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Understanding the thermodynamic effects of chemically reactive working fluids in the Stirling engine

Energy conversion and management. X, 2024-04, Vol.22, p.100573, Article 100573

2024

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Experimental study of heat pump thermodynamic cycles using CO2 based mixtures - Methodology and first results

AIP Conference Proceedings, 2017, Vol.1814 (1)

2017

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Simultaneous liquid–liquid and vapour–liquid equilibria predictions of selected oxygenated aromatic molecules in mixtures with alkanes, alcohols, water, using the polar GC-PC-SAFT

Chemical engineering research & design, 2014-12, Vol.92 (12), p.2912-2935

2014

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Dendritic bubble growth during the sub-atmospheric boiling of water in a narrow vertical channel

Experimental thermal and fluid science, 2023-02, Vol.141, p.110765, Article 110765

2023

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Propylene and DME solubility in PAG oil: Experimental investigations and simplified modeling

International journal of refrigeration, 2024-09, Vol.165, p.58-69

2024

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Experimental investigation of a new CO2 refrigeration system arrangement for supermarket applications

International journal of refrigeration, 2024-06, Vol.162, p.245-256

2024

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Propylene and DME solubility in PAG oil: Experimental investigations and simplified modeling

International journal of refrigeration, 2024-09, Vol.165, p.58-69

2024

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Experimental analysis of pressure drops and heat transfer coefficient during upward two-phase flow of R-134a/R-245fa mixture in an offset-strip finned passage

International journal of heat and mass transfer, 2022-07, Vol.190, p.122779, Article 122779

2022

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Modeling Liquid–Liquid and Liquid–Vapor Equilibria of Binary Systems Containing Water with an Alkane, an Aromatic Hydrocarbon, an Alcohol or a Gas (Methane, Ethane, CO2 or H2S), Using Group Contribution Polar Perturbed-Chain Statistical Associating Fluid Theory

Industrial & engineering chemistry research, 2011-06, Vol.50 (12), p.7467-7483

2011

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Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a kij Correlation Method Based on London’s Theory. 1. Application to CO2 + n-Alkane, Methane + n-Alkane, and Ethane + n-Alkane Systems

Industrial & engineering chemistry research, 2008-11, Vol.47 (22), p.8847-8858

2008

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Group contribution method with SAFT EOS applied to vapor liquid equilibria of various hydrocarbon series

Fluid phase equilibria, 2004-08, Vol.222, p.67-76

2004

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Vapour–liquid equilibrium (VLE) for the systems furan+n-hexane and furan+toluene. Measurements, data treatment and modeling using molecular models

Fluid phase equilibria, 2013, Vol.337, p.234-245

2013

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Application to binary mixtures of a group contribution SAFT EOS (GC-SAFT)

Fluid phase equilibria, 2005-02, Vol.228-229 (Complete), p.409-419

2005

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Application of GC-SAFT EOS to polycyclic aromatic hydrocarbons

Fluid phase equilibria, 2007-06, Vol.254 (1), p.60-66

2007

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Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a kij Group Contribution Method

Industrial & engineering chemistry research, 2006-09, Vol.45 (20), p.6803-6810

2006

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Application of group contribution SAFT equation of state (GC-SAFT) to model phase behaviour of light and heavy esters

Fluid phase equilibria, 2005-12, Vol.238 (2), p.254-261

2005

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Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k ij Correlation Method Based on London’s Theory. 1. Application to CO 2 + n -Alkane, Methane + n -Alkane, and Ethane + n -Alkane Systems

Industrial & engineering chemistry research, 2008-11, Vol.47 (22), p.8847-8858

2008

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High-Pressure Phase Diagrams of Propane + Decahydronaphthalene and Propane + Naphthalene Mixtures

Journal of chemical and engineering data, 2004-07, Vol.49 (4), p.795-799

2004

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Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a k i j Group Contribution Method

Industrial & engineering chemistry research, 2006-09, Vol.45 (20), p.6803-6810

2006

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Modeling Phase Equilibrium of H 2 + n -Alkane and CO 2 + n -Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a k i j Group Contribution Method

Industrial & engineering chemistry research, 2006-09, Vol.45 (20), p.6803-6810

2006

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High-Pressure Phase Diagrams of Methane + Decahydronaphthalene and Methane + Acenaphthene Mixtures

Journal of chemical and engineering data, 2001-09, Vol.46 (5), p.1269-1273

2001

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Predictive use of a SAFT EOS for phase equilibria of some hydrocarbons and their binary mixtures

Fluid phase equilibria, 2001-04, Vol.180 (1), p.1-26

2001

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Synthesis and characterization of volatile mixed-metal yttrium-barium, barium-copper and yttrium-copper β-diketonatofluoroisopropoxides. Molecular structure of BaY2[μ-OCH(CF3)2]4(thd)4

Polyhedron, 1996-08, Vol.15 (16), p.2707-2718

1996

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Application to binary mixtures of a group contribution SAFT ESO (GC-SAFT)

Fluid phase equilibria, 2005, Vol.228-29, p.409-419

2005

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Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k ij Correlation Method Based on London’s Theory. 1. Application to CO2 + n-Alkane, Methane + n-Alkane, and Ethane + n-Alkane Systems

Industrial & engineering chemistry research, 2008-11, Vol.47 (22), p.8847-8858

2008

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Understanding the thermodynamic effects of chemically reactive working fluids in the Stirling engine

Experimental study of heat pump thermodynamic cycles using CO2 based mixtures - Methodology and first results

Simultaneous liquid–liquid and vapour–liquid equilibria predictions of selected oxygenated aromatic molecules in mixtures with alkanes, alcohols, water, using the polar GC-PC-SAFT

Dendritic bubble growth during the sub-atmospheric boiling of water in a narrow vertical channel

Propylene and DME solubility in PAG oil: Experimental investigations and simplified modeling

Experimental investigation of a new CO2 refrigeration system arrangement for supermarket applications

Propylene and DME solubility in PAG oil: Experimental investigations and simplified modeling

Experimental analysis of pressure drops and heat transfer coefficient during upward two-phase flow of R-134a/R-245fa mixture in an offset-strip finned passage

Modeling Liquid–Liquid and Liquid–Vapor Equilibria of Binary Systems Containing Water with an Alkane, an Aromatic Hydrocarbon, an Alcohol or a Gas (Methane, Ethane, CO2 or H2S), Using Group Contribution Polar Perturbed-Chain Statistical Associating Fluid Theory

Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a kij Correlation Method Based on London’s Theory. 1. Application to CO2 + n-Alkane, Methane + n-Alkane, and Ethane + n-Alkane Systems

Group contribution method with SAFT EOS applied to vapor liquid equilibria of various hydrocarbon series

Vapour–liquid equilibrium (VLE) for the systems furan+n-hexane and furan+toluene. Measurements, data treatment and modeling using molecular models

Application to binary mixtures of a group contribution SAFT EOS (GC-SAFT)

Application of GC-SAFT EOS to polycyclic aromatic hydrocarbons

Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a kij Group Contribution Method

Application of group contribution SAFT equation of state (GC-SAFT) to model phase behaviour of light and heavy esters

Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k ij Correlation Method Based on London’s Theory. 1. Application to CO 2 + n -Alkane, Methane + n -Alkane, and Ethane + n -Alkane Systems

High-Pressure Phase Diagrams of Propane + Decahydronaphthalene and Propane + Naphthalene Mixtures

Modeling Phase Equilibrium of H2 + n-Alkane and CO2 + n-Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a k i j Group Contribution Method

Modeling Phase Equilibrium of H 2 + n -Alkane and CO 2 + n -Alkane Binary Mixtures Using a Group Contribution Statistical Association Fluid Theory Equation of State (GC−SAFT−EOS) with a k i j Group Contribution Method

High-Pressure Phase Diagrams of Methane + Decahydronaphthalene and Methane + Acenaphthene Mixtures

Predictive use of a SAFT EOS for phase equilibria of some hydrocarbons and their binary mixtures

Synthesis and characterization of volatile mixed-metal yttrium-barium, barium-copper and yttrium-copper β-diketonatofluoroisopropoxides. Molecular structure of BaY2[μ-OCH(CF3)2]4(thd)4

Application to binary mixtures of a group contribution SAFT ESO (GC-SAFT)

Modeling Phase Equilibria of Asymmetric Mixtures Using a Group-Contribution SAFT (GC-SAFT) with a k ij Correlation Method Based on London’s Theory. 1. Application to CO2 + n-Alkane, Methane + n-Alkane, and Ethane + n-Alkane Systems

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