You are here

Modeling of Saturated Two-Phase Flow Expansion across an Abrupt Area Change

Journal Name:

Publication Year:

Author NameUniversity of Author
Abstract (2. Language): 
In this study, the pressure recovery of two-phase saturated steam-water mixture is determined across sudden expansion fittings with the vapor phase being compressible. The pressure recovery is determined by employing the conservative equations of mass, momentum and energy with entropy generation based on two-phase separated flow model. The pressure and steam quality at the inlet of the abrupt flow area are in a range of 0.15 8.5 MPa and quality of 0.5 1. respectively. Also, the ratio of the inlet to outlet flow area is in the range of 0.1 1. During an adiabatic expansion process, the profile of the entropy does not increase monotonically, but it reaches a maximum value at the inlet quality of x1 0.3, before it goes to zero and the process becomes an isentropic process at the specified inlet pressure of 1 p 0.2 MPa. At this steam quality the conversion rate of the dynamic pressure head into static change becomes a minimum. The trend of the curves for pressure recovery against two phase mass velocity is proportional to the inverse of the inlet pressure so that the higher the inlet pressure the lower increase in pressure recovery is obtained. The results also show a good agreement with the experimental data in the literature.
147
154

REFERENCES

References: 

[1] M. K. Roul and S. K. Dash, “Single-Phase and two-phase flow through
thin and thick orifices in horizontal Pipes,” ASME Journal of Fluids
Engineering, vol.134(9), pp. 091301, 2012.
[2] H. Ozmen-Cagatay and S. Kocaman, “Investigation of dam-break flow
over abruptly contracting channel with trapezoidal-shaped lateral
obstacles,” ASME Journal of Fluids Engineering. Vol. 134(8), 081204,
7pages, 2012.
[3] S. Chakrabarti, D. K. Mandal and S. Rao., S., “Numerical simulation of
the performance of a sudden expansion with fence viewed as a diffuser
in low Reynolds number regime,” ASME Journal of Engineering for
Gas Turbines and Power. Vol. 132(11), 2010.
[4] H. Ohtake, M. Hagiwarai and Y. Koizumi, “Experimental and analytical
studies on frictional pressure drops of gas-liquid two-phase flow at vena
contract and expansion,” Proc. ASME 6th International Conference on
Nanochannels, Microchannels, and Minichannels, p. 379, 2008.
[5] X. Yan, Q. Wang, X. Suo and Y. Wu, “Investigation of flow resistance
in microchannels with a sudden contraction or expansion using DSMC,
“Proc. ASME First International Conference on Micro/Nanoscale Heat
Transfer, Parts A and B 715. 2008.
[6] I. Y. Chen, S. Wongwises, B. C. Yang and C. C.Wang, “Two-Phase
flow across small sudden expansions and contractions,” Heat Transfer
Engineering , vol. 31(4), pp. 298-309, 2010.
[7] M. Y. Gundogdu, A. I. Kutlar, and H. Duz, “Analytical prediction of
pressure loss through a sudden-expansion in two-phase pneumatic
conveying lines,” Advanced Power Technology, 20(1), pp.48-54 2009.
[8] L. Yang and C. L. Zhang, "Two-Fluid mode of refrigeration two-phase
flow through short tube orifice,” Int. J. Refrigeration, vol. 28, pp. 419-
427, 2005.
[9] I. Y. Chen, M. C. Chu, J. S. Liaw and C. C. Wang, “Two-Phase flow
characteristics across sudden contraction in small rectangular channels, “
Experimental Thermal and Fluid Science, vol. 32, pp.1609-1619, 2008.
[10] J. Schmidt and L. Friedel, “Two-Phase pressure drop across sudden
contractions in duct areas,” Int. J. of Multiphase Flow , vol. 23, pp.283–
299, 1997.
[11] K. Kondo, K. Yoshida, T. Okawa and I. Kataoka, “Applicability of twofluid
model and its constitutive equations to gas-liquid two-phase flow
in sudden expansion,” Proceedings of 11th int. Conference on Nuclear
Engineering, Japan, pp.20-23, 2003.
[12] A. Attou, M. Giot and J. M. Seynhaeven, “Modeling of steady-state twophase
bubbly flow through a sudden enlargement,” Int. J. of Heat and
Mass Transfer, vol. 40, pp. 3375–3385, (1997.
[13] F. F. Abdelali, G. Hahn, S. M. Ghiaasiaan, S. L. Abdel-Khalik, S. S.
Jeter, M. Yoda and D. L. Sadowski, “Pressure drop caused by abrupt
flow area changes in small channels,” Experimental Thermal and Fluid
Science, vol. 29, pp.425–434, 2005.
International Journal of Science and Engineering Investigations, Volume 6, Issue 65, June 2017 154
www.IJSEI.com Paper ID: 66517-26
ISSN: 2251-8843
[14] M. Salcudean, D. C. Groeneveld and L. Leung, “Effect of flow obstruction geometry on pressure drops in horizontal air–water flow,”Int. J. of Multiphase Flow, vol. 9(1), pp.73–85, 1983.
[15] F. Romie, 1958, “Private communication to P. A. Lottes, American Standard Co” unpublished.
[16] Z. Rouhani, “Modified correlations for void and two-phase pressure drop,” Report AE-RTV-841, 1958.
[17] G. B. Wallis, One Dimensional two-phase flow, McGraw-Hill, New York, 1969.
[18] P. A. Lottes, “Expansion losses in two-phase flow,” Nuclear Science and Energy, vol. 9, pp.26-31, 1961.
[19] M. D. Chisholm and L. A. Sutherland, “Prediction of pressure gradients in pipelines system during two-phase flow,” Proc. Of Institution of Mechanical Engineers, vol. 184(3), 1969.
[20] R. W. Lockhart and R. C. Martinelli, “Proposed correlation of data for isothermal two-phase two-component flow in pipes,” Chem. Eng. Prog, vol. 45, p.39, 1949.
[21] B. Richardson, B., “Some problems in horizontal two-phase, two-component flow,” Report ANL-5949, 1958.
[22] M. Wadle, M., “A new formula for the pressure recovery in an abrupt diffuser”, Int. J. Multiphase Flow, vol. 15(2), pp.241-256, 1989.
[23] J. M. Mandhane, G. A. Gregory and K. Aziz, “A flow pattern map for gas- liquid flow in horizontal pipes,” Int. Multiphase Flow, vol. 1, pp.537-553, 1974.
[24] R. E. Sonntag and C. Borgnakke, “Fundamentals of Thermodynamics, fifth ed., John Wiley & Sons, Inc., New York, 1998.
[25] R. L. Burden and J.D. Faires, Numerical Analysis, PWS-KENT, Publishing Co., Fifth ed., Boston, 1993.

Thank you for copying data from http://www.arastirmax.com