EXP 1-4 Description: Difference between revisions

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=Axisymmetric drop impact dynamics on a wall film of the same liquid=
=Axisymmetric drop impact dynamics on a wall film of the same liquid=
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__NOTOC__
__NOTOC__
= Description of Study Test Case =
= Description of Study Test Case =
<pre style="color: red">
This section should:
* Convey the general set-up of the test case configuration (e.g. airflow over a bump on the floor of a wind tunnel)
* Describe the geometry, illustrated by a sketch
* Specify the flow parameters which define the flow regime (e.g. Reynolds number, Rayleigh number, angle of incidence etc.)
* give the principal quantities of interest that were measured - these should include global parameters but also mean-flow and turbulence parameters.


The description can be kept fairly short if reference can be made to a publication or a link to a data base where details are given. For other cases a more detailed, self-contained description should be provided.
A sketch of the general set-up of the experiment and the geometry is shown in Fig. 3 in Section [[EXP 1-4 Experimental Set Up]] while the principal quantities measured are given in Section [[EXP 1-4 Measurement Quantities and Techniques]]. The liquid used in the experiments is silicone oil (density ''&rho;'' = 920 kg/m<sup>3</sup>, kinematic viscosity ''&nu;'' = 5 &sdot; 10<sup>-6</sup> m<sup>2</sup>/s, surface tension ''&sigma;'' = 0.0177 N/m) and the ambient gas is air (density 1.2 kg/m<sup>3</sup>, kinematic viscosity 1.52 &sdot; 10<sup>-5</sup> m<sup>2</sup>/s). The film height ''h'' = 500 μm as well as the drop diameter ''D'' = 1.5 mm are kept fixed, resulting in the dimensionless film thickness ''δ'' = ''h''/''D'' = 0.33. The drop velocity ''U'' is varied from 1 to 3 m/s. Accordingly, the Weber number ''We'' = ''&rho;DU''<sup>2</sup>/''&sigma;'' is in the range 78 &ndash; 702 while the Reynolds number ''Re = DU/&nu;'' is in the range 300 &ndash; 900, see Table 1.  
</pre>
For each impact velocity a video is provided for download. The meaning of the file names is as follows: S5 = silicon oil with kinematic viscosity 5 mm<sup>2</sup>/s, D1p5 = drop diameter 1.5 mm , H500 = film height 500 µm. The digit after U denotes the drop impact velocity in m/s, e.g. U3 = 3 m/s. 


The liquid used in the experiments is silicone oil (density ''&rho;'' = 920 kg/m<sup>3</sup>, kinematic viscosity ''&nu;'' = 5 &sdot; 10<sup>-6</sup> m<sup>2</sup>/s, surface tension &sigma; = 0.0177 N/m) while the ambient gas is air (density 1.2 kg/m<sup>3</sup>, kinematic viscosity 1.52 &sdot; 10<sup>-5</sup> m<sup>2</sup>/s). The film height ''h'' = 500 μm as well as the drop diameter ''D'' = 1.5 mm are kept fixed, resulting in the dimensionless film thickness ''δ'' = ''h''/''D'' = 0.33 and the Ohnesorge number ''Oh'' = 0.03, respectively. The drop velocity is varied from 1 to 3 m/s. Accordingly, the Weber number We = is in the range 78 &ndash; 702 while the Reynolds number ''Re'' = ''We''<sup>0.5</sup>/''Oh'' is in the range 300 &ndash; 900, see the Table below.


{|class="wikitable" style="margin:auto;text-align: center"
{|class="wikitable" style="margin:auto;text-align: center"
|+ Investigated drop impact velocities
|+ Table 1: Investigated drop impact velocities
|-
|-
! Impact energy !! Impact velocity !! Weber number !! Reynolds number
! Impact energy !! Impact velocity !! Weber number !! Reynolds number !! Link for video download
|-
|-
| Low || 1 m/s || 78.0 || 300
| Low || 1 m/s || 78.0 || 300 || [[Media:S5_D1p5_H500_U1.avi|Download S5_D1p5_H500_U1]]
|-
|-
| Moderate || 2 m/s || 311.9 || 600
| Moderate || 2 m/s || 311.9 || 600 || [[Media:S5_D1p5_H500_U2.avi|Download S5_D1p5_H500_U2]]
|-
|-
| High || 3 m/s || 701.7 || 900
| High || 3 m/s || 701.7 || 900 || [[Media:S5_D1p5_H500_U3.avi|Download S5_D1p5_H500_U3]]
|}
|}


Further details on the test case can be found in the following publication:
M. Bagheri, B. Stumpf, I.V. Roisman, C. Tropea, J. Hussong, M. Wörner, H. Marschall, Interfacial relaxation – Crucial for phase-field methods to capture low to high energy drop-film impacts, Int. J. Heat Fluid Flow, 94 (2022) 108943, https://doi.org/10.1016/j.ijheatfluidflow.2022.108943


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{{ACContribs
{{ACContribs
|authors=Bastian Stumpf, Milad Bagheri, Ilia V. Roisman, Cameron Tropea, Jeanette Hussong, Martin Wörner, Holger Marschall
|authors=Milad Bagheri, Bastian Stumpf, Ilia V. Roisman, Cameron Tropea, Jeanette Hussong, Martin Wörner, Holger Marschall
|organisation=Technical University of Darmstadt and Karlsruhe Institute of Technology
|organisation=Technical University of Darmstadt and Karlsruhe Institute of Technology
}}
}}
{{EXPHeaderLib
{{EXPHeader
|area=1
|area=1
|number=4
|number=4

Latest revision as of 10:00, 17 August 2023

Axisymmetric drop impact dynamics on a wall film of the same liquid

Front Page

Introduction

Review of experimental studies

Description

Experimental Set Up

Measurement Quantities and Techniques

Data Quality and Accuracy

Measurement Data and Results

Description of Study Test Case

A sketch of the general set-up of the experiment and the geometry is shown in Fig. 3 in Section EXP 1-4 Experimental Set Up while the principal quantities measured are given in Section EXP 1-4 Measurement Quantities and Techniques. The liquid used in the experiments is silicone oil (density ρ = 920 kg/m3, kinematic viscosity ν = 5 ⋅ 10-6 m2/s, surface tension σ = 0.0177 N/m) and the ambient gas is air (density 1.2 kg/m3, kinematic viscosity 1.52 ⋅ 10-5 m2/s). The film height h = 500 μm as well as the drop diameter D = 1.5 mm are kept fixed, resulting in the dimensionless film thickness δ = h/D = 0.33. The drop velocity U is varied from 1 to 3 m/s. Accordingly, the Weber number We = ρDU2/σ is in the range 78 – 702 while the Reynolds number Re = DU/ν is in the range 300 – 900, see Table 1. For each impact velocity a video is provided for download. The meaning of the file names is as follows: S5 = silicon oil with kinematic viscosity 5 mm2/s, D1p5 = drop diameter 1.5 mm , H500 = film height 500 µm. The digit after U denotes the drop impact velocity in m/s, e.g. U3 = 3 m/s.


Table 1: Investigated drop impact velocities
Impact energy Impact velocity Weber number Reynolds number Link for video download
Low 1 m/s 78.0 300 Download S5_D1p5_H500_U1
Moderate 2 m/s 311.9 600 Download S5_D1p5_H500_U2
High 3 m/s 701.7 900 Download S5_D1p5_H500_U3





Contributed by: Milad Bagheri, Bastian Stumpf, Ilia V. Roisman, Cameron Tropea, Jeanette Hussong, Martin Wörner, Holger Marschall — Technical University of Darmstadt and Karlsruhe Institute of Technology

Front Page

Introduction

Review of experimental studies

Description

Experimental Set Up

Measurement Quantities and Techniques

Data Quality and Accuracy

Measurement Data and Results


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