Academic literature on the topic 'Slurry Reactors'

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Journal articles on the topic "Slurry Reactors"

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Bouchy, M., and O. Zahraa. "Photocatalytic reactors." International Journal of Photoenergy 5, no. 3 (2003): 191–97. http://dx.doi.org/10.1155/s1110662x03000321.

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Fundamental concepts for the design of photocatalytic reactors are recalled: specific rate, modeling of the distribution of the irradiation, description and modeling of transport phenomena on the macroscopic and macroscopic scales. These are required for establishing the reactor mass balance. A brief survey of various reactors is given for solar or artificial light, gas- or liquid-phase, slurry or fixed-bed.
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Tschentscher, Roman, Tjeerd Alexander Nijhuis, John van der Schaaf, and Jaap C. Schouten. "Glucose Oxidation in Slurry Reactors and Rotating Foam Reactors." Industrial & Engineering Chemistry Research 51, no. 4 (2011): 1620–34. http://dx.doi.org/10.1021/ie200694z.

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Bukur, D. B., and W. H. Zimmerman. "Modeling of bubble column slurry reactors for multiple reactions." AIChE Journal 33, no. 7 (1987): 1197–206. http://dx.doi.org/10.1002/aic.690330714.

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Ni, Xiong-Wei. "Another Critical Look at Three-Phase Catalysis." Pharmaceutical Fronts 02, no. 03 (2020): e117-e127. http://dx.doi.org/10.1055/s-0040-1722219.

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AbstractThree-phase catalysis, for example, hydrogenation, is a special branch of chemical reactions involving a hydrogen reactant (gas) and a solvent (liquid) in the presence of a metal porous catalyst (solid) to produce a liquid product. Currently, many reactors are being used for three-phase catalysis from packed bed to slurry vessel; the uniqueness for this type of reaction in countless processes is the requirement of transferring gas into liquid, as yet there is not a unified system of quantifying and comparing reactor performances. This article reviews current methodologies in carrying o
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Forret, A., J. M. Schweitzer, T. Gauthier, R. Krishna, and D. Schweich. "Scale Up of Slurry Bubble Reactors." Oil & Gas Science and Technology - Revue de l'IFP 61, no. 3 (2006): 443–58. http://dx.doi.org/10.2516/ogst:2006044a.

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Oinas, Pekka A., and Heikki Haario. "Transient models for multiphase slurry reactors." Catalysis Today 20, no. 3 (1994): 525–39. http://dx.doi.org/10.1016/0920-5861(94)80143-6.

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Wei, Gui, and Hong Chang. "Design of Photocatalytic Reactor with Photocatalyst Film Loaded on Substrate." Advanced Materials Research 823 (October 2013): 214–17. http://dx.doi.org/10.4028/www.scientific.net/amr.823.214.

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After analytical studies of the characteristics of various slurry and supported photocatalytic reactors, a photocatalytic reactor with photocatalyst film loaded on substrate is designed in this paper. This reactor is characterized by the easy attachment and convenient installation & replacement of photocatalyst, higher light utilization, and complete photocatalytic reaction.
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Vlaev, Serafim D., and Jindřich Zahradník. "Energy effectiveness and working characteristics of different tower reactors for aerated slurry systems." Collection of Czechoslovak Chemical Communications 52, no. 11 (1987): 2624–39. http://dx.doi.org/10.1135/cccc19872624.

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Decisive hydrodynamic and mass transfer characteristics of different types of tower reactors (rotating disc reactor, single and multistage sieve-tray bubble columns, tower reactor with ejector gas distributor) as well as the energy effectiveness of their performance were compared with the purpose to establish a quantitative basis for the qualified choice of the proper reactor type according to demands of specific reaction processes. Selected design parameters included gas and solid phase holdup, kLaL, liquid phase residence time distribution, and axial distribution of the solid phase, the expe
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Rados, Novica, Muthanna H. Al-Dahhan, and Milorad P. Duduković. "Dynamic Modeling of Slurry Bubble Column Reactors." Industrial & Engineering Chemistry Research 44, no. 16 (2005): 6086–94. http://dx.doi.org/10.1021/ie040227t.

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Brandi, Rodolfo J., Miguel A. Citroni, Orlando M. Alfano, and Alberto E. Cassano. "Absolute quantum yields in photocatalytic slurry reactors." Chemical Engineering Science 58, no. 3-6 (2003): 979–85. http://dx.doi.org/10.1016/s0009-2509(02)00638-3.

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Dissertations / Theses on the topic "Slurry Reactors"

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Gopala, Krishna K. V. "Aqueous Phase Oxidation Of Sulfur Dioxide In Stirred Slurry Reactors." Thesis, Indian Institute of Science, 1994. http://hdl.handle.net/2005/130.

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Air pollution by sulfur dioxide is of great concern due to its harmful effects on environment, human beings, fauna and flora. Fossil-fuel-fired power plants are one of the major sources of SO2 emissions. Typically the concentration of SO2 in the flue gases of these plants is in the range of 2000 to 20000 ppm. Flue gas desulfurisation is one of the widely practiced strategies to control SO2 emissions. Aqueous phase oxidation of sulfur dioxide catalysed by carbonaceous particles is an attractive alternative to the conventional processes for flue gas desulfurisation because, amongst other reasons
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Yucel, Cakal Gaye O. "Dynamic Behavior Of Continuous Flow Stirred Slurry Reactors In Boric Acid Production." Phd thesis, METU, 2005. http://etd.lib.metu.edu.tr/upload/12605047/index.pdf.

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One of the most important boron minerals, colemanite is reacted with sulfuric acid to produce boric acid. During this reaction, gypsum (calcium sulfate dihydrate) is formed as a byproduct. In this study, the boric acid production was handled both in a batch and four continuously stirred slurry reactors (4-CFSSR&rsquo<br>s) in series system. In this reaction system there are at least three phases, one liquid and two solid phases (colemanite and gypsum). In a batch reactor all the phases have the same operating time (residence time), whereas in a continuous reactor all the phases may have diff
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Mthombeni, Bongani. "Modeling Fischer Tropsch synthesis in two-phase, continuous, well-mixed slurry reactors." Master's thesis, University of Cape Town, 2009. http://hdl.handle.net/11427/10853.

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Includes abstract.<br>Includes bibliographical references (p. 84-87).<br>Fischer Tropsch Synthesis (FTS) is the conversion of syngas (CO and H2) to cleaner liquid transportation fuels. The modelling of such a supercritical, highly non-ideal, multi-component system requires the detailed knowledge of the reaction mechanism, reaction kinetics, phase-equilibrium and reactor technology. The objectives of this work were to: develop a complete Fischer Tropsch model, predict the hydrocarbon product distribution, determine what effect Vapour-Liquid Equilibrium (VLE) has on the product distribution, sel
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Liedtke, Anne-Kathrin. "Study of a new gas-liquid-solid three phase contact mode at millimetric scale : catalytic reactors using “slurry Taylor” flow." Thesis, Lyon 1, 2014. http://www.theses.fr/2014LYO10137/document.

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Des réacteurs avec solide en suspension (« slurry »), très répandu dans l'industrie chimique, du laboratoire à la production, offrent des bonnes capacités en transfert de matière et de chaleur. Leur flexibilité facilite le changement de la phase solide et permet une régénération en continue des catalyseurs en cas de désactivation. Cependant, ils présentent un fort rétro-mélange, et donc un désavantage pour des réactions ayant des enjeux de sélectivité et/ou de conversion poussées. L'écoulement segmenté dit de Taylor est souvent mis en œuvre dans les réacteurs micro-structurés (RMS), grâce à se
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Bigg, Torill. "An iron metal slurry reactor for wastewater treatment." Thesis, Cranfield University, 2002. http://dspace.lib.cranfield.ac.uk/handle/1826/11428.

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The corrosion of iron is a very old and complex phenomenon. Its employment for the treatment of wastewater began in the earliest around ten years ago, with few earlier exceptions. Most researchers have considered its application to groundwater remediation, and its use a a permeable reactive barrier material is well established. The aim of this research is to measure parameters that govern zero-valent iron treatment of wastewater with the treatment of industrial influents prior to discharge to municipal sewage treatment works particularly in mind.
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Bigg, T. "In iron metal slurry reactor for wastewater treatment." Thesis, Cranfield University, 2002. http://dspace.lib.cranfield.ac.uk/handle/1826/11428.

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The corrosion of iron is a very old and complex phenomenon. Its employment for the treatment of wastewater began in the earliest around ten years ago, with few earlier exceptions. Most researchers have considered its application to groundwater remediation, and its use a a permeable reactive barrier material is well established. The aim of this research is to measure parameters that govern zero-valent iron treatment of wastewater with the treatment of industrial influents prior to discharge to municipal sewage treatment works particularly in mind.
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Steynberg, Andre Peter. "Process intensification for the iron-catalysed slurry-phase Fischer-Tropsch Reactor System." Master's thesis, University of Cape Town, 2014. http://hdl.handle.net/11427/13279.

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Includes bibliographical references.<br>A set of operating conditions was identified with the potential to enable improved slurryphase reactor productivity for hydrocarbon production using Fischer-Tropsch synthesis. Compared to the most relevant prior art publication, this requires operation at higher gas velocity, higher catalyst concentration and at higher temperature and/or pressure. The closest prior art proposal was published by Van der Laan et al. (1999) and a target was set to improve the reactor productivity by at least 50 %, relative to this reference, while also ensuring stable catal
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Lamaignère, Valérie. "Effects of hydrodynamic stress on growing Saccharomyces cerevisiae in a slurry reactor." Master's thesis, University of Cape Town, 2003. http://hdl.handle.net/11427/6081.

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Includes bibliography.<br>The objectives of this research thesis were to understand and quantify biological responses to hydrodynamic stress by investigating the activity of the yeast Saccharomyces cerevisiae, cultivated in the presence of a range of solid loadings, solid sizes and agitation rates. The influence of inoculum size, inoculum age and type of agitator were also investigated. This study was carried out with the intention of identifying biological responses to hydrodynamic stress and modelling observed effects on microbial activity.
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Peña, Zapata Diego. "Identification of deactivation mechanisms of cobalt Fischer-Tropsch catalysts in slurry reactor." Thesis, Lille 1, 2013. http://www.theses.fr/2013LIL10149/document.

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La synthèse Fischer -Tropsch (SFT) produit des carburants liquides ultra-propres, ainsi que des produits chimiques à partir du gaz de synthèse issu d’une large gamme de matières premières : gaz naturel, gaz de schiste, charbon, biomasse. Les catalyseurs supportés à base de cobalt sont la meilleure option pour la SFT à basse température, en raison de leur grande stabilité et leur sélectivité en hydrocarbures lourds. Néanmoins, ces catalyseurs se désactivent avec le temps au cours de la réaction. La désactivation réduit la durée de vie et la productivité de ces catalyseurs. Par conséquent, la dé
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Inga, Juan Ricardo. "Hydrodynamic studies and reactor modelling of a three phase slurry reactor in Fischer Tropsch application / Juan Ricardo Inga." Thesis, Potchefstroom University for Christian Higher Education, 1992. http://hdl.handle.net/10394/9611.

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In this .study the hydrodynamic characteristics of the slurry bed reactor was investigated. This study was aimed to the under" standing of the important parameters that describe the hydrodynamic regime and their quantification. In order to determine the relevant parameters the use of a theoretical model was necessary. This model should include all the hydrodynamic parameters in form of correlations. A sensitivity study was done and the parameters which have great impact were determined. An extensive literature review was done in order to gather the experience of previous investigations. Unfort
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Books on the topic "Slurry Reactors"

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Polymerisation of ethylene: In slurry loop reactors. Walter de Gruyter GmbH & Co., KG, 2015.

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Vinke, Heinz. The effect of catalyst particle-to-bubble adhesion on the mass transfer in agitated slurry reactors. s.n.], 1992.

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Stangle, Gregory Charles. Mass transfer with chemical reaction in a three-phase foam slurry reactor. 1985.

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Superfund Innovative Technology Evaluation Program (U.S.), ed. Pilot-scale demonstration of a slurry-phase biological reactor for creosote-contaminated soil. U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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Superfund Innovative Technology Evaluation Program (U.S.), ed. Pilot-scale demonstration of a slurry-phase biological reactor for creosote-contaminated soil. U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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Superfund Innovative Technology Evaluation Program (U.S.), ed. Pilot-scale demonstration of a slurry-phase biological reactor for creosote-contaminated soil. U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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Pilot-scale demonstration of a slurry-phase biological reactor for creosote-contaminated soil. U.S. Environmental Protection Agency, Superfund Innovative Technology Evaluation, 1993.

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Majid, Dosani, and Risk Reduction Engineering Laboratory (U.S.), eds. On-site engineering report of the slurry-phase biological reactor for pilot-scale testing on contaminated soil: Project summary. Risk Reduction Engineering Laboratory, U.S. Environmental Protection Agency, 1993.

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Majid, Dosani, and Risk Reduction Engineering Laboratory (U.S.), eds. On-site engineering report of the slurry-phase biological reactor for pilot-scale testing on contaminated soil: Project summary. Risk Reduction Engineering Laboratory, U.S. Environmental Protection Agency, 1993.

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Majid, Dosani, and Risk Reduction Engineering Laboratory (U.S.), eds. On-site engineering report of the slurry-phase biological reactor for pilot-scale testing on contaminated soil: Project summary. Risk Reduction Engineering Laboratory, U.S. Environmental Protection Agency, 1993.

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Book chapters on the topic "Slurry Reactors"

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Buwa, Vivek V., Shantanu Roy, and Vivek V. Ranade. "Three-phase slurry reactors." In Multiphase Catalytic Reactors. John Wiley & Sons, Inc., 2016. http://dx.doi.org/10.1002/9781119248491.ch6.

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Beenackers, A. A. C. M., and W. P. M. Swaaij. "Slurry Reactors, Fundamentals and Applications." In Chemical Reactor Design and Technology. Springer Netherlands, 1986. http://dx.doi.org/10.1007/978-94-009-4400-8_13.

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Doğu, Gülşen, Gökhan Ölmez, and Timur Doğu. "Removal of SO2 with Lime Slurry in a Spray Dryer." In Chemical Reactor Technology for Environmentally Safe Reactors and Products. Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-011-2747-9_20.

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Arastoopour, Hamid, Dimitri Gidaspow, and Robert W. Lyczkowski. "Synthetic Gas Conversion to Liquid Fuel Using Slurry Bubble Column Reactors." In Mechanical Engineering Series. Springer International Publishing, 2021. http://dx.doi.org/10.1007/978-3-030-68578-2_6.

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Nocentini, M., and F. Magelli. "Solid Distribution in Slurry Reactors Stirred with Multiple Impellers: Continuous Flow Systems." In Fluid Mechanics and Its Applications. Springer Netherlands, 1992. http://dx.doi.org/10.1007/978-94-015-7973-5_9.

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Alfano, Orlando M., Alberto E. Cassano, Rodolfo J. Brandi, and María L. Satuf. "A Methodology for Modeling Slurry Photocatalytic Reactors for Degradation of an Organic Pollutant in Water." In Photocatalysis and Water Purification. Wiley-VCH Verlag GmbH & Co. KGaA, 2013. http://dx.doi.org/10.1002/9783527645404.ch13.

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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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Böhm, L. L. "The Slurry Polymerization Process with Super-Active Ziegler-Type Catalyst Systems: From the 2 L Glass Autoclave to the 200 m3 Stirred Tank Reactor." In Polyolefins: 50 years after Ziegler and Natta I. Springer Berlin Heidelberg, 2013. http://dx.doi.org/10.1007/12_2013_214.

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Vogela, Alex, Andre Steynberg, and Berthold Breman. "Intensification of commercial slurry phase reactors." In Studies in Surface Science and Catalysis. Elsevier, 2007. http://dx.doi.org/10.1016/s0167-2991(07)80109-1.

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Doraiswamy, L. K. "Multiphase Reactions and Reactors." In Organic Synthesis Engineering. Oxford University Press, 2001. http://dx.doi.org/10.1093/oso/9780195096897.003.0025.

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The first three chapters of this part dealt with two-phase reactions. Although catalysts are not generally present in these systems, they can be used in dissolved form in the liquid phase. This, however, does not increase the number of phases. On the other hand, there are innumerable instances of gas-liquid reactions in which the catalyst is present in solid form. A popular example of this is the slurry reactor so extensively employed in reactions such as hydrogenation and oxidation. There are also situations where the solid is a reactant or where a phasetransfer catalyst is immobilized on a solid support that gives rise to a third phase. A broad classification of three-phase reactions and reactors is presented in Table 17.1 (not all of which are considered here). This is not a complete classification, but it includes most of the important (and potentially important) types of reactions and reactors. The thrust of this chapter is on reactions and reactors involving a gas phase, a liquid phase, and a solid phase which can be either a catalyst (but not a phasetransfer catalyst) or a reactant, with greater emphasis on the former. The book by Ramachandran and Chaudhari (1983) on three-phase catalytic reactions is particularly valuable. Other books and reviews include those of Shah (1979), Chaudhari and Ramachandran (1980), Villermaux (1981), Shah et al. (1982), Hofmann (1983), Crine and L’Homme (1983), Doraiswamy and Sharma (1984), Tarmy et al. (1984), Shah and Deckwer (1985), Chaudhari and Shah (1986), Kohler (1986), Chaudhari et al. (1986), Hanika and Stanek (1986), Joshi et al. (1988), Concordia (1990), Mills et al. (1992), Beenackers and Van Swaaij (1993), and Mills and Chaudhari (1997). Doraiswamy and Sharma (1984) also present a discussion of gas-liquid-solid noncatalytic reactions in which the solid is a reactant. In Chapter 7 we saw how Langmuir-Hinshelwood-Hougen-Watson (LHHW) models are normally used to describe the kinetics of gas-solid (catalytic) or liquid-solid (catalytic) reactions, and in Chapters 14 to 16 we saw how mass transfer between gas and liquid phases can significantly alter the rates and regimes of these two-phase reactions.
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Conference papers on the topic "Slurry Reactors"

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Ahsan, Syed Saad, and David Erickson. "Microfluidic Photocatalytic Water-Splitting Reactors." In ASME 2012 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2012. http://dx.doi.org/10.1115/imece2012-87860.

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In this work, we present a novel microfluidic photocatalytic water-splitting reactor. Optofluidics offers advantages over conventional reactors in terms of improved photon transfer efficiency and mass transfer efficiency and are therefore the ideal platform for photocatalytic reactions. Our device is a planar optofluidic device which we used to study the kinetics of Platinum-Impregnated Titanium Oxide as the oxygen and hydrogen producing photocatalyst redox mediated by Iodide/Iodate species. We deposit our catalysts via a sol-gel method while the platinum co-catalyst is added by wet impregnati
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Chen, Haiying, Aizhong Ding, Junfeng Dou, et al. "Optimal Conditions for Biodegradation of Indeno (1,2,3-cd) Pyrene in Soil Slurry Reactors." In 2010 4th International Conference on Bioinformatics and Biomedical Engineering (iCBBE). IEEE, 2010. http://dx.doi.org/10.1109/icbbe.2010.5517395.

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Pasangulapati, V., N. R. Kesana, G. Sharma, F. W. Chambers, M. E. McNally, and R. M. Hoffman. "Computational Study of Slurry Flow in Pipes to Determine Profiles Sensed in Near Infrared Slurry Measurements." In ASME 2011 International Mechanical Engineering Congress and Exposition. ASMEDC, 2011. http://dx.doi.org/10.1115/imece2011-62799.

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It is desired to perform accurate Near Infrared sensor measurements of slurries flowing in pipes leaving large batch reactors. A concern with these measurements is the degree to which the slurry sensed is representative of the material in the reactor and flowing through the pipe. Computational Fluid Dynamics (CFD) has been applied to the flow in the pipe to determine the flow fields and the concentration profiles seen by the sensors. The slurry was comprised of a xylene liquid phase and an ADP (2-amino-4, 6-dimethylpyrimidine) solid phase with a density ratio of 1.7. Computations were performe
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Torabifar, B., A. Torabian, A. A. Azimi, and M. Vossoughi. "Biological treatment of petroleum contaminated soils by soil slurry-sequencing batch reactors (SS-SBRs)." In WASTE MANAGEMENT 2008. WIT Press, 2008. http://dx.doi.org/10.2495/wm080761.

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Ademola O ADEBAYO, Simeon O JEKAYINFA, and Bernd LINKE. "Biogas Potential of Cow Slurry in Continuously Stirred Tank Reactors at Mesophilic and Thermophilic Temperatures." In 2012 Dallas, Texas, July 29 - August 1, 2012. American Society of Agricultural and Biological Engineers, 2012. http://dx.doi.org/10.13031/2013.41922.

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Kritzinger, H. P., B. C. Deelder, C. R. Kleijn, J. J. Derksen, and H. E. A. Van den Akker. "Turbulent Flow in a Stirred Tank With Permeable Impeller Blades." In ASME 2002 Joint U.S.-European Fluids Engineering Division Conference. ASMEDC, 2002. http://dx.doi.org/10.1115/fedsm2002-31360.

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This paper presents results from the experimental investigation of single-phase flow in a prototype stirred tank reactor, which uses monolith catalyst blocks as impeller. These monolith catalyst supports have been used for a dual role: (i) as stirrer blades for agitation and (ii) to bring reactants in contact with the catalyst in a way that eliminates the need for product filtration. The reactors are under investigation as replacement for the standard slurry stirred tank reactors used in the catalytic processes in chemical industry. The flow field in the reactor with this novel impeller, was d
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Kostedt, William L., Mickal A. Witwer, David W. Mazyck, Tony Powell, and Brian Butters. "A Slurry-Based Photocatalytic Reactor with Slurry Separation for Water Recovery." In International Conference On Environmental Systems. SAE International, 2005. http://dx.doi.org/10.4271/2005-01-2994.

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Ahmadi, Goodarz, and Xinyu Zhang. "Gas-Liquid-Particle Three-Phase Flows in Bubble Columns." In ASME/JSME 2003 4th Joint Fluids Summer Engineering Conference. ASMEDC, 2003. http://dx.doi.org/10.1115/fedsm2003-45556.

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An Eulerian-Lagrangian computational model for simulations of gas-liquid-solid flows in three-phase slurry reactors is developed. In this approach, the liquid flow is modeled using a volume-averaged system of governing equations, whereas motions of bubbles and particles are evaluated by Lagrangian trajectory analysis procedure. It is assumed that the bubbles remain spherical and their shape variations are neglected. The two-way interactions between bubble-liquid and particle-liquid are included in the analysis. The discrete phase equations include drag, lift, buoyancy, and virtual mass forces.
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Nwaigwe, Kevin N., Nnamdi V. Ogueke, Chibuike Ononogbo, and Emmanuel E. Anyanwu. "Performance Study of Anaerobic Digestion of Organic Municipal Waste in Upflow Bioreactor With Central Substrate Dispenser." In ASME 2013 International Mechanical Engineering Congress and Exposition. American Society of Mechanical Engineers, 2013. http://dx.doi.org/10.1115/imece2013-64064.

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A performance study of anaerobic digestion of organic municipal waste in upflow bioreactor with central substrate dispenser is presented. The experimental rig is based on an integrated system of bioreactors consisting of Upflow Bioreactor (UB), Upflow Bioreactor with Central Subtrate Dispenser (UBCSD), and Continous Stirred Tank Reactor (CSTR) each having internal volume of 76 litres, 64.8 litres, and 76 litres respectively. The scheme is used for minimizing the mixing and fouling problems associated with some conventional bioreactors during digestion reaction. Organic municipal waste (OMW) wa
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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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Reports on the topic "Slurry Reactors"

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Andrew Lucero. Improved Fischer-Tropsch Slurry Reactors. Office of Scientific and Technical Information (OSTI), 2009. http://dx.doi.org/10.2172/993519.

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Clark, N., J. Kuhlman, I. Celik, R. Gross, E. Nebiolo, and Yi-Zun Wang. Circulation in gas-slurry column reactors. Office of Scientific and Technical Information (OSTI), 1990. http://dx.doi.org/10.2172/6472190.

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Clark, N., J. Kuhlman, and I. Celik. Circulation in gas-slurry column reactors. Office of Scientific and Technical Information (OSTI), 1989. http://dx.doi.org/10.2172/5419261.

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Dimitri Gidaspow. Hydrodynamic models for slurry bubble column reactors. Office of Scientific and Technical Information (OSTI), 1996. http://dx.doi.org/10.2172/750375.

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Goodarz Ahmadi. ADVANCED COMPUTATIONAL MODEL FOR THREE-PHASE SLURRY REACTORS. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/825379.

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Goodarz Ahmadi. ADVANCED COMPUTATIONAL MODEL FOR THREE-PHASE SLURRY REACTORS. Office of Scientific and Technical Information (OSTI), 2001. http://dx.doi.org/10.2172/825380.

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Goodarz Ahmadi. ADVANCED COMPUTATIONAL MODEL FOR THREE-PHASE SLURRY REACTORS. Office of Scientific and Technical Information (OSTI), 2004. http://dx.doi.org/10.2172/838723.

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Paul Lam and Dimitri Gidaspow. COMPUTATIONAL AND EXPERIMENTAL MODELING OF SLURRY BUBBLE COLUMN REACTORS. Office of Scientific and Technical Information (OSTI), 2000. http://dx.doi.org/10.2172/825383.

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Paul Lam and Dimitri Gidaspow. COMPUTATIONAL AND EXPERIMENTAL MODELING OF SLURRY BUBBLE COLUMN REACTORS. Office of Scientific and Technical Information (OSTI), 2001. http://dx.doi.org/10.2172/825384.

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Paul C.K. Lam, Isaac K. Gamwo, and Dimitri Gidaspow. COMPUTATIONAL AND EXPERIMENTAL MODELING OF SLURRY BUBBLE COLUMN REACTORS. Office of Scientific and Technical Information (OSTI), 2002. http://dx.doi.org/10.2172/825795.

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