Abstract
The transient fluid flow and temperature distributions in argon-stirred ladles have been investigated. The governing equations of unsteady fluid flow and energy were solved numeri-cally with a control-volume technique, while the turbulence was modeled by the two-equationk- ∃ model. The two-phase zone was described by novel experimental equations, which char-acterize the gas-fraction distribution in the bath for a wide range of variables in both aqueous and liquid metal systems. Fully transient computational results are presented and compared against transient temperature computations based on a steady-state velocity field. The resulting mixing times compare closely with industrial experience.
Similar content being viewed by others
Abbreviations
- C1,C 2 :
-
constants in the turbulence model
- C d C pg ,C pl :
-
gas specific heat capacity; liquid specific heat capacity, J/kg ‡C
- d o :
-
diameter of nozzle, m Fr Froude number =
- Q o 2 /gd o 5 g :
-
acceleration due to gravity, m/s2
- G :
-
generation of turbulent energy, kg/m s3
- h b :
-
depth of liquid, m
- k :
-
turbulence kinetic energy, m2/s2
- k :
-
thermal conductivity of liquid, W/(m ‡C)
- N :
-
parameter defined as
- [(gdo 5/Qo 2)0.26(pl/pgo)0.13(z/do)0.94]:
-
(Eqs. [11] and [12])
- p :
-
pressure, kg/m s2
- q s ,q wb :
-
heat flux through bath surface; heat flux through ladle refractory wall, W/m2 go volumetric gas flow rate at orifice conditions, m3/s
- r :
-
rα max/2 radial position; half-value radius, m
- R :
-
radius of vessel, m
- R Ø :
-
residuals in the discretized Ø equation
- t :
-
time, s
- T :
-
temperature, ‡C
- T :
-
refreference temperature appearing in the buoyancy term
- u :
-
mean axial velocity component, m/s
- v mean radial velocity component, m/s:
-
z axial position, m
- α,αmax local time-averaged gas volume fraction; gas volume fraction at plume centerline:
-
Βl, coefficient of thermal expansion of
- liquid, ‡C-1 dissipation rate of turbulence kinetic energy, m2/s3 :
-
Μ, Μeff
- molecular, effective, and turbulent viscosity:
-
Μ l
- kg/m s:
-
P go ,P l
- gas density at orifice conditions; liquid p density; density of two-phase mixture, kg/m3 :
-
ΣT, ΣT,t
- laminar and turbulent Prandtl numbers and:
-
Σ k ,Σ te
- Schmidt numbers for:
-
k and ∃
- reff effective exchange coefficient (diffusivity), kg/m s:
-
v t
- turbulent kinematic viscosity:
-
m2/s
References
S. Soeda, H. Nemoto, E. Sakamoto, T. Kawawa, and T. Koyano:Suppl. Trans. ISIJ, 1971, vol. 11, pp. 248–51.
R. Albemy and A. Leclercq:Proc. of Mathematical Process Models in Iron and Steelmaking, TMS, London, 1973, pp. 151–56.
D.A. Domchek:J. Met., 1972, vol. 24 (3), pp. 38–42.
R. Widdowson:Ironmaking and Steelmaking, 1981, vol. 8 (5), pp. 194–200.
H.W. den Hartog, S. Rosier, A.B. Snoeijer, and H.M. Verhoog:Proc. of Mathematical Process Models in Iron and Steelmaking, TMS, London, 1973, pp. 213–18.
O.J. Ilegbusi and J. Szekely:Trans. ISIJ, 1987, vol. 27, pp. 563–69.
M.E. Salcudean, K.Y.M. Lai, and R.I.L. Guthrie:Can. J. Chem. Eng., 1985, vol. 63, pp. 51–61.
T. DebRoy and A.K. Majumdar:J. Met., 1981, vol. 33 (11), pp. 42–47.
J. Szekely, H.J. Wang, and K.M. Riser:Metall. Trans. B, 1976, vol. 7B, pp. 287–95.
J.H. Grevet, J. Szekely, and N. El-Kaddah:Int. J. Heat Mass Transfer, 1982, vol. 25, pp. 487–97.
J.W. McKelliget, M. Cross, R.D. Gibson, and J.K. Brimacombe:Symp. on Heat and Mass Transfer in Metallurgical Systems, D.B. Spalding and N.H. Afgan, eds., Hemisphere Publishing Corp., New York, NY, 1981, pp. 349–72.
T. DebRoy, A.K. Majumdar, and D.B. Spalding:Appl. Math. Modelling, 1978, vol. 2, pp. 146–50.
Y. Sahai and R.I.L. Guthrie:Metall. Trans. B, 1982, vol. 13B, pp. 203–11.
J.S. Woo, J. Szekely, A.H. Castillejos, and J.K. Brimacombe:Metall. Trans. B, in press.
A.H. Castillejos and J.K. Brimacombe:Metall. Trans. B, 1987, vol. 18B, pp. 649–58 and 659-71.
K.Y.M. Lai and M.E. Salcudean:Comput. Fluids, 1987, vol. 15 (3), pp. 281–95.
M.E. Salcudean and K.Y.M. Lai:Int. J. Num. Heat Transfer, in press.
A.H. Castillejos E. and J.K. Brimacombe:Metall. Trans. B, 1989, vol. 20B, pp. 595–601.
K. Nakanishi, T. Fuji, and J. Szekely:Ironmaking and Steel- making, 1975, vol. 2 (3), pp. 193–97.
O. Haida and J.K. Brimacombe:3rd Int. Conf. on Injection Met- allurgy, Luleå, Sweden, 1983, vol. 1, pp. 5:1–5:17.
W.R. Irving:Proc. of Mathematical Process Models in Iron and Steelmaking, TMS, London, 1973, pp. 218–19.
W.P. Jones and B.E. Launder:Int. J. Heat Mass Transfer, 1972, vol. 15, pp. 301–14.
B.E. Launder and D.B. Spalding:Comput. Math. Appl. Mech. Eng., 1974, vol. 3, pp. 269–89.
A.D. Gosman, V.M. Pun, H.E. Runchal, D.B. Spalding, and M. Wolfstein:Heat and Mass Transfer in Recirculating Flows, Academic Press, London, 1969.
D.B. Spalding:Int. J. Numer. Math. Meth. Eng., 1972, vol. 6, pp. 551–59.
S.V. Patankar and D.B. Spalding:Int. J. Heat Mass Transfer, 1972, vol. 15, pp. 1787–806.
A.D. Gosman and F.D.K. Ideriah:TEACH-2E: A General Com- puter Program for Two Dimensional Turbulent Recirculating Flow, Internal Report Department of Mechanical Engineering, Imperial College, University of London, 1976.
Author information
Authors and Affiliations
Additional information
A.H. Castillejos E., formerly Postdoctoral Fellow, The University of British Columbia,.
Rights and permissions
About this article
Cite this article
Castillejos, A.H., Salcudean, M.E. & Brimacombe, J.K. Fluid flow and bath temperature destratification in gas-stirred ladles. Metall Trans B 20, 603–611 (1989). https://doi.org/10.1007/BF02655917
Received:
Issue Date:
DOI: https://doi.org/10.1007/BF02655917