E. John Hinch
Current Organizations / Institutes
The organizations/institutes from the scholar's latest article
Previous Organizations / Institutes
The organizations / institutes from the scholar's other articles in the past ten years
Research Subjects
Research Interests
E. John Hinch has a total of 125 co-authors. Here are the top co-authors by number of shared publications:
L. G. Leal
Chemical Engineering, California Institute of Technology, Pasadena
9 shared publicationsB. Perrin
CNRS, Ecole Normale Supérieure Laboratoire Pierre Aigrain, UMR 8551 Département de Physique, 24 rue Lhomond, 75231 Paris Cedex 05, France
7 shared publicationsD. Salin
Université Paris-Sud, CNRS Université Pierre et Marie Curie-Paris 6 Laboratoire FAST, Bat. 502, Campus Universitaire, Orsay, F-91405, France
7 shared publicationsÉlisabeth Guazzelli
Institut Universitaire des Systèmes Thermiques Industriels, Centre National de la Recherche Scientifique, Aix-Marseille Université, 13453 Marseille Cedex 13, France
6 shared publicationsJ.M. Rallison
Department of Applied Mathematics and Theoretical Physics|Centre for Mathematical Sciences|University of Cambridge
5 shared publicationsA. Acrivos
Levich Institute, T1-M, City College of CUNY, New York, NY 10031, USA
4 shared publications
Latest Publications
- Open Access
- 5 November 2025
- Published by Elsevier in Journal of Non-Newtonian Fluid Mechanics
- Vol. 347
Approach to a similarity solution of the lubrication flow of an Oldroyd-B fluid through a hyperbolic pipe
- 5 November 2025
- Published by Elsevier in Journal of Non-Newtonian Fluid Mechanics
- Vol. 347
Open AccessApproach to a similarity solution of the lubrication flow of an Oldroyd-B fluid through a hyperbolic pipe
- Open Access
- 31 May 2024
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 988, A11
Fast flow of an Oldroyd-B model fluid through a narrow slowly varying contraction
Lubrication theory is adapted to incorporate the large normal stresses that occur for order-one Deborah numbers, $De$ , the ratio of the relaxation time to the residence time. Comparing with the pressure drop for a Newtonian viscous fluid with a viscosity equal to that of an Oldroyd-B fluid in steady simple shear, we find numerically a reduced pressure drop through a contraction and an increased pressure drop through an expansion, both changing linearly with $De$ at high $De$ . For a constriction, there is a smaller pressure drop that plateaus at high $De$ . For a contraction, much of the change in pressure drop occurs in the stress relaxation in a long exit channel. An asymptotic analysis for high $De$ , based on the idea that normal stresses are stretched by an accelerating flow in proportion to the square of the velocity, reveals that the large linear changes in pressure drop are due to higher normal stresses pulling the fluid through the narrowest gap. A secondary cause of the reduction is that the elastic shear stresses do not have time to build up to their steady-state equilibrium value while they accelerate through a contraction. We find for a contraction or expansion that the high $De$ analysis works well for $De>0.4$ .- 31 May 2024
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 988, A11
Open AccessFast flow of an Oldroyd-B model fluid through a narrow slowly varying contraction
Lubrication theory is adapted to incorporate the large normal stresses that occur for order-one Deborah numbers, $De$ , the ratio of the relaxation time to the residence time. Comparing with the pressure drop for a Newtonian viscous fluid with a viscosity equal to that of an Oldroyd-B fluid in steady simple shear, we find numerically a reduced pressure drop through a contraction and an increased pressure drop through an expansion, both changing linearly with $De$ at high $De$ . For a constriction, there is a smaller pressure drop that plateaus at high $De$ . For a contraction, much of the change in pressure drop occurs in the stress relaxation in a long exit channel. An asymptotic analysis for high $De$ , based on the idea that normal stresses are stretched by an accelerating flow in proportion to the square of the velocity, reveals that the large linear changes in pressure drop are due to higher normal stresses pulling the fluid through the narrowest gap. A secondary cause of the reduction is that the elastic shear stresses do not have time to build up to their steady-state equilibrium value while they accelerate through a contraction. We find for a contraction or expansion that the high $De$ analysis works well for $De>0.4$ . - Open Access
- 31 May 2024
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 988, A10
Flow of an Oldroyd-B fluid in a slowly varying contraction: theoretical results for arbitrary values of Deborah number in the ultra-dilute limit
Pressure-driven flows of viscoelastic fluids in narrow non-uniform geometries are common in physiological flows and various industrial applications. For such flows, one of the main interests is understanding the relationship between the flow rate $q$ and the pressure drop $\Delta p$ , which, to date, is studied primarily using numerical simulations. We analyse the flow of the Oldroyd-B fluid in slowly varying arbitrarily shaped, contracting channels and present a theoretical framework for calculating the $q-\Delta p$ relation. We apply lubrication theory and consider the ultra-dilute limit, in which the velocity profile remains parabolic and Newtonian, resulting in a one-way coupling between the velocity and polymer conformation tensor. This one-way coupling enables us to derive closed-form expressions for the conformation tensor and the flow rate–pressure drop relation for arbitrary values of the Deborah number ( $De$ ). Furthermore, we provide analytical expressions for the conformation tensor and the $q-\Delta p$ relation in the high-Deborah-number limit, complementing our previous low-Deborah-number lubrication analysis. We reveal that the pressure drop in the contraction monotonically decreases with $De$ , having linear scaling at high Deborah numbers, and identify the physical mechanisms governing the pressure drop reduction. We further elucidate the spatial relaxation of elastic stresses and pressure gradient in the exit channel following the contraction and show that the downstream distance required for such relaxation scales linearly with $De$ .- 31 May 2024
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 988, A10
Open AccessFlow of an Oldroyd-B fluid in a slowly varying contraction: theoretical results for arbitrary values of Deborah number in the ultra-dilute limit
Pressure-driven flows of viscoelastic fluids in narrow non-uniform geometries are common in physiological flows and various industrial applications. For such flows, one of the main interests is understanding the relationship between the flow rate $q$ and the pressure drop $\Delta p$ , which, to date, is studied primarily using numerical simulations. We analyse the flow of the Oldroyd-B fluid in slowly varying arbitrarily shaped, contracting channels and present a theoretical framework for calculating the $q-\Delta p$ relation. We apply lubrication theory and consider the ultra-dilute limit, in which the velocity profile remains parabolic and Newtonian, resulting in a one-way coupling between the velocity and polymer conformation tensor. This one-way coupling enables us to derive closed-form expressions for the conformation tensor and the flow rate–pressure drop relation for arbitrary values of the Deborah number ( $De$ ). Furthermore, we provide analytical expressions for the conformation tensor and the $q-\Delta p$ relation in the high-Deborah-number limit, complementing our previous low-Deborah-number lubrication analysis. We reveal that the pressure drop in the contraction monotonically decreases with $De$ , having linear scaling at high Deborah numbers, and identify the physical mechanisms governing the pressure drop reduction. We further elucidate the spatial relaxation of elastic stresses and pressure gradient in the exit channel following the contraction and show that the downstream distance required for such relaxation scales linearly with $De$ . - 1 December 2021
- Published by Elsevier in Journal of Non-Newtonian Fluid Mechanics
- Vol. 298
Oldroyd B, and not A?
- 1 December 2021
- Published by Elsevier in Journal of Non-Newtonian Fluid Mechanics
- Vol. 298
Oldroyd B, and not A?
- 30 March 2015
- Published by National Academy of Sciences in Proceedings of the National Academy of Sciences
- Vol. 112 (15) , 4582-4587
Plethora of transitions during breakup of liquid filaments
Significance: Fluid flows, governed by nonlinear equations, permit formation of singularities. Often, singularities are artifacts of neglecting physical effects. However, free-surface flows exhibit observable singularities including filament pinch-off. As filaments thin, slightly (highly) viscous filaments are expected from theory to transition from an inertial (viscous) regime where viscosity (density) is negligible to an inertial–viscous regime where viscous and inertial effects are important. Previous works show this transition either does not occur or occurs for filament radii well below theoretical predictions. We demonstrate that thinning filaments unexpectedly pass through a number of intermediate transient regimes, thereby delaying onset of the final regime. The findings raise the question if similar dynamical transitions arise in problems that are not necessarily hydrodynamic in nature.
- 30 March 2015
- Published by National Academy of Sciences in Proceedings of the National Academy of Sciences
- Vol. 112 (15) , 4582-4587
Plethora of transitions during breakup of liquid filaments
Significance: Fluid flows, governed by nonlinear equations, permit formation of singularities. Often, singularities are artifacts of neglecting physical effects. However, free-surface flows exhibit observable singularities including filament pinch-off. As filaments thin, slightly (highly) viscous filaments are expected from theory to transition from an inertial (viscous) regime where viscosity (density) is negligible to an inertial–viscous regime where viscous and inertial effects are important. Previous works show this transition either does not occur or occurs for filament radii well below theoretical predictions. We demonstrate that thinning filaments unexpectedly pass through a number of intermediate transient regimes, thereby delaying onset of the final regime. The findings raise the question if similar dynamical transitions arise in problems that are not necessarily hydrodynamic in nature.
- 19 June 2014
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 751, 184-215
Drops of power-law fluids falling on a coated vertical fibre
We study the solitary wave solutions in a thin film of a power-law fluid coating a vertical fibre. Different behaviours are observed for shear-thickening and shear-thinning fluids. For shear-thickening fluids, the solitary waves are larger and faster when the reduced Bond number is smaller. For shear-thinning fluids, two branches of solutions exist for a certain range of the Bond number, where the solitary waves are larger and faster on one and smaller and slower on the other as the Bond number decreases. We carry out an asymptotic analysis for the large and fast-travelling solitary waves to explain how their speeds and amplitudes change with the Bond number. The analysis is then extended to examine the stability of the two branches of solutions for the shear-thinning fluids.
- 19 June 2014
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 751, 184-215
Drops of power-law fluids falling on a coated vertical fibre
We study the solitary wave solutions in a thin film of a power-law fluid coating a vertical fibre. Different behaviours are observed for shear-thickening and shear-thinning fluids. For shear-thickening fluids, the solitary waves are larger and faster when the reduced Bond number is smaller. For shear-thinning fluids, two branches of solutions exist for a certain range of the Bond number, where the solitary waves are larger and faster on one and smaller and slower on the other as the Bond number decreases. We carry out an asymptotic analysis for the large and fast-travelling solitary waves to explain how their speeds and amplitudes change with the Bond number. The analysis is then extended to examine the stability of the two branches of solutions for the shear-thinning fluids.
- 25 November 2013
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 737, 232-248
The velocity of ‘large’ viscous drops falling on a coated vertical fibre
Kalliadasis & Chang (J. Fluid Mech., vol. 261, 1994, pp. 135–168) showed within lubrication theory that if a liquid film is thicker than a critical value then drops will accelerate and grow, whereas with thinner films the drops fall at a constant velocity. As the thickness of the film increases to the critical value, the drops move faster and are larger. We revisit their asymptotic analysis of these large drops. While we recover their results for the leading-order and first correction, we do not agree on further corrections. In particular we find it necessary to evaluate the third correction, which they do not consider, before we obtain a first approximation to the dependence of the speed on the non-dimensional control parameter. We proceed to two further corrections in order to improve this first approximation to the speed.
- 25 November 2013
- Published by Cambridge University Press (CUP) in Journal of Fluid Mechanics
- Vol. 737, 232-248
The velocity of ‘large’ viscous drops falling on a coated vertical fibre
Kalliadasis & Chang (J. Fluid Mech., vol. 261, 1994, pp. 135–168) showed within lubrication theory that if a liquid film is thicker than a critical value then drops will accelerate and grow, whereas with thinner films the drops fall at a constant velocity. As the thickness of the film increases to the critical value, the drops move faster and are larger. We revisit their asymptotic analysis of these large drops. While we recover their results for the leading-order and first correction, we do not agree on further corrections. In particular we find it necessary to evaluate the third correction, which they do not consider, before we obtain a first approximation to the dependence of the speed on the non-dimensional control parameter. We proceed to two further corrections in order to improve this first approximation to the speed.
- 15 May 2013
- Published by Springer Nature in Journal of Engineering Mathematics
- Vol. 84 (1) , 41-48
Particles impacting on a granular bed
- 15 May 2013
- Published by Springer Nature in Journal of Engineering Mathematics
- Vol. 84 (1) , 41-48
Particles impacting on a granular bed
- 5 July 2012
- Published by American Physical Society (APS) in Physical Review E
- Vol. 86 (1) , 015301
Self-similar breakup of near-inviscid liquids
The final stages of pinchoff and breakup of dripping droplets of near-inviscid Newtonian fluids are studied experimentally for pure water and ethanol. High-speed imaging and image analysis are used to determine the angle and the minimum neck size of the cone-shaped extrema of the ligaments attached to dripping droplets in the final microseconds before pinchoff. The angle is shown to steadily approach the value of 18.0 \ifmmode\pm\else\textpm\fi{}0.4$\circ${}, independently of the initial flow conditions or the type of breakup. The filament thins and necks following a $\tau${}2/3 law in terms of the time remaining until pinchoff, regardless of the initial conditions. The observed behavior confirms theoretical predictions.
- 5 July 2012
- Published by American Physical Society (APS) in Physical Review E
- Vol. 86 (1) , 015301
Self-similar breakup of near-inviscid liquids
The final stages of pinchoff and breakup of dripping droplets of near-inviscid Newtonian fluids are studied experimentally for pure water and ethanol. High-speed imaging and image analysis are used to determine the angle and the minimum neck size of the cone-shaped extrema of the ligaments attached to dripping droplets in the final microseconds before pinchoff. The angle is shown to steadily approach the value of 18.0 \ifmmode\pm\else\textpm\fi{}0.4$\circ${}, independently of the initial flow conditions or the type of breakup. The filament thins and necks following a $\tau${}2/3 law in terms of the time remaining until pinchoff, regardless of the initial conditions. The observed behavior confirms theoretical predictions.
- 14 June 2012
- Published by Springer Nature in The European Physical Journal E
- Vol. 35 (6) , 1-8
Tackiness and cohesive failure of granular pastes: Mechanistic aspects
Granular pastes are dense dispersions of non-colloidal grains in a simple or a complex fluid. Typical examples are the coating, gluing or sealing mortars used in building applications. We study the rupture of a thick layer of mortar paste in a simple pulling test where the paste is confined between two flat surfaces. It is shown that, depending on the rheological properties of the paste and the plate separation velocity, two main failure modes are obtained. The first mode is the inwards shear flow of the paste with viscous fingering instabilities, similarly to what has been observed with Newtonian fluids and with non-Newtonian colloidal suspensions or polymer solutions. The second failure mode is stemming from the expansion of bubbles, similarly to what has been observed in soft adhesive polymer layers and, more recently, in highly viscous fluids. It is shown that the crossover between the two failure modes is determined by the conditions required to generate a pressure drop able to trigger the growth of pre-existing micro-bubbles smaller than the inter-granular distance.
- 14 June 2012
- Published by Springer Nature in The European Physical Journal E
- Vol. 35 (6) , 1-8
Tackiness and cohesive failure of granular pastes: Mechanistic aspects
Granular pastes are dense dispersions of non-colloidal grains in a simple or a complex fluid. Typical examples are the coating, gluing or sealing mortars used in building applications. We study the rupture of a thick layer of mortar paste in a simple pulling test where the paste is confined between two flat surfaces. It is shown that, depending on the rheological properties of the paste and the plate separation velocity, two main failure modes are obtained. The first mode is the inwards shear flow of the paste with viscous fingering instabilities, similarly to what has been observed with Newtonian fluids and with non-Newtonian colloidal suspensions or polymer solutions. The second failure mode is stemming from the expansion of bubbles, similarly to what has been observed in soft adhesive polymer layers and, more recently, in highly viscous fluids. It is shown that the crossover between the two failure modes is determined by the conditions required to generate a pressure drop able to trigger the growth of pre-existing micro-bubbles smaller than the inter-granular distance.