Transport and removal of a passive tracer in porous media employing surface washing
Pith reviewed 2026-05-17 20:37 UTC · model grok-4.3
The pith
Surface washing removes a passive tracer from porous plates in three distinct stages.
A machine-rendered reading of the paper's core claim, the machinery that carries it, and where it could break.
Core claim
The paper establishes that tracer removal by surface washing follows a three-stage mass-transport process consisting of an initial period of rapid removal of the tracer found within the surface roughness, followed by a period of slower removal limited by vertical diffusion, and a third stage of accelerated advection-dominated removal when the tracer-rich region that was transported downstream during the second stage reaches the downstream boundary of the porous plate. Quantitative fluorescence measurements of effluent concentration and dye-attenuation imaging of the surface distribution provide the evidence for this sequence.
What carries the argument
The three-stage mass-transport process arising from the interplay of surface film flow, vertical diffusion into the porous medium, and downstream advection once tracer reaches the plate boundary.
If this is right
- Removal rates depend on washing-film characteristics and porous-plate permeability.
- Initial tracer amount, spatial extent, and diffusive penetration depth control the duration of the diffusion-limited stage.
- The accelerated final stage occurs reliably once the tracer-rich region reaches the downstream boundary.
- The observed stages supply practical rules for adjusting flow speed or exposure time to optimize total tracer extraction.
Where Pith is reading between the lines
- The staged removal timeline could be used to estimate required washing durations for porous filters or contaminated soil in field settings.
- Analogous three-stage dynamics may appear when surface flow acts on other porous natural materials such as riverbed sediments.
- Introducing surface-active agents might shorten the diffusion-limited stage by changing penetration or interfacial transport.
Load-bearing premise
The tracer remains completely passive with no chemical reactions or adsorption on the porous medium, and the fluorescence and imaging measurements accurately reflect true concentrations without optical artifacts.
What would settle it
A time series of effluent concentration that shows only one or two monotonic phases instead of the predicted rapid-slow-accelerated sequence, or that lacks the final acceleration precisely when the downstream edge is reached, would falsify the three-stage description.
Figures
read the original abstract
This experimental study investigates the dynamics of surface washing to remove a passive tracer from a porous plate by a gravity-driven liquid film across its surface. A disodium fluorescein tracer is introduced at the surface of a water-saturated porous plate and allowed to diffuse into the plate for a number of hours before a film of water solution flows over its surface to extract and transport the tracer away. The removal rate of the tracer is monitored quantitatively by using fluorescence measurements to determine the concentration in the effluent from the washing process. These measurements are supplemented by dye-attenuation imaging, which provides mainly qualitative insights about the tracer's concentration distribution on the porous plate surface. Our findings reveal a three-stage mass-transport process consisting of an initial period of rapid removal of the tracer found within the surface roughness, followed by a period of slower removal, which appears to be limited by vertical diffusion, and a third stage of accelerated advection-dominated removal when the tracer-rich region that was transported downstream during the second stage reaches the downstream boundary of the porous plate. A parametric study explores the influence of the characteristics of the washing film, the permeability of the porous plate, the amount and initial spatial extent of the tracer on the porous plate and the tracer's diffusive penetration depth on the mass removal rates. Our insights offer practical guidance for optimising surface washing protocols for porous systems in industrial and environmental applications.
Editorial analysis
A structured set of objections, weighed in public.
Referee Report
Summary. The manuscript reports an experimental investigation of removing a passive tracer (disodium fluorescein) from a water-saturated porous plate by flowing a gravity-driven liquid film across the surface. Tracer is first allowed to diffuse into the plate for several hours; removal is then quantified via fluorescence-based effluent concentration measurements and supplemented by dye-attenuation imaging of the surface. The central claim is the existence of a three-stage mass-transport process: rapid initial removal of tracer from surface roughness, a slower intermediate stage attributed to vertical diffusion, and a final accelerated advection-dominated stage once the downstream-transported tracer-rich region reaches the plate outlet. A parametric study examines the effects of film characteristics, plate permeability, tracer amount and initial extent, and diffusive penetration depth on removal rates.
Significance. If the three-stage description and its mechanistic attributions hold under quantitative scrutiny, the work supplies useful practical guidance for optimizing surface-washing protocols in porous-media applications such as industrial cleaning or environmental remediation. The combination of quantitative effluent monitoring with imaging provides direct observational access to the transport dynamics, and the parametric variations help map how operating conditions influence removal efficiency. The experimental design is straightforward and reproducible in principle, though the overall impact depends on strengthening the evidence for the diffusion-limited interpretation of the second stage.
major comments (2)
- Results section describing the three-stage process (effluent curves and dye-attenuation images): the attribution of the intermediate slower-removal regime to vertical diffusion is presented as an interpretation based on curve shape and visual appearance. No explicit comparison is made between the observed duration of this regime and the characteristic diffusive timescale set by the reported penetration depth and the diffusivity of fluorescein. Without this check, the data remain consistent with alternative mechanisms such as slow release from roughness or weak internal advection, weakening the mechanistic claim.
- Results or discussion of stage identification: the boundaries separating the three stages are identified by eye from the effluent concentration time series rather than by a reproducible quantitative criterion (e.g., change-point detection, slope threshold, or piecewise fitting). This affects the reliability of any subsequent parametric comparisons that rely on stage-specific rates or durations.
minor comments (2)
- Methods: provide explicit values (with uncertainties) for all key parameters—film flow rate, plate thickness and permeability, initial tracer concentration, and penetration depth—so that the parametric study can be fully reproduced and the diffusive timescale can be calculated by readers.
- Figure captions and text: clarify whether the imaging is used only qualitatively or whether any quantitative intensity-to-concentration calibration was performed and validated.
Simulated Author's Rebuttal
We thank the referee for their thorough review and valuable comments, which have helped us improve the clarity and rigor of our manuscript. We address each major comment below and outline the revisions we will make.
read point-by-point responses
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Referee: Results section describing the three-stage process (effluent curves and dye-attenuation images): the attribution of the intermediate slower-removal regime to vertical diffusion is presented as an interpretation based on curve shape and visual appearance. No explicit comparison is made between the observed duration of this regime and the characteristic diffusive timescale set by the reported penetration depth and the diffusivity of fluorescein. Without this check, the data remain consistent with alternative mechanisms such as slow release from roughness or weak internal advection, weakening the mechanistic claim.
Authors: We agree with the referee that a direct comparison to the diffusive timescale would strengthen the mechanistic attribution. In the revised version, we will calculate the characteristic diffusion time using the penetration depth and the known diffusivity of disodium fluorescein. We will then compare this timescale to the duration of the intermediate stage observed in the effluent curves for different experimental conditions. This addition will help substantiate the diffusion-limited nature of the second stage and address potential alternative explanations. revision: yes
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Referee: Results or discussion of stage identification: the boundaries separating the three stages are identified by eye from the effluent concentration time series rather than by a reproducible quantitative criterion (e.g., change-point detection, slope threshold, or piecewise fitting). This affects the reliability of any subsequent parametric comparisons that rely on stage-specific rates or durations.
Authors: We recognize that visual identification of stage boundaries, while guided by clear changes in slope and supported by imaging, lacks full reproducibility. In the revision, we will introduce a quantitative method for stage delineation, such as applying a threshold on the rate of change in effluent concentration or performing piecewise linear fits to identify transition points. This will be documented in the methods and applied uniformly to all datasets, improving the reliability of our parametric analysis. revision: yes
Circularity Check
No circularity: purely experimental observations with no derivations or fitted predictions
full rationale
This manuscript is an experimental study that reports direct measurements of effluent concentration via fluorescence and qualitative dye-attenuation imaging of tracer distribution on a porous plate. The central claim of a three-stage mass-transport process is presented as an empirical description of observed removal rates under varying film characteristics, permeability, tracer amount, and penetration depth. No equations, first-principles derivations, parameter fits presented as predictions, or self-citation chains appear in the provided text. The attribution of the intermediate stage to vertical diffusion is an interpretive comment on the data shape rather than a reduction of any result to its own inputs by construction. The work is self-contained through its experimental protocol and measurements, with no load-bearing steps that collapse to tautology or renaming of inputs.
Axiom & Free-Parameter Ledger
axioms (2)
- domain assumption The disodium fluorescein tracer behaves as a passive scalar with no significant chemical interactions or adsorption on the porous medium.
- domain assumption Fluorescence intensity and dye-attenuation imaging provide accurate quantitative and qualitative measures of tracer concentration.
Lean theorems connected to this paper
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IndisputableMonolith/Cost/FunctionalEquation.leanwashburn_uniqueness_aczel unclear?
unclearRelation between the paper passage and the cited Recognition theorem.
Our findings reveal a three-stage mass-transport process consisting of an initial period of rapid removal of the tracer found within the surface roughness, followed by a period of slower removal, which appears to be limited by vertical diffusion, and a third stage of accelerated advection-dominated removal
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]
1 mL over a period of around 2 . 5 s. The solution spread rapidly over the wet porous surface in a circ ular pattern with radius of around 30 mm and 45 mm, immediately after the deposition fin ishes, for fluorescein solution volume 0 . 2 mL and 0. 5 mL, respectively. This preparation protocol for the porous plat e ensured reproducibility between experiments...
-
[2]
07) × 10− 12 and (1 . 64 ± 0. 49) × 10− 11 m2, for plates made of 100–200 µm and 300–400 µm glass beads, respectively. The permeability ratio between the two plates, κ 300− 400/κ 100− 200, is found to be 5 . 57 ± 2. 04. For a homogeneous porous medium made of mono-disperse spherical beads with the sam e packing, the Kozeny-Carman equation suggests κ ∝ α 2...
-
[3]
Transmittance imaging The experimental setup for imaging was designed to use a dye atten uation technique [28, 29] similar to the approach in [26] to quantitatively record the depth-averaged tracer conce ntration field. The concentration, CBL (or mass, mBL), of the tracer still present on the plate can be related to the amoun t of light absorbed by the dye...
-
[4]
Measuring tracer concentrations in the effluent As noted in II A, we performed accurate time-resolved quantificat ion of the concentration of our tracer in the effluent from the washing flow for all the experiments. While for initial experiments we employed an absorbance spectroscopy approach (using an inline bespoke flow cell), this did no t yield the necessary...
-
[5]
33, agrees reasonably well with the ratio κ 300− 400/κ 100− 200 = 5
63 ± 0. 33, agrees reasonably well with the ratio κ 300− 400/κ 100− 200 = 5. 57 ± 2. 04. While rescaling time in Fig. 5(d) makes both the inflection point and the e nd of cleaning match for the two curves, the curves themselves do not collapse. In the plate made of bigger b eads (300–400 µm), the initial surface flushing removes approximately twice the mass...
-
[6]
L. B. Hu, C. Savidge, D. M. Rizzo, N. Hayden, J. W. Hagadorn , and M. Dewoolkar, Commonly used porous building materials: Geomorphic pore structure and fluid transport, J ournal of Materials in Civil Engineering 25, 1803 (2013)
work page 2013
-
[7]
C. Hall and W. Hoff, Water Transport in Brick, Stone and Concrete , 3rd ed. (CRC Press, 2021)
work page 2021
- [8]
-
[9]
J. R. Fitch and C. R. Cheeseman, Characterisation of envi ronmentally exposed cement-based stabilised/solidified i ndustrial waste, Journal of Hazardous Materials 101, 239 (2003)
work page 2003
-
[10]
G. S. Settles, Fluid mechanics and homeland security, An nual Review of Fluid Mechanics 38, 87 (2006)
work page 2006
-
[11]
S. A. Boone and C. P. Gerba, Significance of fomites in the s pread of respiratory and enteric viral disease (2007)
work page 2007
-
[12]
E. Gazi, P. R. Whatley, M. D. Walker, S. N. Marriott, E. Hoc knull, C. P. Barr, V. Dwarampudi, D. M. Clough, I. M. Shortman, and S. J. Mitchell, Evaluating vehicle-borne and person-worn spray technologies to deliver target decontam inant doses to urban surfaces for biological remediation, Remedi ation 35, 10.1002/rem.70015 (2025)
-
[13]
S. Ryan, Persistence of Toxic Industrial Chemicals and Chemical War fare Agents on Building Materials Under Conventional Envir onmental Tech. Rep. (National Homeland Security Research Center, Offi ce of Research and Development, U.S. Environmental Protection Agency, 2008)
work page 2008
-
[14]
R. F. Griffiths and I. D. Roberts, Droplet evaporation from porous surfaces; model validation from field and wind tunnel experiments of sand and concrete, Atmospheric Environment 33, 3531 (1999)
work page 1999
-
[15]
S. L. Bartelt-Hunt, M. A. Barlaz, D. R. Knappe, and P. Kje ldsen, Fate of chemical warfare agents and toxic industrial chemicals in landfills, Environmental Science and Technolo gy 40, 4219 (2006)
work page 2006
-
[16]
R. A. Jenkins, M. V. Buchanan, R. Merriweather, R. H. Ilg ner, T. M. Grayle, and A. P. Watson, Movement of chemical warfare agent simulants through porous media, Journal of Ha zardous Materials 37, 303 (1994)
work page 1994
-
[17]
S. N. Westin, S. Winter, E. Karlsson, A. Hin, and F. Oeseb urg, On modeling of the evaporation of chemical warfare agen ts on the ground, Journal of Hazardous Materials A 63, 5 (1998)
work page 1998
-
[18]
M. P. Willis, B. A. Mantooth, and T. A. Lalain, Novel meth odology for the estimation of chemical warfare agent mass transport dynamics. part i: Evaporation, J. Phys. Chem. C 116, 538 (2012)
work page 2012
-
[19]
M. P. Willis, B. A. Mantooth, and T. A. Lalain, Novel meth odology for the estimation of chemical warfare agent mass transport dynamics. part ii: Absorption, J. Phys. Chem. C 116, 546 (2012)
work page 2012
-
[20]
J. R. Landel and D. I. Wilson, The fluid mechanics of clean ing and decontamination of surfaces, Annual Review of Fluid Mechanics 53, 147 (2021)
work page 2021
-
[21]
Y. Geng, A. A. Kamilova, and E. K. Luckins, Fluid-flow effe cts in the reactive decontamination of porous materials dri ven by chemical swelling or contraction, Journal of Engineerin g Mathematics 141, 10.1007/s10665-023-10283-6 (2023)
-
[22]
P. J. Fryer and K. Asteriadou, A prototype cleaning map: A classification of industrial cleaning processes (2009)
work page 2009
-
[23]
M. P. Dalwadi, D. O’Kiely, S. J. Thomson, T. S. Khaleque, and C. L. Hall, Mathematical modeling of chemical agent removal by reaction with an immiscible cleanser, SIAM Journ al on Applied Mathematics 77, 1937 (2017)
work page 1937
- [24]
-
[25]
E. K. Luckins, C. J. W. Breward, C. P. G. I. M., and Please, A homogenised model for the motion of evaporating fronts in porous media, European Journal of Applied Mathematics 34, 806 (2023)
work page 2023
-
[26]
E. K. Luckins, C. J. W. Breward, C. P. G. I. M., and Please, The effect of pore-scale contaminant distribution on the reactive decontamination of porous media, European Journa l of Applied Mathematics 35, 318 (2024)
work page 2024
-
[27]
B. S. Maryshev and L. S. Klimenko, Cleaning porous media by an external vertical flow, Acta Mechanica 234, 3305 (2023)
work page 2023
-
[28]
K. Hatfield, M. Annable, J. Cho, P. S. Rao, and H. Klammler , A direct passive method for measuring water and contaminan t fluxes in porous media, Journal of Contaminant Hydrology 75, 155 (2004)
work page 2004
-
[29]
L. Zhan and Y. C. Yortsos, Identification of the permeabi lity field of a porous medium from the injection of a passive tracer, Phys. Rev. E 62, 863 (2000)
work page 2000
-
[30]
A. K. Patidar, D. Joshi, U. Dristant, and T. Choudhury, A review of tracer testing techniques in porous media special ly attributed to the oil and gas industry, Journal of Petroleum Exploration and Production Technology 12, 3339 (2022)
work page 2022
-
[31]
J. R. Landel, A. L. Thomas, H. McEvoy, and S. B. Dalziel, C onvective mass transfer from a submerged drop in a thin falling film, Journal of Fluid Mechanics 789, 630 (2016)
work page 2016
-
[32]
A. J. Easteal and L. A. Woolf, Pressure and temperature d ependence of tracer diffusion coefficients of methanol, ethan ol, acetonitrile, and formamide in water, The Journal of Physic al Chemistry 89, 1066 (1985)
work page 1985
-
[33]
C. Cenedese and S. Dalziel, Concentration and depth fiel ds determined by the light transmitted through a dyed soluti on, in Proceedings of the 8th International Symposium on Flow Visu alization (1998) pp. 1–37
work page 1998
-
[34]
D. Allgayer and G. Hunt, On the application of the light- attenuation technique as a tool for non-intrusive buoyancy 17 measurements, Experimental Thermal and Fluid Science 38, 257 (2012)
work page 2012
-
[35]
S. E. Pringle, R. J. Glass, and C. A. Cooper, Double-diffu sive finger convection in a hele-shaw cell: An experiment exp loring the evolution of concentration fields, length scales and mas s transfer, Transport in Porous Media 47, 195 (2002)
work page 2002
-
[36]
H. Wang, X. Chen, and J. W. Jawitz, Locally-calibrated l ight transmission visualization methods to quantify nonaq ueous phase liquid mass in porous media, Journal of Contaminant Hy drology 102, 29 (2008)
work page 2008
-
[37]
R. Sj¨ oback, J. Nygren, and M. Kubista, Absorption and fl uorescence properties of fluorescein, Spectrochimica Acta Part A: Molecular and Biomolecular Spectroscopy 51, https://doi.org/10.1016/0584-8539(95)01421-P (1995)
-
[38]
G. S. Beavers and D. D. Joseph, Boundary conditions at a n aturally permeable wall, Journal of Fluid Mechanics 30, 197 (1967)
work page 1967
-
[39]
W. A. W., Dispersion in porous media, in Flow in Porous Rocks (Cambridge University Press, 2014) pp. 70–91
work page 2014
-
[40]
T. Casalini, M. Salvalaglio, G. Perale, M. Masi, and C. C avallotti, Diffusion and aggregation of sodium fluorescein i n aqueous solutions, Journal of Physical Chemistry B 115, 12896 (2011)
work page 2011
-
[41]
T. LI, M. LI, X. JING, W. XIAO, and Q. CUI, Influence mechan ism of pore-scale anisotropy and pore distribution heterogeneity on permeability of porous media, Petroleum E xploration and Development 46, 594 (2019)
work page 2019
-
[42]
A. J. Sederman and L. F. Gladden, Magnetic resonance visualisation of single-and two-phase flow in porous media , Tech. Rep. (2001)
work page 2001
-
[43]
L. Li, Q. Chen, A. E. Marble, L. Romero-Zer´ on, B. Newlin g, and B. J. Balcom, Flow imaging of fluids in porous media by magnetization prepared centric-scan sprite, Journal of Ma gnetic Resonance 197, 1 (2009)
work page 2009
-
[44]
P. J. Barrie, Characterisation of porous media using nm r methods, Annual Reports on NMR Spectroscopy 41 (2000)
work page 2000
-
[45]
Q. Wang, H. Chen, Y. Wang, and J. Sun, Thermal shock effect on the glass thermal stress response and crack propagation, in Procedia Engineering, Vol. 62 (Elsevier Ltd, 2013) pp. 717–724
work page 2013
- [46]
- [47]
discussion (0)
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