A gas ejector for CO2 supercritical cycles

Abstract The CO2 ejectors are recently often used as the main expansion device in the modern refrigeration cycles. On the other hand, according to the newest literature the implementation the ejectors into supercritical CO2 power cycles increase its performance. The recent studies showed that in case of the power cycles the ejector pressure lift and mass entrainment ratio are relatively high. Therefore, the main scope of this paper is the investigation of the possibilities of designing the ejector for supercritical Brayton CO2 system. The CFD based computational tool was used to design the ejector for the considered cycle. The system analysis was used to define the ejector on design point. The results of that analysis showed that the required pressure lift and must be equal to 103 bar and mass entrainment ratio equal to 0.995, respectively. The CFD-based evaluation of the proposed ejector showed that these values are impossible to achieve. Therefore, the modifications of the crucial ejector dimensions was performed to increase its performance. Nevertheless, the maximum possible pressure lift for the proposed ejector was equal to 60 bar The analysis of the gathered results showed that the design of the ejector fulfilling the system requirements may be impossible to achieve.

[1]  Jostein Pettersen,et al.  Fundamental process and system design issues in CO2 vapor compression systems , 2004 .

[2]  Ali Abbas,et al.  A comparative study of solar heliostat assisted supercritical CO2 recompression Brayton cycles: Dynamic modelling and control strategies , 2017 .

[3]  Gumersindo Verdú,et al.  Commercial refrigeration – An overview of current status , 2015 .

[4]  Daniel Favrat,et al.  Transcritical or supercritical CO2 cycles using both low- and high-temperature heat sources , 2012 .

[5]  Andy Pearson,et al.  ICR0021 CARBON DIOXIDE - NEW USES FOR AN OLD REFRIGERANT , 2005 .

[6]  M. A. Reyes-Belmonte,et al.  Optimization of a recompression supercritical carbon dioxide cycle for an innovative central receiver solar power plant , 2016 .

[7]  I. Alatiqi,et al.  Evaluation of steam jet ejectors , 2002 .

[8]  A. Nowak,et al.  System model derivation of the CO2 two-phase ejector based on the CFD-based reduced-order model , 2018 .

[9]  Armin Hafner,et al.  A computational model of a transcritical R744 ejector based on a homogeneous real fluid approach , 2013 .

[10]  Satha Aphornratana,et al.  A theoretical and experimental study of a small-scale steam jet refrigerator , 1995 .

[11]  Armin Hafner,et al.  1D Computational model of a two-phase R744 ejector for expansion work recovery. , 2011 .

[12]  Armin Hafner,et al.  R744 ejector technology future perspectives , 2016 .

[13]  Robbie McNaughton,et al.  Thermodynamic feasibility of alternative supercritical CO2 Brayton cycles integrated with an ejector , 2016 .

[14]  Armin Hafner,et al.  Modified homogeneous relaxation model for the r744 trans-critical flow in a two-phase ejector , 2018 .

[15]  Armin Hafner,et al.  Development and performance mapping of a multi-ejector expansion work recovery pack for R744 vapour compression units. , 2015 .

[16]  M. McLinden,et al.  NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 8.0 , 2007 .

[17]  Seungjoon Baik,et al.  Review of supercritical CO2 power cycle technology and current status of research and development , 2015 .

[18]  Aly Karameldin,et al.  Modelling and simulation of steam jet ejectors , 1999 .

[19]  Waclaw Kus,et al.  CFD-based shape optimisation of a CO2 two-phase ejector mixing section , 2016 .

[20]  J. Navarro-Esbrí,et al.  Analysis based on EU Regulation No 517/2014 of new HFC/HFO mixtures as alternatives of high GWP refrigerants in refrigeration and HVAC systems , 2015 .

[21]  Henryk Rusinowski,et al.  Adaptive Simulation Model of a Double-Pressure Heat Recovery Steam Generator for Current Optimization in Control Systems , 2017, IEEE Transactions on Industry Applications.

[22]  Chris Manzie,et al.  Extremum-seeking control of a supercritical carbon-dioxide closed Brayton cycle in a direct-heated solar thermal power plant , 2013 .

[23]  Ali Abbas,et al.  Analysis for flexible operation of supercritical CO2 Brayton cycle integrated with solar thermal systems , 2017 .

[24]  David Sánchez,et al.  Supercritical carbon dioxide cycles for power generation: A review , 2017 .

[25]  Armin Hafner,et al.  Shape optimisation of a two-phase ejector for CO2 refrigeration systems , 2017 .

[26]  Juergen Koehler,et al.  Numerical investigation of a two-phase CO2 ejector , 2014 .

[27]  Pardeep Garg,et al.  Supercritical carbon dioxide Brayton cycle for concentrated solar power , 2013 .

[28]  Paolo Chiesa,et al.  An Integrated Lumped Parameter-CFD approach for off-design ejector performance evaluation , 2015 .

[29]  Armin Hafner,et al.  A CFD-based investigation of the energy performance of two-phase R744 ejectors to recover the expansion work in refrigeration systems: An irreversibility analysis , 2014 .

[30]  G. Lorentzen Revival of carbon dioxide as a refrigerant , 1994 .

[31]  Alan A. Kornhauser,et al.  The Use of an Ejector as a Refrigerant Expander , 1990 .

[32]  Armin Hafner,et al.  Mathematical modelling of supersonic two-phase R744 flows through converging–diverging nozzles: The effects of phase transition models , 2013 .

[33]  Fahad A. Al-Sulaiman,et al.  Performance comparison of different supercritical carbon dioxide Brayton cycles integrated with a solar power tower , 2015 .

[34]  José Sierra-Pallares,et al.  A computational study about the types of entropy generation in three different R134a ejector mixing chambers , 2016 .

[35]  Armin Hafner,et al.  Full-scale multi-ejector module for a carbon dioxide supermarket refrigeration system: Numerical study of performance evaluation , 2017 .

[36]  Sébastien Poncet,et al.  Turbulence modeling of a single-phase R134a supersonic ejector. Part 1: Numerical benchmark , 2016 .

[37]  J. Anderson,et al.  Computational fluid dynamics : the basics with applications , 1995 .

[38]  Armin Hafner,et al.  HEM and HRM accuracy comparison for the simulation of CO2 expansion in two-phase ejectors for supermarket refrigeration systems , 2017 .

[39]  Eckhard A. Groll,et al.  Investigation on performance of variable geometry ejectors for CO2 refrigeration cycles , 2012 .

[40]  Armin Hafner,et al.  Application range of the HEM approach for CO2 expansion inside two-phase ejectors for supermarket refrigeration systems , 2015 .

[41]  Kenneth Bank Madsen,et al.  Performance mapping of the R744 ejectors for refrigeration and air conditioning supermarket application: A hybrid reduced-order model , 2018, Energy.