Characterization of mixed CO2 + TBPB hydrates for refrigeration applications

The present work investigates the use of semiclathrate hydrates, formed from CO2 + tetra-nbutylphosphonium bromide (TBPB) + water mixtures, as appropriate media for cold storage and distribution in refrigeration applications. Previous studies show that these hydrates are able to trap molecules of carbon dioxide resulting in mixed hydrates. Calorimetry devices were used for determining the dissociation enthalpies of mixed CO2 + TBPB hydrates under various stability conditions (P, T) and salt concentrations. The results reveal that mixed CO2 + TBPB hydrates can be considered as good candidates for air-conditioning, due to positive melting temperatures (between 282 to 289 K) at moderate CO2 pressures (between 0.5 to 2 MPa). A hydrate solid fraction model was developed based on a CO2 mass balance taking into account CO2 solubility in aqueous tetrabutylphosphonium salt solution. The salt effect parameter was evaluated in order to estimate the influence of TBPB on the CO2 solubility. Finally, in order to characterize the flow behavior of mixed CO2 + TBPB hydrate slurries, a rheological study was carried out in a dynamic loop and an Ostwald-de Waele model was obtained.

[1]  A. Delahaye,et al.  CO2 Enclathration in Hydrates of Peralkyl-(Ammonium/Phosphonium) Salts: Stability Conditions and Dissociation Enthalpies , 2010 .

[2]  A. Delahaye,et al.  Rheological study of CO2 hydrate slurry in a dynamic loop applied to secondary refrigeration , 2008 .

[3]  Anthony Delahaye,et al.  Thermodynamic properties of THF + CO2 hydrates in relation with refrigeration applications , 2008 .

[4]  L. Fournaison,et al.  Phase equilibrium and dissociation enthalpy for semi-clathrate hydrate of CO2 + TBAB , 2008 .

[5]  Anthony Delahaye,et al.  Solid fraction modelling for CO2 and CO2-THF hydrate slurries used as secondary refrigerants , 2007 .

[6]  J. Guilpart,et al.  Comparison of the performance of different ice slurry types depending on the application temperature , 2006 .

[7]  J. Petitet,et al.  Modelling of the available latent heat of a CO2 hydrate slurry in an experimental loop applied to secondary refrigeration , 2006 .

[8]  J. Herri,et al.  Rheological study of TBAB hydrate slurries as secondary two-phase refrigerants , 2005 .

[9]  Laurence Fournaison,et al.  CO2 Hydrates in Refrigeration Processes , 2004 .

[10]  L. Diamond,et al.  Solubility of CO2 in water from −1.5 to 100 °C and from 0.1 to 100 MPa: evaluation of literature data and thermodynamic modelling , 2003 .

[11]  T. Ebinuma,et al.  Separation of Gas Molecule Using Tetra-n-butyl Ammonium Bromide Semi-Clathrate Hydrate Crystals , 2003 .

[12]  G. Perron,et al.  Salting-in of alcohols in aqueous solutions by tetraalkylammonium bromides at the freezing temperature , 1978 .

[13]  V. F. Sergeeva SALTING-OUT AND SALTING-IN OF NON-ELECTROLYTES , 1965 .

[14]  Anthony Delahaye,et al.  Effect of THF on Equilibrium Pressure and Dissociation Enthalpy of CO2 Hydrates Applied to Secondary Refrigeration , 2006 .

[15]  Sandrine Marinhas Caractérisation thermohydraulique de coulis d'hydrates de gaz en vue d'une application à la réfrigération secondaire , 2006 .

[16]  C. Poole,et al.  Solute—solvent interactions in tetra-n-butylphosphonium salts studied by gas chromatography , 1988 .

[17]  R. Pierotti,et al.  THE SOLUBILITY OF GASES IN LIQUIDS , 1963 .

[18]  J. Kitchener,et al.  The salting-in effect , 1951 .