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REVIEW 4 major objections 4 minor 7 references

Multiscale analysis of the textural atomization process of a rocket engine assisted coaxial jet

T0 review · 4 major / 4 minor · reviewed 2026-08-12 · deepseek-v4-flash

Pith's one-line read Improved multiscale image analysis lets a rocket-engine coaxial jet's textural atomization be quantified from ligament shapes, yielding bimodal blob/drop diameter distributions whose sizes and counts evolve regularly with injector distance.

desk verdict The measurement improvement is real and the application is new, but the reported blob/drop size distributions rest on a non-unique fit that needs uncertainty quantification before the quantitative claims should be trusted. read the letter →

arxiv 2411.17427 v1 pith:YYMNCBPE submitted 2024-11-26 physics.flu-dyn physics.app-phphysics.data-an

classification physics.flu-dynphysics.app-phphysics.data-an
keywords texturalatomizationmultiscaleanalysisscaledistributionblobdiametercoaxialassistedsubpixelimage3pGGrocketenginecombustion
verification ladder T0 review T1 audit T2 compute T3 formal

The pith

A machine-rendered reading of the paper's core claim, the machinery that carries it, and where it could break.

The reading

Textural atomization—the peeling of short-lived ligaments and droplets from a liquid surface—is usually visible in images but hard to quantify. This paper presents an improved multiscale image-analysis method that measures the scale distribution of those ligaments with subpixel accuracy, then fits the measured distribution with a two-component three-parameter generalized gamma model. The fit returns the sizes and numbers of the 'blobs' (swelling sections of the ligaments) and, treating blobs as drops in formation, turns them into droplet diameter distributions. Applied to a methane–oxygen coaxial jet burning at 7 bar in the fiber-type breakup regime, where the gas flow draws the liquid into long threads, the method reports a bimodal blob diameter distribution whose mean diameters grow linearly with distance from the injector while the blob count first rises and then falls. The authors conclude that the analysis locates the zone of most intense textural atomization (roughly 14–21 mm from the injector) and the point where this process stops, and that the regular parameter trends make mathematical models of textural atomization feasible.

What carries the argument

The central object is the scale distribution $e_2(d)$ of the liquid–gas interface, obtained by eroding the segmented liquid system with disks of diameter $d$ and recording the surface area lost at each scale. Its derivative $-e_2(d)_{,d}$ is proportional to the diameter distribution of the equivalent set of cylinders that has the same scale distribution as the real, arbitrarily deformed ligament population. The paper represents that cylinder distribution by a three-parameter generalized gamma (3pGG) function, and in the fully atomized limit ($\alpha=1$) the blob diameter distribution inherits the same 3pGG form, $f_{0s}(D)\propto D^{q-1}e^{-(D/D_s)^q}$. A two-component version of this model is fitted to the measured derivative, with each component corresponding to one blob family; the fitted parameters directly give the mean diameter, width, and relative number of each family through $D_s = q^{1/q}D_c$, $N_s \propto -e_2(0)_{,d}\,D_s^q/\Gamma(q)$. On the measurement side, the enabling step is an exact-distance computation with fractional-distance binning combined with $4\times4$ bilinear subpixel interpolation, which removes the oscillations and pixelization bias that otherwise corrupt the small-scale part of the distribution.

What would settle it

Measure the actual droplet size distribution just downstream of the ligament zone, in a cold-flow twin of this injector with matched Weber number and momentum-flux ratio, and compare it with the blob diameter distribution predicted by the two-component 3pGG fit; if the predicted bimodality and its spatial evolution do not appear in the measured spray, the blob-equivalence step is wrong. A simpler check is to apply the extraction to synthetic ligament images with known blob sizes and verify that the fitted parameters recover the injected blob diameters.

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Extended reading notes

Core claim

The paper's central claim is that the multiscale scale distribution of textural ligaments, measured with subpixel fidelity, carries enough information to reconstruct the diameter distribution of the blobs that structure ligament deformation, and that treating these blobs as drops in formation yields quantitative spray information where conventional droplet diagnostics cannot operate. The argument runs through the identity $e_2(d)=L(d)/2$, which relates the scale distribution to the interface length of the eroded liquid system; differentiating once gives a quantity proportional to the diameter distribution of an equivalent set of cylinders, and a second differentiation connects the fully atomized limit to a spherical-drop distribution. Fitting the measured $-e_2(d)_{,d}$ with two 3pGG components separates blob families by scale. In the present reactive coaxial jet the fit identifies two such families, giving a bimodal diameter distribution: small blobs formed by textural deformation of the ligament surface and larger blobs formed by structural deformation of the ligament body. The mean diameters of both families increase linearly with distance from the injector, while the total blob number peaks between roughly 14 mm and 21 mm and the small-blob family disappears at the farthest positions, marking where textural atomization stops.

Load-bearing premise

The entire drop-size estimate rests on treating the swelling bumps of a deformed ligament as spherical drops and on reading the selected straight segments of a double-log plot as distinct blob families; the paper does not check that equivalence against independent droplet measurements.

Editorial extensions

If this is right

  • Textural atomization can be followed quantitatively along the injector: blob mean diameters grow linearly with distance, and the blob number per unit width rises then falls, locating the intense atomization zone near 14–21 mm.
  • The bimodal blob diameter distribution points to two coexisting production mechanisms in the textural process, one attached to the ligament surface and one to the ligament body.
  • The regular spatial evolution of the fitted 3pGG parameters ($q_1,q_2,D_{s1},D_{s2}$) means a closed-form expression for the blob diameter distribution as a function of injector distance is within reach.
  • In reactive flows where laser-diffraction or phase-Doppler instruments fail, this image-based route provides an alternative estimate of the droplet population being formed and of where its production is strongest.

Reading between the lines

Editorial extensions of the paper, not claims the author makes directly.

  • A natural next test would be to run the same analysis on a cold-flow twin with matched Weber number and momentum-flux ratio, where conventional droplet sizing is possible, and compare the predicted blob distributions with measured spray diameters; agreement would validate the blob-as-drop assumption, disagreement would localize the error in the equivalence step.
  • Because the method needs only images of the liquid interface, it should transfer directly to numerical simulation data: applying the extraction to simulated ligament fields with known blob populations would provide a ground-truth check of the linear-region selection and the two-component fit.
  • If the linear growth of blob mean diameter with injector distance is confirmed as a general trend, the multiscale parameters could serve as a surrogate for the local turbulent scales that initiate textural ligaments, linking image-derived morphology to turbulence-driven breakup models.
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Editorial analysis

A structured set of objections, weighed in public.

Desk editor's note, referee report, and a circularity audit.

Referee Report

4 major / 4 minor

Summary. The paper presents a multiscale image-analysis method for characterizing the textural atomization ligaments of a cryogenic coaxial rocket injector operating under combustion. It improves the measurement of the scale distribution e2(d) by replacing the integer distance map with an exact distance transform and a 4x4 subpixel interpolation, and it validates this improvement on a synthetic sinusoidally perturbed cylinder. The paper then models the right-hand tail of the second derivative -e2(d),d as a sum of two three-parameter Generalized Gamma (3pGG) components and converts each component into a number-based blob/drop diameter distribution using previously derived equivalent-cylinder/sphere relations. Applying the model as a function of injector distance, it reports bimodal blob diameter distributions whose peak diameters, widths, and numbers evolve regularly with z, and it interprets these as drops in formation.

Significance. The improved scale-distribution measurement is a genuine methodological contribution: the synthetic test in Fig. 5 shows that the subpixel and exact-distance corrections remove pixelization oscillations and sharpen the measured peaks, and the availability of converged averages from 100 images is useful for future work in harsh combusting environments. If the blob-extraction step were independently validated, the paper would offer a route to quantitative estimates of ligament swelling scales and potential drop sizes where conventional droplet diagnostics cannot be used. However, the paper's central quantitative claim, namely the bimodal blob/drop diameter distributions and their spatial evolutions, is not yet supported, because the 3pGG decomposition is non-unique and the conversion has no ground-truth validation. The qualitative result that ligament scales increase with distance and then the textural population ceases is plausible, but the specific peak diameters and parameter trends should be treated as conditional.

major comments (4)
  1. [§4, Fig. 13, Eqs. (15)-(16)] The two-component 3pGG extraction is non-unique. At z=12.1 mm the paper fits the 'region 2' blob population twice: as the second component of the [52,124] um fit and as the first component of the [74,180] um fit (Figs. 13a-13d). The two recovered region-2 distributions differ in width, and the first extends to the 190 um region-3 peak. No selection criterion, likelihood comparison, or uncertainty estimate is given for choosing the regions-1-and-2 analysis over the regions-2-and-3 analysis. Because each component is a stretched exponential, many two-component sums can approximate the smooth measured curve over finite intervals, so the reported bimodality and the parameter trends in Fig. 15 are not uniquely determined by the data.
  2. [§4, Eqs. (6)-(12) and (15)-(16)] The conversion of the scale-distribution tail into blob/drop diameter distributions relies on assumptions that are not tested. Section 4 assumes that the swelling scales of the ligaments correspond to circular blobs, that alpha=1 holds for the equivalent sphere set, and that the linear regions identified in Fig. 12 correspond to distinct physical blob families. The synthetic validation in Fig. 5 covers only the measurement of -e2(d),d; it does not test the blob-extraction model. The paper therefore needs either a synthetic test with known blob populations or independent droplet-size measurements to support the claim that the fitted components represent drops in formation.
  3. [§4, Fig. 12 and Fig. 14 (z=23.5, 25.6 mm)] The manual identification of the linear regions and the handling of absent regions are not quantified. Fig. 12 identifies linear regions by inspection; Region 0 is excluded with only a qualitative justification; and at z=23.5 and 25.6 mm, where region 1 is not found, the scale intervals [d1,d2] are extrapolated from linear trends of d1(z) and d2(z). These choices determine which data enter each fit, but no sensitivity analysis is reported. Consequently, the disappearance of region 1 and the switch to a single-component model at the farthest positions are not robustly established.
  4. [§4, Fig. 15] No uncertainty quantification accompanies the parameter evolutions in Fig. 15. The quantities q1, q2, Ds1, Ds2, Ns1, and Ns2 are reported as functions of z without confidence intervals, bootstrap estimates, or multi-start checks. In view of the non-uniqueness documented in Fig. 13, the 'clear spatial evolutions' may be within the ambiguity of the fitting procedure rather than physical trends. The paper should quantify the fit uncertainty and demonstrate that the trends are robust to initial parameter choices and interval definitions.
minor comments (4)
  1. [§4] The sentence 'An example is shown in Fig. 10 for the result obtained at z = 12.1 mm' should refer to Fig. 12, not Fig. 10.
  2. [§3.2 and §4] Equation (14) is used twice: once for the distance-bin repartition in Section 3.2 and again for the log-linearity relation in Section 4; the equations should be renumbered to avoid ambiguity.
  3. [Fig. 5 caption] The caption for Fig. 5 should make explicit that panel b is the corrected measurement without subpixel interpolation and that panels c and d use 4x4 and 8x8 interpolation, respectively; the current wording is easy to misread.
  4. [§3.2, Eq. (16)] The notation m(r_I) is introduced as the total distance count in bin r_I, but the preceding text describes splitting each pixel's contribution between bins r_I and r_I+1; rewording this passage would improve clarity.

Circularity Check

0 steps flagged · score 0.0 of 10

No significant circularity: the blob/drop size information is an explicitly fitted transformation of the measured scale distribution, not a claim of out-of-sample prediction, and the cited multiscale identities are not re-derived from the present data.

full rationale

The paper's central product is an estimation procedure, not a prediction. The measured object is the scale distribution e2(d) (Section 3), and the blob/drop diameter distributions are obtained by fitting a two-component 3pGG model to -e2(d),d (Eqs. 15-16) and converting the fitted components through previously established cylinder/sphere relations (Eqs. 3-12). No quantity is fit on one subset and then 'predicted' on a closely related subset; the spatial evolutions reported in Figs. 14-15 are trends in the fitted parameters themselves and are presented as such. The identities e2(d)=L(d)/2, the equivalent-cylinder representation, and the d_pc=0 sphere limit are cited from prior work by the same group, but they are parameter-free mathematical/geometric relations with stated assumptions and are not fitted in this paper, so those citations constitute legitimate evidence rather than a circular reduction. The measurement chain is independently benchmarked on a synthetic sinusoidally perturbed cylinder (Fig. 5), and the subpixel improvements are validated against that theoretical distribution. The non-uniqueness of the two-component decomposition at z=12.1 mm (Figs. 13b vs 13d), where region 2 is fitted twice with different widths, is a real identifiability and model-selection concern; however, the paper explicitly discloses the difference and gives a physical reason for preferring the regions-1-and-2 analysis. That is a robustness weakness, not a case in which the output is equivalent to the input by construction.

Assumptions & free parameters 4 free parameters · 4 assumptions · 1 invented entities

The central quantitative outputs (blob diameter distributions, their bimodality, and their spatial evolutions) are obtained by fitting the measured scale distribution with a two-component 3pGG model. The model parameters, the scale intervals, and the arbitrary cylinder length Lc are all fitted or chosen by hand. The theoretical relations connecting scale distributions to equivalent cylinders and spheres are taken from the authors' prior publications, and the physical interpretation of the fitted components as drops in formation is an assumption with no independent validation.

free parameters (4)
  • 3pGG parameters q1, Dc1, Nc1 for blob population 1 = Varies with z; see Fig 15
    Fitted to -e2(d),d over the selected scale interval [d1,d2] using the two-component model (Eq 15-16).
  • 3pGG parameters q2, Dc2, Nc2 for blob population 2 = Varies with z; see Fig 15
    Second component in the two-component fit to the same measured distribution.
  • Scale interval [d1,d2] for each fit = e.g., [52,124] µm and [74,180] µm at z=12.1 mm
    Chosen by identifying linear regions in the log-log plot (Fig 12); for the two farthest positions intervals are extrapolated from preceding positions.
  • Equivalent cylinder length Lc = 1 µm (arbitrary)
    Set to unity; blob numbers Nsi are proportional to real blob numbers, enabling comparisons but not absolute counts.
assumptions (4)
  • domain assumption The scale distribution e2(d) satisfies e2(d)=L(d)/2 and the equivalent cylinder/sphere relations (Eqs. 3-12).
    Taken from the authors' prior work (Dumouchel et al. 2019, 2022, 2023; Thiesset et al. 2019); not re-derived in this paper.
  • ad hoc to paper The right-hand side of -e2(d),d (scales greater than the modal scale) is dominated by swelling scales and can be modeled by a 3pGG function with alpha=1.
    This is the key modeling choice enabling the blob size distribution; no independent justification is given beyond the linear regions in Fig. 12.
  • domain assumption The segmented images faithfully represent the liquid interface down to the minimum resolved scale of about 16 µm after 4x4 subpixel interpolation.
    Supported by a synthetic-image test, but real combustion images suffer from optical index gradients, blur, and window deposition.
  • ad hoc to paper The fitted blob populations correspond to drops in formation.
    Explicitly stated as an assumption in the abstract and Section 4; no droplet size measurements are provided for validation.
invented entities (1)
  • Blob populations (Regions 1, 2, 3 families)
    purpose: Represent ligament swellings as spherical drops in formation and estimate their size distribution and number.
    The blobs are inferred from a two-component 3pGG fit to the scale distribution; there is no direct imaging or measurement of these blobs as distinct objects, and no validation that they produce the assumed drops.

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Pith. "Pith review of Multiscale analysis of the textural atomization process of a rocket engine assisted coaxial jet." pith.science (2026). https://pith.science/paper/YYMNCBPE

@misc{pith2026241117427,
  author       = {Pith},
  title        = {Pith review of: Multiscale analysis of the textural atomization process of a rocket engine assisted coaxial jet},
  year         = {2026},
  howpublished = {\url{https://pith.science/paper/YYMNCBPE}},
  note         = {Machine review of arXiv:2411.17427}
}
read the original abstract

A method for analyzing liquid ligaments of a textural atomization process is presented in this article for the case of a rocket engine type assisted atomization process under combustion. The operating point positions the atomization process in the fiber type regime carrying an intense textural atomization process. Multiscale in nature, the method based on image analysis associates a scale distribution with a family of ligaments, this distribution being sensitive to the number, size and shape of these ligaments. The quality of scale distributions measured by image analysis depends on the spatial resolution and the precision of area measurements of surfaces with curved boundaries but described by square pixels. Part of the work consisted of improving the method for measuring scale distributions by using a subpixel image analysis technique and refining the surface area measurement method. Another part directed the multiscale analysis towards the estimation of the diameter distributions of the blobs that characterize the large-scale deformation of the ligaments. The analysis describes the atomization process at a level of detail never reached. For instance, assuming that the blobs are drops in formation, the estimated diameter distribution (bimodal in the case examined here) as well as the number of these drops are evaluated as a function of the distance from the injector. This information indicates where the process is most intense and where it stops. Furthermore, these diameter distributions receive a mathematical expression whose parameters report clear evolutions with the distance from the injector. This shows the possibility of elaborating mathematical models appropriate for textural atomization mechanisms.

Figures

Figures reproduced from arXiv: 2411.17427 by the authors.

Figure 1
Figure 1. Positions of the three-image series (z = 0 corresponds to the position of the injector exit section) The combustion chamber is equipped with two opposite rectangular quartz optical windows of 25 mm x 60 mm to record images by adopting a backlighting optical arrangement. The imaging system is composed of a pulsed laser source illuminating the flow field through the combustion chamber. This source (Cavilux Smart 400 W… view at source ↗
Figure 2
Figure 2. a – Disc of diameter D, b – Eroded operation at scale d, c – The eroded system at scale d is a disc of diameter D – d. Since the embedded dimension of the analysis is 2, the liquid system and its parallel systems can be described by three integral quantities, i.e., their surface area S(d), their interface length L(d) and their length-integrated-curvature H(d) [PITH_FULL_IMAGE:figures/full_fig_p007_2.png] view at source ↗
Figure 3
Figure 3. a – Ellipse, b – Ellipse eroded at a small scale: the eroded system retains a smooth boundary, c – Ellipse eroded at a large scale: the eroded system shows two tips. The analysis carried out in this work is based on the study of the distribution –e2(d),d. To help with the analysis, a theoretical set of cylinders whose diameters D are distributed according to a given distribution is considered. This synthetic set is … view at source ↗
Figures from the paper (12 more)
Figure 4
Figure 4. Figure 4: Synthetic image of a sinusoidally perturbed cylinder (unperturbed diameter: 70 pixels; image width and perturbation wavelength: 800 pixels; perturbation amplitude: 31 pixels) The theoretical and measured distributions –e2(d),d of the system shown in [PITH_FULL_IMAGE:f…
Figure 5
Figure 5. Figure 5: Comparison between the theoretical and the measured distribution –e2(d),d a – Initial measurement, b – Corrected measurement c – Corrected measurement with 4x4 subpixel interpolation d - Corrected measurement with 8x8 subpixel interpolation > >C + >D (14) where rI and …
Figure 6
Figure 6. Figure 6: Definition of nx and ny introduced in Eq. (13). Examples of applications of Eqs. (13) to (15). The surface areas expressed by Eq. (16) are no longer necessarily equal to an integer number of pixels and this has a positive repercussion on the determination of –e2(d),d a…
Figure 7
Figure 7. Figure 7: Measurement of –e2(d),d at z = 13.8 mm (see [PITH_FULL_IMAGE:figures/full_fig_p014_7.png]
Figure 8
Figure 8. Figure 8: Snapshot of the liquid jet upper interface as a function of the distance from the injector exit (Images after treatment, Liquid appears in black, Position of the ROI). We see also in [PITH_FULL_IMAGE:figures/full_fig_p015_8.png]
Figure 9
Figure 9. Figure 9: Identification of circular blobs on a textural ligament [PITH_FULL_IMAGE:figures/full_fig_p016_9.png]
Figure 10
Figure 10. Figure 10: Distribution e2(d)/wROI for all z positions (For clarity, the curves show every third point) [PITH_FULL_IMAGE:figures/full_fig_p017_10.png]
Figure 11
Figure 11. Figure 11: Distribution –e2(d),d/wROI for all z positions (For clarity, the curves show every third point) The derivatives –e2(d),d of the scale distribution e2(d) are plotted in [PITH_FULL_IMAGE:figures/full_fig_p017_11.png]
Figure 12
Figure 12. Figure 12: Illustration of Eq. (14) at z = 12.1 mm: ln(ln(-e2(d),d/-e2(dp0),d) = f(ln(d)) Dash lines indicate linear behaviors of the curve [PITH_FULL_IMAGE:figures/full_fig_p018_12.png]
Figure 13
Figure 13. Figure 13: Fit of –e2(d),d (left graphs) and corresponding weighted blob distributions (right graphs, Eq. (11), each component and sum) z = 12.1 mm - a and b: regions 1 and 2, scale range [52 µm; 124 µm] - c and d: regions 2 and 3, scale range [74 µm; 180 µm] [PITH_FULL_IMAGE:f…
Figure 14
Figure 14. Figure 14: Components Nsif0si(D)/wROI and sum for each position (vertical dash lines delimit the analyzed scale interval) [PITH_FULL_IMAGE:figures/full_fig_p021_14.png]
Figure 15
Figure 15. Figure 15: The parameters of the model. Ds1 and Ds2 also report a linear increase but, with a change of slope for Ds2. The slopes of the mean diameter Ds2 linear increase are slightly greater than the one of Ds1. Note here that the Ds2 obtained at z = 23 mm and 25.6 mm align per…

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Works this paper leans on

7 extracted references · 7 canonical work pages

  1. [1]

    The primary atomization process refers to first events of liquid fragment detachmen t from the bulk flow and the secondary process concerns the atomization of these fragments

    Introduction The atomization of a liquid flow in a gaseous environment is a two-step mechanism referred in the literature as primary and secondary atomization processes. The primary atomization process refers to first events of liquid fragment detachmen t from the bulk flow and the secondary process concerns the atomization of these fragments. The primary...

  2. [2]

    Experimental setup and optical diagnostic The ONERA's MASCOTTE test-bench is used for the pre sent experiments. This bench is a subscale cryogenic rocket combustor capable of reproducing operating conditions similar to those encountered inside liquid rocket engine combustion chambers, i.e, high pressures and high mixture ratios. It is equipped with multip...

  3. [3]

    Introduced and applied in several previous works (Thiesset et al

    Multiscale analysis – Description and Measurement 3.1 Multiscale description The description of the textural deformation of the liquid gas interface in the injector near field region uses the multiscale analysis of the visualized liquid system. Introduced and applied in several previous works (Thiesset et al. 2019, Dumou chel et al. 2017, 2019, 2022, 2023...

  4. [4]

    # " ! $% & exp # &

    Since by definition f0c(0) = 0 then –e2(0) ,d = 0. In a real atomizing liquid system, the textural str uctures are ligamentous but not purely cylindrical: they can be seen as cylinders showing successive contracted and dilated sections. The distribution – e2(d),d, and thus the equivalent-system diameter distribut ion f0c(D), reflect the distribution of th...

  5. [5]

    8 as a function of the position z

    Results and Analysis A series of segmented images of the oxygen jet uppe r interface in the near injector nozzle region are shown in Fig. 8 as a function of the position z. These images, in which the liquid appears in black, are not correlated in time. The liquid-gas interface shows large-scale and smal l-scale deformations. The large-scale deformation ca...

  6. [6]

    An important part of this success is linked to the association of high-quality experimental images with improved image processing and image analysis measurement technique s

    Conclusion The method presented in this article for the descri ption of textural atomization liquid ligaments is convincing and brings back little-known information on this type of process. An important part of this success is linked to the association of high-quality experimental images with improved image processing and image analysis measurement techni...

  7. [7]

    National Bureau of Standards, Applied Mathematics Series 55, June 1964 Boulal S, Fdida N, Matuszewski L, Vingert L, Martin -Benito M (2022)

    References Abramowitz M, Stegun, IA (1964) Handbook of Mathema tical Functions. National Bureau of Standards, Applied Mathematics Series 55, June 1964 Boulal S, Fdida N, Matuszewski L, Vingert L, Martin -Benito M (2022). Flame dynamics of a subscale rocket combustor operating with gaseous me thane and gaseous, subcritical or transcritical oxygen. Combusti...

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