as an agreed combination of fluid properties, a characteristic dimension and a velocity. In papers on agitation or using non-Newtonian fluids, the authors are generally careful to say "The Reynolds Number, defined as.....". It is NOT defined as a force ratio.Chemical Engineer (talk) 16:34, 17 March 2008 (UTC)
The Reynolds number is the ratio of advection of momentum (velocity "diffusion") to the diffusion of angular momentum (vorticity "diffusion"). Most dimensionless numbers in fluid mechanics are defined as the ratio of diffusion constants for different quantities (e.g., heat, mass) to either the "diffusion" constants of momentum (specific momentum = velocity) or angular momentum (specific angular momentum = vorticity). From a dimensional analysis standpoint, diffusion coefficients have units of l2 / t. The "diffusion coefficient" for momentum (i.e., velocity transport) is just ul. The diffusion coefficient for vorticity is just the kinematic viscosity (see the vorticity page). I would suggest that this definition be used since other non-dimensional numbers are defined in terms of a ratio of advection to diffusion of two properties (e.g., see Prandtl Number, ratio of advection to heat diffusion and Schmidt Number, ratio of momentum to mass diffusion). This is the academic standard for defining dimensionless numbers in fluid mechanics. Hope this helps. --Allen314159 (talk) 01:09, 12 July 2008 (UTC)
The definition focuses on Reynolds numbers for fluid flows, as does most of the discussion, which is sensible enough. But then the "typical values" section right away mentions Reynolds numbers for solid objects, such as spermatozoa (well, semi-solid) and ocean liners. It would be useful to have a discussion of how the definition (which speaks of fluids flowing) can be extended and applied to solids moving through a fluid; i don't see much in that way. 188.8.131.52 (talk) 15:59, 25 July 2008 (UTC)
The "typical values" section is only utilizing the length scale of the solid objects and the velocities of fluid flow for the calculation of the Reynolds numbers. The Reynolds numbers calculated for these solid objects describe the fluid flow around them and at their length scales (and not the flow of these solid objects within or with the fluid - that would use of different numbers like the Schmidt Number. I still stand by my academic description above. --Allen314159 (talk) 00:08, 1 August 2008 (UTC)
- This is all very great if you happen to be a mathamatician, but can we get a definition here that is better translated into common language. My understanding of Reynold's Number is that it is a dimensionless number, whose parmeters are defined by the ratio of dynamic pressure to shearing stress. (eg: At what scale does viscosity overcome shear, or visa-versa.) Is this correct? Zaereth (talk) 17:20, 2 October 2008 (UTC)
- The math I find to define Re is:
- Re = (ρ u2) / (μ u / L)
- = ρ u L / μ
- = u L / ν (1)
- Re = Reynolds Number (non-dimensional)
- ρ = density (kg/m3, lbm/ft3 )
- u = velocity (m/s, ft/s)
- μ = dynamic viscosity (Ns/m2, lbm/s ft)
- L = characteristic length (m, ft)
- ν = kinematic viscosity (m2/s, ft2/s)
- But since I am no mathamatician, I still think a good English definition is neededZaereth (talk) 18:09, 2 October 2008 (UTC)
- I think this is a good idea - it should not be defined in terms of flow in a pipe, a very specific (if the original) application. Mirams (talk) 15:46, 4 June 2009 (UTC)
- Thanks for the response. Reynold's number is a rather important topic when explaining aerodynamic fluid flows, such as the boundary layer of air that surrounds an aircraft wing, which actually alters the shape of the wing, making lift possible. (ie: Too much angle of attack will shear the boundary layer away, and the plane will areodynamically stall.) This effect at a much smaller scale helps explain why a bumble bee can fly, but at a scale any larger it would not be able to, or how an ant can become stuck like glue in a single drop of water.
- I think the first thing that could use a little "dumbing down for the rest of us" would be the opening paragraph, which is confusing to me. To quote, "In fluid mechanics and heat transfer, the Reynolds number Re is a dimensionless number that gives a measure of the ratio of inertial forces () to viscous forces (μ / L) and, consequently, it quantifies the relative importance of these two types of forces for given flow conditions." Any ideas on how to translate this into something that is a little more understandable to the masses? Zaereth (talk) 18:42, 4 June 2009 (UTC)
- expert needed. From above: "When two geometrically similar flow patterns...have the same values [=THE CAUSE]...they...have similar flow geometry. [=THE EFFECT]" -- Isn't this saying geometrically-similar things may have similar geometry? (like furry bears may have fur) Is "similar flow" part of the cause, or the effect? 10/27/07
- Assuming this refers to similitude, I think the intent of the statement (perhaps it needs rewording) is to say that flows with similar geometry (but different in other ways) have similar flow characteristics if you match Re. Is that the section you're referring to, because I can't find the part you quoted. - EndingPop (talk) 12:52, 10 September 2008 (UTC)
Adimensional vs. Non-dimensional vs. Dimensionless
To the best of my knowledge adimensional is not a word. I have never seen it used in any fluid texts. The correct formation is either the compound non-dimensional or the short-form nondimensional. Bradweir (talk) 21:05, 29 June 2009 (UTC)
- I believe adimensional is the Spanish word for non-dimensional. see Spanish Wikipedia. It is not in the Oxford English Dictionary.Chemical Engineer (talk) 21:53, 29 June 2009 (UTC)
- Wouldn't it be better to just use the correct term: "Dimensionless"? And what is with that funky character for density? That's not a rho, can we switch it back please?184.108.40.206 (talk) 04:33, 8 August 2009 (UTC)
Why Doesn't Anyone Do the Corrections?
There are several errors in the article. People have pointed them out. Why don't they make the changes? Clearly the first line has "Forces" stated when both inertial and viscous "forces" have the wrong units. There are other issues also. Someone needs to fix these. I teach classes that deal somewhat with this area and my students were finding this article more confusion than helpful. —Preceding unsigned comment added by 220.127.116.11 (talk) 17:07, 11 October 2009 (UTC)
- If you teach classes you should be in a position to help. Wikipedia is a collaborative effort. Why not register and see how you can help to improve it. However, please note that the articles should not come from personal knowledge (however good) but from cited sources. The "ratio of forces" description is a perennial argument with several sides. However, note that an encyclopedia is not really the place for a rigorous intellectual dissection of theoretical concepts but a short and (intended to be) helpful brief explanation of facts. Many of us have day jobs and thus not enough time to do all we would like. Your input would be most welcome, please bring your textbooks! Chemical Engineer (talk) 17:48, 11 October 2009 (UTC)
- And I do some work in fluid dynamics and we use the terms "force" quite loosely (e.g., in the Navier-Stokes equations we use "force" even after converting everything to accelerations). And since it is a nondimensional number, the top and bottom have different units depending on how the variables are arranged. I second Chemical Engineer - it is ironic to ask why people don't make changes that they point out and then point out an error without changing it - if it is that much of a problem to your students, by all means, contribute on the article page! Awickert (talk) 18:00, 11 October 2009 (UTC)
The value "D" in the section regarding the Reynolds number of flow through a pipe is ambiguous. Does that D reference the diameter of the pipe or the length of the pipe. There is no further clarification in the rest of the article. —Preceding unsigned comment added by Adroa (talk • contribs) 02:02, 14 October 2009 (UTC)
The effect of pipe length is very different from that of the diameter, and for pipes the diameter must be chosen for Re, not the length. Even (above a certain length) the pipe length doesn't matter at the same flow speed. I think that the article does mention that the diameter is chosen; however, it is not made clear why... Harald88 (talk) 08:44, 26 January 2010 (UTC)
Article needs diagram showing effects of varying reynolds
We need a diagram of, for example, the flow around a sphere at different reynolds, going from laminar to vortex street. I think it really helps cement the concept in intuitively.-13:43, 15 February 2010 (UTC)
Example of the importance of the Reynolds number
If for example the scale model has linear dimensions one quarter of full size, the flow velocity of the model would have to be multiplied by a factor of 4 to obtain similar flow behavior.
This is obviously wrong. A 1/10th scale model of a Piper Cub will not be tested with a wind speed approaching Mach 3. As models scale down, wind speed also scales down (but in a non-linear fashion, I think). It is true however that the Reynold's Number is used to figure out exactly what the speed is. —Preceding unsigned comment added by 18.104.22.168 (talk) 15:30, 23 March 2010 (UTC)
remarks - geometry of the system; attached vs separated flows
The section about typical values of Reynolds number must state that those values depend on the geometry of the system/flow. For instance a flow in a pipe stays laminar longer than a flow around a cylinder. Typical values of Reynolds may hint at the fact that transition from laminar -> turbulent hides varied types of flows, in particular attached laminar steady flow -> separated laminar steady -> laminar separated periodic -> transitional periodic -> turbulent (chaotic) This should be explained in the page on flow separation which is quite poor, and could be enhanced by diagram in page 3 of this document: http://www.stanford.edu/class/me469b/handouts/turbulence.pdf — Preceding unsigned comment added by 22.214.171.124 (talk) 13:16, 1 August 2012 (UTC)
- You probably understand the subject better than I, (I only know Reynolds as far as it applies to aircraft), you are most welcome to make the changes that would improve this article. Just remember to cite a source for your information, so others can verify it, and try to put it in your own words, to avoid plagiarism. Diagrams are always helpful, but you may have to get permission from the owner, or just make your own to avoid copyright problems. Thanks for your comments, and any assistance you can provide. Zaereth (talk) 16:22, 1 August 2012 (UTC)
- On a side note, (which is somewhat related to your comment), one thing I do find interesting is that Reynolds number is often described as "the relationship between pressure and shear forces, yet the word "shear" is never used in this article. Here is one source describing it in those terms. Zaereth (talk) 22:24, 1 August 2012 (UTC)
Lower limit for vortex street?
- Most sources I've seen agree with Re 49 to be the lower limit. However, I think the book Hydrodynamics Around Cylindrical Structures provides one of the best explanations. Between Re 0 and 5, the flow will be laminar. Between Re 5 and 40, there are a fixed pair of vortices, with laminar flow around them. Between Re 40 and 200, the laminar flow forms a vortex street. Between Re 200 and 300, the wake becomes turbulent. Between re 300 and 30,000 (subcritical range), the boundary layer begins to separate, and the wake is completely turbulent. Between 30,000 and 35,000 (critical range), the boundary layer becomes turbulent as it separates, but the boundary layer itself is laminar. Between Re 35,000 and 150,000 (supercritical range), the boundary layer becomes partially laminar and partially turbulnet. Between Re 150,000 and 400,000, the boundary layer is completely turbulent on only one side, but, at Re higher than 400,000 (transcritical), and the boundary layerlayer will be completely turbulent on both sides. Zaereth (talk) 21:17, 13 August 2012 (UTC)
Unilluminating (to me) article
I want to say in some sort of constructive fashion (seriously) that this is one of the least helpful articles I have ever consulted in Wikipedia. Maybe the problem is with me, but the article did almost exactly nothing to help me find out "What is a Reynolds number?"
Instead of getting an answer to that question, I found out at the very beginning of the article that "Reynolds number (Re) is a dimensionless number that gives a measure of the ratio of inertial forces to viscous forces." This was encouraging, but it was followed by a sort of disclaimer: "The term inertial forces, which characterize how much a particular fluid resists any change in motion, are not to be confused with inertial forces defined in the classical way."
Because I could not comprehend what the second sentence was telling me not to confuse, the two effectively cancelled out, leaving me with honestly no idea what Reynolds number refers to. Dratman (talk) 22:54, 24 February 2013 (UTC)
u r right
dratman, you are 100% right, this intro is typcial of many technical articles in wiki, the authors have no sense of how to write for a general audience. I think a good intro would be something like: The reynolds numbers describe the behaviour of a fluid (gas or liquid) in terms of how "smooth" the flow is. The fluid flow we are all familiar with - say water coming out of a nozzle - is high Re, and such flow is characterized as unpredictable; a small change in the nozzle causes a big change in teh stream. Fluid flow at low Re is not a common sight; we can say such flow is predictable. In general, low Re occurs at microscopic scales. WE can connect these ideas by thinking of the liquid folding... well, that isn't very good, but it is better then what is there !! — Preceding unsigned comment added by 126.96.36.199 (talk) 18:48, 7 October 2013 (UTC)
- I agree that this article could use a lede and introduction with a simplified approach. In general, I would start by saying that "Reynolds number ia a ratio that defines the turbulence of a fluid in motion. This turbulence is often referred to as "eddy currents" and is caused by fluctuations in the flow. These eddy currents occur at many different size scales, which are determined by the Reynolds number. At low Reynolds number, the eddies are very small and the flow is mostly laminar, causing the fluid to shear cleanly past non-moving fluids or surfaces. At high Reynolds number, the eddies become larger and the flow becomes more tubulent than laminar, rolling and spinning past other fluids or surfaces..." or something like that. Zaereth (talk) 02:10, 10 October 2013 (UTC)
- Unfortunately, it's not as simple as that, the general shape and surface of the object that the flow is going past is also very important; you can get both smooth flow or turbulent behaviour over a wide range of reynolds numbers, just by changing tiny details of the object. Also, mainly at high Reynolds number, some of the eddies are very, very small. Fluid flow is, in general, chaotic. So there's a big danger here of oversimplifying things.GliderMaven (talk) 20:49, 10 October 2013 (UTC)
- I understand what you're saying, but you can't put that all in the first sentence. A good many readers are only going to read that first sentence, so it should give the most basic of definitions that can generally encompass the entire article. These people probably ran across the term in some other article, and just want to get the gist-of-it in the fewest amount of words possible. Then it should expand on that definition within just a few paragraphs, touching on many of the finer point as you've just mentioned. (I was only trrying to offer a starting point, that people could build on.) Zaereth (talk) 21:32, 10 October 2013 (UTC)
- (On a side note: Personally, for me, its often easiest to visualize some of these concepts by using analogies between hydraulics and electronics. In the case of Reynolds number, an analogy can be made between Re and the combination of inductance and resistance in electrical flow, which leads to the concept of magnetic Reynolds number.) Zaereth (talk) 22:06, 10 October 2013 (UTC)
- On problem I see with the approach this article takes is that it deals too much with Reynolds number in relation to solid surfaces. While important, it tends to ignore Re with respect to fluid-on-fluid flows. I doesn't describe in great detail the relation between Re and boundary layer, nor does it describe how Re is used in the study of cloud formations and meteorology, plate tectonics, plasma physics, ocean currents, or astrophysics, etc... Zaereth (talk) 14:40, 11 October 2013 (UTC)
The typesetting of formulæ in this article at present is haphazard, being neither internally consistent, nor consistent with standard recommendations.". —DIV (188.8.131.52 (talk) 07:03, 21 August 2015 (UTC))
- This is the domain of WP:MOSMATH, not of anything external. If you see specific problems which, after referencing MOSMATH, you think you can fix, then you should do so. If, after referencing MOSMATH, you identify no issues with this article regards MOSMATH, you should seek change at WT:MOSMATH, not here. --Izno (talk) 16:04, 21 August 2015 (UTC)
- Mills, I. M.; Metanomski, W. V. (December 1999), On the use of italic and roman fonts for symbols in scientific text (PDF), IUPAC Interdivisional Committee on Nomenclature and Symbols, retrieved 9 November 2012. This document was slightly revised in 2007 and full text included in the Guidelines For Drafting IUPAC Technical Reports And Recommendations and also in the 3rd edition of the IUPAC Green Book.
- See also Typefaces for Symbols in Scientific Manuscripts, NIST, January 1998. This cites the family of ISO standards 31-0:1992 to 31-13:1992.
- "More on Printing and Using Symbols and Numbers in Scientific and Technical Documents". Chapter 10 of NIST Special Publication 811 (SP 811): Guide for the Use of the International System of Units (SI). 2008 Edition, by Ambler Thompson and Barry N. Taylor. National Institute of Standards and Technology, Gaithersburg, MD, U.S.A.. March 2008. 76 pages. This cites the ISO standards 31-0:1992 and 31-11:1992, but notes "Currently ISO 31 is being revised [...]. The revised joint standards ISO/IEC 80000-1—ISO/IEC 80000-15 will supersede ISO 31-0:1992—ISO 31-13.".