Skip to main content
Log in

Comprehensive performance analysis and optimization of 1,3-dimethylimidazolylium dimethylphosphate-water binary mixture for a single effect absorption refrigeration system

  • Research Article
  • Published:
Frontiers in Energy Aims and scope Submit manuscript

Abstract

The energy and exergy analyses of the absorption refrigeration system (ARS) using H2O-[mmim][DMP] mixture were investigated for a wide range of temperature. The equilibrium Dühring (P-T-XIL) and enthalpy (h-T-XIL) of mixture were assessed using the excess Gibbs free non-random two liquid (NRTL) model for a temperature range ??? of 20°C to 140°C and XIL from 0.1 to 0.9. The performance validation of the ARS cycle showed a better coefficient of performance (COP) of 0.834 for H2O-[mmim][DMP] in comparison to NH3-H2O, H2O-LiBr, H2O-[emim][DMP], and H2O-[emim][BF4]. Further, ARS performances with various operating temperatures of the absorber (Ta), condenser (Tc), generator (Tg), and evaporator (Te) were simulated and optimized for a maximum COP and exergetic COP (ECOP). The effects of Tg from 50°C to 150°C and Ta and Tc from 30°C to 50°C on COP and ECOP, the Xa, Xg, and circulation ratio (CR) of the ARS were evaluated and optimized for Te from 5°C to 15°C. The optimization revealed that Tg needed to achieve a maximum COP which was more than that for a maximum ECOP. Therefore, this investigation provides criteria to select low grade heat source temperature. Most of the series flow of the cases of cooling water from the condenser to the absorber was found to be better than the absorber to the condenser.

This is a preview of subscription content, log in via an institution to check access.

Access this article

Price excludes VAT (USA)
Tax calculation will be finalised during checkout.

Instant access to the full article PDF.

Similar content being viewed by others

Abbreviations

τ :

NRTL parameter

γ 1 :

Activity coefficient of water

α :

Temperature independent NRTL model parameter

C p :

Specific heat capacity at constant pressure /(kJ·(kg·K)−1)

g :

Gibbs energy

h :

Enthalpy/(kJ·kg−1)

m :

Mass flow rate/(kg·s−1)

p 1 :

Partial pressure of H2O/kPa

P :

Total vapor pressure/kPa

\(P_1^{{\rm{sat}}}\) :

Saturation pressure of H2O

Q :

Heat load/kW

R :

Gas constant/(kJ·(kmol·K)−1)

T :

Temperature/°C

X IL :

Mass fraction of IL into a binary mixture

x 1 :

Mole fraction of H2O into a binary mixture

1,2,3:

State points

a:

Absorber

c:

Condenser

E:

Excess

e:

Evaporator

g:

Generator

max:

Maximum

ARS:

Absorption refrigeration and cooling system

ARD:

Average relative deviation

COP:

Energetic coefficient of performance

CR:

Mixture circulation ratio

ECOP:

Exergetic coefficient of performance

LiBr:

Lithium bromide

[mmim][DMP]:

1,3-dimethylimidazolylium dimethylphosphate

[emim][DMP]:

1-ethyl-3-methylimidazolium dimethyl phosphate

[emim][BF4]:

1-ethyl-3-methylimidazolium tetrafluoroborate

References

  1. Fernandes M S, Brites G J V N, Costa J J, et al. Review and future trends of solar adsorption refrigeration systems. Renewable & Sustainable Energy Reviews, 2014, 39: 102–123

    Article  Google Scholar 

  2. Sleiti A K. Tidal power technology review with potential applications in Gulf Stream. Renewable & Sustainable Energy Reviews, 2017, 69: 435–441

    Article  Google Scholar 

  3. Sleiti A K, Al-Ammari W A, Al-Khawaja M. Review of innovative approaches of thermo-mechanical refrigeration systems using low grade heat. International Journal of Energy Research, 2020, 44(13): 9808–9838

    Article  Google Scholar 

  4. Takalkar G. Simulation and experimental study of heat based refrigeration cycles. Dissertation for the Doctoral Degree. India: Institute of Chemical Technology, 2013

    Google Scholar 

  5. Sleiti A K, Al-ammari W A, Al-khawaja M. A novel solar integrated distillation and cooling system — design and analysis. Solar Energy, 2020, 206: 68–83

    Article  Google Scholar 

  6. Sarbu I, Sebarchievici C. Review of solar refrigeration and cooling systems. Energy and Buildings, 2013, 67: 286–297

    Article  Google Scholar 

  7. Shublaq M, Sleiti A K. Experimental analysis of water evaporation losses in cooling towers using filters. Applied Thermal Engineering, 2020, 175: 115418

    Article  Google Scholar 

  8. Sun Y, Di G, Wang J, et al. Gaseous solubility and thermodynamic performance of absorption system using R1234yf/IL working pairs. Applied Thermal Engineering, 2020, 172: 115161

    Article  Google Scholar 

  9. Perez-Astudillo D, Bachour D. DNI, GHI and DHI ground measurements in Doha, Qatar. Energy Procedia, 2014, 49: 2398–2404

    Article  Google Scholar 

  10. Bachour D, Perez-Astudillo D. Ground-measurement GHI map for Qatar. Energy Procedia, 2014, 49: 2297–2302

    Article  Google Scholar 

  11. Papadopoulos A I, Kyriakides A S, Seferlis P, et al. Absorption refrigeration processes with organic working fluid mixtures—a review. Renewable & Sustainable Energy Reviews, 2019, 109: 239–270

    Article  Google Scholar 

  12. Boman D B, Hoysall D C, Staedter M A, et al. A method for comparison of absorption heat pump working pairs. International Journal of Refrigeration, 2017, 77: 149–175

    Article  Google Scholar 

  13. Shiflett M B, Yokozeki A. Solubility and diffusivity of hydrofluorocarbons in room-temperature ionic liquids. AIChE Journal, 2006, 52(3): 1205–1219

    Article  Google Scholar 

  14. Yokozeki A, Shiflett M B. Ammonia solubilities in room temperatures ionic liquids. Industrial & Engineering Chemistry Research, 2007, 46: 1605–1610

    Article  Google Scholar 

  15. Shiflett M B, Yokozcki A. Absorption cycle utilizing ionic liquids and water as working fluids. US patent: US-8715521-BZ, 2005

  16. Mehari A, Xu Z Y, Wang R Z. Thermal energy storage using absorption cycle and system: a comprehensive review. Energy Conversion and Management, 2020, 206: 112482

    Article  Google Scholar 

  17. Parab P, Takalkar G, Bhagwat S. Vapour liquid equilibrium of Potassium formate-water: measurements and correlation by e-NRTL model. Indian Chemical Engineer, 2019, 61(4): 361–373

    Article  Google Scholar 

  18. Wu W, You T, Leung M. Screening of novel water/ionic liquid working fluids for absorption thermal energy storage in cooling systems. International Journal of Energy Research, 2019, 44(12): 9367–9381

    Article  Google Scholar 

  19. Takalkar G D, Bhosale R R, Mali N A, et al. Thermodynamic analysis of EMISE-water as a working pair for absorption refrigeration system. Applied Thermal Engineering, 2019, 148: 787–795

    Article  Google Scholar 

  20. Liu X, Bai L, Liu S, et al. Vapor-liquid equilibrium of R1234yf/[HMIM][Tf2N] and R1234ze(E)/[HMIM][Tf2N] working pairs for the absorption refrigeration cycle. Journal of Chemical & Engineering Data, 2016, 61(11): 3952–3957

    Article  Google Scholar 

  21. Wu W, Zhang H, You T, et al. Thermodynamic investigation and comparison of absorption cycles using hydrofluoroolefins and ionic liquid. Industrial & Engineering Chemistry Research, 2017, 56(35): 9906–9916

    Article  Google Scholar 

  22. Kim S, Kohl P A. Theoretical and experimental investigation of an absorption refrigeration system using R134/[bmim][PF6] working fluid. Industrial & Engineering Chemistry Research, 2013, 52(37): 13459–13465

    Article  Google Scholar 

  23. Shiflett M B, Yokozeki A. Solubility and diffusivity of hydrofluorocarbons in room-temperature ionic liquids. AIChE Journal, 2006, 52(3): 1205–1219

    Article  Google Scholar 

  24. Wang M, Infante Ferreira C A. Absorption heat pump cycles with NH3 — ionic liquid working pairs. Applied Energy, 2017, 204: 819–830

    Article  Google Scholar 

  25. Chen W, Bai Y. Thermal performance of an absorption-refrigeration system with [emim]Cu2Cl5/NH3 as working fluid. Energy, 2016, 112: 332–341

    Article  Google Scholar 

  26. Takalkar G D, Bhosale R R, Mali N A, et al. Energetic and exergetic performance of NH3-H2O-based absorption refrigeration cycle: effect of operating factor. International Journal of Exergy, 2020, 31 (4): 352

    Article  Google Scholar 

  27. Zhang B, Chen W, Sun Q, et al. Numerical evaluation of thermal performances of diffusion-absorption refrigeration using 1,3-dimethylimidazolylium dimethylphosphate/methanol/helium as working fluid. Energy Conversion and Management, 2017, 152: 201–213

    Article  Google Scholar 

  28. He Z, Zhao Z, Zhang X, et al. Thermodynamic properties of new heat pump working pairs: 1,3-dimethylimidazolium dimethylpho-sphate and water, ethanol and methanol. Fluid Phase Equilibria, 2010, 298(1): 83–91

    Article  Google Scholar 

  29. Chen W, Liang S. Thermodynamic analysis of absorption heat transformers using [mmim]DMP/H2O and [mmim]DMP/CH3OH as working fluids. Applied Thermal Engineering, 2016, 99: 846–856

    Article  Google Scholar 

  30. Zheng D, Dong L, Huang W, et al. A review of imidazolium ionic liquids research and development towards working pair of absorption cycle. Renewable & Sustainable Energy Reviews, 2014, 37: 47–68

    Article  Google Scholar 

  31. Popp S, Bösmann A, Wölfel R, et al. Screening of ionic liquid/H2O working pairs for application in low temperature driven sorption heat pump systems. ACS Sustainable Chemistry & Engineering, 2015, 3(4): 750–757

    Article  Google Scholar 

  32. Wang M, Becker T M, Infante Ferreira C A. Assessment of vapor-liquid equilibrium models for ionic liquid based working pairs in absorption cycles. International Journal of Refrigeration, 2018, 87: 10–25

    Article  Google Scholar 

  33. Kim S, Kohl P A. Analysis of [hmim][PF6] and [hmim][Tf2N] ionic liquids as absorbents for an absorption refrigeration system. International Journal of Refrigeration, 2014, 48: 105–113

    Article  Google Scholar 

  34. Sujatha I, Venkatarathnam G. Performance of a vapour absorption heat transformer operating with ionic liquids and ammonia. Energy, 2017, 141: 924–936

    Article  Google Scholar 

  35. Chen W, Xu C, Wu H, et al. Energy and exergy analyses of a novel hybrid system consisting of a phosphoric acid fuel cell and a triple-effect compression-absorption refrigerator with [mmim]DMP/CH3OH as working fluid. Energy, 2020, 195: 116951

    Article  Google Scholar 

  36. Wu W, Leung M, Ding Z, et al. Comparative analysis of conventional and low-GWP refrigerants with ionic liquid used for compression-assisted absorption cooling cycles. Applied Thermal Engineering, 2020, 172: 115145

    Article  Google Scholar 

  37. Dong L, Zheng D, Nie N, et al. Performance prediction of absorption refrigeration cycle based on the measurements of vapor pressure and heat capacity of H2O +[DMIM]DMP system. Applied Energy, 2012, 98: 326–332

    Article  Google Scholar 

  38. Anand S, Gupta A, Tyagi S K, et al. An absorption chiller system using lithium bromide and water as working fluids: exergy analysis. ASHRAE Transactions, 2014, 120: 226–239

    Google Scholar 

  39. Kim Y J, Gonzalez M. Exergy analysis of an ionic-liquid absorption refrigeration system utilizing waste-heat from datacenters. International Journal of Refrigeration, 2014, 48: 26–37

    Article  Google Scholar 

  40. Ayou D S, Currás M R, Salavera D, et al. Performance analysis of absorption heat transformer cycles using ionic liquids based on imidazolium cation as absorbents with 2,2,2-trifluoroethanol as refrigerant. Energy Conversion and Management, 2014, 84: 512–523

    Article  Google Scholar 

  41. Swarnkar S K, Srinivasa Murthy S, et al. Performance of a vapour absorption refrigeration system operating with ionic liquid-ammonia combination with water as cosolvent. Applied Thermal Engineering, 2014, 72(2): 250–257

    Article  Google Scholar 

  42. Wagner W, Pruß A. The IAPWS formulation 1995 for the thermodynamic properties of ordinary water substance for general and scientific use. Journal of Physical and Chemical Reference Data, 2002, 31(2): 387

    Article  Google Scholar 

  43. Abumandour E S, Mutelet F, Alonso D. Performance of an absorption heat transformer using new working binary systems composed of {ionic liquid and water}. Applied Thermal Engineering, 2016, 94: 579–589

    Article  Google Scholar 

  44. Kamali M, Parham K, Assadi M. Performance analysis of a single stage absorption heat transformer-based desalination system employing a new working pair of (EMIM) (DMP)/H2O. International Journal of Energy Research, 2018, 42(15): 4790–4804

    Article  Google Scholar 

  45. Yokozeki A. Theoretical performances of various refrigerant-absorbent pairs in a vapor-absorption refrigeration cycle by the use of equations of state. Applied Energy, 2005, 80(4): 383–399

    Article  Google Scholar 

  46. Shiflett M B, Yokozeki A. Absorption cycle utilizing ionic liquids and water as working fluids. US Patent Application 20070144186, 2006

  47. Takalkar G. Thermodynamic properties and performance evaluation of [EMIM] [DMP]-H2O working pair for absorption cooling cycle. International Journal of Energy Research, 2019, 44(15): 12269–12283

    Article  Google Scholar 

Download references

Acknowledgements

This work was jointly supported by Qatar University International Research Collaboration Co Fund (Grant No. IRCC-2019-012).

Author information

Authors and Affiliations

Authors

Corresponding authors

Correspondence to Gorakshnath Takalkar or Ahmad K. Sleiti.

Rights and permissions

Reprints and permissions

About this article

Check for updates. Verify currency and authenticity via CrossMark

Cite this article

Takalkar, G., Sleiti, A.K. Comprehensive performance analysis and optimization of 1,3-dimethylimidazolylium dimethylphosphate-water binary mixture for a single effect absorption refrigeration system. Front. Energy 16, 521–535 (2022). https://doi.org/10.1007/s11708-021-0720-9

Download citation

  • Received:

  • Accepted:

  • Published:

  • Issue Date:

  • DOI: https://doi.org/10.1007/s11708-021-0720-9

Keywords

Navigation