Low transition temperature mixtures as innovative and sustainable CO2 capture solvents.

The potential of three newly discovered low transition temperature mixtures (LTTMs) is explored as sustainable substituents for the traditional carbon dioxide (CO2) absorbents. LTTMs are mixtures of two solid compounds, a hydrogen bond donor (HBD) and a hydrogen bond acceptor (HBA), which form liquids upon mixing with melting points far below those of the individual compounds. In this work the HBD is lactic acid and the HBAs are tetramethylammonium chloride, tetraethylammonium chloride, and tetrabutylammonium chloride. These compounds were found to form LTTMs for the first time at molar ratios of HBD:HBA = 2:1. First, the LTTMs were characterized by determining the thermal operating window (e.g., decomposition temperature and glass transition temperature) and the physical properties (e.g., density and viscosity). Thereafter, the phase behavior of CO2 with the LTTMs has been measured using a gravimetric magnetic suspension balance operating in the static mode at 308 and 318 K and pressures up to 2 MPa. The CO2 solubility increased with increasing chain length, increasing pressure, and decreasing temperature. The Peng-Robinson equation of state was applied to correlate the phase equilibria. From the solubility data, thermodynamic parameters were determined (e.g., Henry's law coefficient and enthalpy of absorption). The heat of absorption was found to be similar to that in conventional physical solvents (-11.21 to -14.87 kJ·mol(-1)). Furthermore, the kinetics in terms of the diffusion coefficient of CO2 in all LTTMs were determined (10(-11)-10(-10) m(2)·s(-1)). Even though the CO2 solubilities in the studied LTTMs were found to be slightly lower than those in thoroughly studied conventional physical solvents, LTTMs are a promising new class of absorbents due to their low cost, their environmentally friendly character, and their easy tunability, allowing further optimization for carbon capture.

[1]  David L Davies,et al.  Novel solvent properties of choline chloride/urea mixtures. , 2003, Chemical communications.

[2]  Ziniu Yu,et al.  A Mini-Review on Greenness of Ionic Liquids , 2009 .

[3]  B. Han,et al.  Solubility of CO2 in a Choline Chloride + Urea Eutectic Mixture , 2008 .

[4]  G. Höhne,et al.  Differential Scanning Calorimetry , 2007 .

[5]  Joan F. Brennecke,et al.  Solubilities and Thermodynamic Properties of Gases in the Ionic Liquid 1-n-Butyl-3-methylimidazolium Hexafluorophosphate , 2002 .

[6]  J. J. Renard,et al.  Fate of ammonia in the atmosphere--a review for applicability to hazardous releases. , 2004, Journal of hazardous materials.

[7]  B. Hille,et al.  The Inner Quaternary Ammonium Ion Receptor in Potassium Channels of the Node of Ranvier , 1972, The Journal of general physiology.

[8]  Maaike C. Kroon,et al.  A new low transition temperature mixture (LTTM) formed by choline chloride + lactic acid : characterization as solvent for CO2 capture , 2013 .

[9]  Mark B. Shiflett,et al.  Solubility and diffusivity of hydrofluorocarbons in room-temperature ionic liquids , 2006 .

[10]  Paitoon Tontiwachwuthikul,et al.  Analysis of Monoethanolamine and Its Oxidative Degradation Products during CO2 Absorption from Flue Gases: A Comparative Study of GC-MS, HPLC-RID, and CE-DAD Analytical Techniques and Possible Optimum Combinations , 2006 .

[11]  J. Brennecke,et al.  Why Is CO2 so soluble in imidazolium-based ionic liquids? , 2004, Journal of the American Chemical Society.

[12]  R. Borah,et al.  Non-isothermal thermogravimetric pyrolysis kinetics of waste petroleum refinery sludge by isoconversional approach , 2007 .

[13]  Jin Han,et al.  Determination of Absorption Rate and Capacity of CO2 in Ionic Liquids at Atmospheric Pressure by Thermogravimetric Analysis , 2011 .

[14]  J. Plaza,et al.  Modeling CO2 capture with aqueous monoethanolamine , 2003 .

[15]  J. Brennecke,et al.  High-Pressure Phase Behavior of Carbon Dioxide with Imidazolium-Based Ionic Liquids , 2004 .

[16]  Luís M. N. B. F. Santos,et al.  Alkylimidazolium based ionic liquids: impact of cation symmetry on their nanoscale structural organization. , 2013, The journal of physical chemistry. B.

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

[18]  A. Yokozeki,et al.  Solubilities and Diffusivities of Carbon Dioxide in Ionic Liquids: [bmim][PF6] and [bmim][BF4] , 2005 .

[19]  Farouq S. Mjalli,et al.  Solubility of CO2 in deep eutectic solvents: Experiments and modelling using the Peng-Robinson equation of state , 2014 .

[20]  R. Reid,et al.  The Properties of Gases and Liquids , 1977 .

[21]  Raphael Idem,et al.  Comprehensive study of the kinetics of the oxidative degradation of CO2 loaded and concentrated aqueous monoethanolamine (MEA) with and without sodium metavanadate during CO2 absorption from flue gases , 2006 .

[22]  Luís M. N. B. F. Santos,et al.  Volatility study of [C1C1im][NTf2] and [C2C3im][NTf2] ionic liquids , 2014 .

[23]  J. Valderrama,et al.  Critical Properties, Normal Boiling Temperatures, and Acentric Factors of Fifty Ionic Liquids , 2007 .

[24]  J. Segovia-Hernández,et al.  Author's Personal Copy Chemical Engineering Research and Design 9 2 ( 2 0 1 4 ) 1–12 , 2022 .

[25]  Juan A. Lazzús,et al.  Critical Properties, Normal Boiling Temperature, and Acentric Factor of Another 200 Ionic Liquids , 2008 .

[26]  J. Carson,et al.  Enthalpy of solution of carbon dioxide in (water + monoethanolamine, or diethanolamine, orN-methyldiethanolamine) and (water + monoethanolamine + N-methyldiethanolamine) atT = 298.15 K , 2000 .

[27]  M. C. Kroon,et al.  Low-transition-temperature mixtures (LTTMs): a new generation of designer solvents. , 2013, Angewandte Chemie.

[28]  Joan F. Brennecke,et al.  High-Pressure Phase Behavior of Ionic Liquid/CO2 Systems , 2001 .

[29]  L. I. Eide,et al.  Precombustion Decarbonisation Processes , 2005 .

[30]  K. Joback,et al.  ESTIMATION OF PURE-COMPONENT PROPERTIES FROM GROUP-CONTRIBUTIONS , 1987 .

[31]  John A. Nelder,et al.  A Simplex Method for Function Minimization , 1965, Comput. J..