scholarly journals Transient Fluid Flow during Steady Continuous Casting of Steel Slabs: Part I. Measurements and Modeling of Two-phase Flow

2014 ◽  
Vol 54 (4) ◽  
pp. 845-854 ◽  
Author(s):  
Seong-Mook Cho ◽  
Seon-Hyo Kim ◽  
Brian G. Thomas
2005 ◽  
Vol 36 (6) ◽  
pp. 801-823 ◽  
Author(s):  
B. Zhao ◽  
B. G. Thomas ◽  
S. P. Vanka ◽  
R. J. O’Malley

1966 ◽  
Vol 6 (04) ◽  
pp. 350-362 ◽  
Author(s):  
K.H. Coats ◽  
M.H. Terhune

Abstract Analysis and example applications have been performed to compare the accuracy and computing speed of alternating-direction explicit and implicit procedures (ADEP and ADIP) in numerical solution of reservoir fluid flow problems. ADIP yields significantly greater accuracy and requires about 60 per cent more computing time than ADEP, not 300 or 500 per cent more as reported elsewhere. Introduction Several recent papers discuss an alternating-direction explicit difference approximation (ADEP) to the diffusion equation. Example applications of ADEP and ADIP were reported to support conclusions that ADEP is comparable in accuracy to ADIP and requires one-fifth to one-third the computing time of ADIP. Applications of ADEP in calculation of two-phase flow in reservoirs was also proposed. This study was performed to compare further the relative merits of ADEP and ADIP in simulation of two-dimensional flow of one and two fluid phases in reservoirs. Since two-phase flow equations are often essentially elliptic rather than parabolic, the efficiency of ADEP in solving the elliptic equation was also examined. ADIP AND ADEP DIFFERENCE EQUATIONS The diffusion equation: ...................(1) governs heat conduction, molecular diffusion and slightly compressible fluid flow through porous media for the case of homogeneous, isotropic media. The ADEP procedure involves replacement of Eq. 1 at odd time steps by: ,.................(2) and at even time steps by: ,.................(3) where Sweeping a two-dimensional grid from southwest to northeast using Eq. 2 and from northeast to southwest using Eq. 3 allows direct (explicit) calculation of u at the new time step at each grid point. SPEJ P. 350ˆ


2001 ◽  
Author(s):  
S. Bautista-Fragoso ◽  
Yuri V. Fairuzov

Abstract A numerical model of transient two-phase flow and conjugate heat transfer in a vertical pipeline is presented in the present paper. The drift-flux model is used to describe the fluid flow in the pipeline. The modeling of transient conjugate heat transfer is based on a mathematical formulation in which the pipe wall and the fluid are assumed to be in local thermal equilibrium. The effect of the thermal capacity of the pipe wall is taken into account by an additional term in the energy equation for the fluid flow. Such an approach allows significant simplifying the problem and reducing the computer running time. Numerical simulations of blowdown of a pipeline/riser system were performed. The effect of the pipe wall on the flow behavior was investigated.


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