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Thermodynamics analysis of hydrogen storage based on compressed gaseous hydrogen, liquid hydrogen and cryo-compressed hydrogen

International journal of hydrogen energy, 2019-06, Vol.44 (31), p.16833-16840

2019

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The isobaric heat capacity of 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) at temperatures from (230 to 285) K and pressures up to 8 MPa using a new flow calorimeter

The Journal of chemical thermodynamics, 2022-01, Vol.164, p.106626, Article 106626

2022

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Phase equilibrium for the binary mixture of {1,1-difluoroethane (R152a)+trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} at various temperatures from 258.150 to 288.150K

Fluid phase equilibria, 2013-10, Vol.355, p.99-103

2013

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Adiabatic calorimeter for isochoric specific heat capacity measurements and experimental data of compressed liquid R1234yf

The Journal of chemical thermodynamics, 2018-10, Vol.125, p.86-92

2018

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Development of mobile miniature natural gas liquefiers

Frontiers in Energy, 2020-12, Vol.14 (4), p.667-682

2020

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Effects of slip length and hydraulic diameter on hydraulic entrance length of microchannels with superhydrophobic surfaces

Frontiers in Energy, 2020-03, Vol.14 (1), p.127-138

2020

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(Vapour + liquid) equilibrium data for the binary system of {trifluoroiodomethane (R13I1) + trans-1, 3, 3, 3-tetrafluoropropene (R1234ze (E))} at various temperatures from (258.150 to 298.150) K

The Journal of chemical thermodynamics, 2012-04, Vol.47, p.397-401

2012

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Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows

The Journal of chemical thermodynamics, 2011-03, Vol.43 (3), p.505-510

2011

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Phase equilibrium for the binary azeotropic mixture of trifluoroiodomethane (R13I1 )+ 1,1,2,2-tetrafluoroethane (R134) at temperatures from 258.150 to 283.150K

Fluid phase equilibria, 2012-02, Vol.315, p.35-39

2012

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Vapor-liquid equilibria of CH4, CO2 and their binary system CH4 ＋ CO2： A comparison between the molecular simulation and equation of state

Science China. Technological sciences, 2015-04, Vol.58 (4), p.650-658

2015

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(Vapour+liquid) equilibrium data for the azeotropic {1,1-difluoroethane (R152a)+1,1,2,2-Tetrafluoroethane (R134)} system at various temperatures from (258.150 to 288.150)K

The Journal of chemical thermodynamics, 2012-11, Vol.54, p.129-133

2012

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Performances comparison of adsorption hydrogen storage tanks at a wide temperature and pressure zone

International journal of hydrogen energy, 2023-08, Vol.48 (69), p.26881-26893

2023

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Isothermal (vapour + liquid) equilibrium for the binary {1,1,2,2-tetrafluoroethane (R134) + propane (R290)} and {1,1,2,2-tetrafluoroethane (R134) + isobutane (R600a)} systems

The Journal of chemical thermodynamics, 2010-09, Vol.42 (9), p.1152-1157

2010

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A new heat transfer model based on non-equilibrium theory for annular flow condensation-part Ⅱ: Ternary zeotropic mixtures

International journal of heat and mass transfer, 2024-04, Vol.221, p.125026, Article 125026

2024

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Vapor−Liquid Equilibria for 1,1,2,2-Tetrafluoroethane (R134) + Fluoroethane (R161) at Temperatures between (263.15 and 288.15) K

Journal of chemical and engineering data, 2010-09, Vol.55 (9), p.3383-3386

2010

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Thermodynamic analysis of a petroleum volatile organic compounds (VOCs) condensation recovery system combined with mixed-refrigerant refrigeration

International journal of refrigeration, 2020-08, Vol.116, p.23-35

2020

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Measurement of Critical Parameters for the Binary Mixture of R744 (Carbon Dioxide) + R1243zf (3,3,3-Trifluoropropene)

Journal of chemical and engineering data, 2022-09, Vol.67 (9), p.2128-2135

2022

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Experimental study on boiling flow patterns of the zeotropic mixtures of R290/R600a in a horizontal smooth tube

International journal of heat and mass transfer, 2022-11, Vol.196, p.123268, Article 123268

2022

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A new heat transfer model based on non-equilibrium film theory for annular flow condensation of binary zeotropic mixtures

International journal of heat and mass transfer, 2023-05, Vol.205, p.123899, Article 123899

2023

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A generalized isobaric specific heat capacity model for hydrocarbons, hydrofluorocarbons, hydrofluoroolefins and their mixtures in the liquid phase

Fluid phase equilibria, 2024-05, Vol.580, p.114057, Article 114057

2024

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Isothermal Vapor−Liquid Equilibria for 1,1-Difluoroethane (R152a) + Propane (R290) at Temperatures between (254.31 and 287.94) K

Journal of chemical and engineering data, 2010-06, Vol.55 (6), p.2145-2148

2010

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The isobaric specific heat capacity and viscosity for 3,3,3-trifluoroprop-1-ene in liquid phase at temperatures from (230 to 293) K and pressures up to 8 MPa

The Journal of chemical thermodynamics, 2024-07, Vol.194, p.107277, Article 107277

2024

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A new apparatus for measurement of the critical p-ρ-T properties based on the variable-volume method

International journal of refrigeration, 2022-04, Vol.136, p.220-228

2022

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Density and isochoric heat capacity of {x trans-1,3,3,3-Tetrafluoropropene + (1-x) Propane} at temperatures from (285.45 to 349.71) K and pressures up to 10.384 MPa

International journal of refrigeration, 2023-06, Vol.150, p.349-356

2023

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The experimental investigation of the vapor-liquid-liquid and solid-liquid phase equilibrium for (difluoromethane + octafluoropropane) mixture

Fluid phase equilibria, 2022-07, Vol.558, p.113454, Article 113454

2022

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Thermodynamics analysis of hydrogen storage based on compressed gaseous hydrogen, liquid hydrogen and cryo-compressed hydrogen

The isobaric heat capacity of 2,3,3,3-tetrafluoroprop-1-ene (R1234yf) at temperatures from (230 to 285) K and pressures up to 8 MPa using a new flow calorimeter

Phase equilibrium for the binary mixture of {1,1-difluoroethane (R152a)+trans-1,3,3,3-tetrafluoropropene (R1234ze (E))} at various temperatures from 258.150 to 288.150K

Adiabatic calorimeter for isochoric specific heat capacity measurements and experimental data of compressed liquid R1234yf

Development of mobile miniature natural gas liquefiers

Effects of slip length and hydraulic diameter on hydraulic entrance length of microchannels with superhydrophobic surfaces

(Vapour + liquid) equilibrium data for the binary system of {trifluoroiodomethane (R13I1) + trans-1, 3, 3, 3-tetrafluoropropene (R1234ze (E))} at various temperatures from (258.150 to 298.150) K

Experimental measurement of vapor pressures and (vapor + liquid) equilibrium for {1,1,1,2-tetrafluoroethane (R134a) + propane (R290)} by a recirculation apparatus with view windows

Phase equilibrium for the binary azeotropic mixture of trifluoroiodomethane (R13I1 )+ 1,1,2,2-tetrafluoroethane (R134) at temperatures from 258.150 to 283.150K

Vapor-liquid equilibria of CH4, CO2 and their binary system CH4 ＋ CO2： A comparison between the molecular simulation and equation of state

(Vapour+liquid) equilibrium data for the azeotropic {1,1-difluoroethane (R152a)+1,1,2,2-Tetrafluoroethane (R134)} system at various temperatures from (258.150 to 288.150)K

Performances comparison of adsorption hydrogen storage tanks at a wide temperature and pressure zone

Isothermal (vapour + liquid) equilibrium for the binary {1,1,2,2-tetrafluoroethane (R134) + propane (R290)} and {1,1,2,2-tetrafluoroethane (R134) + isobutane (R600a)} systems

A new heat transfer model based on non-equilibrium theory for annular flow condensation-part Ⅱ: Ternary zeotropic mixtures

Vapor−Liquid Equilibria for 1,1,2,2-Tetrafluoroethane (R134) + Fluoroethane (R161) at Temperatures between (263.15 and 288.15) K

Thermodynamic analysis of a petroleum volatile organic compounds (VOCs) condensation recovery system combined with mixed-refrigerant refrigeration

Measurement of Critical Parameters for the Binary Mixture of R744 (Carbon Dioxide) + R1243zf (3,3,3-Trifluoropropene)

Experimental study on boiling flow patterns of the zeotropic mixtures of R290/R600a in a horizontal smooth tube

A new heat transfer model based on non-equilibrium film theory for annular flow condensation of binary zeotropic mixtures

A generalized isobaric specific heat capacity model for hydrocarbons, hydrofluorocarbons, hydrofluoroolefins and their mixtures in the liquid phase

Isothermal Vapor−Liquid Equilibria for 1,1-Difluoroethane (R152a) + Propane (R290) at Temperatures between (254.31 and 287.94) K

The isobaric specific heat capacity and viscosity for 3,3,3-trifluoroprop-1-ene in liquid phase at temperatures from (230 to 293) K and pressures up to 8 MPa

A new apparatus for measurement of the critical p-ρ-T properties based on the variable-volume method

Density and isochoric heat capacity of {x trans-1,3,3,3-Tetrafluoropropene + (1-x) Propane} at temperatures from (285.45 to 349.71) K and pressures up to 10.384 MPa

The experimental investigation of the vapor-liquid-liquid and solid-liquid phase equilibrium for (difluoromethane + octafluoropropane) mixture

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