Dataset Open Access
Skrypnik, Artem;
Lappan, Tobias;
Knüpfer, Leon;
Ziauddin, Muhammad;
Arnal Tribaldos, Icíar;
Shevchenko, Natalia;
Heitkam, Sascha
{ "description": "<p>The hydrodynamic theory of pneumatic foam analytically predicts the advective transport of liquid by foam rising continuously in a vertical column or pipe, relying on cross-sectional averaging of the foam velocity and liquid fraction. This experimental study accumulates a database for assessing the pneumatic foam theory in a vertically aligned diverging nozzle, i.e. at increasing cross-sectional area in nominal flow direction. The velocity distribution of the flowing foam and its liquid fraction distribution were measured by means of X-ray, optical and electrical techniques in three different nozzles distinguished by their half angle θ = 5°, 10°, 20°. The experimental setup and the measurements are described in detail in Skrypnik et al. (<a href=\"https://www.hzdr.de/publications/Publ-41024\">https://www.hzdr.de/publications/Publ-41024</a>).</p>\n\n<ul>\n\t<li>X-ray radiography (XR) has measured the distribution of the liquid fraction (ε<sub>XR</sub>) inside the nozzle as a two-dimensional projection, i.e. integrated in the X-ray beam direction.</li>\n\t<li>X-ray particle tracking (XPTV) has measured the local velocity u<sub>T</sub> inside the nozzle, along the motion path of each tracer particle described by the radial (r) and vertical position (z) in consecutive frames. The velocity u<sub>T</sub> was normalised by the superficial gas velocity j<sub>g</sub>(z) = Q<sub>g</sub> / (π * R(z)<sup>2</sup>), with Q<sub>g</sub> denoting the gas flow rate of compressed air applied for foam generation, and R(z) denoting the radius of the cross-sectional area depending on the vertical position z. To compare different nozzles, the vertical position z was normalised by the total length L = 25 mm / tan(θ) of the nozzle depending on its half angle θ = 5°, 10°, 20°.</li>\n\t<li>Optical PIV adapted to foam (FoamPIV) has measured the time-averaged velocity u<sub>W</sub> through the transparent wall of the nozzle, i.e. at the nozzle radius r = R(z) depending on the vertical position z. As described above, the velocity u<sub>W</sub> was normalised by the superficial gas velocity j<sub>g</sub>(z), and the vertical position z was normalised by the total length L of the nozzle.</li>\n\t<li>Electrode pairs (EP) have measured the cross-sectional average values of the liquid fraction (ε<sub>EP</sub>) upstream and downstream the nozzle, simultaneously to the X-ray radiographic measurement of the liquid fraction distribution (ε<sub>XR</sub>) inside the nozzle.</li>\n</ul>\n\n<p>The experimental data in this repository is structured into different folders and files as follows.</p>\n\n<ul>\n\t<li>FoamNozzle_Overview.CSV gives an overview of all measurements runs, nozzles, and techniques.</li>\n\t<li>Level 1 are folders classified by the measurement technique: 01_XR: X-ray radiography, 02_XPTV: X-ray particles tracking velocimetry, 03_FoamPIV: Optical PIV adapted to foam, 04_EP: Electrode pairs.</li>\n\t<li>Level 2 are folders classified by the different nozzles, distinguished by the nozzle half angle θ = 5°, 10°, 20°, and divided into bottom and top part in the case of θ = 5°, 10°.</li>\n\t<li>Level 3 are TIF and CSV files of measurement results.\n\t<ul>\n\t\t<li>01_XR: Each TIF image shows the time-averaged distribution of the liquid fraction inside the nozzle; the liquid fraction (0 < ε<sub>XR</sub> < 1) is indicated by the value of each pixel.</li>\n\t\t<li>02_XPTV: Each CSV file consists of three columns, namely the radial position (r, in mm), the normalised vertical position (z / L), and the normalised velocity (u<sub>T</sub> / j<sub>g</sub>(z)).</li>\n\t\t<li>03_FoamPIV: Each CSV file consists of two columns, namely the normalised vertical position (z / L), and the normalised velocity (u<sub>W</sub> / j<sub>g</sub>(z)).</li>\n\t\t<li>04_EP: Each CSV file consists of three columns, namely the cross-sectional average of the liquid fraction (0 < ε<sub>EP</sub> < 1) downstream as well as upstream the nozzle, and the time (in s).</li>\n\t</ul>\n\t</li>\n</ul>", "creator": [ { "@type": "Person", "@id": "https://orcid.org/0000-0002-3472-3421", "name": "Skrypnik, Artem" }, { "@type": "Person", "@id": "https://orcid.org/0000-0003-2826-1395", "name": "Lappan, Tobias" }, { "@type": "Person", "@id": "https://orcid.org/0000-0001-7012-7662", "name": "Kn\u00fcpfer, Leon" }, { "@type": "Person", "@id": "https://orcid.org/0000-0002-4580-9482", "name": "Ziauddin, Muhammad" }, { "@type": "Person", "name": "Arnal Tribaldos, Ic\u00edar" }, { "@type": "Person", "@id": "https://orcid.org/0000-0002-6177-2130", "name": "Shevchenko, Natalia" }, { "@type": "Person", "@id": "https://orcid.org/0000-0002-2493-7629", "name": "Heitkam, Sascha" } ], "@type": "Dataset", "keywords": [ "Drainage", "Liquid fraction", "Particle tracking velocimetry", "Particle image velocimetry", "Pneumatic foam theory", "X-ray radiography" ], "@context": "https://schema.org/", "license": "https://creativecommons.org/licenses/by/4.0/legalcode", "@id": "https://doi.org/10.14278/rodare.3624", "distribution": [ { "@type": "DataDownload", "contentUrl": "https://rodare.hzdr.de/api/files/310fd8ca-e5b7-4519-9af5-fb5d360e66fc/FoamNozzle.zip", "fileFormat": "zip" } ], "datePublished": "2025-03-07", "name": "Data publication: Measurement of liquid foam flow through a diverging nozzle", "url": "https://rodare.hzdr.de/record/3624", "inLanguage": { "@type": "Language", "alternateName": "eng", "name": "English" }, "sameAs": [ "https://www.hzdr.de/publications/Publ-41083" ], "identifier": "https://doi.org/10.14278/rodare.3624" }
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Skrypnik, Artem, Lappan, Tobias, Knüpfer, Leon, Ziauddin, Muhammad, Arnal Tribaldos, Icíar, Shevchenko, Natalia, & Heitkam, Sascha. (2025). Data publication: Measurement of liquid foam flow through a diverging nozzle [Data set]. Rodare. http://doi.org/10.14278/rodare.3624