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Droplet impact on a highly viscous liquid basin
Zhen JIAN∗
, Guy-Jean Michon, Christophe Josserand, St´ephane Zaleski & Pascal Ray
Institut Jean Le Rond D’Alembert, CNRS & UPMC, UMR 7190, 4 place Jussieu, 75005 Paris, France
jian@dalembert.upmc.fr
Ethanol drop impacting on honey basin under different air background pressures
d0 = 3.6 ± 0.1 mm, U0 = 4 ± 0.04 m · s−1
, ∆t = 0.2ms; top: 1.01325 × 105
Pa (SAP), bottom: 21325 Pa (1/5 SAP)
Proposed numerical model
• Simulation with the code Gerris
• Variation of ρ and γ in mixed liquid area neglected
• ρ(c1) = c1ρl + (1 − c1)ρg, γ = constant
• Viscosity of the system:
µ(c1, c2) = c1c2µl2 + c1(1 − c2)µl1 + (1 − c1)µg
c1, c2: volume fraction, liquid 1, liquid 2 and gas.
• Liquid-viscosity ratio ml = µl2/µl1 (µl1: normal liquid):
measure viscosity deviation from normal liquid
• r = ρg/ρl1, m = µg/µl1: control properties of normal liquid
Numerical setup
Axisymmetric
Semi-circular drop:
normal liquid,
initial U0, without gravity
Basin:
highly-viscous liquid
VOF tracers:
T : distinguish L/S,
Tl : track drop,
Tls : track liquid basin
γ
γ
D
U0
ρl1, µl1
ρl2, µl2
ρg, µg
r
z
0
h
d
T
Tl
Tls
Physical parameters in simulations
ρ∗
l1 ρ∗
l2 ρ∗
g µ∗
l1 µ∗
l2 µ∗
g γ∗ U∗
0 D∗ d∗ h∗
1 1 0.001 0.001 0.001ml 0.0001 0.0027 1 1 0.5 0.1
Continuous transition from L/L impact to L/S impact by varying liquid-viscosity ratio ml = µl2/µl1
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.2 0.4 0.6 0.8 1 1.2 1.4
z/D
r/D
t=0
t=0.04
t=0.05
t=0.07
t=0.09
t=0.11
t=0.20
t=0.30
t=0.90
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.2 0.4 0.6 0.8 1 1.2 1.4
z/D
r/D
t=0
t=0.04
t=0.05
t=0.07
t=0.11
t=0.20
t=0.30
t=0.90
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.2 0.4 0.6 0.8 1 1.2 1.4
z/D
r/D
t=0
t=0.04
t=0.05
t=0.07
t=0.09
t=0.11
t=0.20
t=0.30
t=0.90
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.2 0.4 0.6 0.8 1 1.2 1.4
z/D
r/D
t=0
t=0.04
t=0.05
t=0.07
t=0.09
t=0.11
t=0.20
t=0.30
t=0.90
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.2 0.4 0.6 0.8 1 1.2 1.4
z/D
r/D
t=0
t=0.04
t=0.05
t=0.07
t=0.09
t=0.11
t=0.20
t=0.30
t=0.90
0
0.2
0.4
0.6
0.8
1
1.2
1.4
0 0.2 0.4 0.6 0.8 1 1.2 1.4
z/D
r/D
t=0
t=0.04
t=0.05
t=0.07
t=0.09
t=0.11
t=0.20
t=0.30
t=0.90
ml = 1 ml = 5 ml = 20 ml = 50 ml = 500 ml = 10000
Interface evolution in time for different liquid-viscosity ratio ml
Physical properties
Drops : Ethanol Basin : Honey of Acacia ml = 7407.4
Physical parameters in experiments and simulations∗
ρl ρg µethanol µhoney
R 789 kg · m−3 1 kg · m−3 0.0027 Pa · s 20 Pa · s
Dl 1 1.267 × 10−3 2.376 × 10−3 0.8802
µg γ U0 D
R 1.8444 × 10−5 Pa · s 0.0224 N · m−1 4 m · s−1 3.6 mm
Dl 1.623 × 10−6 4.929 × 10−4 1 1
∗:R denotes real parameters, Dl denotes dimensionless parameters
Manipulation setup
• Drops generated by a syringe system with different diameters.
• Stepping-motor system to insure reproducible diameter of drops.
• Drops released from rest in a vacuum chamber.
• Impact velocity controlled by changing initial falling height.
• Gas pressure in the vacuum chamber varied from ambient to low pressures by a pump system.
• Ultra-high-speed camera (Photron FASTCAM SA5 model 1000K-M1) to record impact dynamics.
• Record rate is 10000 fps ⇔ temporal distinction of 0.1 ms.
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1 2 3 4 5 6 7 8
z(mm)
r(mm)
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1 2 3 4 5 6 7 8
z(mm)
r(mm)
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1 2 3 4 5 6 7 8
z(mm)
r(mm)
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1 2 3 4 5 6 7 8
z(mm)
r(mm)
Qualitative (top and middle) and quantitative (bottom) comparison of photographs (top) with simulations (middle) of an ethanol drop impacting on a honey basin
under the standard atmospheric pressure pg = 1.01325 × 105
Pa, d0 = 3.6 mm, U0 = 4 m · s−1
, ∆t = 0.1ms
Conclusion
A numerical model is proposed to deal with the three-phase impact dynamics, of which a droplet of normal liquid impacts on a highly viscous liquid basin. Viscous effect is dominant as compared
to the inertial and surface tension effects during the dynamics. By varying liquid viscosity ratio ml = µbasin/µdroplet,normal, a continuous transition from L/L impact to L/S impact can be
achieved. For highly-viscous liquid (ml > 5000), the basin performs as a solid substrate. Experiments of ethanol drop impacting on honey basin is executed. The honey basin performs as a solid
and the complete suppression of splash by decreasing the gas pressure is observed. Agreement of the drop shapes predicted by our simulations with the experiments is encouraging.

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Sciences of Europe journal No 142 (2024)
 

Droplet impact on a highly viscous liquid basin

  • 1. Droplet impact on a highly viscous liquid basin Zhen JIAN∗ , Guy-Jean Michon, Christophe Josserand, St´ephane Zaleski & Pascal Ray Institut Jean Le Rond D’Alembert, CNRS & UPMC, UMR 7190, 4 place Jussieu, 75005 Paris, France jian@dalembert.upmc.fr Ethanol drop impacting on honey basin under different air background pressures d0 = 3.6 ± 0.1 mm, U0 = 4 ± 0.04 m · s−1 , ∆t = 0.2ms; top: 1.01325 × 105 Pa (SAP), bottom: 21325 Pa (1/5 SAP) Proposed numerical model • Simulation with the code Gerris • Variation of ρ and γ in mixed liquid area neglected • ρ(c1) = c1ρl + (1 − c1)ρg, γ = constant • Viscosity of the system: µ(c1, c2) = c1c2µl2 + c1(1 − c2)µl1 + (1 − c1)µg c1, c2: volume fraction, liquid 1, liquid 2 and gas. • Liquid-viscosity ratio ml = µl2/µl1 (µl1: normal liquid): measure viscosity deviation from normal liquid • r = ρg/ρl1, m = µg/µl1: control properties of normal liquid Numerical setup Axisymmetric Semi-circular drop: normal liquid, initial U0, without gravity Basin: highly-viscous liquid VOF tracers: T : distinguish L/S, Tl : track drop, Tls : track liquid basin γ γ D U0 ρl1, µl1 ρl2, µl2 ρg, µg r z 0 h d T Tl Tls Physical parameters in simulations ρ∗ l1 ρ∗ l2 ρ∗ g µ∗ l1 µ∗ l2 µ∗ g γ∗ U∗ 0 D∗ d∗ h∗ 1 1 0.001 0.001 0.001ml 0.0001 0.0027 1 1 0.5 0.1 Continuous transition from L/L impact to L/S impact by varying liquid-viscosity ratio ml = µl2/µl1 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 0.2 0.4 0.6 0.8 1 1.2 1.4 z/D r/D t=0 t=0.04 t=0.05 t=0.07 t=0.09 t=0.11 t=0.20 t=0.30 t=0.90 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 0.2 0.4 0.6 0.8 1 1.2 1.4 z/D r/D t=0 t=0.04 t=0.05 t=0.07 t=0.11 t=0.20 t=0.30 t=0.90 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 0.2 0.4 0.6 0.8 1 1.2 1.4 z/D r/D t=0 t=0.04 t=0.05 t=0.07 t=0.09 t=0.11 t=0.20 t=0.30 t=0.90 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 0.2 0.4 0.6 0.8 1 1.2 1.4 z/D r/D t=0 t=0.04 t=0.05 t=0.07 t=0.09 t=0.11 t=0.20 t=0.30 t=0.90 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 0.2 0.4 0.6 0.8 1 1.2 1.4 z/D r/D t=0 t=0.04 t=0.05 t=0.07 t=0.09 t=0.11 t=0.20 t=0.30 t=0.90 0 0.2 0.4 0.6 0.8 1 1.2 1.4 0 0.2 0.4 0.6 0.8 1 1.2 1.4 z/D r/D t=0 t=0.04 t=0.05 t=0.07 t=0.09 t=0.11 t=0.20 t=0.30 t=0.90 ml = 1 ml = 5 ml = 20 ml = 50 ml = 500 ml = 10000 Interface evolution in time for different liquid-viscosity ratio ml Physical properties Drops : Ethanol Basin : Honey of Acacia ml = 7407.4 Physical parameters in experiments and simulations∗ ρl ρg µethanol µhoney R 789 kg · m−3 1 kg · m−3 0.0027 Pa · s 20 Pa · s Dl 1 1.267 × 10−3 2.376 × 10−3 0.8802 µg γ U0 D R 1.8444 × 10−5 Pa · s 0.0224 N · m−1 4 m · s−1 3.6 mm Dl 1.623 × 10−6 4.929 × 10−4 1 1 ∗:R denotes real parameters, Dl denotes dimensionless parameters Manipulation setup • Drops generated by a syringe system with different diameters. • Stepping-motor system to insure reproducible diameter of drops. • Drops released from rest in a vacuum chamber. • Impact velocity controlled by changing initial falling height. • Gas pressure in the vacuum chamber varied from ambient to low pressures by a pump system. • Ultra-high-speed camera (Photron FASTCAM SA5 model 1000K-M1) to record impact dynamics. • Record rate is 10000 fps ⇔ temporal distinction of 0.1 ms. 0 0.5 1 1.5 2 2.5 3 3.5 4 0 1 2 3 4 5 6 7 8 z(mm) r(mm) 0 0.5 1 1.5 2 2.5 3 3.5 4 0 1 2 3 4 5 6 7 8 z(mm) r(mm) 0 0.5 1 1.5 2 2.5 3 3.5 4 0 1 2 3 4 5 6 7 8 z(mm) r(mm) 0 0.5 1 1.5 2 2.5 3 3.5 4 0 1 2 3 4 5 6 7 8 z(mm) r(mm) Qualitative (top and middle) and quantitative (bottom) comparison of photographs (top) with simulations (middle) of an ethanol drop impacting on a honey basin under the standard atmospheric pressure pg = 1.01325 × 105 Pa, d0 = 3.6 mm, U0 = 4 m · s−1 , ∆t = 0.1ms Conclusion A numerical model is proposed to deal with the three-phase impact dynamics, of which a droplet of normal liquid impacts on a highly viscous liquid basin. Viscous effect is dominant as compared to the inertial and surface tension effects during the dynamics. By varying liquid viscosity ratio ml = µbasin/µdroplet,normal, a continuous transition from L/L impact to L/S impact can be achieved. For highly-viscous liquid (ml > 5000), the basin performs as a solid substrate. Experiments of ethanol drop impacting on honey basin is executed. The honey basin performs as a solid and the complete suppression of splash by decreasing the gas pressure is observed. Agreement of the drop shapes predicted by our simulations with the experiments is encouraging.