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Local heat transfer analysis for boiling of hydrocarbons in complex geometries: a new approach for heat transfer prediction in staggered tube bundle. (English) Zbl 1227.80006

Summary: This paper deals with heat transfer analysis for boiling flow in staggered tube bundle. A local analysis is performed to determine the heat transfer coefficient linked to local flow regimes by optical fibre. The first part of the paper is devoted to the literature survey of the main existing studies on the topic. We show that published heat transfer correlations deviate largely from each others and also from the experimental results that have been carried out. On these features, a new approach has been developed. It is based on the relationship between flow regimes and thermal characteristics. An experimental setup has been developed for the determination of the local heat transfer and the two-phase flow void fraction. A detailed analysis of the two-phase flow has been performed in a previous paper of the authors [“Experimental analysis of local void fractions measurements for boiling hydrocarbons in complex geometry. Int. J. Multiphase Flow 33, No. 4, 371–393 (2007; doi:10.1016/j.ijmultiphaseflow.2006.10.001)] in which two regimes were identified. In the present paper, focus is done on the heat transfer analysis in relation with the flow regime map. This new approach allows a better prediction of the heat transfer coefficient. For the bubbly flow, the heat transfer coefficient is well predicted by a classical correlation corresponding to nucleate boiling regime. For the dispersed flow, classical correlations for convective boiling are not adapted anymore for tube bundle. We evidenced that heat coefficient is mainly controlled by the vapour flow and a heat transfer law is derived using the vapour Reynolds number and vapour Prandlt number. These two heat transfer laws are used to evaluate heat transfer coefficient in the intermediate regime.

MSC:

80A20 Heat and mass transfer, heat flow (MSC2010)
76T10 Liquid-gas two-phase flows, bubbly flows
80-05 Experimental work for problems pertaining to classical thermodynamics

References:

[1] Aprin, L.; Mercier, P.; Tadrist, L.: Experimental analysis of local void fractions measurements for boiling hydrocarbons in complex geometry, Int. J. Multiph. flow 33, No. 4, 371-393 (2007)
[2] Armand, A. A.: The resistance during movement of two-phase system in horizontal pipes, Izv. vses. Tepl. inst. 1, 16-23 (1946)
[3] Bennet, L.; Chen, J. C.: Forced convective boiling in vertical tubes for saturated pure components and binary mixtures, Aiche J. 26, No. 3, 454-461 (1980)
[4] Burnside, B. M.: 2-D kettle reboiler circulation model, Int. J. Heat fluid flow. 20, 437-445 (1999)
[5] Burnside, B. M.; Neil, D. A. Mc; Miller, K. M.; Tarrad, A. H.: A comparison between HIGHFLUX and plain tubes, boiling pentane in a horizontal kettle reboiler, Appl. therm. Eng. 22, 803-814 (2001)
[6] B.M. Burnside, K.M. Miller, D.A. Mc Neil T. Bruce, Conditions at the outside of a thin slice reboiler bundle determined by particle image velocimetry, in: Proceeding of the 12th International Heat Transfer Conference, Grenoble, (2002), France.
[7] Chen, J. C.: Correlation for boiling heat transfer to saturated liquids in convective flow, Ind. eng. Chem. process design development 5, No. 3, 322-329 (1966)
[8] Chisholm, D.: Pressure gradients due to friction during the flow of evaporating two-phase mixtures in smooth tubes and channels, Int. J. Heat mass transfer 16, 347-358 (1973)
[9] M. G. Cooper, Saturation nucleate pool boiling – A simple correlation, 1st U.K. National Conference on heat transfer, Leeds, U.K., IChemE Symposium Series, vol. 2, n 86, (1984), 785 – 793.
[10] Cooper, M. G.: Flow boiling – the apparently nucleate regime, Int. J. Heat mass transfer 32, No. 3, 459-464 (1989) · Zbl 0665.76113 · doi:10.1016/0017-9310(89)90133-6
[11] Cornwell, K.; Duffin, N. W.; Schüller, R. B.: An experimental study of the effects of fluid flow on boiling within a kettle reboiler tube bundle, Asme (1980)
[12] Cornwell, K.; Schüller, R. B.: A study of boiling outside a tube bundle using a high speed photography, Int. J. Heat mass transfer 25, No. 5, 683-690 (1982)
[13] K. Cornwell, A.J. Addlesee. Heat transfer to a sliding bubble on a tube, Eurotherm Seminar 8, Paderborn, (1988), 57 – 64.
[14] K. Cornwell, J.G. Einersson, The influence of fluid flow on nucleate boiling from a tube, in: Proceeding of Eurotherm 8, Advances in pool boiling heat transfer, Paderborn, Germany, May 11 – 12, (1989), 28 – 41.
[15] Cornwell, K.: The influence of bubbly flow on boiling from tube in a bundle, Int. J. Heat mass transfer 33, No. 12, 2579-2584 (1990)
[16] K. Cornwell, The role of sliding bubbles in boiling on tube bundles, Heat Transfer 1990, in: Proceeding of the 9th International Heat Transfer Conference, paper 9-TPF-11, vol. 3, (1990), 455 – 460.
[17] Cornwell, K.; Houston, D.: Nucleate pool boiling on horizontal tubes: a convection based correlation, Int. J. Heat mass transfer 37, No. Suppl. 1, 303-309 (1994)
[18] K. Cornwell, I.A. Grant., The physical dimension in convective boiling, in: Proceedings of Convective Flow Boiling Conference, Banff, Alberta, Canada, April 30 – May 5, Taylor & Francis Publishers, (1995), 167 – 173.
[19] E.S.D.U., Convective heat transfer during crossflow of fluids over plain tube banks, Item n 73031, Eng. Sci. Data Unit, London, (1973).
[20] Fujita, Y.; Ohta, H.; Hoshida, K.; Hidaka, S.: Heat transfer in nucleate boiling outside horizontal tube bundles, part 2 – prediction for tube bundle effect, Trans. JSME, B. 53, 486-535 (1987)
[21] Gnielinski, V.: New equations for heat and mass transfer in turbulent pipe and channel flow, Int. chem. Eng. 16, No. 2, 359-368 (1976)
[22] D. Gorenflo, Pool boiling, VDI Heat Atlas, Chap. Ha, VDI Verlag, Dusseldorf, (1993), Ha1 – Ha25.
[23] D. Gorenflo, M. Buscheimeier, P. Kaupman, Heat transfer from horizontal tube to boiling binary mixture with surimposed convective flow, in: Proceeding of convective flow boiling conference, Banff, Alberta, Canada, Taylor & Francis Publishers, April 30 – May 5, (1995), 265 – 270.
[24] Ishihara, K.; Palen, J. W.; Taborek, J.: Critical review of correlations for predicting two-phase flow pressure drop across tube banks, Heat transfer eng. 1, No. 3, 23-32 (1980)
[25] Jensen, M. K.; Hsu, J. T.; Lin, C. S.: Boiling heat transfer mechanisms in a horizontal tube bundle, Experimental heat transfer 6, 259-271 (1993)
[26] Jung, D.; Kim, Y.; Ko, Y.; Song, K.: Nucleate boiling heat transfer coefficients of pure halogenated refrigerants, Int. J. Refrig. 26, 240-248 (2003)
[27] Moffat, R. J.: Describing the uncertainties in experimental results, Exp. thermal fluid sci. 1, 3-17 (1998)
[28] Motinski, I. L.: Calculation of heat transfer and critical heat flux in boiling liquids based on law of corresponding states, Teploenergetika. 10, No. 4, 66-71 (1963)
[29] Polley, G. T.: Reboilers developments in heat exchangers technology, Reboilers developments in heat exchangers technology 1 (1980)
[30] G.T. Polley, T. Ralston, J.R. Grant, Forced crossflow boiling in an ideal in-line tube bundle, in: Proceeding of the 19th National Heat Transfer Conference ASME/AIChE, Orlando, USA80-HT-46, (1980).
[31] Schrage, D. S.; Hsu, J. T.; Jensen, M. K.: Two-phase pressure drop in vertical crossflow across a horizontal tube bundle, Aiche J. 34, No. 1, 107-115 (1988)
[32] Stephan, K.; Abdelsalam, M.: Heat transfer correlations for natural convection boiling, Int. J. Heat mass transfer 23, 73-87 (1980)
[33] Webb, R. L.; Gupte, N. S.: A critical review of correlation for convective vaporization in tubes and tube banks, Heat transfer eng. 13, No. 3, 58-81 (1992)
[34] Webb, R. L.; Chien, L. H.: Correlation of convective vaporization on banks of plain tubes using refrigerants, Heat transfer eng. 15, No. 3, 57-69 (1994)
[35] Voloshko, A. A.: Free convection boiling of freon, Heat transfer – soviet reseach. 4, No. 4, 60-66 (1972)
[36] A. Zukauskas, Heat transfer from tubes in cross flow, Advances in Heat Transfer, Academic pres, New York, Hartnett J.P. and Irvine T.F. editions, (1972), vol. 8.
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