EXP 1-4 Description: Difference between revisions

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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.  
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.  


For each impact velocity a video is provided for download in Table 1. The meaning of the file names is as follows: S5 = silicon oil viscosity 5 mm^2/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 = 3m/s.   
For each impact velocity a video is provided for download in Table 1. The meaning of the file names is as follows: S5 = silicon oil viscosity 5 mm^2/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.   


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Revision as of 12:42, 1 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 Lib:EXP 1-4 Experimental Set Up while the principal quantities measured are given in Section Lib: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.

For each impact velocity a video is provided for download in Table 1. The meaning of the file names is as follows: S5 = silicon oil viscosity 5 mm^2/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 Video for 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


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




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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