Ascending non-Newtonian long drops in vertical tubes
From MaRDI portal
Publication:5041029
DOI10.1017/JFM.2022.676OpenAlexW4304943224MaRDI QIDQ5041029
D. Petrolo, Sandro Longo, L. Chiapponi, Vittorio Di Federico, Silvia Bosa
Publication date: 18 October 2022
Published in: Journal of Fluid Mechanics (Search for Journal in Brave)
Full work available at URL: https://doi.org/10.1017/jfm.2022.676
Cites Work
- Mud removal and cement placement during primary cementing of an oil well. II: Steady-state displacements
- Mud removal and cement placement during primary cementing of an oil well. Laminar non-Newtonian displacements in an eccentric annular Hele-Shaw cell
- Deposition of a viscous fluid on the wall of a tube
- Lubricated pipelining: stability of core–annular flow. Part 4. Ginzburg–Landau equations
- Bi-directional flows in constrained systems
- Interface instabilities during displacements of two miscible fluids in a vertical pipe
- The movement of single large bubbles in closed vertical tubes
- Uniaxial exchange flows of two Bingham fluids in a cylindrical duct
- Universal correlation for the rise velocity of long gas bubbles in round pipes
- The Effects of Yield Stress Variation on Uniaxial Exchange Flows of Two Bingham Fluids in a Pipe
- Bistability of buoyancy-driven exchange flows in vertical tubes
- Visco-plastic fluid displacements in near-vertical narrow eccentric annuli: prediction of travelling-wave solutions and interfacial instability
- Taylor drop in a closed vertical pipe
- Motion of a confined bubble in a shear-thinning liquid
- Effects of non-uniform rheology on the motion of bubbles in a yield-stress fluid
- Yield-stress fluid deposition in circular channels
- Gravity-driven flow of Herschel–Bulkley fluid in a fracture and in a 2D porous medium
- Modelling of gas entrainment from Taylor bubbles. Part A: Slug flow
- Instability due to Viscosity and Density Stratification in Axisymmetric Pipe Flow
This page was built for publication: Ascending non-Newtonian long drops in vertical tubes
