On the Density Prediction of Multicomponent Hydrocarbon Mixtures at Near- and Supercritical Conditions

[1]  H. Li,et al.  More Accurate Determination of Isothermal Compressibility and Isobaric Thermal Expansivity Using Volume-Translated Equations of State , 2022, Fluid Phase Equilibria.

[2]  R. Privat,et al.  SAFT and cubic EoS: Type of deviation from ideality naturally predicted in the absence of BIPs. Application to the modelling of athermal mixtures , 2021 .

[3]  E. Stenby,et al.  Density Modeling of High-Pressure Mixtures using Cubic and Non-Cubic EoS and an Excess Volume Method , 2020, Fluid Phase Equilibria.

[4]  M. Belyakov,et al.  Thermodynamic properties of a model hydrocarbon ternary mixture in the vicinity of critical point: Measurements and modeling with crossover equation of state , 2020 .

[5]  Erjiang Hu,et al.  A new surrogate fuel for emulating the physical and chemical properties of RP-3 kerosene , 2020 .

[6]  Yong Qian,et al.  Surrogate fuels for RP-3 kerosene formulated by emulating molecular structures, functional groups, physical and chemical properties , 2019, Combustion and Flame.

[7]  M. Birouk,et al.  On greenhouse gas emissions and thermal efficiency of natural gas/diesel dual-fuel engine at low load conditions: Coupled effect of injector rail pressure and split injection , 2019, Applied Energy.

[8]  Zhong Huang,et al.  A multi-component surrogate of commercial diesel for trans-critical and supercritical injections study , 2019, Fuel.

[9]  M. Gavaises,et al.  Simulation of supercritical diesel jets using the PC-SAFT EoS , 2019, The Journal of Supercritical Fluids.

[10]  H. Ghassemi,et al.  Fully transient modeling of the heavy fuel oil droplets evaporation , 2018, Fuel.

[11]  Phoevos Koukouvinis,et al.  Simulation of transcritical fluid jets using the PC-SAFT EoS , 2018, J. Comput. Phys..

[12]  Patrick G. Szymkowicz,et al.  Development of a Diesel Surrogate Fuel Library , 2018, Fuel.

[13]  Thanh NguyenThi,et al.  Density Measurements of Waste Cooking Oil Biodiesel and Diesel Blends Over Extended Pressure and Temperature Ranges , 2018 .

[14]  Zilong Li,et al.  A new methodology for diesel surrogate fuel formulation: Bridging fuel fundamental properties and real engine combustion characteristics , 2018 .

[15]  E. Hassel,et al.  Thermophysical properties of Diesel fuel over a wide range of temperatures and pressures , 2018 .

[16]  Chien-pei Chen,et al.  Simulated Kinetics and Chemical and Physical Properties of a Four-Component Diesel Surrogate Fuel , 2017 .

[17]  Xiaohan Wang,et al.  Property evaluations of hydrocarbon fuels under supercritical conditions based on cubic equation of state , 2017 .

[18]  Mirjana Lj. Kijevčanin,et al.  Thermodynamic properties of biodiesel and petro-diesel blends at high pressures and temperatures. Experimental and modeling , 2016 .

[19]  Z. Tao,et al.  Numerical investigation of heat transfer characteristics and flow resistance of kerosene RP-3 under supercritical pressure , 2015 .

[20]  G. Montoya,et al.  Modelling the phase behavior of alkane mixtures in wide ranges of conditions: New parameterization and predictive correlations of binary interactions for the RKPR EOS , 2015 .

[21]  R. Privat,et al.  Extension of the E-PPR78 equation of state to predict fluid phase equilibria of natural gases containing carbon monoxide, helium-4 and argon , 2015 .

[22]  Daniel T. Banuti,et al.  Crossing the Widom-line – Supercritical pseudo-boiling , 2015 .

[23]  E. Stenby,et al.  PVT modeling of reservoir fluids using PC-SAFT EoS and Soave-BWR EoS , 2015 .

[24]  Q. Bi,et al.  Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure , 2014 .

[25]  Jason Martz,et al.  A surrogate for emulating the physical and chemical properties of conventional jet fuel , 2014 .

[26]  M. J. Gómez,et al.  High pressure phase behavior modeling of asymmetric alkane + alkane binary systems with the RKPR EOS , 2014 .

[27]  Mark A. McHugh,et al.  Volume-translated cubic EoS and PC-SAFT density models and a free volume-based viscosity model for hydrocarbons at extreme temperature and pressure conditions , 2013 .

[28]  S. Leekumjorn,et al.  Phase behavior of reservoir fluids: Comparisons of PC-SAFT and cubic EOS simulations ☆ , 2013 .

[29]  Majid Mohadesi,et al.  Densities and Kinematic Viscosities in Biodiesel–Diesel Blends at Various Temperatures , 2013 .

[30]  Wenming Yang,et al.  Spray and combustion visualization of bio-diesel in a direct injection diesel engine , 2013 .

[31]  L. Tavlarides,et al.  Thermophysical properties needed for the development of the supercritical diesel combustion technology: Evaluation of diesel fuel surrogate models , 2012 .

[32]  Deepak Tapriyal,et al.  Prediction of hydrocarbon densities at extreme conditions using volume-translated SRK and PR equations of state fit to high temperature, high pressure PVT data , 2012 .

[33]  I. Polishuk.  Semi-Theoretical Versus Entirely Empirical: Comparing SAFT + Cubic and Soave–Benedict–Webb–Rubin (SBWR) Equations of State , 2011 .

[34]  Z. Tao,et al.  Density Measurements of Endothermic Hydrocarbon Fuel at Sub- and Supercritical Conditions , 2011 .

[35]  Mark A. McHugh,et al.  Equation of state modeling of high-pressure, high-temperature hydrocarbon density data , 2010 .

[36]  Jean-Noël Jaubert,et al.  Relationship between the binary interaction parameters (kij) of the Peng–Robinson and those of the Soave–Redlich–Kwong equations of state: Application to the definition of the PR2SRK model , 2010 .

[37]  Charles J. Mueller,et al.  Recent progress in the development of diesel surrogate fuels , 2009 .

[38]  F. Mutelet,et al.  Addition of the Hydrogen Sulfide Group to the PPR78 Model (Predictive 1978, Peng–Robinson Equation of State with Temperature Dependent kij Calculated through a Group Contribution Method) , 2008 .

[39]  T. Bruno,et al.  Composition-explicit distillation curves of diesel fuel with glycol ether and glycol ester oxygenates: fuel analysis metrology to enable decreased particulate emissions. , 2008, Environmental science & technology.

[40]  Nicholas P. Cernansky,et al.  Experimental investigation of surrogates for jet and diesel fuels , 2008 .

[41]  F. Mutelet,et al.  Predicting the phase equilibria of CO2+hydrocarbon systems with the PPR78 model (PR EOS and kij calculated through a group contribution method) , 2008 .

[42]  F. Mutelet,et al.  Addition of the Nitrogen Group to the PPR78 Model (Predictive 1978, Peng Robinson EOS with Temperature-Dependent kij Calculated through a Group Contribution Method) , 2008 .

[43]  Norbert Peters,et al.  Experimental Validation of a Surrogate Fuel for Diesel , 2007 .

[44]  Jean-Noël Jaubert,et al.  Extension of the PPR78 model (Predictive 1978, Peng-Robinson EOS with temperature dependent kij calculated through a group contribution method) to systems containing naphtenic compounds , 2005 .

[45]  J. Mollerup,et al.  Development and application of a three-parameter RK–PR equation of state , 2005 .

[46]  Jean-Noël Jaubert,et al.  VLE predictions with the Peng–Robinson equation of state and temperature dependent kij calculated through a group contribution method , 2004 .

[47]  Erich A. Müller,et al.  Molecular-Based Equations of State for Associating Fluids: A Review of SAFT and Related Approaches , 2001 .

[48]  Gabriele Sadowski,et al.  Perturbed-Chain SAFT: An Equation of State Based on a Perturbation Theory for Chain Molecules , 2001 .

[49]  Giorgio S. Soave,et al.  An effective modification of the Benedict–Webb–Rubin equation of state , 1999 .

[50]  Giorgio S. Soave,et al.  A noncubic equation of state for the treatment of hydrocarbon fluids at reservoir conditions , 1995 .

[51]  W. Hallett,et al.  A continuous thermodynamics model for multicomponent droplet vaporization , 1995 .

[52]  Lixiong Li,et al.  ESTIMATION OF CRITICAL PROPERTIES OF BINARY MIXTURES USING GROUP CONTRIBUTION METHODS , 1990 .

[53]  K. E. Starling,et al.  Multiparameter corresponding‐states correlation of coal‐fluid thermodynamic properties , 1982 .

[54]  W. J. Sim,et al.  Prediction of Vapor-Liquid Equilibria of Undefined Mixtures , 1980 .

[55]  D. Peng,et al.  A New Two-Constant Equation of State , 1976 .

[56]  S. Saito,et al.  AN IMPROVED GENERALIZED BWR EQUATION OF STATE APPLICABLE TO LOW REDUCED TEMPERATURES , 1975 .

[57]  G. Soave.  Equilibrium constants from a modified Redlich-Kwong equation of state , 1972 .

[58]  D. Robinson,et al.  New mixing rules for the BWR parameters to predict mixture properties , 1972 .

[59]  K. E. Starling,et al.  Enthalpy of Mixtures by Modified BWR Equation , 1970 .

[60]  Manson Benedict,et al.  An Empirical Equation for Thermodynamic Properties of Light Hydrocarbons and Their Mixtures I. Methane, Ethane, Propane and n‐Butane , 1940 .