Abstract:Short liquid bridges are stable under the action of surface tension. In applications like electronic packaging, food engineering, and additive manufacturing, this poses challenges to the clean and fast dispensing of viscoelastic fluids. Here, we investigate how viscoelastic liquid bridges can be destabilized by torsion. By combining high-speed imaging and numerical simulation, we show that concave surfaces of liquid bridges can localize shear, in turn localizing normal stresses and making the surface more conc… Show more
“…Edge fracture is a flow instability characterized by the sudden indentation of the fluid's free surface when a viscoelastic fluid is sheared at above a certain critical shear rate. 17–24 Historically, Tanner and Keentok 18 first realized that the second normal stress difference N 2 is important in driving edge fracture. By assuming a semicircular indent of radius a in a second-order fluid with surface tension σ , they derived a criterion of edge fracture which reads | N 2 | > 2 σ /3 a .…”
Section: Resultsmentioning
confidence: 99%
“…The second way is to define two additional dimensionless parameters, namely, the elastocapillary number Ec and the recently introduced Tanner number Tn. 17 The elastocapillary number Ec ≡ Wi/Ca = λσ / ηR characterizes the combined importance of elastic stress and capillary stress as compared to viscous stress. The Tanner number Tn ≡ WiCa = ληRΩ 2 / σ characterizes the relative importance of torsion-induced normal stress and capillary stress.…”
Section: Dimensional Analysismentioning
confidence: 99%
“…In this work, we take a step further and show that torsion can effectively destabilize liquid bridges made of constant viscosity elastic liquid (Boger fluid) as well. The Boger fluid we used has a relaxation time of λ ∈ O (1 s), which is 1000 times larger than that of the silicone oil used by Chan et al 17 Hence, elastocapillarity is expected to play a much more pivotal role in the liquid bridge deformation process. In fact, deformation of the liquid bridge under torsion depends on how the elastocapillary effect competes with the torsion-induced normal stress effect.…”
Section: Introductionmentioning
confidence: 99%
“…Recently, Chan et al 17 propose that the aforementioned two drawbacks of the elongation method can be overcome using torsion, i.e. , rotating one end of the viscoelastic liquid bridge while keeping the other end fixed.…”
Section: Introductionmentioning
confidence: 99%
“…Using a viscoelastic silicone oil with a characteristic relaxation time of λ ∈ O (1 ms) as the model fluid, they show that when the liquid bridge is subjected to torsion it undergoes edge fracture, a flow instability characterized by the sudden indentation of the fluid's free surface when a viscoelastic fluid is sheared at above a critical rate. 17–24 The indent caused by the viscoelastic stresses propagates towards the vertical centerline of the liquid bridge, which creates a horizontal cut and causes the bridge radius to undergo power-law decay, hence resulting in the clean and quick breakup of the liquid bridge.…”
“…Edge fracture is a flow instability characterized by the sudden indentation of the fluid's free surface when a viscoelastic fluid is sheared at above a certain critical shear rate. 17–24 Historically, Tanner and Keentok 18 first realized that the second normal stress difference N 2 is important in driving edge fracture. By assuming a semicircular indent of radius a in a second-order fluid with surface tension σ , they derived a criterion of edge fracture which reads | N 2 | > 2 σ /3 a .…”
Section: Resultsmentioning
confidence: 99%
“…The second way is to define two additional dimensionless parameters, namely, the elastocapillary number Ec and the recently introduced Tanner number Tn. 17 The elastocapillary number Ec ≡ Wi/Ca = λσ / ηR characterizes the combined importance of elastic stress and capillary stress as compared to viscous stress. The Tanner number Tn ≡ WiCa = ληRΩ 2 / σ characterizes the relative importance of torsion-induced normal stress and capillary stress.…”
Section: Dimensional Analysismentioning
confidence: 99%
“…In this work, we take a step further and show that torsion can effectively destabilize liquid bridges made of constant viscosity elastic liquid (Boger fluid) as well. The Boger fluid we used has a relaxation time of λ ∈ O (1 s), which is 1000 times larger than that of the silicone oil used by Chan et al 17 Hence, elastocapillarity is expected to play a much more pivotal role in the liquid bridge deformation process. In fact, deformation of the liquid bridge under torsion depends on how the elastocapillary effect competes with the torsion-induced normal stress effect.…”
Section: Introductionmentioning
confidence: 99%
“…Recently, Chan et al 17 propose that the aforementioned two drawbacks of the elongation method can be overcome using torsion, i.e. , rotating one end of the viscoelastic liquid bridge while keeping the other end fixed.…”
Section: Introductionmentioning
confidence: 99%
“…Using a viscoelastic silicone oil with a characteristic relaxation time of λ ∈ O (1 ms) as the model fluid, they show that when the liquid bridge is subjected to torsion it undergoes edge fracture, a flow instability characterized by the sudden indentation of the fluid's free surface when a viscoelastic fluid is sheared at above a critical rate. 17–24 The indent caused by the viscoelastic stresses propagates towards the vertical centerline of the liquid bridge, which creates a horizontal cut and causes the bridge radius to undergo power-law decay, hence resulting in the clean and quick breakup of the liquid bridge.…”
We study the injection flow of a heavy viscoplastic fluid into a light Newtonian fluid, via modelling and experiments. The injection is carried out downward, via an eccentric inner pipe inside a vertical closed-end outer pipe. This configuration results in a core viscoplastic fluid surrounded by an annular Newtonian fluid. The flow is structured and mixing is negligible. As the injection rate increases in a typical experiment, we observe three distinct flow regimes, associated with the core fluid behaviour, namely the breakup, coiling and buckling (bulging) regimes. In the breakup regime, the core fluid is yielded due to the extension caused by buoyancy, while in the buckling regime the yielding occurs due to the compression promoted by the pressure and the interfacial shear stress applied by the upward flow of the annular fluid. For the coiling regime, the core fluid remains largely unyielded until it exhibits a coiling behaviour. We develop a lubrication approximation model, using the Herschel–Bulkley constitutive equation, with dimensionless flow parameters including the Bingham number, the power-law index, the buoyancy number, the viscosity ratio, the diameter ratio, the eccentricity and the aspect ratio. Based on a reasonable prediction to the yielding onset, the model allows us to classify the flow regimes versus an elegant combination of the dimensionless numbers.
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