Dossier: Methodology for Process Development at IFP Energies nouvelles
Open Access
Oil Gas Sci. Technol. – Rev. IFP Energies nouvelles
Volume 71, Number 3, May–June 2016
Dossier: Methodology for Process Development at IFP Energies nouvelles
Article Number 43
Number of page(s) 18
Published online 27 October 2015
  • Ataki A., Bart H.J. (2006) Experimental and CFD simulation study for the weeting of s structured packing element with liquids, Chem. Eng. Technol. 29, 3, 336–347. [CrossRef]
  • Asprion N. (2005) Surface tension models for aqueous amine blends, Ind. Eng. Chem. Res. 44, 7270–7278. [CrossRef]
  • Bai H., Theuerkauf J., Gillis P.A. (2009) A Coupled DEM and CFD Simulation of Flow Field and Pressure Drop in Fixed Bed Reactor with Randomly Packed Catalyst Particles, Ind. Eng. Chem. Res. 48, 4060–4074. [CrossRef]
  • Bazer-Bachi F., Haroun Y., Augier F., Boyer C. (2013) Experimental evaluation of distributor technologies for trickle-bed reactors, Ind. Eng. Chem. Res. 52, 11189–11197. [CrossRef]
  • Billet R. (1995) Packed Towers, VCH Eds, Weinheim. [CrossRef]
  • Bravo J.L., Rocha J.A., Fair J.R. (1985) Mass transfer in gauze packings, Hydrocarbon Processing 64, 1, 91–95.
  • Brackbill J.U., Khote D.B., Zemach C. (1992) A continuum method for modelling surface tension, J. Comput. Phys. 100, 335–354. [CrossRef] [MathSciNet]
  • Brian P.L.T., Hurey J.F., Hassettine E.H. (1961) AIChE J. 7, 226. [CrossRef]
  • Brunazzi E., Nardini G., Paglianti A., Petraca L. (1995) Interfacial area of Mellapak packing Absorption of 1,1,1-trichloroethane by Genosorb 300, Chem. Eng. Technol. 18, 248. [CrossRef]
  • Brunazzi E.P. (1997) Liquid-Film Mass-Transfer Coefficient in a Column Equipped with Structured Packings, Ind. Eng. Chem. Res. 36, 3792–3799. [CrossRef]
  • Celebi M.S., Akyildiz H. (2002) Nonlinear modeling of liquid sloshing in a moving rectangular tank, Ocean Eng. 29, 1527–1553. [CrossRef]
  • Charpentier J.C. (2009) Perspective on multiscale methodology for product design and engineering, Comp. Chem. Eng. 33, 936–946. [CrossRef]
  • Chilton T.C. (1934) Mass Transfer Coefficient, Prediction from Data on Heat Transfer and Fluid Friction, Ind. Eng. Chem. 1183–1187. [CrossRef]
  • Danckwerts P.V. (1970) Gaz-Liquid Reaction, McGraw-Hill, New York.
  • Erasmus A.B. (2004) Mass Transfer in Structured Packing, Ph.D. Dissertation Chem. Eng., University of Stellenbosch, South Africa.
  • Fair J.R., Bravo J.L. (1990) Distillation columns containing structured packings, Chem. Eng. Prog. 86, 19–29.
  • Fernandes J., Lisboa P.F., Simoes P.C., Mota J.P.B., Saatdjian E. (2009) Application of CFD in the study of supercritical fluid extraction with structured packing: wet pressure drop calculations, J. Supercrit. Fluids 50, 61. [CrossRef]
  • Fourati M., Roig V., Raynal L. (2012) Experimental study of liquid spreading in structured packings, Chem. Eng. Sci. 80, 1–15. [CrossRef]
  • Fourati M., Roig V., Raynal L. (2013) Liquid dispersion in packed columns: experiments and numerical modelling, Chem. Eng. Sci. 100, 266–278. [CrossRef]
  • Haroun Y., Legendre D., Raynal L. (2010a) Direct numerical simulation of reactive absorption in gas–liquid flow on structured packing using interface capturing method, Chem. Eng. Sci. 65, 351–356. [CrossRef]
  • Haroun Y., Legendre D., Raynal L. (2010b) Volume of fluid method for interfacial reactive mass transfer: application to stable liquid film, Chem. Eng. Sci. 65, 2896–2909. [CrossRef]
  • Haroun Y., Raynal L., Legendre D. (2012) Mass transfer and liquid hold-up determination in structured packing by CFD, Chem. Eng. Sci. 75, 342–348. [CrossRef]
  • Haroun Y., Raynal L., Alix P. (2013) Partitioned distributor tray for offshore gas/liquid contact column, Patent US 20130277868.
  • Haroun Y., Raynal L., Alix P. (2014) Prediction of effective area and liquid hold-up in structured packings by CFD, Chem. Eng. Res. Des. 92, 2247–2254. [CrossRef]
  • Heggemann M., Hirschberg S., Spiegel L., Bachmann C. (2007) CFD Simulation and Experimental Validation of Fluid Flow in Liquid Distributors, Chem. Eng. Res. Des. 85, 59–64. [CrossRef]
  • Higbie R. (1935) The rate of absorption of a pure gas into a still liquid during short periods of exposure, Trans. AIChE 35, 365.
  • Hirt C.W., Nichols B.D. (1981) Volume of Fluid method for the dynamics of free boundaries, J. Comput. Phys. 39, 201–225. [CrossRef]
  • Hoffmann A., Ausner I., Repke J.-U., Wozny G. (2006) Detailed investigation of multiphase (gas–liquid and gas–liquid–liquid) flow behaviour on inclined plates, Chem. Eng. Res. Des. 84, 147–154. [CrossRef]
  • Ishimatsu M., Nosoko T., Nagata T. (1990) Flow patterns and wave characteristics of falling liquid films, Heat Trans. Japanese Res. 19, 602–615.
  • Iso Y., Chen X. (2011) Flow transition behavior of the wetting flow between the film flow and rivulet flow on an inclined wall, J. Fluids Eng. 133, 091101–91111. [CrossRef]
  • Iso Y., Huang J., Kato M., Matsuno S., Takano K. (2013) Numerical and experimental study on liquid film flows on packing elements in absorbers for post-combustion CO2 capture, Energy Procedia 37, 860–868. [CrossRef]
  • Kister H.Z. (1990) Distillation Operation, McGraw-Hill, New York, USA.
  • Lautenschleger A., Olenberg A., Kenig E.Y. (2015) Systematic CFD-based method to investigate and optimise novel structured packings, Chem. Eng. Sci. 122, 452–464. [CrossRef]
  • Lassauce A., Alix P., Raynal L., Royon-Lebeaud A., Haroun Y. (2014) Pressure Drop, Capacity and Mass Transfer Area Requirements for Post-Combustion Carbon Capture by Solvents, Oil Gas Sci. Technol. 69, 6, 1021–1034. [CrossRef] [EDP Sciences]
  • Li H.-L., Li J., Zong Z., Chen Z. (2014) Numerical studies on sloshing in rectangular tanks using a tree-based adaptive solver and experimental validation, Ocean Eng. 82, 20–31. [CrossRef]
  • Mahr B., Mewes D. (2007) CFD Modelling and calculation of dynamic two phase flow in columns equipped with structured packing, Chem. Eng. Res. Des. 85, 1112–1122. [CrossRef]
  • Moore F., Rukovena F. (1987) Liquid and gas distribution in commercial packed towers, Chem. Plants and Processing No. 8, 11.
  • Mohamed Ali A., Jansens P.J., Olujic Z. (2003) Experimental Characterization and Computational Fluid Dynamics Simulation of Gas Distribution Performance of Liquid (Re)Distributors and Collectors in Packed Columns, Chem. Eng. Res. Des. 81, 1, 108–115. [CrossRef]
  • Nikou K., Ehsani M.R. (2008) Turbulence models application on CFD simulation of hydrodynamics, heat and mass transfer in a structured packing, Int. Commun. Heat Mass Transfer 35, 1211. [CrossRef]
  • Nicoud F., Ducros F. (1999) Subgrid-Scale Stress Modelling Based on the Square of the Velocity Gradient Tensor, Flow Turb. Comb. 62, 3, 183–200. [CrossRef]
  • Olujic Z., de Graauw J. (1989) Appearence of maldistribution in distillation columns equiped with hight performance packings, Chem. Biochem. Eng. Q. 3, 181–196.
  • Olujic Z., de Graauw J. (1990) Experimental studies on interaction between the initial liquid distribution and the performance of structured packing, Separation Sci. Tech. 25, 1723–1735. [CrossRef]
  • Olujic Z., Mohamed Ali A., Jansens P.J. (2004) Effect of the initial gas maldistribution on the pressure drop of structured packings, Chem. Eng. Process. 43, 465–476. [CrossRef]
  • Petre C.F., Larachi F., Illiuta I., Grandjean B.P.A. (2003) Pressure drop through structured packings: breakdown into the contributing mechanisms by CFD modelling, Chem. Eng. Sci. 58, 163–177. [CrossRef]
  • Pierson F.W., Whitaker S. (1977) Some theoretical and experimental observations of the wave structure of falling liquid film, Ind. Eng. Chem. Fundam. 16, 401–408. [CrossRef]
  • Raynal L., Harter I. (2001) Studies of Gas-Liquid flow through distributing devices using VOF-CFD simulations, Chem. Eng. Sci. 56, 6385–6391. [CrossRef]
  • Raynal L., Boyer C., Ballaguet J.P. (2004) Liquid holdup and pressure drop determination in structured packing with CFD simulation, Can. J. Chem. Eng. 82, 871–879. [CrossRef]
  • Raynal L., Royon-Lebeaud A. (2007) A multi-scale approach for CFD calculations of gas–liquid flow within large size column equipped with structured packing, Chem. Eng. Sci. 62, 7196–7204. [CrossRef]
  • Raynal L., Ben Rayana F., Royon-Lebeaud A. (2009) Use of CFD for CO2 absorbers optimum design: from local scale to large industrial scale, Energy Procedia 1, 917–924. [CrossRef]
  • Raynal L., Gomez A., Caillat B., Haroun Y. (2013) CO2 capture cost reduction: Use of a multiscale simulations strategy for a multiscale issue, Oil Gas Sci. Technol. 68, 1093–1108. [CrossRef] [EDP Sciences]
  • Said W., Nemer M., Clodic D. (2011) Modeling of dry pressure drop for fully developed gas flow in structured packing using CFD simulations, Chem. Eng. Sci. 66, 2107–2117. [CrossRef]
  • Scardovelli R., Zaleski S. (1999) Direct numerical simulation of free-surface and interfacial flow, Annu. Rev. Fluid Mech. 31, 567–603. [CrossRef]
  • Sebastia-Saez D., Gu S., Ranganathan P., Papadikis K. (2013) 3D modeling of hydrodynamics and physical mass transfer characteristics of liquid film flows in structured packing elements, Int. J. Greenhouse Gas Control 19, 492–502. [CrossRef]
  • Sebastia-Saez D., Gu S., Ranganathan P., Papadikis K. (2014) Micro-scale CFD study about the influence of operative parameters onphysical mass transfer within structured packing elements, Int. J. Greenhouse Gas Control 28, 180–188. [CrossRef]
  • Shojaee S., Hosseini S.H., Rafati A., Ahmadi G. (2011) Prediction of the effective area in structured packings by computational fluid dynamics, Ind. Eng. Chem. Res. 50, 10833–10842. [CrossRef]
  • Soulaine C., Horgue P., Franc J., Quintard M. (2014) Gas–liquid flow modeling in columns equipped with structured packing, AIChE Journal 60, 10, 3665–3674. [CrossRef]
  • Stemich C., Spiegel L. (2011) Characterization and quantification of the quality of gas flow distributions, Chem. Eng. Res. Design 89, 1392–1396. [CrossRef]
  • Spiegel L., Meier W. (1992) A generalized pressure drop model for structured packings, Distillation and Absorption, IChemE Symp. 128, B85–B94.
  • Szulczewska B., Sek J., Gorak A., Zbicinski I. (2000) CFD calculation of two-phase flow on elements of structured packing, Chisa Int. Conf., Praha, Czech Republic, Aug. 27-37, Paper #565, 1-10.
  • Tailby S.R., Portalski S. (1962) Wave inception on a liquid film flowing down a hydrodynamically smooth plate, Chem. Eng. Sci. 19, 283–290. [CrossRef]
  • Tsai R.E., Seibert A.F., Eldridge R.B., Rochelle G.T. (2011) A dimensionless model for predicting the mass-transfer area of structured packing, AIChE J. 57, 1173–1184. [CrossRef]
  • Wacławczyk T., Koronowicz T. (2008) Comparison of CICSAM and HRIC high-Resolution schemes for interface capturing, J. Theo. App. Mech. 46, 2, 325–345.
  • Wang C. (2012) Measurement of Packing Effective Area and Mass Transfer Coefficients, Luminant Carbon Management Program and Process Science and Technology Center, Austin, Texas, pp. 1–9.

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