A Numerical Model of Multiphase Flow Around a Well

1973 ◽  
Vol 13 (06) ◽  
pp. 311-320 ◽  
Author(s):  
F. Sonier ◽  
O. Ombret

Abstract This paper describes a two-dimensional three-phase numerical model for simulating two- or three-phase coning behavior. The model is fully implicit with respect to all variables and uses the simultaneous solution of the different equations describing multiphase flow. For determining well flow rates from all blocks communicating with the well, particular attention has been paid to the well boundary condition, which is considered to be a physical boundary. The mathematical expression of these well conditions enables flow rates to be calculated in a perfectly implicit manner and thus makes the model very stable so that the computational error in time is very small. The model described is appreciably different in this respect from previous models in which the well is represented by source points and in which the flour terms are calculated by using various simplifications. The results of several tests are presented. The model was checked by the simulation of several water coning cases that had previously been studied on a physical model. Four examples are given here. In these examples, the boundary influx conditions and fluid mobility ratio are made to vary. One of them illustrates the care that must be taken when using simplified solution schemes for the boundary conditions. Introduction Multiphase numerical models have usually employed finite-difference approximations in which relative permeabilities are evaluated explicitly at the beginning of each time step. But simulators of this type are not capable of solving problems characterized by high flow velocities and such phenomena as well coning, except perhaps at phenomena as well coning, except perhaps at extremely high cost. Recently, some papers were published describing a method that employs semi-implicit relative permeabilities and uses the simultaneous solution of multiphase equations. This method is very efficient. In these simulators, the well is represented by source points, and flow rate terms are calculated by using various simplifications (mobility or potential methods). potential methods). This paper describes a new numerical coning model. The numerical part of the model is similar to that in the latest models, but its representation of wellbore conditions is quite different and more nearly expresses physical phenomena caused by end effects. The well is represented full-scale and not by source points. Furthermore, so as not to partially screen out wellbore conditions, the partially screen out wellbore conditions, the producing interval, even if it is small, may be producing interval, even if it is small, may be advantageously represented by several layers. Any condition may be specified for the external boundaries. All the leading physical parameters are treated semi-implicitly. When a flow rate is imposed on the well, taking into account the well-wall boundary conditions, the calculation of production terms is fully implicit. This calculation is iterative, but at almost each time step a simple algorithm enables a direct solution to be obtained. The results of numerous simulations are presented. Studies on physical models have demonstrated the full validity of the numerical model. The simulation of actual field cases shows that the model is very efficient. CONING MODEL The numerical model described in this paper is a two-dimensional one with radial symmetry. A compressible three-phase system is considered, with possible exchange between the gas and oil phases independently of the composition. phases independently of the composition. The introduction of Darcy's law into the continuity equation for each of the three fluids leads to a system of partial differential equations. SPEJ p. 311

Author(s):  
Kiran K. Muramalla ◽  
Yitung Chen ◽  
Anthony E. Hechanova

This paper deals with the development of a two-dimensional numerical model to predict the wall-catalyzed homogeneous decomposition of sulfur trioxide in a tubular component geometry for the production of hydrogen by the sulfur-iodine thermochemical water splitting cycle, a candidate cycle in the U.S. Department of Energy Nuclear Hydrogen Initiative. The reacting fluid is a mixture of sulfur trioxide gas and water vapor inside the tubes of a heat exchanger. The heat exchanger is made of Incoloy alloy 800H with ALFA-4 coated on the inner walls which acts as a catalyst. Decomposition of sulfur trioxide depends on many different parameters such as wall surface temperature, mole flow rate of the reacting mixture, diameter of the reactor tube, length of the reactor tube, operating pressure and inlet temperature of the reacting mixture. The effects of wall surface temperature, diameter of the reactor tube and mole flow rate on the decomposition of sulfur trioxide were investigated using a two-dimensional numerical model using Computational Fluid Dynamics (CFD) techniques. The preprocessor GAMBIT was used to create a computational mesh and the CFD software package FLUENT 6.2.16 [1] which is based on finite volume methods was used to simulate the problem. Both FLUENT 6.2.16 and Tecplot 10.0 are used to post process the problem.


Author(s):  
Vishal Singhal ◽  
Suresh V. Garimella

A novel micropump design for electronics cooling applications capable of integration into microchannel heat sinks is presented. The pumping action is due to the combined action of Coulomb forces due to induction electrohydrodynamics (EHD) and a vibrating diaphragm with nozzle-diffuser elements for flow rectification. A comprehensive numerical model of the micropump accounting for transient charge transport and vibrating diaphragm deformation is developed. Each component of the model is validated by comparing to analytical, numerical or experimental results from the literature. It is shown that the flow rate achieved by the micropump with combined action of EHD and vibrating diaphragm can be higher than the sum of flow rates achieved from the action of the EHD and the vibrating diaphragm, independent of each other.


2001 ◽  
Vol 123 (2) ◽  
pp. 70-75 ◽  
Author(s):  
S. F. Baudic ◽  
A. N. Williams ◽  
A. Kareem

A numerical model is developed to simulate fully nonlinear transient waves in a semi-infinite, two-dimensional wave tank. A mixed Eulerian-Lagrangian formulation is adopted and a high-order boundary element method is used to solve for the fluid motion at each time step. Input wave characteristics are specified at the upstream boundary of the computational domain using an appropriate wave theory. At the downstream boundary, a damping region is used in conjunction with a radiation condition to prevent wave reflections back into the computational domain. The convergence characteristics of the numerical model are studied and the numerical results are validated through a comparison with previous published data.


1970 ◽  
Vol 10 (04) ◽  
pp. 425-436 ◽  
Author(s):  
R.C. MacDonald

Abstract This paper describes and evaluates three numerical methods for the simulation of well coning behavior. The first method employs the implicit pressure-explicit saturation (IMPES) analysis with pressure-explicit saturation (IMPES) analysis with the production terms treated implicitly. The second technique is similar to the first model except that the interblock transmissibilities are also treated implicitly in the saturation equation. The third model is fully implicitly with respect to all variables in a manner qualified in the introduction and utilizes simultaneous solution of the difference equations describing the multiphase flow. The use of implicit transmissibilities in the IMPES model results in a several-fold increase in the allowable time-increment size over that attainable with the implicit production IMPES scheme, while the computing time per step is increased by less than 10 percent. The fully implicit model accepts larger time-increment sizes than possible with the first two methods but requires 3.3 times the computing time per time step needed by the second model. The fully implicit model is substantially more efficient for problems involving high capillary forces (treated explicitly in the IMPES methods) and small computing grid blocks at the wellbore. In problems involving moderate capillary forces and larger grid spacings, the fully implicit method and the implicit transmissibility IMPES technique are comparable in computing efficiency. The results of three coning studies are presented: a water-oil problem, a three-phase coning presented: a water-oil problem, a three-phase coning example, and a comparison of simulation results with a laboratory coning experiment. Also presented is an analysis of truncation error and a comparison of computational work requirements. Introduction This study was performed to evaluate three finite-difference schemes for simulating well coning behavior. The basis for this evaluation was the IMPES (implicit pressure-explicit saturation) model with explicit transmissibilities and implicit production terms. This model is referred to hereafter production terms. This model is referred to hereafter as Model 1. The next model evaluated in this work is an IMPES model similar to Model 1, except that the saturation-dependent interblock transmissibilities are treated implicitly rather than explicitly in the saturation equation. The third model is fully implicitly with respect to all variables and terms transmissibilities, pressure, saturation an capillary pressure - and utilizes simultaneous solution of the difference equations describing the multiphase flow. These two models are referred to hereafter simply as Model 2 and Model 3. For the purpose of clarity all models are described in purpose of clarity all models are described in reference to the problem of incompressible, two-phase flow. The techniques are equally applicable, however, to compressible, three-phase flow models. The examples chosen for illustration employ both incompressible and compressible simulation models. SPEJ p. 425


1996 ◽  
Vol 34 (5-6) ◽  
pp. 1-9 ◽  
Author(s):  
Peter Krebs ◽  
Anastasios I. Stamou ◽  
Jaime L. García-Heras ◽  
Wolfgang Rodi

A numerical model for predicting the flow in clarifiers is presented which accounts for density-affected and turbulent flow as well as for the settling of activated sludge. The reliability of the two-dimensional model is demonstrated through verification by means of a laboratory experiment which was specially designed for this purpose. The numerical model is then applied for an evaluation of inlet and outlet arrangements. The inlet is positioned at the bottom and the inlet aperture is varied. An outlet at the top of the end wall is compared with outlets longitudinally extended at the surface. The alternatives are assessed by analysis of streamline patterns, layer charactersitics and the entrainment into the bottom current, i.e. the increase of its flow rate. The study demonstrates how numerical modelling can be used for systematic evaluation of the effect of geometrical configurations on the flow in secondary clarifiers.


Author(s):  
Juray De Wilde ◽  
Edward Baudrez ◽  
Geraldine J. Heynderickx ◽  
Jan Vierendeels ◽  
Denis Constales ◽  
...  

A pointwise simultaneous solution algorithm based on dual time stepping was developed by De Wilde et al. (2002). With increasing grid aspect ratios, the efficiency of the point method quickly drops. Most realistic flow cases, however, require high grid aspect ratio grids, with the highest grid spacing in the streamwise direction. In this direction, the stiffness is efficiently removed by applying preconditioning (Weiss and Smith, 1995). In the direction perpendicular to the stream wise direction, stiffness remains because of the viscous and the acoustic terms. To resolve this problem, a line method is presented. All nodes in a plane perpendicular to the stream wise direction, a so-called line, are solved simultaneously. This allows a fully implicit treatment of the fluxes in the line, removing the stiffness in the line wise directions. Calculations with different grid aspect ratios are presented to investigate the convergence behavior of the line method. The line method presented is particularly suited for parallelization. At each pseudo-time step, the lines (typically hundreds) can be solved independently of each other. The Message Passing Interface (MPI) standard (Snir et al., 1996) is used. The communication between the processors can be easily reduced by solving a block of lines per processor. The communication is then limited to information regarding only the outer lines of the block. In common practice, the number of lines is much higher than the number of processors available. In this region of the lines/processor space, the reduction of the calculation time is linear with the number of processors that is used.


2011 ◽  
Vol 674 ◽  
pp. 359-388 ◽  
Author(s):  
V. DOYEUX ◽  
T. PODGORSKI ◽  
S. PEPONAS ◽  
M. ISMAIL ◽  
G. COUPIER

The problem of the splitting of a suspension in bifurcating channels divided into two branches of non-equal flow rates is addressed. As has long been observed, in particular in blood flow studies, the volume fraction of particles generally increases in the high-flow-rate branch and decreases in the low-flow-rate branch. In the literature, this phenomenon is sometimes interpreted as the result of some attraction of the particles towards this high-flow-rate branch. In this paper, we focus on the existence of such an attraction through microfluidic experiments and two-dimensional simulations and show clearly that such an attraction does not occur but is, on the contrary, directed towards the low-flow-rate branch. Arguments for this attraction are given and a discussion on the sometimes misleading arguments found in the literature is given. Finally, the enrichment of particles in the high-flow-rate branch is shown to be mainly a consequence of the initial distribution in the inlet branch, which shows necessarily some depletion near the walls.


Author(s):  
Yingyuan Liu ◽  
Leqin Wang ◽  
Zuchao Zhu

This work is purposed to study the flow characteristics of rotor pumps including cavitation. First, a simplified two-dimensional numerical model is developed and computing strategies of the numerical analysis for cavitation are set up, including the selection of cavitation model and its parameters. Second, the reliability and accuracy of the two-dimensional numerical model are verified by experimental results. Then, several factors affecting the cavitation are discussed, including the rotational speeds, pressure differences, clearance sizes, and inlet pressures. For different rotational speeds and pressure differences, the mass flow rates with cavitation are a little larger than that without cavitation, but the amplitudes of the mass flow rates with cavitation are much larger than that without cavitation. Meanwhile, the volume fraction of the water vapor increases with the increasing speeds and the decreasing pressure differences. However, compared with the influence of rotational speeds, the influence of the pressure differences on the vapor contents is relatively smaller. Regarding the clearance size, the smaller the clearance size is, the stronger the cavitation will be. Furthermore, the clearance size between two rotors has a larger effect on the cavitation than that between rotor and pump case. For inlet pressure, it has a little effect on the mass flow rates when cavitation is not considered, but it presents a remarkable effect for the model with cavitation. In addition, the peaks of the volume fractions of vapor and the mass flow rates generally offset backward with the decreasing inlet pressures.


2012 ◽  
Vol 212-213 ◽  
pp. 1151-1154
Author(s):  
Yan Jun Ji ◽  
Xin Zhang ◽  
Hai Feng Zhai ◽  
Dong Yang Ren ◽  
Ling Hua

Surface tension associated with temperature is usually considered non-negligible to affect discharge capacity of sharp-crested weir when head is low. In the study, a two-dimensional numerical model verified by experiments was applied to simulate the effect of water temperature on discharge capacity of clinging flow for a rectangular sharp-crested weir at low head levels. The results showed that with a same flow rate, differences in the elevation of free surface were minimal between different temperature levels despite a slightly higher elevation of free surface at lower water temperature. The head-discharge relationships were very similar for different temperature levels. This study concluded that the effect of water temperature on head-discharge relationships and the discharge capacity of clinging flow for a rectangular sharp-crested weir was negligible at low heads.


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