Access the full text.
Sign up today, get DeepDyve free for 14 days.
Loading next page...
/lp/wiley/design-parameters-estimation-for-scale-up-of-high-pressure-bubble-1EvxzXl4eK
References (43)
-
Wilkinson Wilkinson, van Dierendonck van Dierendonck (1990a)
Pressure and Gas Density Effects on Bubble Breakup and Gas Holdup in Bubble ColumnsChem. Eng. Sci., 45
-
Cho Cho, Wakao Wakao (1988)
Determination of Liquid‐Side and Gas‐Side Volumetric Mass Transfer Coefficient in a Bubble ColumnJ. Chem. Eng. Jap., 21
-
Joshi Joshi (1982)
Gas‐Phase Dispersion in Bubble ColumnsChem. Eng. J., 24
-
Walter Walter, Blanch Blanch (1986)
Bubble Breakup in Gas‐Liquid Bioreactors: Breakup in Turbulent FlowsChem. Eng. Sci., 32
-
Zahradník Zahradník, Kaštánek Kaštánek, Kratochvíl Kratochvíl (1982)
Hydrodynamics and Mass Transfer in Uniformly Aerated Bubble Column ReactorsCollection Czechoslovak Chem. Commun., 47
-
Kelkar Kelkar, Phulgaonkar Phulgaonkar, Shah Shah (1983)
The Effect of Electrolyte Solutions on Hydrodynamics and Backmixing Characteristics in Bubble ColumnsChem. Eng. J., 27
-
Guy Guy, Carreau Carreau, Paris Paris (1986)
Mixing Characteristics and Gas Holdup of a Bubble ColumnCan. J. Chem. Eng., 64
-
Godbole Godbole, Honath Honath, Shah Shah (1982)
Holdup Structure in Highly Viscous Newtonian and Non‐Newtonian Liquids in Bubble ColumnsChem. Eng. Commun., 16
-
Idogawa Idogawa, Ikeda Ikeda, Fukuda Fukuda, Morooka Morooka (1985)
Effect of Gas and Liquid Properties on the Behavior of Bubbles in a Bubble Column under High PressureKag. Kog. Ronb., 11
-
Bach Bach, Pilhofer Pilhofer (1978)
Variation of Gas Holdup in Bubble Columns with Physical Properties of Liquids and Operating Parameters of ColumnsGer. Chem. Eng., 1
-
Deckwer Deckwer, Louisi Louisi, Zaidi Zaidi, Ralek Ralek (1980)
Hydrodynamic Properties of the Fischer‐Tropsch Slurry ProcessInd. Eng. Chem. Process Des. Dev., 19
-
Khare Khare, Joshi Joshi (1990)
Effect of Fine Particles on Gas Holdup in Three‐Phase Sparged ReactorsChem. Eng. J., 44
-
Kürten Kürten (1982)
Verfahrenstechnik der Kohlehydrierung in Sumpfphasen‐ReaktorenChem. Ing. Techn., 54
-
Mashelkar Mashelkar (1970)
Bubble ColumnsBrit. Chem. Eng., 15
-
Mangartz Mangartz, Pilhofer Pilhofer (1980)
Untersuchungen zur Gasphasendispersion in Blasensäulen ReaktorenVerfahrenstechnik, 14
-
Zou Zou, Jiang Jiang, Li Li, Zu Zu, Zhang Zhang (1988)
Studies on Gas Holdup in a Bubble Column Operated at Elevated TemperaturesInd. Eng. Chem. Res., 27
-
Idogawa Idogawa, Ikeda Ikeda, Fukuda Fukuda, Morooka Morooka (1986)
Behavior of Bubbles of the Air‐Water System in a Column under High PressureInt. Chem. Eng., 26
-
Pandit Pandit, Joshi Joshi (1984)
Three‐Phase Sparged Reactors—Some Design AspectsRev. Chem. Eng., 2
-
Yoshida Yoshida, Akita Akita (1965)
Performance of Gas Bubble Columns: Volumetric Liquid‐Phase Mass Transfer Coefficient and Gas HoldupAIChE J., 11
-
de Bruijn de Bruijn, Chase Chase, Dawson Dawson (1988)
Gas Holdup in a Two‐Phase Vertical Tubular Reactor at High PressureCan. J. Chem. Eng., 66
-
Blum Blum, Toman Toman (1978)
Three‐Phase Fluidization in a Liquid‐Phase MethanatorAIChE Symp. Ser., 73
-
Hills Hills (1976)
The Operation of a Bubble Column at High Throughputs: I. Gas Holdup MeasurementsChem. Eng. J., 12
-
Krishna Krishna, Wilkinson Wilkinson, van Dierendonck van Dierendonck (1991)
A Model for Gas Holdup in Bubble Columns Incorporating the Influence of Gas Density on Flow Regime TransitionsChem. Eng. Sci., 46
-
Hikita Hikita, Asai Asai, Tanigawa Tanigawa, Segawa Segawa, Kitao Kitao (1981)
The Volumetric Liquid‐Phase Mass Transfer Coefficient in Bubble ColumnsChem. Eng. J., 22
-
Shah Shah, Kelkar Kelkar, Deckwer Deckwer (1982)
Design Parameters Estimation for Bubble Column ReactorsALChE J., 28
-
Clark Clark (1990)
The Effect of High Pressure and Temperature on Phase Distribution in a Bubble ColumnChem. Eng. Sci., 45
-
Deckwer Deckwer (1976)
Nonisobaric Bubble Columns with Variable Gas VelocityChem. Eng. Sci., 31
-
Idogawa Idogawa, Ikeda Ikeda, Fukuda Fukuda, Morooka Morooka (1987b)
Formation and Flow of Gas Bubbles in a Bubble Column with a Single Orifice or Nozzle Gas DistributorChem. Eng. Commun., 59
-
Akita Akita, Yoshida Yoshida (1974)
Bubble Size, Interfacial Area, and Liquid‐Phase Mass Transfer Coefficient in Bubble ColumnsInd. Eng. Chem. Proc. Des. Dev., 13
-
Reilly Reilly, Scott Scott, de Bruijn de Bruijn, Jain Jain, Diskorz Diskorz (1986)
Correlation for Gas Holdup in Turbulent Coalescing Bubble ColumnsCan. J. Chem. Eng., 64
-
Akita Akita, Yoshida Yoshida (1973)
Gas Holdup and Volumetric Mass Transfer Coefficient in Bubble ColumnsInd. Eng. Chem. Proc. Des. Dev., 12
-
Idogawa Idogawa, Ikeda Ikeda, Fukuda Fukuda, Morooka Morooka (1987a)
Effect of Gas and Liquid Properties on the Behavior of Bubbles in a Bubble Column under High PressureInt. Chem. Eng., 27
-
Hikita Hikita, Asai Asai, Tanigawa Tanigawa, Segawa Segawa, Kitao Kitao (1980)
Gas Holdup in Bubble ColumnsChem. Eng. J., 20
-
Wilkinson Wilkinson, van Dierendonck van Dierendonck (1990b)
Comments on Studies on Gas Holdup in a Bubble Column Operated at Elevated TemperaturesInd. Eng. Chem. Res., 29
-
Crabtree Crabtree, Bridgwater Bridgwater (1971)
Bubble Coalescence in Viscous LiquidsChem. Eng. Sci., 26
-
Otake Otake, Tone Tone, Nakao Nakao, Mitsuhashi Mitsuhashi (1977)
Coalescence and Breakup of Bubbles in LiquidsChem. Eng. Sci., 32
-
Brown Brown (1984)
Modeling of Methanol Synthesis in the Liquid PhaseInst. Chem. Eng. Symp. Ser., 87
-
Tarmy Tarmy, Chang Chang, Coulaloglou Coulaloglou, Ponzi Ponzi (1984)
The Three‐Phase Hydrodynamic Characteristics of the EDS Coal Liquefaction Reactors: Their Development and Use in Reactor ScaleUpInst. Chem. Eng. Symp. Ser., 87
-
Argo Argo, Cova Cova (1965)
Longitudinal Mixing in Gas‐Sparged Tubular VesselsInd. Eng. Chem. Proc. Des. Dev., 4
-
Pandit Pandit, Joshi Joshi (1986)
Mass and Heat Transfer Characteristics of Three‐Phase Sparged ReactorsChem. Eng. Res. Des., 64
-
Otake Otake, Tone Tone, Shinohara Shinohara (1981)
Gas Holdup in the Bubble Column with Cocurrent and Countercurrent Gas‐Liquid FlowJ. Chem. Eng. Jap., 14
-
Petukhov Petukhov, Kolokol'tsev Kolokol'tsev (1965)
Effect of Liquid Viscosity on Droplet Entrainment and Volumetric Air ContentTherm. Eng., 12
-
Calderbank Calderbank, Moo‐Young Moo‐Young (1961)
The Continuous‐Phase Heat and Mass‐Transfer Properties of DispersionsChem. Eng. Sci., 16
- Publisher
- Wiley
- Copyright
- Copyright © 1992 American Institute of Chemical Engineers
- ISSN
- 0001-1541
- eISSN
- 1547-5905
- DOI
- 10.1002/aic.690380408
- Publisher site
- See Article on Publisher Site
Abstract
Experiments were carried out in bubble columns for a number of liquids at pressures between 0.1 and 2.0 MPa for two column sizes. Based on the experimental results as well as extensive literature data, the extent of the effect column dimensions have on gas holdup were determined, both at low and high pressures (which is of importance to scale‐up). It was also demonstrated that none of the published empirical gas holdup equations incorporate the influence of gas density accurately. Therefore, a new improved gas hold‐up equation is developed that incorporates the influence of gas and liquid properties with an average error of approximately 10%. Finally, it is also discussed to what extent theinfluence of pressure on other important design parameters such as the interfacial area, the liquid volumetric mass transfer coefficient, and gas and liquid mixing, can be estimated on the basis of empirical equations.
Journal
Aiche Journal – Wiley
Published: Apr 1, 1992