Erratum to: “Flow regimes and two-phase pressure gradient in horizontal straight tubes:...

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Erratum Erratum to: ‘‘Flow regimes and two-phase pressure gradient in horizontal straight tubes: Experimental results for HFO-1234yf, R-134a and R-410A’’ [Exp. Thermal Fluid Sci. 35 (2011) 1113–1126] Miguel Padilla, Rémi Revellin , Philippe Haberschill, Ahmed Bensafi, Jocelyn Bonjour Université de Lyon, CNRS, France INSA-Lyon, CETHIL, UMR5008 F-69621, Villeurbanne, France Université Lyon 1, F-69622, France In Fig. 10(a) of the above article, the data presented do not cor- respond to the experimental conditions shown in the figure. The corrected Figure is presented below: In the annexes, there is a misprint in Tables A1 and A2. The corrected tables are: 0894-1777/$ - see front matter Ó 2012 Elsevier Inc. All rights reserved. http://dx.doi.org/10.1016/j.expthermflusci.2012.04.005 DOI of original article: http://dx.doi.org/10.1016/j.expthermflusci.2011.03.006 Corresponding author. Tel.: +33 4 72 43 72 31; fax: +33 4 72 43 88 10. E-mail address: [email protected] (R. Revellin). 0 0.2 0.4 0.6 0.8 1 0 1000 2000 3000 4000 5000 6000 7000 Vapor quality [-] Frictional pressure drop [Pa] D = 10.85 mm T sat = 15 °C G = 400 kg/m 2 s HFO-1234yf R-134a R-410A Fig. 10. Pressure drop vs. vapor quality for three different fluids: R-134a, R-410A and HFO-1234yf. Experimental Thermal and Fluid Science 40 (2012) 195–197 Contents lists available at SciVerse ScienceDirect Experimental Thermal and Fluid Science journal homepage: www.elsevier.com/locate/etfs

Transcript of Erratum to: “Flow regimes and two-phase pressure gradient in horizontal straight tubes:...

Experimental Thermal and Fluid Science 40 (2012) 195–197

Contents lists available at SciVerse ScienceDirect

Experimental Thermal and Fluid Science

journal homepage: www.elsevier .com/locate /et fs

Erratum

Erratum to: ‘‘Flow regimes and two-phase pressure gradient in horizontalstraight tubes: Experimental results for HFO-1234yf, R-134a and R-410A’’[Exp. Thermal Fluid Sci. 35 (2011) 1113–1126]

Miguel Padilla, Rémi Revellin ⇑, Philippe Haberschill, Ahmed Bensafi, Jocelyn BonjourUniversité de Lyon, CNRS, FranceINSA-Lyon, CETHIL, UMR5008 F-69621, Villeurbanne, FranceUniversité Lyon 1, F-69622, France

In Fig. 10(a) of the above article, the data presented do not cor-respond to the experimental conditions shown in the figure. Thecorrected Figure is presented below:

0894-1777/$ - see front matter � 2012 Elsevier Inc. All rights reserved.http://dx.doi.org/10.1016/j.expthermflusci.2012.04.005

DOI of original article: http://dx.doi.org/10.1016/j.expthermflusci.2011.03.006⇑ Corresponding author. Tel.: +33 4 72 43 72 31; fax: +33 4 72 43 88 10.

E-mail address: [email protected] (R. Revellin).

0 0.2 0.4 0.6 0.8 10

1000

2000

3000

4000

5000

6000

7000

Vapor quality [−]

Fric

tiona

l pre

ssur

e dr

op [

Pa]

D = 10.85 mmTsat = 15 °C

G = 400 kg/m2s

HFO−1234yfR−134aR−410A

Fig. 10. Pressure drop vs. vapor quality for three different fluids: R-134a, R-410Aand HFO-1234yf.

In the annexes, there is a misprint in Tables A1 and A2. Thecorrected tables are:

Table A1HFO-1234yf experimental data in straight tube D = 10.85 mm, L0 = 1 m.

Test G (kg m�2 s�1) Tsat (�C) x Dpst (Pa) Test G (kg m�2 s�1) Tsat (�C) x Dpst (Pa)

1 291.8 5.0 0.06 261.06 77 404.3 9.8 0.1 705.382 302.0 5.1 0.11 504.31 78 406.1 9.9 0.21 1595.543 297.6 5.1 0.2 995.9 79 405.6 10.0 0.31 2475.044 302.0 5.1 0.3 1581.05 80 403.8 10.2 0.41 3452.55 309.0 5.3 0.4 2392.62 81 402.0 10.1 0.5 4296.026 307.5 5.4 0.5 3055.85 82 400.3 10.7 0.61 5077.457 303.0 6.2 0.61 3688.84 83 404.9 9.8 0.69 5945.888 299.3 10.0 0.05 114.18 84 398.5 11.3 0.82 6736.589 298.2 9.9 0.1 360.71 85 398.3 11.9 0.87 6424.73

10 293.2 10.0 0.2 903.08 86 399.5 14.8 0.05 307.4211 295.9 9.9 0.3 1354.29 87 399.4 14.9 0.11 861.9712 302.5 10.0 0.41 2085.12 88 403.8 15.0 0.2 1346.2313 303.2 10.0 0.51 2588.27 89 406.4 15.0 0.31 2151.4814 304.0 10.1 0.61 3458.98 90 407.5 14.9 0.4 3064.8515 295.5 9.9 0.72 3738.68 91 400.9 15.1 0.5 3821.2116 298.7 10.5 0.81 4243.16 92 403.2 15.2 0.6 4546.4117 300.0 10.2 0.85 4508.4 93 406.7 15.1 0.7 5369.1218 304.0 10.5 0.91 4707.23 94 407.7 15.9 0.81 5869.6219 303.5 10.7 0.96 4749.97 95 408.1 15.3 0.85 6044.720 294.1 14.8 0.11 237.75 96 406.6 15.0 0.9 6332.2121 298.6 14.8 0.21 783.98 97 408.3 15.5 0.96 6224.4522 300.1 14.9 0.31 1242.65 98 402.4 20.0 0.1 467.9123 305.9 14.9 0.4 1848.13 99 403.7 20.1 0.21 1198.3924 303.8 14.9 0.5 2388.84 100 405.7 20.0 0.31 1830.7825 300.4 15.0 0.6 2904.56 101 399.7 20.2 0.41 2540.7826 299.2 15.0 0.71 3415.62 102 400.5 20.1 0.51 3281.0527 305.2 15.0 0.81 3966.7 103 404.8 20.1 0.61 4334.8328 305.0 15.1 0.85 4080.2 104 407.8 20.3 0.7 5005.1929 304.1 15.1 0.91 4225.81 105 406.9 20.3 0.81 5504.8330 306.9 15.1 0.95 4139.54 106 407.9 20.3 0.86 5876.131 308.5 20.0 0.1 217.13 107 409.3 20.2 0.9 603832 306.7 20.0 0.2 740.29 108 409.8 20.3 0.96 6092.3133 306.0 20.0 0.3 1030.48 109 504.9 9.9 0.05 601.2734 302.0 20.0 0.41 1610.39 110 499.5 9.9 0.1 1165.1835 300.2 20.0 0.51 2043.02 111 500.5 10.0 0.21 2217.3236 300.0 20.0 0.6 2481.39 112 501.8 10.1 0.3 3473.5337 300.6 19.9 0.7 3024.99 113 503.6 10.1 0.4 4745.4738 301.6 20.0 0.82 3392.59 114 507.2 10.6 0.5 5890.5239 298.7 20.1 0.87 3504.11 115 503.7 11.7 0.6 6726.8740 306.6 20.2 0.9 3571.67 116 498.9 14.8 0.05 543.1341 304.9 20.1 0.96 3488.1 117 499.6 14.9 0.11 1070.8942 364.3 9.9 0.06 418.47 118 503.4 15.0 0.21 1973.9643 363.7 10.0 0.11 783.41 119 497.2 15.1 0.31 3077.2544 372.5 10.0 0.21 1398.52 120 509.0 15.2 0.39 4139.0245 368.9 10.0 0.31 2077.06 121 509.7 15.0 0.5 5351.2646 373.0 10.1 0.41 3004.14 122 508.0 15.6 0.6 6171.3147 370.8 10.1 0.51 4019.33 123 515.3 15.9 0.7 7176.1248 370.6 10.3 0.61 4651.58 124 505.1 15.2 0.81 8078.6849 377.1 10.3 0.7 5440.17 125 496.8 15.8 0.87 7794.750 374.9 11.2 0.81 5930.17 126 498.8 20.0 0.06 266.651 373.5 10.8 0.87 6100.65 127 508.1 19.9 0.12 1074.0352 373.3 11.0 0.9 6060.23 128 507.9 20.0 0.2 1727.553 375.4 14.9 0.05 288.47 129 512.6 20.0 0.3 2704.5454 374.5 14.8 0.1 752.78 130 505.7 20.1 0.4 3675.8455 372.4 14.8 0.21 1204.08 131 512.0 20.2 0.49 4574.9756 371.8 15.0 0.3 1843.54 132 512.7 20.3 0.61 5578.0657 375.7 15.1 0.4 2697.02 133 505.3 20.2 0.72 6334.0658 371.4 15.0 0.51 3404.87 134 504.4 20.4 0.81 6583.0859 375.4 15.1 0.59 4051.01 135 604.6 10.0 0.05 822.8260 372.6 15.1 0.71 4836.99 136 608.0 10.0 0.11 1636.3761 372.1 15.3 0.81 5296.52 137 609.9 10.0 0.2 2907.3162 374.7 15.2 0.85 5686.19 138 603.2 10.2 0.3 4528.863 377.9 15.3 0.9 5959.83 139 606.1 10.7 0.4 5963.9664 376.7 15.6 0.96 5927.53 140 605.0 15.0 0.05 874.1765 373.9 20.1 0.11 413.52 141 607.7 14.9 0.11 1408.2166 374.4 20.0 0.2 952.73 142 606.1 15.2 0.21 2651.2567 376.7 20.0 0.3 1474.24 143 598.2 15.1 0.32 4145.0668 377.3 20.1 0.41 2432.85 144 606.5 15.4 0.4 5225.369 378.4 20.0 0.51 3060.83 145 608.6 15.3 0.5 7366.3870 375.2 20.1 0.62 3971.42 146 597.3 19.9 0.06 389.2171 381.4 20.1 0.71 4779.25 147 610.4 20.0 0.11 1322.4872 374.3 20.2 0.82 5296.14 148 606.0 20.1 0.21 2280.2273 377.0 20.2 0.87 5530.13 149 602.3 20.1 0.31 3507.2574 375.1 20.1 0.91 5607.3 150 603.1 20.2 0.41 4757.8675 374.2 20.1 0.97 5512.66 151 599.3 20.3 0.51 5705.9176 400.0 9.8 0.05 187.08

196 Erratum / Experimental Thermal and Fluid Science 40 (2012) 195–197

Table A2HFO-1234yf experimental data in straight tube D = 7.90 mm, L5 = 1 m.

Test G (kg m�2 s�1) Tsat (�C) x Dpst (Pa) Test G (kg m�2 s�1) Tsat (�C) x Dpst (Pa)

152 570.9 5.9 0.71 4231.35 231 705.9 20.3 0.97 21306.22153 550.4 5.0 0.06 1461 232 754.5 9.8 0.05 1986.22154 569.6 5.1 0.11 2780.36 233 762.5 9.8 0.11 4150.54155 561.3 5.1 0.2 5440.26 234 766.1 10.0 0.21 8396.25156 569.7 5.2 0.3 9365.53 235 765.1 10.0 0.31 13109.5157 582.9 5.4 0.4 12656.48 236 761.7 10.3 0.41 16931.41158 580.0 5.5 0.51 15358 237 758.3 10.3 0.5 20012.26159 571.6 6.4 0.61 17015.73 238 755.0 10.9 0.61 22986.57160 567.6 6.0 0.72 18798.16 239 763.8 10.0 0.69 25782.76161 564.6 10.0 0.05 1154.12 240 751.8 11.5 0.82 26827.03162 562.5 9.9 0.1 2170.12 241 751.4 12.1 0.88 26337.59163 553.1 10.0 0.2 4577.02 242 753.5 14.9 0.05 1773.51164 558.2 10.0 0.3 7537.16 243 753.4 14.9 0.11 3531.39165 570.6 10.1 0.41 10784.77 244 761.6 15.0 0.2 6549.02166 572.0 10.1 0.51 13679.39 245 766.5 15.0 0.31 10929.11167 573.4 10.2 0.61 15901.78 246 768.6 15.0 0.4 14516.39168 557.5 10.1 0.72 17059.19 247 756.3 15.2 0.51 17567.94169 563.5 10.6 0.81 18163.85 248 760.5 15.3 0.6 20333.53170 565.8 10.3 0.86 18852.37 249 767.1 15.3 0.71 22909.84171 573.5 10.6 0.91 19463.47 250 768.9 16.1 0.81 24438.15172 572.5 10.8 0.96 19491.31 251 769.7 15.5 0.85 25019.28173 569.8 14.8 0.05 975.49 252 767.0 15.2 0.9 25520.89174 554.8 14.8 0.11 1849.89 253 770.1 15.6 0.96 25745.49175 563.3 14.9 0.21 4012.41 254 755.8 20.0 0.05 1540.83176 566.1 14.9 0.31 6594.86 255 759.1 20.0 0.1 2736.33177 577.0 15.0 0.4 9215.18 256 761.5 20.1 0.21 5829.79178 573.1 15.0 0.5 11549.91 257 765.3 20.0 0.31 9300.03179 566.7 15.1 0.61 13332.84 258 754.0 20.3 0.41 12034.17180 564.4 15.1 0.71 15036.41 259 755.5 20.2 0.52 16463.81181 575.7 15.1 0.81 16841.32 260 763.6 20.2 0.61 19387.26182 575.3 15.2 0.85 17061.01 261 769.3 20.4 0.7 21356.96183 573.7 15.2 0.91 17603.14 262 767.6 20.4 0.81 22919.33184 578.8 15.2 0.95 17392.71 263 769.4 20.5 0.86 24321.44185 579.8 19.9 0.05 1112.94 264 772.0 20.4 0.9 24756.42186 581.9 20.0 0.1 1689.47 265 772.9 20.4 0.96 24770.1187 578.6 20.0 0.2 3788.79 266 952.3 9.9 0.05 2854.41188 577.1 20.0 0.3 5468.84 267 942.3 9.9 0.1 5835.03189 569.7 20.0 0.41 8029.77 268 944.1 10.1 0.21 12082.14190 566.3 20.1 0.51 9877.87 269 946.4 10.2 0.3 17829.22191 565.8 20.1 0.6 11390.35 270 950.0 10.3 0.4 23081.57192 567.0 20.0 0.7 12876.53 271 956.7 10.8 0.5 28189.56193 568.9 20.1 0.82 15252.98 272 950.2 11.9 0.61 30847.98194 563.5 20.1 0.87 15906.56 273 941.2 14.8 0.05 2475.56195 578.4 20.3 0.9 15711.37 274 942.3 14.9 0.11 4938.37196 575.1 20.2 0.96 15495.94 275 949.6 15.0 0.21 10328.9197 687.2 9.9 0.06 1870.65 276 937.8 15.2 0.31 15433.61198 686.1 10.0 0.11 3529.01 277 960.1 15.3 0.39 19884.63199 702.7 10.0 0.21 7496.37 278 961.3 15.2 0.51 24883.75200 695.9 10.1 0.31 11329.44 279 958.1 15.8 0.6 27993.67201 703.6 10.2 0.41 15258.8 280 972.0 16.1 0.7 31264.86202 699.4 10.2 0.51 19301.34 281 952.7 15.5 0.82 32550.05203 699.1 10.4 0.61 21887.73 282 937.2 16.1 0.87 32110.22204 711.2 10.5 0.7 23778.23 283 940.9 20.0 0.06 2333.08205 707.2 11.4 0.81 25288.7 284 958.5 20.0 0.12 4854.71206 704.6 11.0 0.87 25605.06 285 958.0 20.1 0.2 8538.31207 704.2 11.1 0.9 24844.57 286 966.9 20.1 0.3 13412.78208 708.1 14.9 0.05 1546.2 287 953.9 20.2 0.41 17176.79209 706.4 14.8 0.1 2908.17 288 965.8 20.3 0.49 21027.75210 702.5 14.9 0.21 6091.55 289 967.0 20.5 0.61 24675.32211 701.3 15.0 0.3 9456.18 290 953.2 20.4 0.72 27053.57212 708.7 15.1 0.4 13091.08 291 951.4 20.6 0.81 27148.1213 700.6 15.1 0.51 15913.05 292 1140.4 10.1 0.05 3957.58214 708.1 15.2 0.59 18237.47 293 1146.9 10.0 0.11 8860.73215 702.8 15.2 0.71 20453.85 294 1150.5 10.1 0.2 16586.06216 701.8 15.5 0.81 22012.78 295 1137.9 10.4 0.31 23629.58217 706.8 15.4 0.85 23026.66 296 1143.3 10.9 0.41 30412.34218 712.8 15.4 0.91 23388.37 297 1141.1 15.0 0.05 3800.66219 710.6 15.8 0.96 22909.71 298 1146.4 14.9 0.11 7281.11220 697.2 20.0 0.05 1316.54 299 1143.2 15.3 0.21 14295.65221 705.3 20.1 0.11 2370.2 300 1128.4 15.2 0.32 20851.14222 706.3 20.1 0.2 4819.97 301 1144.1 15.5 0.4 25710.8223 710.5 20.0 0.31 9613.69 302 1147.9 15.5 0.51 33276.25224 711.7 20.2 0.41 13264.98 303 1126.8 19.9 0.06 3308.12225 713.7 20.1 0.51 15707.23 304 1151.4 20.0 0.11 6424.98226 707.7 20.2 0.62 17879.16 305 1143.1 20.2 0.21 11747.72227 719.4 20.2 0.71 20209.7 306 1136.1 20.2 0.31 17405.7228 706.0 20.4 0.82 22011.22 307 1137.6 20.3 0.41 22733.04229 711.1 20.4 0.87 22394.68 308 1130.5 20.4 0.51 26906.22230 707.5 20.3 0.91 22004.93

Erratum / Experimental Thermal and Fluid Science 40 (2012) 195–197 197