Abstract
R-410A distribution in a two pass evaporator with lower horizontal combining–dividing header was investigated. Tubes were heated to yield a test section outlet superheat of 5 °C with inlet quality of 0.2. The number of tubes was ten for the inlet pass and 12 or 14 for the outlet pass. For each case, mass flux was varied from 73 to 143 kg/m2 s. In the combining/dividing header, two-phase mixture out of the inlet pass is first merged and then re-distributed to the outlet pass. More liquid is forced downstream as mass flux or quality increases Effect of insertion device in the inlet header was also investigated. Efforts were made to develop correlations to predict the liquid or gas distribution in a header with limited success. Header pressure drop data are also provided.
Similar content being viewed by others
Abbreviations
- c p :
-
Specific heat (J/kg K)
- CR :
-
Ratio of inlet and outlet channel number
- d :
-
Tube inner diameter (m)
- D :
-
Header diameter (m)
- f :
-
Friction factor
- Fr:
-
Froude number
- G :
-
Mass flux (kg/m2 s)
- GFR :
-
Gas flow ratio
- h :
-
Enthalpy (J/kg)
- L :
-
Length (m)
- LFR :
-
Liquid flow ratio
- m :
-
Mass flow rate (kg/s)
- N :
-
Number of channel
- P :
-
Pressure (Pa)
- P c :
-
Critical pressure (Pa)
- R:
-
Function of measured variable
- Q :
-
Supplied heat (W)
- Re:
-
Reynolds number
- SD:
-
Standard deviation
- T :
-
Temperature (K)
- v :
-
Specific volume (m3/kg)
- w :
-
Uncertainty of parameter
- We:
-
Weber number
- x :
-
Quality or measured variable
- α :
-
Void fraction
- ΔP :
-
Pressure drop (Pa)
- μ :
-
Viscosity (kg/ms)
- \( \Phi ^{\text{2}} \) :
-
Two-phase multiplier
- ρ :
-
Density (kg/m3)
- σ :
-
Surface tension (N/m)
- a:
-
Acceleration
- avg:
-
Average
- ch:
-
Channel
- cont:
-
Contraction
- deg:
-
Degradation
- exp:
-
Expansion
- f:
-
Friction factor or friction
- ft:
-
Flat tube
- g:
-
Gas or gravitation
- go:
-
All gas
- H:
-
Header or homogeneous
- head:
-
Header
- i:
-
Inlet or ith
- ideal:
-
Ideal
- in:
-
Inlet
- l:
-
Liquid
- lg:
-
Latent heat
- lo:
-
All liquid
- meas:
-
Measured
- minor:
-
Minor
- o:
-
Outlet
- out:
-
Outlet
- p:
-
Preheater
- r:
-
Refrigerant
- rt:
-
Round tube
- sat:
-
Saturation
- T:
-
Tube
- w:
-
Cooling water
References
Kulkarni T, Bullard CW, Cho K (2004) Header design tradeoffs in microchannel evaporators. Appl Therm Eng 24:759–776
Webb RL, Chung K (2004) Two-phase flow distribution in tubes of parallel flow heat exchangers. Heat Transf Eng 26:3–18
Hrnjak PS (2004) Flow distribution issues in parallel flow heat exchangers. In: ASHRAE annual meeting. AN-04-1-2
Lee SY (2006) Flow distribution behaviour in condensers and evaporators. In: Proceedings of the 13th international heat transfer conference. Sydney, Australia, KN-08
Ahmad M, Berthoud G, Mercier P (2009) General characteristics of two-phase flow distribution in a compact heat exchanger. Int J Heat Mass Transf 52:442–450
Watanabe M, Katsuda M, Nagata K (1995) Two-phase flow distribution in multi-pass tube modeling serpentine type evaporator. ASME/JSME Therm Eng Conf 2:35–42
Vist S, Pettersen J (2004) Two-phase flow distribution in compact heat exchanger manifolds. Exp Therm Fluid Sci 28:209–215
Koyama S, Wijayanta AT, Kuwahara K, Ikuda S, Developing two-phase flow distribution in horizontal headers with downward micro-channel branches. In: Proceedings of the 11th international refrigeration and air conditioning conference at Purdue. R142
Bowers CS, Hrnjak PS, Newell TA (2006) Two-phase refrigerant distribution in a micro-channel manifold. In: Proceedings of the 11th international refrigeration and air conditioning conference at Purdue. R161
Hwang Y, Jin DH, Radermacher R (2007) Refrigerant distribution in minichannel evaporator manifolds. HVAC&R Res 13(4):543–555
Kim NH, Kim DY, Byun HW (2011) Effect of inlet configuration on the refrigerant distribution in a parallel flow heat exchanger header. Int J Refrig 34:1209–1221
Kim NH, Byun HW (2013) Effect of inlet configuration on upward branching of two-phase refrigerant in parallel flow heat exchanger. Int J Refrig 36:1062–1077
Byun HW, Kim NH (2011) Refrigerant distribution in a parallel flow heat exchanger having vertical headers and heated horizontal tubes. Exp Therm Fluid Sci 35:920–932
Zou Y, Hrnjak P (2013) Experiment and visualization on R-134a upward flow in the vertical header of microchannel heat exchanger and its effect on distribution. Int J Heat Mass Transf 62:124–134
Kline SJ, McClintock FA (1953) The description of uncertainties in single sample experiments. Mech Eng 75:3–9
Shah MM (1976) A new correlation for heat transfer during boiling flow through pipes. ASHRAE Trans 82(2):66–86
Kim NH, Lee EJ, Byun HW (2013) Improvement of two-phase refrigerant distribution in a parallel flow minichannel heat exchanger using insertion devices. Appl Therm Eng 59:116–130
Data AB, Majumdar AK (1983) A calculation procedure for two phase flow distribution in manifolds with and without heat transfer. Int J Heat Mass Transf 26(9):1321–1328
Bajura RA, Jones EH (1976) Flow distribution manifolds. J Fluids Eng 98:654–665
Ablanque N, Oliet C, Rigola J, Perez-Segarra CD, Oliva A (2010) Two-phase flow distribution in multiple parallel tubes. Int J Therm Sci 49:909–921
Seeger W, Reimann J, Muller U (1986) Two-phase flow in a T-junction with a horizontal inlet, part 1: phase saparation. Int J Multiph Flow 12(4):575–585
Hwang ST, Soliman HM, Lahey RT (1998) Phase separation in dividing two-phase flow. Int J Multiph Flow 14(4):439–458
Tuo H, Bielskus A, Hrnjak P (2012) An experimentally validated modeling of refrigerant distribution in a parallel microchannel evaporator. ASHRAE Trans 118(1):CH-12-C-48
Datafit (1996) Oakdale engineering. http://www.oakdaleengr.com/, version 8.2
Zhang M, Webb RL (2001) Correlation of two-phase friction for refrigerants in small-diameter tubes. Exp Therm Fluid Sci 25:131–139
Friedel L (1979) Improved pressure drop correlations for horizontal and vertical two-phase pipe flow. 3R Int 18:485–492
Collier JG, Thome JR (1994) Convective boiling and condensation, 3rd edn. Oxford University Press, Oxford
Zivi SM (1964) Estimation of steady-state steam void fraction by means of the principle of minimum entropy production. J Heat Transf 86:247–251
Author information
Authors and Affiliations
Corresponding author
Rights and permissions
About this article
Cite this article
Byun, HW., Kim, NH. Two-phase refrigerant distribution in a parallel flow minichannel heat exchanger having lower combining/dividing header. Heat Mass Transfer 51, 1445–1459 (2015). https://doi.org/10.1007/s00231-015-1517-3
Received:
Accepted:
Published:
Issue Date:
DOI: https://doi.org/10.1007/s00231-015-1517-3