Using mixtures of the zeotropic refrigerant mixture R-22/R-142b, a series of experiments was performed to determine the sectional and average heat transfer coefficients. Experiments were also conducted to compare three different heat transfer enhancement methods to that of smooth tubes. They were microfins, twisted tapes, and high fins. Measurements at different mass fluxes were obtained at six refrigerant mass fractions from 100 percent R-22 up to a 50 percent/50 percent mixture of R-22/R-142b. All condensation measurements were conducted at an isobaric inlet pressure of 2.43 MPa. This pressure corresponds to a saturation temperature of 60°C for R-22. The measurements were taken in 9.53 mm outer diameter smooth tubes and microfin tubes with lengths of 1603 mm. The heat transfer coefficients were determined with the Log Mean Temperature Difference equations. It was found that microfins were more suitable as an enhancement method than twisted tubes or high fins. Also, that the heat transfer coefficients and pressure drops decrease as the mass fraction of R-142b increases.

1.
Bergles
,
A. E.
,
1999
, “
Enhanced Heat Transfer: Endless Frontier, or Mature and Routine?
,”
Enhanced Heat Transfer
,
6
, pp.
79
99
.
2.
Bergles
,
A. E.
,
Jensen
,
M. K.
, and
Shome
,
B.
,
1996
, “
The Literature on Enhancement of Convective Heat and Mass Transfer
,”
Enhanced Heat Transfer
,
4
, pp.
1
6
.
3.
Thome
,
J. R.
,
1996
, “
Boiling of New Refrigerants: A State-of-the-Art Review
,”
Int. J. Refrig.
,
19
(
7
), pp.
435
457
.
4.
Meyer
,
J. P.
, and
Greyvenstein
,
G. P.
,
1991
, “
Hot Water for Homes in South Africa
,”
Energy—The International Journal
,
16
(
7
), pp.
1039
1044
.
5.
Meyer
,
J. P.
, and
Greyvenstein
,
G. P.
,
1992
, “
Hot Water for Large Residential Units, Hospitals and Laundries with Heat Pumps in South Africa: A Technoeconomic Analysis
,”
Energy, Conversion, and Management
,
33
, pp.
135
143
.
6.
Smit
,
F. J.
, and
Meyer
,
J. P.
,
1998
, “
Investigation of the Potential Effect of Zeotropic Refrigerant Mixture on Performance of a Hot-Water Heat Pump
,”
ASHRAE Trans.
,
104
, (Part 1A), pp.
387
394
.
7.
Johannsen, A. F. B., 1992, “Potential of Non-Azeotropic Refrigerant Mixtures for Water-Heating Heat Pumps in South Africa,” Department of Mineral and Energy Affairs, Report no. ED 8807, Pretoria, South Africa.
8.
Smit, F. J., 1996, “The Influence of a Non-Azeotropic Refrigerant Mixture on the Performance of a Hot-Water Heat Pump,” M. Eng. dissertation, Rand Afrikaans University, Johannesburg, South Africa.
9.
Kebonte, S. A., 1999, “Condensation Heat Transfer and Pressure Drop Coefficients of R22/R142b in a Water Cooled Helically Coiled Tube-in-Tube Heat Exchanger,” M. Eng. dissertation, Rand Afrikaans University, Johannesburg, South Africa.
10.
Bukasa, J. M., 1999, “Average Boiling Heat Transfer and Pressure Drop Coefficients of R22/R142b in a Helically Coiled Water Heated Tube-in-Tube Heat Exchanger,” M.Eng. dissertation, Rand Afrikaans University, Johannesburg, South Africa.
11.
Meyer
,
J. P.
,
Bukasa
,
J. M.
, and
Kebonte
,
S. A.
,
2000
, “
Average Boiling and Condensation Heat Transfer Coefficients of the Zeotropic Refrigerant Mixture R22/R142b in a Coaxial Tube-in-Tube Heat Exchanger
,”
ASME J. Heat Transfer
,
122
, pp.
186
188
.
12.
Shizuyo
,
M.
,
Itoh
,
M.
, and
Hijrkata
,
K.
,
1995
, “
Condensation of Nonazeotropic Binary Refrigerant Mixtures Including R-22 as a More Volatile Component Inside a Horizontal Tube
,”
ASME J. Heat Transfer
,
117
, pp.
538
543
.
13.
NIST, 1998, “NIST Thermodynamic and Transport Properties of Refrigerants and Refrigerant Mixtures Database,” (REFPROP Ver. 6.01), National Institute of Standards and Technology, Gaithersburg, MD.
14.
ANSI/ASHRAE 1996, ASHRAE STANDARD 41.4, “Standard Method for Measurement of Proportion of Lubricant in Liquid Refrigerant,” American Society of Heating, Refrigerating and Air-Conditioning Engineers, Atlanta, GA.
15.
Briggs
,
D.
, and
Young
,
E.
,
1969
, “
Modified Wilson Plot Technique for Obtaining Heat Transfer Correlations for Shell and Tube Heat Exchangers
,”
Chem. Eng. Prog., Symp. Ser.
,
65
(
2
), pp.
35
45
.
16.
Kline
,
S.
, and
McClintock
,
F.
,
1953
, “
Describing Uncertainties in Single-Sample Experiments
,”
Mech. Eng. (Am. Soc. Mech. Eng.)
,
75
, pp.
3
8
.
17.
Eckels, S. J., and Tesene, B. A., 1999, “A Comparison of R-22, R-134a, R-410a, and R-407c Condensation Performance in Smooth and Enhanced Tubes: Part I, Heat Transfer,” ASHRAE Trans., 105, Pt. 2
18.
Eckels, S. J., and Tesene, B. A., 1999, “A Comparison of R-22, R-134a, R-410a, and R-407c Condensation Performance in Smooth and Enhanced Tubes: Part II, Heat Transfer,” ASHRAE Trans., 105, Pt. 2.
19.
Liebenberg, L, Bergles, A. E., and Meyer, J. P., 2000, “A Review of Refrigerant Condensation in Horizontal Micro-fin Tubes,” Proceedings of the ASME Advanced Energy Systems Division, International Mechanical Engineering Congress and Exhibition, November 5–10, Orlando, Florida, AES-Vol. 40, pp. 155–168.
20.
Cavallini
,
A.
,
Del Col
,
D.
,
Doretti
,
L.
,
Longo
,
G. A.
, and
Rosetto
,
L.
,
2000
, “
Heat Transfer and Pressure Drop During Condensation of Refrigerants Inside Horizontal Enhanced Tubes
,”
Int. J. Refrig.
,
23
(
4
), pp.
4
25
.
21.
Silver
,
L.
,
1947
, “
Gas Cooling with Aqueous Condensation
,”
Trans. Inst. Chem. Eng.
,
25
, pp.
30
42
.
22.
Bell
,
K. J.
, and
Ghaly
,
M. A.
,
1973
, “
An Approximate Generalized Design Method for Multicomponent/Partial Condenser
,”
AIChE Symp. Ser.
,
69
, pp.
72
79
.
23.
Ravigururajan, T. S., and Bergles, A. E., 1985, “General Correlations for Pressure Drop and Heat Transfer for Single Phase Turbulent Flow in Internally Ribbed Tubes,” ASME HTD, 52, pp. 9–20.
24.
Shao
,
D. W.
, and
Granryd
,
E.
,
1998
, “
Experimental and Theoretical Study on Flow Condensation With Non-Azeotropic Refrigerant Mixtures of R32/R134a
,”
Int. J. Refrig.
,
12
(
3
), pp.
230
246
.
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