Hostname: page-component-586b7cd67f-rdxmf Total loading time: 0 Render date: 2024-11-28T09:00:52.288Z Has data issue: false hasContentIssue false

Dynamic Modeling of Phase Crossings in Two-Phase Flow

Published online by Cambridge University Press:  20 August 2015

S. Madsen*
Affiliation:
Alsion 2, Mads Clausen Institute, University of Southern Denmark, DK-6400 Sønderborg, Denmark
C. Veje*
Affiliation:
Alsion 2, Mads Clausen Institute, University of Southern Denmark, DK-6400 Sønderborg, Denmark
M. Willatzen*
Affiliation:
Alsion 2, Mads Clausen Institute, University of Southern Denmark, DK-6400 Sønderborg, Denmark
*
Corresponding author.Email:[email protected]
Get access

Abstract

Two-phase flow and heat transfer, such as boiling and condensing flows, are complicated physical phenomena that generally prohibit an exact solution and even pose severe challenges for numerical approaches. If numerical solution time is also an issue the challenge increases even further. We present here a numerical implementation and novel study of a fully distributed dynamic one-dimensional model of two-phase flow in a tube, including pressure drop, heat transfer, and variations in tube cross-section. The model is based on a homogeneous formulation of the governing equations, discretized by a high resolution finite difference scheme due to Kurganov and Tadmore.

The homogeneous formulation requires a set of thermodynamic relations to cover the entire range from liquid to gas state. This leads a number of numerical challenges since these relations introduce discontinuities in the derivative of the variables and are usually very slow to evaluate. To overcome these challenges, we use an interpolation scheme with local refinement.

The simulations show that the method handles crossing of the saturation lines for both liquid to two-phase and two-phase to gas regions. Furthermore, a novel result obtained in this work, the method is stable towards dynamic transitions of the inlet/outlet boundaries across the saturation lines. Results for these cases are presented along with a numerical demonstration of conservation of mass under dynamically varying boundary conditions. Finally we present results for the stability of the code in a case of a tube with a narrow section.

Type
Research Article
Copyright
Copyright © Global Science Press Limited 2012

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)

References

[1]He, X.D., Liu, S., Asada, H., and Itoh, H., Multivariable control of vapor compression systems, HVAC&R Research, 4, 205–230, 1998.Google Scholar
[2]Willatzen, M., Pettit, N.B.O.L., and Ploug-Sørensen, L., A general simulation model for evaporators and condensers in refrigeration. Part I: Moving boundary formulation of two-phase flows with heat exchange, Int. J. Refrig., 21, 398–403, 1998.Google Scholar
[3]Zhang, W.‐J., Zhang, C.‐L., A generalized moving-boundary model for transient simulation of dry-expansion evaporators under larger disturbances, Int. J. Refrig., 29, 1119–1127, 2006.Google Scholar
[4]McKinley, T. L., Alleyne, A. G., An advanced nonlinear switched heat exchanger model for vapor compression cycles using the moving-boundary method, Int. J. Refrig., 31, 1253–1264, 2008.CrossRefGoogle Scholar
[5] S. Madsen, Veje, C.T. and Willatzen, M., Implementation Of The Kurganov-Tadmor High Resolution Semi-Discrete Central Scheme For Numerical Solution Of The Evaporation Process In Dry Expansion Evaporators, in Proceedings of the 50’th SIMS Conference, 2009.Google Scholar
[6]Jia, X., Tso, C.P., Chia, P.K. and Jolly, P., A distributed model for prediction of the transient response of an evaporator, Int. J. Refrig., 18, 336–342, 1995.Google Scholar
[7]Jia, X., Tso, C.P., Jolly, P. and Wong, Y.W., Distributed steady and dynamic modeling of dry-expansion evaporators, Int. J. Refrig., 22, 126–136, 1999.Google Scholar
[8]Garcia-Valladares, O.,Perez-SegarraandJ, C.D..Rigola, j., Numerical simulation of double-pipe condensers and evaporators, Int. J. Refrig., 27, 173–182, 2004.Google Scholar
[9]Morales-Ruiz, S., Rigola, J., Perez-Segarra, C.D., Garcia-Valladares, O., Numerical analysis of two-phase flow in condensers and evaporators with special emphasis on single-phase/two-phase transition zones, Appl. Therm. Eng., 29, 1032–1042, 2009.Google Scholar
[10]Kurganov, A., Tadmor, E., New high-resolution semi-discrete central schemes for Hamilton-Jacobi equations, Journal of Computational Physics, 160, 720–742, 2000.Google Scholar
[11]Kurganov, A., Tadmor, E., New high-resolution central schemes for nonlinear conservation laws and convection-duiffusion equations, Journal of Computational Physics, 160, 241–282, 2000.Google Scholar
[12]Karni, S., Kirr, E., Kurganov, A., and Petrova, G., Compressible two-phase flows by central and upwind schemes, ESIAM: Math. Model. and Num. Anal., 38, 477–493, 2004.Google Scholar
[13]Mostafa Ghiaasiaan, S., Two-Phase Flow, Boiling, and Condensation: In Conventional and Miniature Systems, Cambridge University Press, 1st edition, October 22, 2007.CrossRefGoogle Scholar
[14]Lemmon, E.W., Huber, M.L., McLinden, M.O.NIST Standard Reference Database 23: Reference Fluid Thermodynamic and Transport Properties-REFPROP, Version 9.0, National Institute of Standards and Technology, Standard Reference Data Program, Gaithersburg, 2010.Google Scholar
[15]Wallis, G., One-dimensional Two-phase Flow, McGraw-Hill, 1969.Google Scholar
[16]Collier, John G. and Thome, John R., Convective Boiling and Condensation, 3rd Edition, Oxford University Press, 198 Madison Avenue, New York, 1996.Google Scholar
[17]Carlson, R. E. and Fritsch, F. N., An Algorithm For Monotone Piecewise Bicubic Interpolation, SIAM J. Numer. Anal., 26, No. 1, 230–238, 1989.CrossRefGoogle Scholar
[18]Gottlieb, S., On High Order Strong Stability Preserving Runge-Kutta and Multi Step Time Discretizations, J. Sci. Comput., 25, 105–128, 2005.Google Scholar
[19]Buecker, D. and Wagner, W., Reference Equations of State for the Thermodynamic Properties of Fluid Phase n-Butane and Isobutane, J. Phys. Chem. Ref. Data, 35(2), 929–1019, 2006.Google Scholar