Relevant bibliographies by topics / Bubble column reactor

Contents

  1. Journal articles
  2. Dissertations / Theses
  3. Books
  4. Book chapters
  5. Conference papers
  6. Reports

Academic literature on the topic 'Bubble column reactor'

Author: Grafiati
Published: 4 June 2021
Last updated: 15 June 2025

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Journal articles on the topic "Bubble column reactor"

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Ning, Chen, and Fang Bing Wang. "Numerical Simulation of Hydrodynamics in Slurry Bubble Column Reactor." Applied Mechanics and Materials 303-306 (February 2013): 2679–82. http://dx.doi.org/10.4028/www.scientific.net/amm.303-306.2679.

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Gas dispersion and solid suspension in industrial size slurry bubble column reactors for producing sodium dichromate are simulated numerically by using of computational fluid dynamics (CFD). The Eulerian multi-fluid model and standard k-ε turbulence model are used to describe the flow behavior in bubble columns. The simulated results show that gas is easy to flow toward the centre of the bubble column and in relatively high local gas holdup there. Installing gas-re-distributors in the bubble column is favorable for gas dispersion. Solid suspension in the bubble columns under the operating cond
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Arunkumar, S., V. Harshavardhan Reddy, T. M. Sreevathsav, and M. Venkatesan. "Hydrodynamic Study of Bubbles in a Bubble Column Reactor Part II – Numerical Study." Applied Mechanics and Materials 813-814 (November 2015): 1023–27. http://dx.doi.org/10.4028/www.scientific.net/amm.813-814.1023.

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The present work deals with the use of CFD analysis and the validation of the experimental work carried out on the artificial splitting of an air bubble in a bubble column reactor. In Part I of this work, artificial splitting of bubble in a bubble column rector is experimentally studied by using a high speed camera. Image processing technique was used to identify bubble size and bubble velocity. In present work CFD simulations are carried out using ANSYS FLUENT software using Volume of Fluids (VOF) method. VOF is based on a surface tracking technique applied to a fixed Eulerian space. The phas
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Hammond, Keren Naa Merley, Kofi Aduhene Bosumbru, Kelvin Aduse-Poku, and Kwame Sarkodie. "Flow regime dynamics in a bubble column reactor." Journal of the Ghana Institution of Engineering (JGhIE) 24, no. 3 (2024): 9–20. https://doi.org/10.56049/jghie.v24i3.215.

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This study investigates fluid dynamics within bubble column reactors. Using an air-water system, flow regimes were generated and assessed using predictive models such as homogenous, Armand, and drift flux models. This study highlights the complexities of two-phase fluid flow, particularly focusing on the dynamic behaviours of fluids and bubbles within the column reactor. The experimental setup consisted of a transparent test section, utilizing advanced image processing techniques to accurately determine gas holdups and their relationship with superficial velocities. The results show that the H
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Hadavand, Laleh, and Ali Fadavi. "Effect of Vibrating Sparger on Mass Transfer, Gas Holdup, and Bubble Size in a Bubble Column Reactor." International Journal of Chemical Reactor Engineering 11, no. 1 (2013): 47–56. http://dx.doi.org/10.1515/ijcre-2012-0094.

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Abstract Bubble size has a key role in gas holdup and mass transfer in bubble column reactors. In order to have small and uniform bubbles, a new structure was designed; the reactor operates in two modes, with vibrating sparger and conventional bubble column in which sparger is fixed. In vibrating mode, the sparger vibrates gently during gas entering. The vibrating sparger performs like a paddle, resulting in a forced recirculation of gas–liquid inside the reactor; moreover, the bubble detachment is accelerated. The superficial gas velocity was between 0.003 and 0.013 ms− 1, and the vibration f
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Kováts, P., and K. Zähringer. "Statistical Analysis of Bubble Parameters from a Model Bubble Column with and without Counter-Current Flow." Fluids 9, no. 6 (2024): 126. http://dx.doi.org/10.3390/fluids9060126.

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Bubble columns are widely used in numerous industrial processes because of their advantages in operation, design, and maintenance compared to other multiphase reactor types. In contrast to their simple design, the generated flow conditions inside a bubble column reactor are quite complex, especially in continuous mode with counter-current liquid flow. For the design and optimization of such reactors, precise numerical simulations and modelling are needed. These simulations and models have to be validated with experimental data. For this reason, experiments were carried out in a laboratory-scal
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Naveen, S., T. Sriram, S. Prithvi Raj, and M. Venkatesan. "Hydrodynamic Study of Bubbles in a Bubble Column Reactor Part I – Image Processing." Applied Mechanics and Materials 813-814 (November 2015): 1018–22. http://dx.doi.org/10.4028/www.scientific.net/amm.813-814.1018.

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The study of bubble column reactors has its significance in applications such as multiphase reactors, aerators and in industrial waste-water treatment. Extensive works has been done in studying the hydrodynamics of a single gas bubble flowing through stationary liquid phase. The natural breakup of bubble during its motion has been studied in the past. In the Part I of the present work, hydrodynamics of an air bubble after its artificial splitting using a stainless steel mesh is experimentally studied using image processing and high speed photography. The significance of bubble splitting is tha
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Popa, Simona, Andra Tamas, Vasile Simulescu, Dorin Jurcau, Sorina Boran, and Giannin Mosoarca. "A Novel Approach of Bioesters Synthesis through Different Technologies by Highlighting the Lowest Energetic Consumption One." Polymers 13, no. 23 (2021): 4190. http://dx.doi.org/10.3390/polym13234190.

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Fatty acids esters have a wide application as bioplasticizers and biolubricants in different industries, obtained mainly in classic batch reactors, through an equilibrium complex reaction, that involves high temperatures, long reaction times, vigorously stirring, and much energy consumption. To overcome these shortcomings, we synthesized a series of fatty acid esters (soybean oil fatty acids being the acid components with various hydroxyl compounds) through novel low energy consumption technologies using a bubble column reactor, a microwave field reactor and for comparison meaning, a classic b
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Alattar, Saja A., Khalid A. Sukkar, and May A. Alsaffar. "The role of TiO2 NPs catalyst and packing material in removal of phenol from wastewater using an ozonized bubble column reactor." Acta Innovations, no. 46 (November 4, 2022): 93–105. http://dx.doi.org/10.32933/actainnovations.46.7.

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Phenol is present as a highly toxic pollutant in wastewater, and it has a dangerous impact on the environment. In the present research, the phenol removal from wastewater has been achieved using four treatment methods in a bubble column reactor (treatment by ozone only, using packed bubble column reactor with ozone, utilizing ozone with TiO2 NPs catalyst in the reactor without packing, and employing ozone with TiO2 NPs in the presence of packing). The effects of phenol concentration, ozone dosage, TiO2 NPs additions, and contact time on the phenol removal efficiency were determined. It was fou
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Mohagheghian, Shahrouz, Afshin J. Ghajar, and Brian R. Elbing. "Effect of Vertical Vibration on the Mixing Time of a Passive Scalar in a Sparged Bubble Column Reactor." Fluids 5, no. 1 (2020): 6. http://dx.doi.org/10.3390/fluids5010006.

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The present study used a sparged bubble column to study the mixing of a passive scalar under bubble-induced diffusion. The effect of gas superficial velocity (up to 69 mm/s) and external vertical vibrations (amplitudes up to 10 mm, frequency <23 Hz) on the mixing time scale were investigated. The bubble-induced mixing was characterized by tracking the distribution of a passive scalar within a sparged swarm of bubbles. Void fraction and bubble size distribution were also measured at each test condition. Without vibrations (static), the bubble column operated in the homogenous regime and the
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Yavorskyy, Alexander, Oksana Shvydkiv, Carolin Limburg, Kieran Nolan, Yan M. C. Delauré, and Michael Oelgemöller. "Photooxygenations in a bubble column reactor." Green Chemistry 14, no. 4 (2012): 888. http://dx.doi.org/10.1039/c2gc16439f.

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Dissertations / Theses on the topic "Bubble column reactor"

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Cox, Shane Joseph Chemical Sciences &amp Engineering Faculty of Engineering UNSW. "Design and analysis of a photocatalytic bubble column reactor." Awarded by:University of New South Wales, 2007. http://handle.unsw.edu.au/1959.4/37818.

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The current work has developed a CFD model to characterise a pseudo-annular photocatalytic bubble column reactor. The model development was divided into three stages. Firstly, hydrodynamic assessment of the multiphase fluid flow in the vessel, which incorporated residence time distribution analysis both numerically and experimentally for validation purposes. Secondly, the radiation distribution of the UV source was completed. The final stage incorporated the kinetics for the degradation the model pollutant, sodium oxalate. The hydrodynamics were modelled using an Eulerian-Eulerian approach to
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Goraki, Fard Mojtaba. "CFD Modeling of Multiphase Turbulent Flows in a Bubble Column Reactor." Doctoral thesis, Universitat Rovira i Virgili, 2020. http://hdl.handle.net/10803/670965.

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Aquest treball presenta l'estudi numèric de fluxos turbulents bifàssics en un reactor de columna de bombolles en 3D utilitzant diferents models a diferents escales. En primer lloc se centra en la hidrodinàmica, las transicions del règim de flux i la transferència de massa utilitzant el model de barreja Euler-Euler k-ε per amplis rangs de velocitats superficials de gas. S'ha posat èmfasi en avaluar el rendiment d'aquest model i l'anàlisi de les transicions del règim de flux i el comportament del flux transitori dins del reactor de columna de bombolles. Es presenta la quantificació de les forces
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Cloete, Jannean Christelle. "Oxygen transfer in a model hydrocarbon bioprocess in a bubble column reactor." Thesis, Stellenbosch : Stellenbosch University, 2015. http://hdl.handle.net/10019.1/96981.

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Thesis (MEng)--Stellenbosch University, 2015.<br>ENGLISH ABSTRACT: The expansion of the global fuels industry has caused an increase in the quantity of hydrocarbons produced as a by-product of refinery gas-to-liquid processes. Conversion of hydrocarbons to higher value products is possible using bioprocesses, which are sustainable and environmentally benign. Due to the deficiency of oxygen in the alkane molecule, the supply of sufficient oxygen through aeration is a major obstacle for the optimization of hydrocarbon bioprocesses. While the oxygen solubility is increased in the presence o
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Studley, Allison F. "Numerical Modeling of Air-Water Flows in Bubble Columns and Airlift Reactors." Thesis, Virginia Tech, 2010. http://hdl.handle.net/10919/36380.

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Bubble columns and airlift reactors were modeled numerically to better understand the hydrodynamics and analyze the mixing characteristics for each configuration. An Eulerian-Eulerian approach was used to model air as the dispersed phase within a continuous phase of water using the commercial software FLUENT. The Schiller-Naumann drag model was employed along with virtual mass and the standard k-e turbulence model. The equations were discretized using the QUICK scheme and solved with the SIMPLE coupling algorithm. The flow regimes of a bubble column were investigated by varying the column diam
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Lefebvre, Jonathan [Verfasser]. "Three-phase CO2 methanation Methanation reaction kinetics and transient behavior of a slurry bubble column reactor / Jonathan Lefebvre." München : Verlag Dr. Hut, 2019. http://d-nb.info/1181515408/34.

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Lefebvre, Jonathan [Verfasser]. "Three-phase CO$_2}$ methanation: methanation reaction kinetics and transient behavior of a slurry bubble column reactor / Jonathan Lefebvre." Karlsruhe : KIT-Bibliothek, 2019. http://d-nb.info/1187343382/34.

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Adetunji, Olubode Caleb. "Hybridization of electrical resistance tomography to population balance model for accurate bubble column reactor hydrodynamic parameter predictions." Doctoral thesis, University of Cape Town, 2016. http://hdl.handle.net/11427/22979.

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A novel approach of obtaining bubble size and spatial distribution is developed by hybridising techniques of Electrical Resistance Tomography and the Gas Disengagement Technique using a Population Balance as a framework. As a result, detailed hydrodynamic predictions suitable for Bubble Column Reactor [BER] optimisation results with minimal computing effort. Electrical Resistance Tomography [ERT] is a technique for creating 3D images of objects occurring in space. The images are obtained through current stimulations through a body surface electrodes and measurements of resulting voltage signal
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Qazaq, Amjad Saleh Hussein Chemical Sciences &amp Engineering Faculty of Engineering UNSW. "Application of photocatalysis to the treatment of complex industrial aqueous effluent in a pilot-scale bubble column reactor." Awarded by:University of New South Wales. Chemical Sciences & Engineering, 2009. http://handle.unsw.edu.au/1959.4/44774.

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In this study, the photocatalytic mineralization of the industrial dump-site leachate was evaluated using an internally-irradiated 18-Litre pilot-scale aerated annular bubble column photoreactor. The study includes evaluating the effect of catalyst loading, leachate initial concentration, initial solution pH, light intensity and oxygen partial pressure. The reaction runs were performed over a 48-hours period at room temperature and atmospheric pressure. Titanium catalyst loading was optimized to be 3 gL-1 where the reaction rate constant 20x10-6 mol L-1 min-1.Beyond this dosage, the effect of
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Sarah, Oddy. "Effect of Phase-Contacting Patters and Operating Conditions on Gas Hydrate Formation." Thesis, Université d'Ottawa / University of Ottawa, 2014. http://hdl.handle.net/10393/31414.

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Research into hydrate production technologies has increased in the past years. While many technologies have been presented, there is no consensus on which reactor design is best for each potential application. A direct experimental comparison of hydrate production technologies has been carried out in between a variety of reactor configurations at similar driving force conditions. Three main reactor types were used: a stirred tank, a fixed bed and a bubble column and compared different phase contacting patterns for the stirred tank and bubble column. In the initial phase of hydrate formatio
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Xiao-Xiong, Lu. "A study of the characteristics of a novel cocurrent downflow bubble column contactor for use as a three-phase reactor." Thesis, University of Birmingham, 1988. http://ethos.bl.uk/OrderDetails.do?uin=uk.bl.ethos.589427.

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A cocurrent downflow contactor (CDC) has been constructed in and potential as a reactions. Prior to studying the CDC as a reactor its performance order reactor to investigate its for use with behaviour gas-liquid-solid was investigated with respect to its hydrodynamic behaviour with liquids of varying viscosity and surface tension. Liquid systems employed were water based, containing various concentrations of sodium alginate, glycerol, and I-propanol. Parameters such as minimum inlet liquid velocity, column liquid velocity, pressure drop, bubble size, gas holdup, and gas liquid interfacial are
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Books on the topic "Bubble column reactor"

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Robert Gerardus Jacobus Maria Van der Lans. Hydrodynamics of a bubble column loop reactor. Zoetermeer, 1985.

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Wadley, R. J. Studies of a bubble column reactor system for finechemicalsproduction. UMIST, 1994.

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Lu, Xiao-Xiong. A study of the characteristics of a novel cocurrent downflow bubble column contactor for use as athree-phase reactor. University of Birmingham, 1988.

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Sulidis, Andrew Thomas. Application of the occurrent downflow bubble column contactor (CDC) for use as a photocatalytic reactor and associated mass transfer studies. University of Birmingham, 1995.

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Deckwer, Wolf-Dieter. Bubble column reactors. Wiley, 1992.

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Majumder, Subrata Kumar. Hydrodynamics and Mass Transfer in Downflow Slurry Bubble Columns. Apple Academic Press, Incorporated, 2019.

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Majumder, Subrata Kumar. Hydrodynamics and Mass Transfer in Downflow Slurry Bubble Columns. Apple Academic Press, Incorporated, 2019.

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Majumder, Subrata Kumar. Hydrodynamics and Mass Transfer in Downflow Slurry Bubble Columns. Taylor & Francis Group, 2021.

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Hydrodynamics and Mass Transfer in Downflow Slurry Bubble Columns. Taylor & Francis Group, 2018.

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Book chapters on the topic "Bubble column reactor"

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Jakobsen, Hugo A. "Bubble Column Reactors." In Chemical Reactor Modeling. Springer International Publishing, 2014. http://dx.doi.org/10.1007/978-3-319-05092-8_8.

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Gamwo, Isaac K., Dimitri Gidaspow, and Jonghwun Jung. "Slurry Bubble Column Reactor Optimization." In ACS Symposium Series. American Chemical Society, 2007. http://dx.doi.org/10.1021/bk-2007-0959.ch017.

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Duduković, M. P., and N. Devanathan. "Bubble Column Reactors: Some Recent Developments." In Chemical Reactor Technology for Environmentally Safe Reactors and Products. Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2747-9_14.

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Deckwer, Wolf-Dieter. "Design and Simulation of Bubble Column Reactors." In Chemical Reactor Design and Technology. Springer Netherlands, 1986. http://dx.doi.org/10.1007/978-94-009-4400-8_12.

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Baum, Sören, Jakob J. Mueller, Lutz Hilterhaus, Marrit Eckstein, Oliver Thum, and Andreas Liese. "The Bubble Column Reactor: A Novel Reactor Type for Cosmetic Esters." In Applied Biocatalysis: From Fundamental Science to Industrial Applications. Wiley-VCH Verlag GmbH & Co. KGaA, 2016. http://dx.doi.org/10.1002/9783527677122.ch15.

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Palit, Sukanchan. "Advanced Oxidation Processes, Nanofiltration, and Application of Bubble Column Reactor." In Nanomaterials for Environmental Protection. John Wiley & Sons, Inc, 2014. http://dx.doi.org/10.1002/9781118845530.ch13.

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Mohd Yusof, Muhammad Nur Amirulhaq, and Nurul Fitriah Nasir. "Effects of Reaction Temperature and Inlet Velocity of a Bubble Column Reactor on the Bubble Size for Biodiesel Production." In Lecture Notes in Mechanical Engineering. Springer Nature Singapore, 2022. http://dx.doi.org/10.1007/978-981-19-3179-6_54.

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Madhania, Suci, Lailatul Alawiyah, Azriel Iqbal Hamayaputra, Kusdianto, and Sugeng Winardi. "Scale-Up of Bubble Column Reactor for Carbon Mineralization with Precipitated CaCO3 Product." In Lecture Notes in Mechanical Engineering. Springer Nature Singapore, 2025. https://doi.org/10.1007/978-981-97-7898-0_23.

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Godo, S., K. Junghans, A. Lapin, and A. Lübbert. "Dynamics of the Flow in Bubble Column Reactors." In Bubbly Flows. Springer Berlin Heidelberg, 2004. http://dx.doi.org/10.1007/978-3-642-18540-3_6.

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Febrada, Mayongga Heriz, Wanda Oktavia Maharani, Kusdianto, et al. "Carbon Capture and Utilization Technology to Upgrading Biogas Using Bubble Column Reactor: Effect of Concentration of Ca(OH)2 Solution on CO2 Removal." In Lecture Notes in Electrical Engineering. Springer Nature Singapore, 2025. https://doi.org/10.1007/978-981-97-8197-3_17.

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Conference papers on the topic "Bubble column reactor"

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Marais, Willem-Louis. "MEA Triazine Contactor Optimization to Increase Efficiency and Reduce Fouling Potential." In CONFERENCE 2024. AMPP, 2024. https://doi.org/10.5006/c2024-20391.

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Abstract Liquid absorbents have been utilized for decades to remove impurities from produced natural gas. Throughout the last 15 years, monoethanolamine (MEA) triazine has become an industry-recognized name for the removal of sour gas (H2S). MEA triazine has one of the lowest cost profiles in terms of cost per mass of H2S removed and has obtained a commodity status. It is widely used in the oil and gas industry, both on production (upstream, midstream) and processing (downstream). MEA Triazine is typically applied via direct injection into flowlines or applied in contactor vessels (“scrubbers”
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Chai, I. C. H., Y. H. Chan, K. Nikulainen, J. Laukka, and M. A. Ishak. "Methane Pyrolysis to Produce Hydrogen and Carbon Solids Using Thermocatalytic Pathway." In APOGCE 2024. SPE, 2024. http://dx.doi.org/10.2118/221204-ms.

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Thermo-catalytic decomposition (TCD) of natural gas is a suitable technology to provide clean hydrogen (H2). This TCD process directly splits hydrocarbons, mainly methane (CH4), into H2 and carbon as illustrated in Equation 1. [Equation 1]CH4(g)→C(s)+2H2(g)ΔH∘=74 kJ/mol In TCD process, H2 is produced as a gas while carbon is generated in solid form. Though the reaction can occur with heat energy alone, the use of a catalyst significantly reduces the required reaction temperature, making the process less energy-intensive. Various reactor designs are used for TCD to pyrolyze CH4, including fluid
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Strasser, W., and A. Wonders. "Commercial scale slurry bubble column reactor optimization." In ADVANCES IN FLUID MECHANICS 2008. WIT Press, 2008. http://dx.doi.org/10.2495/afm080271.

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Studley, Allison, and Francine Battaglia. "CFD Analyses of the Mixing Characteristics in Bubble Columns and Airlift Reactors." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-63221.

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The mixing characteristics in bubble columns and airlift reactors are analyzed using computational fluid dynamics. In the simulations, an Eulerian-Eulerian approach was used to model air as the dispersed phase within a continuous phase of water using the commercial software FLUENT. The Schiller-Naumann drag model was employed along with virtual mass and the standard k–ε turbulence model. An effective bubble diameter was specified for each case studied and depended on the inlet gas velocity specified. The predicted flow field in the airlift geometry showed a regular oscillation of the gas flow
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Ravinuthala, Sharad Chand, and Ismail B. Celik. "Numerical Modelling of Bubble Columns for High Temperature Glass Melting Applications." In ASME 2014 4th Joint US-European Fluids Engineering Division Summer Meeting collocated with the ASME 2014 12th International Conference on Nanochannels, Microchannels, and Minichannels. American Society of Mechanical Engineers, 2014. http://dx.doi.org/10.1115/fedsm2014-22054.

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Bottom heating approach for glass melting offers potential benefits of higher efficiency and lower emissions compared to the conventional surface fired melters with burners above the bath surface. Recent advances in the enabling technologies such as burners, controls, heat recovery and refractive materials have led to successful demonstration of bottom heating Submerged Combustion Melting (SCM) of glass. In the proposed reactor, combustion products of natural gas oxy combustion are bubbled through the three phase re-circulating tank reactor. The turbulence generated by the rising bubble column
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Ibrahim, Nur Afizah, Amir Khalid, Izzuddin Zaman, Azwan Sapit, and Bukhari Manshoor. "Flow visualization of bubble structure in bubble column reactor for fluid mixing." In 7TH INTERNATIONAL CONFERENCE ON MECHANICAL AND MANUFACTURING ENGINEERING: Proceedings of the 7th International Conference on Mechanical and Manufacturing Engineering, Sustainable Energy Towards Global Synergy. Author(s), 2017. http://dx.doi.org/10.1063/1.4981165.

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Mortuza, S. M., Anil Kommareddy, Stephen P. Gent, and Gary A. Anderson. "Computational and Experimental Investigation of Bubble Circulation Patterns Within a Column Photobioreactor." In ASME 2011 5th International Conference on Energy Sustainability. ASMEDC, 2011. http://dx.doi.org/10.1115/es2011-54205.

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This research project investigates bubble and liquid circulation patterns in a vertical column photobioreactor (PBR) both experimentally as well as computationally using Computational Fluid Dynamics (CFD). Dispersed gas–liquid flow in the rectangular bubble column PBR are modeled using Eulerian–Lagrangian approach. A low Reynolds number k–ε CFD model is used to describe the flow pattern near the wall. Bubble size distribution measurements are carried out using a high-speed digital camera. A flat surface bubble column PBR is used to achieve sufficient light penetration into the system. Carbon d
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Mudde, Robert F. "Gravity Driven Bubbly Flows: The Role of Vortical Structures." In ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/fedsm2003-45672.

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Gravity driven bubbles are found in many industrial applications. Two typical reactors are the bubble column, in which the liquid is stagnant and the air lift reactor in which the liquid circulates, under the action of gravity, through the reactor. These reactors are attractive for a number of reasons: they have no moving parts and are thus low in maintenance; the size can be enormous (diameters of several meters, heights of tens of meters) allowing large volume flows to be processed; good mixing and heat transfer characteristics, etc. Our knowledge about the structure of the flow induced is r
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Iyer, Kritika, S. Shridharani, S. Arunkumar, and M. Venkatesan. "Application of image processing for a bubble column reactor." In 2013 IEEE International Conference on Computational Intelligence and Computing Research (ICCIC). IEEE, 2013. http://dx.doi.org/10.1109/iccic.2013.6724169.

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McGuffie, Sean M., Mike A. Porter, and Dennis H. Martens. "Experimental and CFD Evaluation of a Bubble Column Reactor." In ASME 2010 Pressure Vessels and Piping Division/K-PVP Conference. ASMEDC, 2010. http://dx.doi.org/10.1115/pvp2010-25823.

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During the scale-up design of a slurry bubble column reactor from a pilot demonstration facility to a production reactor, the design team used computational fluid dynamics (CFD) as a tool to quantify design variables, such as gas holdup and liquid velocities/structural pressures within the reactor. At the time of the analysis, all available physics models for modeling the multi-phase flow had significant limitations that would require “tuning” of the CFD input parameters to ensure confidence in the results. The authors initially conducted a literature search to find data that could be used to
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Reports on the topic "Bubble column reactor"

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Dimitri Gidaspow. Hydrodynamic models for slurry bubble column reactor. Office of Scientific and Technical Information (OSTI), 1997. http://dx.doi.org/10.2172/750383.

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Shollenberger, K. A., J. R. Torczynski, N. B. Jackson, and T. J. O`Hern. Experimental characterization of slurry bubble-column reactor hydrodynamics. Office of Scientific and Technical Information (OSTI), 1997. http://dx.doi.org/10.2172/292851.

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Bernard A. Toseland, Ph D. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR)TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/783047.

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Bernard A. Toseland, Ph D. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR) TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/783049.

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Toseland, B. A. Engineering Development of Slurry Bubble Column Reactor (SBCR) Technology. Office of Scientific and Technical Information (OSTI), 1998. http://dx.doi.org/10.2172/1304.

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Bernard A Toseland, Ph D. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR) TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/793999.

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Bernard A Toseland, Ph D. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR) TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 2002. http://dx.doi.org/10.2172/794000.

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Bernard A Toseland, Ph D. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR) TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 2002. http://dx.doi.org/10.2172/794001.

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Bernard A Toseland, Ph D. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR) TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 1999. http://dx.doi.org/10.2172/794298.

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Toseland, Bernard A. ENGINEERING DEVELOPMENT OF SLURRY BUBBLE COLUMN REACTOR (SBCR) TECHNOLOGY. Office of Scientific and Technical Information (OSTI), 1998. http://dx.doi.org/10.2172/803205.

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