Hydrodynamics of Taylor Flow in Vertical Capillaries: Flow Regimes, Bubble Rise Velocity, Liquid Slug Length, and Pressure Drop
- 16 December 2004
- journal article
- Published by American Chemical Society (ACS) in Industrial & Engineering Chemistry Research
- Vol. 44 (14), 4884-4897
- https://doi.org/10.1021/ie049307n
Abstract
No abstract availableKeywords
This publication has 40 references indexed in Scilit:
- Using monolithic catalysts for highly selective Fischer–Tropsch synthesisCatalysis Today, 2003
- Multiphase catalytic reactors: a perspective on current knowledge and future trendsCatalysis Reviews, 2002
- Pressure drop characteristics of gas–liquid two-phase flow in vertical miniature triangular channelsInternational Journal of Heat and Mass Transfer, 2001
- Two-phase pressure drop of air–water and R-410A in small horizontal tubesInternational Journal of Multiphase Flow, 2001
- Co-current air–water two-phase flow patterns in vertical triangular microchannelsInternational Journal of Multiphase Flow, 2001
- Characterization of two-phase flow patterns in small diameter round and rectangular tubesInternational Journal of Heat and Mass Transfer, 1999
- Effect of bubble shape on pressure drop calculations in vertical slug flowInternational Journal of Multiphase Flow, 1990
- Scaling up of a monolithic catalyst reactor with two-phase flowIndustrial & Engineering Chemistry Research, 1989
- Performance of a honeycomb monolith bioreactor in a gas-liquid-solid three-phase systemIndustrial & Engineering Chemistry Research, 1989
- Flow regime transition criteria for upward two-phase flow in vertical tubesInternational Journal of Heat and Mass Transfer, 1984