KnE Materials Science

ISSN: 2519-1438

The latest conference proceedings on physical materials, energy materials, electrical materials.

Study on the Flow and Heat Transfer Characteristics in the Tube Side of Spiral-Wound Heat Exchanger

Published date: Oct 14 2018

Journal Title: KnE Materials Science

Issue title: Sino-Russian ASRTU Conference Alternative Energy: Materials, Technologies, and Devices

Pages: 125-133

DOI: 10.18502/kms.v4i2.3046

Authors:
Abstract:

In this article, the characteristics of hydrocarbons condensation flow and heat transfe in tube-side of spiral wound heat exchanger under static and sloshing conditions were numerically investigated based on the verified model. It is shown that at static conditions, as the vapor quality increases, the heat transfer coefficient first increases and then decreases, whereas the frictional pressure drop always increases. The pure hydrocarbon shows better flow and heat transfer performances than hydrocarbon mixture. Moreover, sloshing motions could bring about both drag reduction and heat transfer enhancement. These results are helpful to understand condensation flow in a spiral pipe.

Keywords: hydrocarbons, condensation, spiral pipe, sloshing motion

References:

[1] Li, S., Jiang, Y., Cai, W., et al. (2018). The influence of structural parameters on heat transfer and pressure drop for hydrocarbon mixture refrigerant during condensation in enhanced spiral pipes. Applied Thermal Engineering, vol. 140, pp. 759–774.


[2] Li, S., Cai, W., Chen, J., et al. (2018). Evaluation analysis of correlations for predicting void fraction of condensation hydrocarbon refrigerant upward flow in a spiral pipe. Applied Thermal Engineering, vol. 140, pp. 716–732.


[3] Wongwises, S. and Polsongkram, M. (2006). Condensation heat transfer and pressure drop of HFC-134a in a helically coiled concentric tube-in-tube heat exchanger. International Journal of Heat and Mass Transfer, vol. 49, no. 23–24, pp. 4386–4398.


[4] Gupta, A., Kumar, R., and Gupta, A. (2014). Condensation of R-134a inside a helically coiled tube-in-shell heat exchanger. Experimental Thermal and Fluid Science, vol. 54, pp. 279–289.


[5] Mozafari, M., Akhavan-Behabadi, M. A., Qobadi-Arfaee H, Fakoor-Pakdaman M: Condensation and pressure drop characteristics of R600a in a helical tube-in-tube heat exchanger at different inclination angles. Applied Thermal Engineering, 2015; 90: 571-578.


[6] Salimpour, M. R., Shahmoradi, A., and Khoeini, D. (2017). Experimental study of condensation heat transfer of R-404A in helically coiled tubes. International Journal of Refrigeration, vol. 74, pp. 584–591.


[7] Li, S., Cai, W., Chen, J., et al. (2018). Numerical study on the flow and heat transfer characteristics of forced convective condensation with propane in a spiral pipe. International Journal of Heat and Mass Transfer, vol. 117, pp. 1169–1187.


[8] Li, S., Cai, W., Chen, J., et al. (2018). Numerical study on condensation heat transfer and pressure drop characteristics of ethane/propane mixture upward flow in a spiral pipe. International Journal of Heat and Mass Transfer, vol. 121, pp. 170–186.


[9] Neeraas, B. O. (1993). Condensation of Hydrocarbon Mixtures in Coil-wound LNG Heat Exchangers, Tube-side Heat Transfer and Pressure Drop. PhD thesis, Norwegian Institute of Technology.


[10] Tan, S., Su, G. H., Pu-Zhen, G. (2009). Heat transfer model of single-phase natural circulation flow under a rolling motion condition. Nuclear Engineering and Design, vol. 239, no. 10, pp. 2212–2216.


[11] Yu, S., Wang, J., Yan, M., et al. (2017). Experimental and numerical study on single-phase flow characteristics of natural circulation system with heated narrow rectangular channel under rolling motion condition. Annals of Nuclear Energy, vol. 103, pp. 97–113.


[12] Jin, G., Yan, C., Sun, L., et al. (2014). Effect of rolling motion on transient flow resistance of two-phase flow in a narrow rectangular duct. Annals of Nuclear Energy, vol. 64, pp. 135–143.


[13] Chen, C., Gao, P., Tan, S., et al. (2015). Effect of rolling motion on two-phase frictional pressure drop of boiling flows in a rectangular narrow channel. Annals of Nuclear Energy, vol. 83, pp. 125–136.


[14] Chen, C., Gao, P., Tan, S., et al. (2015). Effects of rolling motion on thermal–hydraulic characteristics of boiling flow in rectangular narrow channel. Annals of Nuclear Energy, vol. 76, pp. 504–513.


[15] Lemmon, E. W., Huber, M. L., and Mclinden, M. O. (2010). NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP. 9.0.

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