use ionic liquid to decrease the pressure after the compressor for
TRANSCRIPT
Technology Summary Approach
Progress to Date
Compact, Efficient Air Condi<oning with Ionic Liquid Based Refrigerants
William F. Schneider. Brandon L. Ashfeld, Joan F. Brennecke, Edward J. Maginn, Mark J. McCready, Patrick Murphy, Steven R. Schmid, Mihir Sen and Mark A. Stadtherr:
University of Notre Dame James Raudabaugh, DomeJc, Inc George Mozurkewich, Consultant
Entropy
Tempe
rature
1 2
3
4
Pressure = 100 – 120 atm
Compact, efficient air conditioning (AC) using CO2 -IL mixtures as the working fluid offers an opportunity for cooling systems with efficiency well beyond that of existing ACs. ILs are non-volatile liquid salts with zero GWP that can be designed with thermodynamic and tribological characteristics to optimize them as co-fluids in a vapor compression (VC) cooling cycle. Using systems and molecular modeling to guide designs, we will conduct experimental synthesis and characterization of previously undiscovered compounds for investigation in full-scale, compact AC systems.
Transcri<cal CO2 cycle
Use ionic liquid to decrease the pressure aWer the compressor for CO2 based air-‐condiJoning system
CO2-‐based refrigeraJon systems require approximately 100 Jmes atmospheric pressure for operaJon.
Co-‐fluid
CO2
Discovery -‐ Chemically complexing ILs designed to have tunable CO2 uptake
Inven<on – Design and synthesis of CO2–IL mixtures specifically tailored for VC operaJon
Goal -‐ demonstrate compact, efficient AC with low GWP IL-‐based working fluids • Design, synthesize, and characterize mulJple CO2–IL mixtures
• Demonstrate opJmal mixture in a compact AC to show a 30% improvement in efficiency over exisJng compact ACs using HFC-‐134a/410a refrigerants
PE I: Modeling and Simulation
• Defined VC system level model equations appropriate for CO2-IL co-fluid operations.
PE II: Synthesis and Characterization
• First generation IL (Gen 1 IL) isotherm and pressure-enthalpy models are in place.
• Force field models for Gen 1 IL have been developed. • Validating simulation methods for computing bulk viscosity. • Initiated first principles calculations of new IL candidates.
PE III: Laboratory Demonstration
• Selected 2 ILs for characterization and testing as VC co-fluids. • Accumulated thermodynamic data for selected ILs. • Initiated measurement of viscoelastic properties for selected ILs. • Initiated development of synthesis plans for improved, chemically
complexing ILs.
3D mapping of film thickness for IL 1.
Co-‐fluid CO2 cycle
Ideal refrigeration cycle for refrigerant [IL 1]+CO2 .
References G. Mozurkewich, M.L. Greenfield, W.F. Schneider, D.C. Zeitlow and J.J. Meyer,
“Simulated performance and cofluid dependence of a CO2-‐cofluid refrigeraJon cycle with wet compression,” Int. J. of Refrigera/on, Vol. 25, No. 8, pp. 1123-‐1136, 2002.
B. E. Gurkan, B. F. Goodrich, E. M. Mindrup, L. E. Ficke, M. Massel, S. Seo, T. P. SenWle, H. Wu, M. F. Glaser, J. K. Shah, J. F. Brennecke, E. J. Maginn, and W. F. Schneider, “Molecular Design of High Capacity, Low Viscosity, Chemically Tunable Ionic Liquids for CO2 Capture,” J. Phys. Chem. Le7., 2010, 1, 3494-‐3499