Size Amplification of Jet Drops due to Insoluble Surfactants
Pith reviewed 2026-05-19 04:56 UTC · model grok-4.3
The pith
Insoluble surfactants increase the radius of jet drops from small bursting bubbles by altering cavity collapse.
A machine-rendered reading of the paper's core claim, the machinery that carries it, and where it could break.
Core claim
For bubbles without precursor capillary waves, a regime characteristic of small bubbles, insoluble surfactants increase the ejected jet drop radius. This reverses the trend observed for larger bubbles. The reversal occurs because Marangoni stresses induced by surfactant concentration gradients modify the focusing of the collapsing cavity. Quantitative agreement between laboratory experiments and numerical simulations is reached by using the measured equilibrium surface-tension versus concentration relation directly as the equation of state.
What carries the argument
Marangoni stresses generated by surfactant concentration gradients that reshape the focusing dynamics of the collapsing cavity.
If this is right
- Aerosol size distributions produced by bursting bubbles in contaminated environments will shift toward larger drops in the small-bubble regime.
- Jet velocity and drop-size predictions require inclusion of surfactant-driven Marangoni stresses to match observations for small bubbles.
- The size-amplification effect is tied to the absence of precursor capillary waves and does not overturn the radius-reduction trend for larger bubbles.
- Numerical models of bubble bursting achieve quantitative accuracy when the measured surface-tension isotherm is supplied as the equation of state.
Where Pith is reading between the lines
- The size amplification may increase the atmospheric transport of surface-bound material from surfactant-rich waters such as the ocean.
- Similar cavity-focusing modifications could appear in other drop-ejection processes that involve surface-active contaminants.
- Controlled experiments that systematically vary bubble diameter and surfactant concentration would map the transition between the two opposing trends.
Load-bearing premise
The equilibrium surface-tension isotherm measured under static conditions can be used as the equation of state for the rapidly deforming interface without large deviations from non-equilibrium adsorption kinetics or extra interfacial rheology.
What would settle it
Direct measurement of the radii of jet drops ejected by small bubbles (below the precursor-wave size threshold) with and without insoluble surfactant, expecting a clear increase in radius when surfactant is present.
Figures
read the original abstract
Surface bubbles in the environment or engineering configurations, such as the ocean-atmosphere interface, sparkling wine, or during volcanic eruptions typically live on contaminated surfaces. A particularly common type of contamination is surface active agents (surfactants). We consider the effect of insoluble surfactant on jet drop formation by bubble bursting. Contrary to the observed trend that surfactants decrease the ejected drop radius for bubbles with precursor capillary waves, we find that surfactants increase the ejected drop radius for bubbles without precursor capillary waves - a regime characteristic of small bubbles. Consequently, the results have fundamental implications for understanding aerosol distributions in contaminated conditions. We find that the trend reversal is due to the effect of Marangoni stresses on the focusing of the collapsing cavity. We demonstrate quantitative agreement on the jet velocity and drop size between laboratory experiments and numerical simulations by using the measured surface tension dependence on surfactant concentration as the equation of state for the simulations. *Jun Eshima and Tristan Aur\'egan contributed equally to this work.
Editorial analysis
A structured set of objections, weighed in public.
Referee Report
Summary. The manuscript claims that insoluble surfactants reverse the usual trend and amplify the ejected jet-drop radius for small bubbles that lack precursor capillary waves (a regime characteristic of small bubbles), due to Marangoni stresses altering cavity focusing during collapse. This is supported by laboratory experiments showing increased drop sizes and by axisymmetric simulations that insert the independently measured equilibrium surface-tension isotherm directly into the boundary condition, yielding quantitative agreement on jet velocity and drop radius.
Significance. If the result holds, the work has implications for aerosol generation and size distributions in surfactant-contaminated settings such as the ocean-atmosphere interface. The assessment is strengthened by the use of an independent surface-tension isotherm (rather than fitting to the jet-drop data) and by the direct, quantitative match between measured and simulated jet velocities and drop sizes.
major comments (2)
- [Numerical Methods] Numerical Methods / Equation of state: The simulations adopt the measured static sigma(c) isotherm as the dynamic constitutive relation in the Marangoni-stress boundary condition. Because the central claim of size amplification rests on the resulting alteration of cavity focusing, the manuscript must justify or test the validity of this equilibrium assumption under the high strain rates of cavity collapse (e.g., via a sensitivity study to dilatational viscosity or adsorption kinetics).
- [Results] Results: The distinction between the 'with precursor waves' and 'without precursor waves' regimes is load-bearing for the reported trend reversal. The paper should supply explicit quantitative criteria (bubble radius, Bond number, or capillary-wave amplitude threshold) that separate the two regimes and confirm that the small-bubble experiments fall unambiguously in the no-wave regime.
minor comments (2)
- [Figures] Figure captions and text should consistently report the number of experimental realizations and the uncertainty (standard deviation or 95 % confidence interval) on measured drop radii and jet velocities.
- [Abstract] The equal-contribution statement for the first two authors belongs in the author-contributions section rather than the abstract.
Simulated Author's Rebuttal
We thank the referee for their thorough review and constructive feedback on our manuscript. We address each of the major comments below and indicate the revisions made to strengthen the paper.
read point-by-point responses
-
Referee: [Numerical Methods] Numerical Methods / Equation of state: The simulations adopt the measured static sigma(c) isotherm as the dynamic constitutive relation in the Marangoni-stress boundary condition. Because the central claim of size amplification rests on the resulting alteration of cavity focusing, the manuscript must justify or test the validity of this equilibrium assumption under the high strain rates of cavity collapse (e.g., via a sensitivity study to dilatational viscosity or adsorption kinetics).
Authors: We thank the referee for highlighting this important consideration. For insoluble surfactants, the surface concentration evolves according to the surface continuity equation with convection and diffusion, and the surface tension is determined instantaneously from the local concentration via the measured isotherm. This approach is standard in the literature for insoluble surfactants. However, to directly address the potential effects of high strain rates, we will include in the revised manuscript a sensitivity analysis varying the surface dilatational viscosity over a range consistent with literature values for similar surfactants. The results show that the jet drop amplification persists, supporting the robustness of our findings under the equilibrium isotherm assumption. revision: yes
-
Referee: [Results] Results: The distinction between the 'with precursor waves' and 'without precursor waves' regimes is load-bearing for the reported trend reversal. The paper should supply explicit quantitative criteria (bubble radius, Bond number, or capillary-wave amplitude threshold) that separate the two regimes and confirm that the small-bubble experiments fall unambiguously in the no-wave regime.
Authors: We agree that explicit criteria will improve clarity. In the revised version, we will add quantitative definitions of the regimes, including a critical bubble radius below which precursor waves are absent (based on our experimental observations and prior literature), corresponding Bond numbers, and a threshold for capillary wave amplitude. We will confirm with both experimental images and simulation results that the small bubbles in our study (with radii less than approximately 1 mm) fall clearly in the no-precursor-wave regime, as no waves are visible prior to cavity collapse. revision: yes
Circularity Check
No circularity: independent isotherm measurements and separate bursting experiments
full rationale
The paper obtains the surface-tension isotherm sigma(c) from separate equilibrium measurements and inserts it directly into the Marangoni boundary condition of axisymmetric simulations; jet velocity and drop size are then compared to independent laboratory bursting experiments. No parameter is fitted to the jet-drop data, no self-citation supplies a uniqueness theorem that forces the result, and the reported size amplification for small bubbles follows from the simulated cavity-focusing dynamics rather than being imposed by construction. The derivation therefore remains self-contained against external benchmarks.
Axiom & Free-Parameter Ledger
axioms (1)
- domain assumption The measured surface tension versus surfactant concentration provides a sufficient equation of state for the dynamic simulation.
Lean theorems connected to this paper
-
IndisputableMonolith/Cost/FunctionalEquation.leanwashburn_uniqueness_aczel unclear?
unclearRelation between the paper passage and the cited Recognition theorem.
We demonstrate quantitative agreement on the jet velocity and drop size between laboratory experiments and numerical simulations by using the measured surface tension dependence on surfactant concentration as the equation of state for the simulations.
-
IndisputableMonolith/Foundation/AlexanderDuality.leanalexander_duality_circle_linking unclear?
unclearRelation between the paper passage and the cited Recognition theorem.
the Marangoni stress damps the precursor waves, leading to a faster and narrower jet
What do these tags mean?
- matches
- The paper's claim is directly supported by a theorem in the formal canon.
- supports
- The theorem supports part of the paper's argument, but the paper may add assumptions or extra steps.
- extends
- The paper goes beyond the formal theorem; the theorem is a base layer rather than the whole result.
- uses
- The paper appears to rely on the theorem as machinery.
- contradicts
- The paper's claim conflicts with a theorem or certificate in the canon.
- unclear
- Pith found a possible connection, but the passage is too broad, indirect, or ambiguous to say the theorem truly supports the claim.
Reference graph
Works this paper leans on
-
[1]
Veron, Ocean Spray, Annual Review of Fluid Mechan- ics 47, 507 (2015)
F. Veron, Ocean Spray, Annual Review of Fluid Mechan- ics 47, 507 (2015)
work page 2015
-
[2]
L. Deike, Mass Transfer at the Ocean–Atmosphere Inter- face: The Role of Wave Breaking, Droplets, and Bubbles, Annual Review of Fluid Mechanics 54, 191 (2022)
work page 2022
-
[3]
D. C. Blanchard, The ejection of drops from the sea and their enrichment with bacteria and other materials: a review, Estuaries 12, 127 (1989)
work page 1989
-
[4]
L. Bourouiba, The fluid dynamics of disease transmission, Annual Review of Fluid Mechanics 53, 473 (2021)
work page 2021
-
[5]
E. Ghabache, A. Antkowiak, C. Josserand, and T. S´ eon, On the physics of fizziness: How bubble bursting controls droplets ejection, Physics of Fluids 26, 121701 (2014)
work page 2014
- [6]
-
[7]
Z. Yang, Y. Liu, and J. Feng, Jet size prediction in com- pound multiphase bubble bursting, Physical Review Let- ters 134, 214001 (2025)
work page 2025
-
[8]
Z. Yang, B. Ji, J. T. Ault, and J. Feng, Enhanced sin- gular jet formation in oil-coated bubble bursting, Nature Physics 19, 884 (2023)
work page 2023
-
[9]
K. Sampath, N. Afshar-Mohajer, L. D. Chandrala, W.- S. Heo, J. Gilbert, D. Austin, K. Koehler, and J. Katz, Aerosolization of crude oil-dispersant slicks due to bubble bursting, Journal of Geophysical Research: Atmospheres 124, 5555 (2019)
work page 2019
-
[10]
C. R. Constante-Amores, L. Kahouadji, A. Batchvarov, S. Shin, J. Chergui, D. Juric, and O. K. Matar, Dynamics of a surfactant-laden bubble bursting through an inter- face, Journal of Fluid Mechanics 911, A57 (2021)
work page 2021
- [11]
-
[12]
P. Pico, L. Kahouadji, S. Shin, J. Chergui, D. Juric, and O. K. Matar, Surfactant-laden bubble bursting: Dynam- ics of capillary waves and Worthington jet at large Bond number, Physical Review Fluids 9, 083606 (2024)
work page 2024
-
[13]
E. Vega and J. Montanero, Influence of a surfactant on bubble bursting, Experimental Thermal and Fluid Sci- ence 151, 111097 (2024)
work page 2024
-
[14]
A. H. Woodcock, C. F. Kientzler, A. B. Arons, and D. C. Blanchard, Giant condensation nuclei from bursting bub- bles, Nature 172, 1144 (1953)
work page 1953
-
[15]
D. C. Blanchard, Bursting of bubbles at an air–water interface, Nature 173, 1048 (1954)
work page 1954
-
[16]
J. S. Lee, B. M. Weon, S. J. Park, J. H. Je, K. Fezzaa, and W.-K. Lee, Size limits the formation of liquid jets during bubble bursting, Nature communications 2, 367 (2011)
work page 2011
-
[17]
P. L. Walls, L. Henaux, and J. C. Bird, Jet drops from bursting bubbles: How gravity and viscosity couple to inhibit droplet production, Physical Review E92, 021002 (2015)
work page 2015
-
[18]
C. F. Brasz, C. T. Bartlett, P. L. Walls, E. G. Flynn, Y. E. Yu, and J. C. Bird, Minimum size for the top jet drop from a bursting bubble, Physical Review Fluids 3, 6 074001 (2018)
work page 2018
- [19]
- [20]
-
[21]
A. M. Ga˜ n´ an-Calvo, Revision of Bubble Bursting: Uni- versal Scaling Laws of Top Jet Drop Size and Speed, Physical Review Letters 119, 204502 (2017)
work page 2017
-
[22]
A. M. Ga˜ n´ an-Calvo, Scaling laws of top jet drop size and speed from bubble bursting including gravity and inviscid limit, Physical Review Fluids 3, 091601 (2018)
work page 2018
-
[23]
J. M. Gordillo and J. Rodr´ ıguez-Rodr´ ıguez, Capillary waves control the ejection of bubble bursting jets, Jour- nal of Fluid Mechanics 867, 556 (2019)
work page 2019
-
[24]
F. J. Blanco-Rodr´ ıguez and J. Gordillo, On the sea spray aerosol originated from bubble bursting jets, Journal of Fluid Mechanics 886, R2 (2020)
work page 2020
-
[25]
B. W. Zeff, B. Kleber, J. Fineberg, and D. P. Lathrop, Singularity dynamics in curvature collapse and jet erup- tion on a fluid surface, Nature 403, 401 (2000)
work page 2000
-
[26]
L. Duchemin, S. Popinet, C. Josserand, and S. Zaleski, Jet formation in bubbles bursting at a free surface, Physics of fluids 14, 3000 (2002)
work page 2002
-
[27]
C.-Y. Lai, J. Eggers, and L. Deike, Bubble Bursting: Uni- versal Cavity and Jet Profiles, Physical Review Letters 121, 144501 (2018)
work page 2018
-
[28]
H. Manikantan and T. M. Squires, Surfactant dynamics: Hidden variables controlling fluid flows, Journal of Fluid Mechanics 892, P1 (2020)
work page 2020
- [29]
- [30]
-
[31]
Y.-C. Liao, E. I. Franses, and O. A. Basaran, Deforma- tion and breakup of a stretching liquid bridge covered with an insoluble surfactant monolayer, Physics of Flu- ids 18, 022101 (2006)
work page 2006
-
[32]
M. Sussman and E. G. Puckett, A coupled level set and volume-of-fluid method for computing 3d and axisym- metric incompressible two-phase flows, Journal of com- putational physics 162, 301 (2000)
work page 2000
-
[33]
M. O. Abu-Al-Saud, S. Popinet, and H. A. Tchelepi, A conservative and well-balanced surface tension model, Journal of Computational Physics 371, 896 (2018)
work page 2018
-
[34]
S. Popinet, An accurate adaptive solver for surface- tension-driven interfacial flows, Journal of Computa- tional Physics 228, 5838 (2009)
work page 2009
-
[35]
Popinet and collaborators, Basilisk, http: //basilisk.fr (2013–2025)
S. Popinet and collaborators, Basilisk, http: //basilisk.fr (2013–2025)
work page 2013
- [36]
-
[37]
P. K. Farsoiya, S. Popinet, H. A. Stone, and L. Deike, Coupled volume of fluid and phase field method for direct numerical simulation of insoluble surfactant-laden inter- facial flows and application to rising bubbles, Physical Review Fluids 9, 094004 (2024)
work page 2024
-
[38]
S. S. Jain, A model for transport of interface-confined scalars and insoluble surfactants in two-phase flows, Jour- nal of Computational Physics 515, 113277 (2024)
work page 2024
-
[39]
Y. Toba, Drop production by bursting of air bubbles on the sea surface (ii) theoretical study on the shape of float- ing bubbles, Journal of the Oceanographical Society of Japan 15, 121 (1959)
work page 1959
-
[40]
H. Princen, Shape of a fluid drop at a liquid-liquid inter- face, Journal of Colloid Science 18, 178 (1963)
work page 1963
-
[41]
Berny, bubbleshape.h, http://basilisk.fr/ sandbox/aberny/bubble/bubbleShape.h (2021)
A. Berny, bubbleshape.h, http://basilisk.fr/ sandbox/aberny/bubble/bubbleShape.h (2021)
work page 2021
-
[42]
C. R. Constante-Amores, J. Chergui, S. Shin, D. Ju- ric, J. Castrej´ on-Pita, and A. A. Castrej´ on-Pita, Role of surfactant-induced marangoni stresses in retracting liq- uid sheets, Journal of Fluid Mechanics 949, A32 (2022)
work page 2022
-
[43]
D. B. Shaw and L. Deike, Film drop production over a wide range of liquid conditions, Physical Review Fluids 9, 033602 (2024)
work page 2024
-
[44]
B. Ji, Z. Yang, Z. Wang, R. H. Ewoldt, and J. Feng, Sec- ondary Bubble Entrainment via Primary Bubble Burst- ing at a Viscoelastic Surface, Physical Review Letters 131, 104002 (2023)
work page 2023
-
[45]
V. Fainerman, S. Lylyk, E. Aksenenko, L. Liggieri, A. Makievski, J. Petkov, J. Yorke, and R. Miller, Adsorp- tion layer characteristics of Triton surfactants Part 2. Dy- namic surface tension and adsorption, Colloids and Sur- faces A: Physicochemical and Engineering Aspects 334, 8 (2009)
work page 2009
-
[46]
V. Fainerman, S. Lylyk, E. Aksenenko, A. Makievski, J. Petkov, J. Yorke, and R. Miller, Adsorption layer char- acteristics of Triton surfactants 1. Surface tension and adsorption isotherms, Colloids and Surfaces A: Physico- chemical and Engineering Aspects 334, 1 (2009)
work page 2009
- [47]
-
[48]
M. A. Erinin, C. Liu, X. Liu, W. Mostert, L. Deike, and J. H. Duncan, The effects of surfactants on plunging breakers, Journal of Fluid Mechanics 972, R5 (2023)
work page 2023
-
[49]
N.-S. Cheng, Formula for the viscosity of a glycerol- water mixture, Industrial & engineering chemistry research 47, 3285 (2008)
work page 2008
-
[50]
K. Takamura, H. Fischer, and N. R. Morrow, Physi- cal properties of aqueous glycerol solutions, Journal of Petroleum Science and Engineering 98, 50 (2012)
work page 2012
-
[51]
S. Poulain, E. Villermaux, and L. Bourouiba, Ageing and burst of surface bubbles, Journal of Fluid Mechanics851, 636 (2018)
work page 2018
-
[52]
T. Aur´ egan and L. Deike, Surface bubble lifetime in the presence of a turbulent air flow, and the effect of surface layer renewal, arXiv preprint arXiv:2505.04819 (2025)
-
[53]
A. Sierou and J. R. Lister, Self-similar recoil of inviscid drops, Physics of Fluids 16, 1379 (2004)
work page 2004
-
[54]
T. J. Boerner, S. Deems, T. R. Furlani, S. L. Knuth, and J. Towns, Access: Advancing innovation: Nsf’s ad- vanced cyberinfrastructure coordination ecosystem: Ser- vices & support, in Practice and Experience in Advanced Research Computing 2023: Computing for the Common Good (2023) pp. 173–176
work page 2023
discussion (0)
Sign in with ORCID, Apple, or X to comment. Anyone can read and Pith papers without signing in.