I discovered an unusual bubble structure which is unexpectedly very stable. To make it, you blow a hemispherical bubble in a pan of soap water using a straw. Then, while still blowing through the straw, withdraw the straw from the bubble. Under the right conditions, a corrugated tube of soap film will form between the straw and the bubble. The tube collapses when you stop blowing. It can be proved that long cylindrical bubbles are unstable without airflow. As far as I know, nobody has studied bubble stability with airflow. It might be possible to publish a short article about this topic.
Proposal: Here bubble_proposal.pdf is the proposal that Sean & Lucas sent to Brett & Duncan, requesting equipment for this project.
Observations so far:
Blowing the bubbles by hand: In order to make the longest tubes, it's necessary to have a large flow rate, enough to cause audible & visible turbulence inside the tube. It is clear that these tubes are robustly stable, since they can oscillate enough during the turbulent phase to produce sound, without breaking! I think I saw transient states with up to 4 nodes or more. When I reduced the airflow after forming the tube, the number of nodes was reduced, and the turbulence went away. This is how I captured the picture with the distinct 2-node structure.
Blowing the bubbles with the comressed air supply: We used much larger tubes, 3/8" to 1/2" ID, compared to the straws I was using initially. It seemed to be harder to get more than 3 nodes (two anti-nodes), until we increased the concentration of detergent, added glycerine, and used distilled water. We also found that using a metal tube for the nozzle is much better than just blowing the bubbles with the end of a hose (which is curved, and the end is cut at an angle). Finally, tuning the airflow is critical. If the flow is too fast, the airflow is turbulent and this bursts the bubble. At low flow rate, trying to draw out the tube in order to produce more antinodes resulted in lateral oscillations of the neck, and the bubble would eventually snap before we could reach the next antinode. With the proper flow rate, it appears to be possible to create tubes of arbitrary length.
Examining the videos shows that the first antinode decreases in diameter when the nozzle is being pulled out to create the longest bubbles. With low flow rate, moving the nozzle slowly closer & farther away causes the first antinode to vanish and re-form with the same shape. It may be important to pull the nozzle away quickly to induce a transition of some kind. Reducing the airflow causes antinodes to have larger diameter (can be much larger than the nozzle), while increased airflow causes the corrugations to flatten, resulting in a tube the same diameter as the nozzle. Reducing the flow also tends to reduce the number of antinodes, indicating that the wavelength of the structure is changing.
Using the fog generator, I observed that with low flow rate and forming one single, large antinode, that the air flowing from the nozzle travels across the bulge as a cylindrical column, initially leaving the outer part of the bulge free of fog for a second or so. The fog eventually reaches the edge as well, and then persists there as the fog pulse ends and clear air flushes in. The patterns in the fog are irregular rather than smooth, so it appears that the airflow is turbulent rather than laminar.
A common feature is the tight neck where the tube enters the base bubble. It would be interesting to see if the diameter of this neck changed with airflow rate. It appears to always be as small or smaller than the straw. At high airflow, it is not much, if any, smaller than the rest of the bubble tube.
It is possible to blow at a tangential angle without popping the bubble; in fact, the bubble tube can execute a 90-degree turn! With a bit of luck, you can also produce a stream that breaks up into bubble 'drops,' just like water streams do.
Pictures & Videos
Blowing bubbles with fog: on the 4th attempt, if you watch closely, you can see the smoke circulating in the vortex as the clear air flushes it out. ian_fog_video
Experimental equipment & techniques:
Here's what we have for equipment:
*A baking sheet for holding the bubble solution
*Dish detergent, glycerine & distilled water
*Some Tygon tubing attatched to the building air supply
*Various size of straight pipes (better than using curved tubing)
*Digital camera (personal)
*Smoke injector! We hacked a fog machine.
*Air flow meter (have 1-10 SCFH meter, need 10-100 to measure full range)
Things we can investigate:
*Surface tension: We may be able to measure surface tension using bubble pressure & our pressure sensor.
*Air flow (liters/second)
*Air flow stream lines (using fog/smoke)
*Pressure inside the straw, or the large bubble at the end
Things we'd eventually like to measure:
*Air speed within the bubble (tricky!)
Peizoelectric sensor, while extremely sensitive, are only effective for measuring pressure fluctuations and not static pressures, due to charge leakage. A better method seems to be measuring the deflection of a thin membrane exposed to a pressure difference. This can be done using capacitance or optically, among many other ways.
Optical method: http://link.aip.org/link/doi/10.1063/1.1143989 -- this may be the easiest. it looks very simple.
More complicated optical method: http://dx.doi.org/10.1364/OL.8.000286 -- has the advantage of compensating for changes in source intensity.
Capacitive method with LC oscillator: http://www.sensata.com/download/ipt_tech-note_1.pdf -- all the capacitive readout methods look tricky
Surface tension measurement: We'd like to measure the surface tension in order to compare the surface pressure to the stagnation pressure of the flow.
Bubble pressure method seems simple and accurate: http://dx.doi.org/10.1119/1.3623414
Internal flow velocity measurements: eventually we will need a way to measure the flow profiles inside the bubble tube. PIV and LDV are probably the two best choices I've seen. These methods require a bit of work, and also a laser. PIV is nice because it gives a 2-D profile and it goes along well with the goal of measuring the tube dimensions. Since it turns out that the fog machine produces a high optical density of fog, it might be too difficult to use PIV. An alternative is Turbulence Imaging Velocimetry, originally developed for smoke, but also being used for plasma physics by some of our colleagues. (Cool, huh?)
Particle image velocimetry: http://tejas.serc.iisc.ernet.in/currsci/jul102000/review%20article.pdf
Laser Doppler velocitimetry: http://link.aip.org/link/doi/10.1119/1.18051?ver=pdfcov
Turublence imaging velocimetry: http://scitation.aip.org/content/aip/journal/rsi/75/10/10.1063/1.1790043
Surface flow measurement:
We could try putting very small particles in the soap solution to help visualize the flow of the film.
Mark Nornberg suggested placing blades with different pitches inside the blowing tube, to induce airflow rotation around the axis of the tube. This could add centrifugal force to the flow, possibly changing the stability or the amplitude of the corrugations.
Equilibrium: the bubbles appear to be surfaces of roughly-constant 'mean curvature.' This means that the pressure inside the bubbles is also approximately constant along the length, according to the Young-Laplace law and force balance. The pressure in the tube must be higher than in the terminating hemispherical bubble, since the larger bubble has lower curvature. This means that there is some pressure drop across the narrow neck where the tube joins the large bubble. It should be possible to create a long bubble tube with no corrugations if the downstream pressure could be increased, so that the narrow neck was unnecessary. There is also evidently very little pressure drop along the cylindrical part of the tube, so an arbitrarily long tube might be possible. It might also be possible to create a very long corrugated tube by lowering the flow rate of a pre-existing cylindrical tube; however, it may be that pressure loss is incurred at every neck, limiting the length of the tube. It is not clear why the flow rate controls the aspect ratio of the corrugations.
Stability: the constant-mean-curvature surfaces (unduloids) are not stable; they tend to 'neck off' into a string of spheres. That is to say, if the narrow part is pushed in a bit, it is no longer in equilibrium, and it continues to move inward until it collapses. If air is flowing through the neck, it must have a higher velocity as the throat decreases in radius, in order to keep the volumetric flow rate constant. But according to Bernoulli's principle, the pressure is lower where the velocity is higher. This implies that the pressure decreases in the neck, which would accelerate the inward motion of the walls! Clearly this is not the whole story. There appears to be a vortex, or flow separation, in the wide part, which means that the airflow is not necessarily any faster in the neck. Thus, the pressure may be constant along the wall from narrow to wide places.
Unduloid: a surface with constant mean curvature; they are solutions to the force balance for the case of constant pressure. They look alot like the bubble tubes we're blowing.
Wikipedia has a nice diagram: http://en.wikipedia.org/wiki/Unduloid
Mathematical formula for the unduloid is here: http://www.emis.de/journals/AM/07-5/mladenov.pdf
Description of stability of various forms including unduloids: http://www.math.ucla.edu/~bertozzi/papers/surfdiff98.pdf
Bubble Stability Without Flow: This is what happens without flow. These papers illustrate different techniques for solving the problem.
Analysis of Instability of a Cylindrical Soap Film of Finite Dimensions.http://dx.doi.org/10.1021/la970595k
Stability of interfaces of revolution with constant surface tension—the case of the catenoid. http://dx.doi.org/10.1016/0300-9467(70)85003-1
Stability and oscillations of a soap film: An analytic treatment. http://dx.doi.org/10.1119/1.12506
Good treatment of variational method for bubbles: http://farside.ph.utexas.edu/teaching/336l/fluidhtml/node51.html
Plateau-Rayleigh Instability: This is why a falling stream of water breaks into droplets. There is some similarity, but in our case the surface is not attached to the flow, and there is drag instead of acceleration due to gravity.
Wikipedia has a nice introduction: http://en.wikipedia.org/wiki/Plateau%E2%80%93Rayleigh_instability
On the breakup of viscous liquid thread. http://dx.doi.org/10.1063/1.868540
Nonlinear dynamics and breakup of free-surface flows. http://dx.doi.org/10.1103/RevModPhys.69.865
Lecture notes on surface tension, ch 5. web.mit.edu/1.63/www/Lec-notes/Surfacetension/Lecture5.pdf
Fluid flow in undulating tubes:
Navier - stokes equation http://en.wikipedia.org/wiki/Navier%E2%80%93Stokes_equations
Theory of vortexes in undulating tubes, with diagrams (Ralph): http://dx.doi.org/10.1115/1.3242656
Image of vortex in undulating tube!!! (Deiber & Schowalter) : http://dx.doi.org/10.1002/aic.690250410
Some theory about flow in undulating tubes, with diagrams of vortexes (Lahbabi & Chang): http://dx.doi.org/10.1016/0009-2509(86)80034-3
Theory of flow in an undulating tube (not so many pretty pictures) (Floryan): http://dx.doi.org/10.1017/S0022112003003987
External-flow-stabilization of long liquid columns
Add your name here if you'd like to become involved with the project:
* Lucas Morton
* Duncan Carlsmith