Abstract
In the present article, the effect of heat source temperature, heat sink temperature, short-tube orifice diameter and short-tube orifice length on the performance characteristics of HFC-140A and HFC-134a refrigeration system using a short-tube orifice as expansion device, i.e., mass flow rate, cooling capacity, compressor pressure ratio, power consumption, and second law efficiency are experimentally studied. The short-tube orifices diameters ranging from 0.849 to 1.085 mm with length ranging from 10 to 20 mm are used in this examination. The test run are done at heat source temperature ranging between 16.5 and 18.5°C, and heat sink temperature ranging between 30 and 35°C. The results show that the tendency of second law efficiency is increased as the short-tube orifice diameter and heat source temperature are enhanced, but it is decreased by increasing the short-tube orifice length and heat sink temperature. Under the similar conditions, the mass flow rate, cooling capacity, and compressor power consumption obtained from HFC-410A are higher than those obtained from HFC-134a.
Similar content being viewed by others
Abbreviations
- COP actual :
-
Actual coefficient of performance
- COP carnot :
-
Carnot coefficient of performance
- c p, hw :
-
Specific heat at constant pressure of the hot water, kJ/kg K
- D :
-
Short-tube orifice diameter, m
- L :
-
Short-tube orifice length, m
- \( \dot{m}_{\text{hw}} \) :
-
Mass flow rate of hot water, kg/s
- \( \dot{m}_{\text{cw}} \) :
-
Mass flow rate of cold water, kg/s
- Q evap :
-
Heat transfer rate at evaporator, kW
- T sink :
-
Heat sink temperature, °C
- T source :
-
Heat source temperature, °C
- T hw, in :
-
Hot water temperature at the inlet of the evaporator, °C
- T hw, out :
-
Hot water temperature at the outlet of the evaporator, °C
- ∆T sub :
-
Degree of subcooling, °C
- ∆T sup :
-
Degree of superheat, °C
- W comp :
-
Electrical power supplied to the compressor, kW
References
Aprea C, Renno C (2004) Experimental comparison of R22 with R417A performance in a vapour compression refrigeration plant subjected to a cold store. Energy Convers Manag 45:1807–1819
Aprea C, Mastrullo R, Renno C (2004) An analysis of the performances of a vapour compression plant working both as a water chiller and a heat pump using R22 and R417A. Appl Therm Eng 24:487–499
Cabello R, Navarro-Esbrı′ J, Llopis R, Torrella E (2007) Analysis of the variation mechanism in the main energetic parameters in a single-stage vapour compression plant. Appl Therm Eng 27:167–176
Chaiwongsa P, Wongwises S (2007) Effect of throat diameters of the ejector on the performance of the refrigeration cycle using a two-phase ejector as an expansion device. Int J Refrig 30:601–608
Chaiwongsa P, Wongwises S (2008) Experimental study on R-134a refrigeration system using a two-phase ejector as an expansion device. Appl Therm Eng 28:467–477
Disawas S, Wongwises S (2004) Experimental investigation on the performance of the refrigeration cycle using a two-phase ejector as an expansion device. Int J Refrig 27(6):587–594
Giuliani G, Hewitt NJ, Marchesi Donati F, Polonara F (1999) Composition shift in liquid-recirculation refrigeration systems: an experimental investigation for the pure fluid R134a and the mixture R32/134a. Int J Refrig 22(6):486–498
Hoegberg M, Vamling L, Berntsson T (1993) Calculation methods for comparing the performance of pure and mixed working fluids in heat pump applications. Int J Refrig 16(6):403–413
Kim Y (1993) Two-phase flow of HFC134a and HCFC22 through short tube orifices PhD thesis. Texas A&M University, USA
Kim Y, Payne V, Choi J, Domanski P (2005) Mass flow of R410A through short tube working near the critical point. Int J Refrig 28:547–553
Liu JP, Niu YM, Chen JP, Chen ZJ, Feng X (2004) Experimental and correlation of R744 two-phase flow through short tubes. Exp Therm Fluid Sci 28:565–573
Llopis R, Torrella E, Cabello R, S′anchez D (2009) Performance evaluation of R404A and R507A refrigerant mixtures in an experimental double-stage vapour compression plant. Appl Energy, (in press)
Navarro-Esbrı′ J, Cabello R, Torrella E (2005) Experimental evaluation of the internal heat exchanger influence on a vapour compression plant energy efficiency working with R22, R134a and R407C. Energy 30:621–636
Nilpueng K, Wongwises S (2009) Experimental investigation of two-phase flow characteristics of HFC-134a through short-tube orifices. Int J Refrig 32:854–864
Nilpueng K, Supavarasuwat C, Wongwises S (2009) Flow pattern, mass flow rate, pressure distribution, and temperature distribution of two-phase flow of HFC-134a inside short-tube orifices. Int J Refrig 32:1864–1875
Payne WV, O’Neal DL (1998) Mass flow characteristics of R407C through short-tube orifices. ASHRAE Trans 104(3):197–209
Singh GM, Hrnjak PS, Bullard CW (2001) Flow of refrigerant R134a through orifice tubes. Int J HVAC&R Res 7:245–262
Tu X, Hrnjak PS, Bullard CW (2006) Refrigerant 134a liquid flow through micro-scale short tube orifices with/without phase change. Exp. Therm. Fluid Sci 30(3):253–262
Wongwises S, Disawas S (2005) Performance of the two-phase ejector expansion refrigeration cycle. Int J Heat Mass Trans 48:4282–4286
Acknowledgments
The authors would like to express their appreciation to the Thailand Research Fund (TRF), the Office of the Higher Education Commission and the National Research University Project for providing financial support for this study.
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Nilpueng, K., Supavarasuwat, C. & Wongwises, S. Performance characteristics of HFC-134a and HFC-410A refrigeration system using a short-tube orifice as an expansion device. Heat Mass Transfer 47, 1219–1227 (2011). https://doi.org/10.1007/s00231-011-0783-y
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s00231-011-0783-y