Comparison of Alternating Direction Explicit and Implicit Procedures in Two-Dimensional Flow Calculations

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 ◽  
Vol 123 (4) ◽  
pp. 811-818 ◽  
Author(s):  
Jun Ishimoto ◽  
Mamoru Oike ◽  
Kenjiro Kamijo

The two-dimensional characteristics of the vapor-liquid two-phase flow of liquid helium in a pipe are numerically investigated to realize the further development and high performance of new cryogenic engineering applications. First, the governing equations of the two-phase flow of liquid helium based on the unsteady thermal nonequilibrium multi-fluid model are presented and several flow characteristics are numerically calculated, taking into account the effect of superfluidity. Based on the numerical results, the two-dimensional structure of the two-phase flow of liquid helium is shown in detail, and it is also found that the phase transition of the normal fluid to the superfluid and the generation of superfluid counterflow against normal fluid flow are conspicuous in the large gas phase volume fraction region where the liquid to gas phase change actively occurs. Furthermore, it is clarified that the mechanism of the He I to He II phase transition caused by the temperature decrease is due to the deprivation of latent heat for vaporization from the liquid phase. According to these theoretical results, the fundamental characteristics of the cryogenic two-phase flow are predicted. The numerical results obtained should contribute to the realization of advanced cryogenic industrial applications.


Author(s):  
Yumi Yamada ◽  
Toyou Akashi ◽  
Minoru Takahashi

In a lead-bismuth alloy (45%Pb-55%Bi) cooled direct contact boiling water fast reactor (PBWFR), steam can be produced by direct contact of feed water with primary Pb-Bi coolant in the upper core plenum, and Pb-Bi coolant can be circulated by buoyancy forces of steam bubbles. As a basic study to investigate the two-phase flow characteristics in the chimneys of PBWFR, a two-dimensional two-phase flow was simulated by injecting argon gas into Pb-Bi pool in a rectangular vessel (400mm in length, 1500mm in height, 50mm in width), and bubble behaviors were investigated experimentally. Bubble sizes, bubble rising velocities and void fractions were measured using void probes. Argon gas was injected through five nozzles of 4mm in diameter into Pb-Bi at two locations. The experimental conditions are the pressure of atmospheric pressure, Pb-Bi temperatures of 443K, and the flow rate of injection Ar gas is 10, 20, and 30 NL/min. The measured bubble rising velocities were distributed in the range from 1 to 3 m/s. The average velocity was about 0.6 m/s. The measured bubble chord lengths were distributed from 1mm up to 30mm. The average chord length was about 7mm. An analysis was performed by two-dimensional and two-fluid model. The experimental results were compared with the analytical results to evaluate the validity of the analytical model. Although large diameter bubbles were observed in the experiment, the drag force model for spherical bubbles performed better for simulation of the experimental result because of high surface tension force of Pb-Bi.


2013 ◽  
Vol 54 (7) ◽  
Author(s):  
Simo A. Mäkiharju ◽  
Celine Gabillet ◽  
Bu-Geun Paik ◽  
Natasha A. Chang ◽  
Marc Perlin ◽  
...  

1991 ◽  
Vol 77 (2) ◽  
pp. 236-243 ◽  
Author(s):  
Koichiro SHIBATA ◽  
Masakata SHIMIZU ◽  
Sin-ichi INABA ◽  
Reijiro TAKAHASHI ◽  
Jun-ichiro YAGI

2019 ◽  
Vol 52 (1) ◽  
pp. 015501
Author(s):  
Shirin Najafizadeh ◽  
Afshin Ahmadi Nadooshan ◽  
Morteza Bayareh

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