CFD simulation of multicomponent mixture within a packed Deethanizer column

The aim of this study is to develop a model of a Deethanizer Column (DC). A fuel mixture of Methane CH 4 , Ethane C 2 H 6 , Propane C 3 H 8 , N-butane n-C 4 H 10 and some hydrocarbons is used to get an insight on the DC operation. A multicomponent gas-liquid flow in DC is investigated using the Comp...

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Vydáno v:	Heat and mass transfer Ročník 55; číslo 9; s. 2605 - 2622
Hlavní autoři:	Troudi, Hajer, Ghiss, Moncef, Ellejmi, Mohamed, Tourki, Zoubeir
Médium:	Journal Article
Jazyk:	angličtina
Vydáno:	Berlin/Heidelberg Springer Berlin Heidelberg 01.09.2019 Springer Nature B.V
Témata:	CAD Computational fluid dynamics Computer aided design Computer simulation Droplets Engineering Engineering Thermodynamics Ethane Fuel mixtures Heat and Mass Transfer Industrial Chemistry/Chemical Engineering Liquid flow Mathematical models Methane Original Porosity Pressure drop Simulation Surface temperature Thermodynamics CFD Deethanizer column Porosity Droplet Multicomponent
ISSN:	0947-7411, 1432-1181
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Abstract	The aim of this study is to develop a model of a Deethanizer Column (DC). A fuel mixture of Methane CH 4 , Ethane C 2 H 6 , Propane C 3 H 8 , N-butane n-C 4 H 10 and some hydrocarbons is used to get an insight on the DC operation. A multicomponent gas-liquid flow in DC is investigated using the Computational Fluid Dynamics (CFD) method. The droplet size change, the droplet surface temperature and the pressure drop are investigated with a Eulerian-Lagrangian model using ANSYS-Fluent R15. The computation results are compared with the experimental data of a binary and multicomponent mixture in a stationary droplet. A good agreement between them is established. Additionally, the predicted pressure drop obtained at varied porosity is compared with the data got from the Ergun formulation. The results show that the presence of CH 4 and C 2 H 6 has a big impact on the droplet surface temperature. This temperature initially reaches the lower value because of the fastest evaporation of light components (CH 4 and C 2 H 6 ) rather than the heavy ones (C 5+ ). The current work provides a better understanding of the behavior of light components in DC.
AbstractList	The aim of this study is to develop a model of a Deethanizer Column (DC). A fuel mixture of Methane CH4, Ethane C2H6, Propane C3H8, N-butane n-C4H10 and some hydrocarbons is used to get an insight on the DC operation. A multicomponent gas-liquid flow in DC is investigated using the Computational Fluid Dynamics (CFD) method. The droplet size change, the droplet surface temperature and the pressure drop are investigated with a Eulerian-Lagrangian model using ANSYS-Fluent R15. The computation results are compared with the experimental data of a binary and multicomponent mixture in a stationary droplet. A good agreement between them is established. Additionally, the predicted pressure drop obtained at varied porosity is compared with the data got from the Ergun formulation. The results show that the presence of CH4 and C2H6 has a big impact on the droplet surface temperature. This temperature initially reaches the lower value because of the fastest evaporation of light components (CH4 and C2H6) rather than the heavy ones (C5+). The current work provides a better understanding of the behavior of light components in DC. The aim of this study is to develop a model of a Deethanizer Column (DC). A fuel mixture of Methane CH 4 , Ethane C 2 H 6 , Propane C 3 H 8 , N-butane n-C 4 H 10 and some hydrocarbons is used to get an insight on the DC operation. A multicomponent gas-liquid flow in DC is investigated using the Computational Fluid Dynamics (CFD) method. The droplet size change, the droplet surface temperature and the pressure drop are investigated with a Eulerian-Lagrangian model using ANSYS-Fluent R15. The computation results are compared with the experimental data of a binary and multicomponent mixture in a stationary droplet. A good agreement between them is established. Additionally, the predicted pressure drop obtained at varied porosity is compared with the data got from the Ergun formulation. The results show that the presence of CH 4 and C 2 H 6 has a big impact on the droplet surface temperature. This temperature initially reaches the lower value because of the fastest evaporation of light components (CH 4 and C 2 H 6 ) rather than the heavy ones (C 5+ ). The current work provides a better understanding of the behavior of light components in DC.
Author	Ellejmi, Mohamed Troudi, Hajer Tourki, Zoubeir Ghiss, Moncef
Author_xml	– sequence: 1 givenname: Hajer surname: Troudi fullname: Troudi, Hajer email: hajer.troudi@eniso.rnu.tn organization: Mechanical Laboratory of Sousse, National Engineering School of Sousse, University of Sousse – sequence: 2 givenname: Moncef surname: Ghiss fullname: Ghiss, Moncef organization: Mechanical Laboratory of Sousse, National Engineering School of Sousse, University of Sousse – sequence: 3 givenname: Mohamed surname: Ellejmi fullname: Ellejmi, Mohamed organization: Alpha Engineering International, AEI. Sahloul III 4054 – sequence: 4 givenname: Zoubeir surname: Tourki fullname: Tourki, Zoubeir organization: Mechanical Laboratory of Sousse, National Engineering School of Sousse, University of Sousse
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References_xml	– reference: GerbaudVRodriguez-donisIHegelyLLangPDenesFYouXReview of extractive distillation. Process design, operation, optimization and controlChem Eng Res Des201814122927110.1016/j.cherd.2018.09.020 – reference: MalangJKumarPSaptoroAComputational fluid dynamics-based hydrodynamics studies in packed bed columns: current status and future directionsInt J Chem React Eng2015133289303 – reference: TomiyamaAKataokaIZunISakaguchiTDrag coefficients of single bubbles under Normal and micro gravity conditionsJSME Int J Ser B199841247247910.1299/jsmeb.41.472 – reference: SuMChenCPHeating and evaporation of a new gasoline surrogate fuel: a discrete multicomponent modeling studyFuel201516121522110.1016/j.fuel.2015.08.048 – reference: PadoinNDal’ToéATORangelLPRopelatoKSoaresCHeat and mass transfer modeling for multicomponent multiphase flow with CFDInt J Heat Mass Transf20147323924910.1016/j.ijheatmasstransfer.2014.01.075 – reference: Henry ZK (2006) Distillation troubleshooting – reference: KimDMartzJVioliAEffects of fuel physical properties on direct injection spray and ignition behaviorFuel201618048149610.1016/j.fuel.2016.03.085 – reference: YinFHAfacanANandakumarKChuangKTCFD simulation and experimental study of liquid dispersion in randomly packed metal pall ringsChem Eng Res Des200280213514410.1205/026387602753501852 – reference: HernándezaJGSHernándezaSPetricioletABReactive distillation: a review of optimal design using deterministic and stochastic techniquesChem Eng Process Process Intensificatio20159713414310.1016/j.cep.2015.09.004 – reference: HarounYRaynalLLegendreDMass transfer and liquid hold-up determination in structured packing by CFDChem Eng Sci20127534234810.1016/j.ces.2012.03.011 – reference: Yaws CL (2003) Yaws’ Handbook of Thermodynamic and Physical Properties of Chemical Compounds: Physical, Thermodynamic and Transport Properties for 5,000 Organic Chemical Compounds – reference: Wang Y, Rutland ÆCJ (2006) Direct numerical simulation of turbulent flow with evaporating droplets at high temperature. Heat Mass Transf:1103–1110 – reference: ChenGAggarwalSJacksonTASwitzerGLExperimental study of pure and multicomponent fuel droplet evaporation in a heated air flowAt Sprays19977331733710.1615/AtomizSpr.v7.i3.50 – reference: BhranAAEKHassaneanMHHelalMGMaximization of natural gas liquids production from an existing gas plantEgypt J Pet201625333334110.1016/j.ejpe.2015.08.003 – reference: RaYReitzRDA vaporization model for discrete multi-component fuel spraysInt J Multiph Flow200935210111710.1016/j.ijmultiphaseflow.2008.10.006 – reference: FiebergCReicheltLMartinDRenzUKneerRExperimental and numerical investigation of droplet evaporation under diesel engine conditionsInt J Heat Mass Transf20095215–163738374610.1016/j.ijheatmasstransfer.2009.01.0441167.80390 – reference: ElwardanyAESazhinSSFarooqAModelling of heating and evaporation of gasoline fuel droplets: a comparative analysis of approximationsFuel201311164364710.1016/j.fuel.2013.03.030 – reference: StrotosGGavaisesMTheodorakakosABergelesGNumerical investigation of the evaporation of two-component dropletsFuel20119041492150710.1016/j.fuel.2011.01.0171140.80391 – reference: PopeKNatererGFWangZPressure drop of packed bed vertical flow for multiphase hydrogen productionInt J Hydrog Energy20113617113381134410.1016/j.ijhydene.2010.10.102 – reference: SazhinSSA multi-dimensional quasi-discrete model for the analysis of diesel fuel droplet heating and evaporationFuel201412923826610.1016/j.fuel.2014.03.028 – reference: HuangLWChenCHTransient combustion of a heating droplet in a gravitational environmentHeat Mass Transf199631533934610.1007/BF02184048 – reference: ErgunSFluid flow through packed columnsJ Chem Eng Prog19524828994 – reference: GavhaneSPatiSSomSKEvaporation of multicomponent liquid fuel droplets: influences of component composition in droplet and vapor concentration in free stream ambienceInt J Therm Sci2016105839510.1016/j.ijthermalsci.2016.03.003 – reference: KoekemoerALuckosAEffect of material type and particle size distribution on pressure drop in packed beds of large particles: extending the Ergun equationFuel201515823223810.1016/j.fuel.2015.05.036 – reference: DaïfABouazizMChesneauXAli ChérifAComparison of multicomponent fuel droplet vaporization experiments in forced convection with the Sirignano modelExp Thermal Fluid Sci199818428229010.1016/S0894-1777(98)10035-3 – reference: WankatPCDecreasing costs of distillation columns with vapor feedsChem Eng Sci201513795596310.1016/j.ces.2015.07.047 – reference: StichlmairJBravoJLFairJRGeneral model for prediction of pressure drop and capacity of countercurrent gas/liquid packed columnsGas Sep Purif198931192810.1016/0950-4214(89)80016-7 – reference: BiroukMGökalpICurrent status of droplet evaporation in turbulent flowsProg Energy Combust Sci200632440842310.1016/j.pecs.2006.05.001 – volume: 52 start-page: 3738 issue: 15–16 year: 2009 ident: 2586_CR21 publication-title: Int J Heat Mass Transf 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Snippet	The aim of this study is to develop a model of a Deethanizer Column (DC). A fuel mixture of Methane CH 4 , Ethane C 2 H 6 , Propane C 3 H 8 , N-butane n-C 4 H... The aim of this study is to develop a model of a Deethanizer Column (DC). A fuel mixture of Methane CH4, Ethane C2H6, Propane C3H8, N-butane n-C4H10 and some...
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SubjectTerms	CAD Computational fluid dynamics Computer aided design Computer simulation Droplets Engineering Engineering Thermodynamics Ethane Fuel mixtures Heat and Mass Transfer Industrial Chemistry/Chemical Engineering Liquid flow Mathematical models Methane Original Porosity Pressure drop Simulation Surface temperature Thermodynamics
Title	CFD simulation of multicomponent mixture within a packed Deethanizer column
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