Multidimensional Displacement of a Viscous Phase by a Non-Viscous Phase

1968 ◽  
Vol 8 (04) ◽  
pp. 325-330
Author(s):  
Alan D. Modine ◽  
Keith H. Coats

Abstract A mathematical model has been formulated for simulating three-dimensional displacement of a viscous fluid by a displacing fluid of zero viscosity. The model has been incorporated into a FORTRAN IV computer program for application in low-rate, high-permeability systems. Where applicable, the zero-viscosity program reduces computer time by a factor of 5 to 10 relative to conventional two- and three-dimensional programs. To determine the area of applicability, a gas-oil cross-section model representation of a high-dip, high-permeability reservoir was simulated with the zero-viscosity and conventional two-dimension programs for a range of flow rates up to 80 percent programs for a range of flow rates up to 80 percent of the critical rate. In comparing the two solutions, the conventional one was assumed to be the correct one because its program is based upon a more physically realistic model than that of the physically realistic model than that of the zero-viscosity solution. The two solutions agreed at rates up to 50 percent of the critical; at 80 percent they disagreed significantly. This indicates percent they disagreed significantly. This indicates that the zero-viscosity model, which is quite simple and inexpensive to apply, can be used with accuracy at rates up to at least 50 percent of the critical. This area of applicability is important in improving computational capability, for it is at these lower rates that the conventional programs are excessively costly. At the higher rates, where the zero-viscosity solution is not accurate, the conventional programs are easy and economical to apply. The zero-viscosity model accounts for capillary and gravitational forces, effects of viscosity and relative permeability for the displaced phase, and arbitrary reservoir heterogeneity. The program handles up to 1,800 blocks on an in-core basis. Introduction Computational difficulties caused by slow or metastable convergence in gas-oil calculations using conventional two-phase reservoir simulation programs have been correlatable with the effects of programs have been correlatable with the effects of low viscosity in the gas phase. In many such problems, a very small deviation in the calculated problems, a very small deviation in the calculated flow potentials causes a large deviation in the calculated gas flow due to the low viscosity. Thus, the program is trying to converge on a small variation in potential, which makes the computations difficult. A previous method of overcoming this difficulty has been to introduce in the conventional two-phase calculations an artificial resistance to gas flow; this method causes a more significant variation in the calculated flow potential. This paper describes a new method for treatment of gas-oil problems in which a zero-viscosity gas phase is used. Both methods are based on the assumption that oil mobility is the controlling factor in the displacement and that the behavior is insensitive to gas mobility over a relatively wide range. We show that the two methods give identical results, and since the correct gas mobility is bracketed by the two methods, we may conclude that either method gives valid results for low rate displacements. The chief advantage of the zero-viscosity program is lower computing costs. This report presents a mathematical description of the zero-viscosity model and compares saturation distributions calculated for several typical problems using the zero-viscosity and conventional two-phase programs. ZERO-VISCOSITY MODEL The zero-viscosity model simulates the immiscible displacement of a viscous fluid by a displacing fluid of zero viscosity. The method includes the effects of capillary and gravitational forces, relative permeability and viscosity in the displaced phase, permeability and viscosity in the displaced phase, and arbitrary reservoir heterogeneity. SPEJ P. 325

1986 ◽  
Vol 51 (5) ◽  
pp. 1001-1015 ◽  
Author(s):  
Ivan Fořt ◽  
Vladimír Rogalewicz ◽  
Miroslav Richter

The study describes simulation of the motion of bubbles in gas, dispersed by a mechanical impeller in a turbulent low-viscosity liquid flow. The model employs the Monte Carlo method and it is based both on the knowledge of the mean velocity field of mixed liquid (mean motion) and of the spatial distribution of turbulence intensity ( fluctuating motion) in the investigated system - a cylindrical tank with radial baffles at the wall and with a standard (Rushton) turbine impeller in the vessel axis. Motion of the liquid is then superimposed with that of the bubbles in a still environment (ascending motion). The computation of the simulation includes determination of the spatial distribution of the gas holds-up (volumetric concentrations) in the agitated charge as well as of the total gas hold-up system depending on the impeller size and its frequency of revolutions, on the volumetric gas flow rate and the physical properties of gas and liquid. As model parameters, both liquid velocity field and normal gas bubbles distribution characteristics are considered, assuming that the bubbles in the system do not coalesce.


2020 ◽  
Vol 17 (162) ◽  
pp. 20190792 ◽  
Author(s):  
Candido Diaz ◽  
Daniel Maksuta ◽  
Gaurav Amarpuri ◽  
Akio Tanikawa ◽  
Tadashi Miyashita ◽  
...  

Contaminants decrease adhesive strength by interfering with substrate contact. Spider webs adhering to moths present an ideal model to investigate how natural adhesives overcome contamination because moths' sacrificial layer of scales rubs off on sticky silk, facilitating escape. However, Cyrtarachninae spiders have evolved gluey capture threads that adhere well to moths. Cyrtarachne capture threads contain large glue droplets oversaturated with water, readily flowing but also prone to drying out. Here, we compare the spreading and adhesion of Cyrtarachne akirai glue on intact mothwings, denuded cuticle and glass to the glue of a common orb-weaving spider, Larinioides cornutus, to understand how C. akirai glue overcomes dirty surfaces. Videos show that C. akirai 's glue spreading accelerates along the underlying moth cuticle after the glue seeps beneath the moth scales—not seen on denuded cuticle or hydrophilic glass. Larinioides cornutus glue droplets failed to penetrate the moth scales, their force of adhesion thus limited by the strength of attachment of scales to the cuticle. The large size and low viscosity of C. akirai glue droplets function together to use the three-dimensional topography of the moth's scales against itself via capillary forces. Infrared spectroscopy shows C. akirai glue droplets readily lose free-flowing water. We hypothesize that this loss of water leads to increased viscosity during spreading, increasing cohesive forces during pull-off. This glue's two-phase behaviour shows how natural selection can leverage a defensive specialization of prey against themselves and highlights a new design principle for synthetic adhesives for adhering to troublesome surfaces.


Volume 1 ◽  
2004 ◽  
Author(s):  
Carlos Gamio ◽  
Juan Castro ◽  
Fabian Garcia-Nocetti ◽  
Luis Aguilar ◽  
Leonardo Rivera ◽  
...  

Electrical capacitance tomography (ECT) was used to image various two-phase gas-oil flows in a 3-inch pressurized test loop. ECT is a novel non-invasive technique for imaging mixtures of electrically non-conducting substances. One of its most promising applications is the visualization of gas-oil flows. This work presents a series imaging experiments using a pressure-resistant ECT sensor. Varying the oil and gas flow rates, different flow regimes were established in the test loop. ECT images were obtained for each case and compared with (a) the flow observed through a transparent section in the loop and (b) the prediction of the Taitel-Duckler flow map. The results confirm the suitability of ECT for imaging gas-oil flows.


2017 ◽  
Author(s):  
E. Rogdakis ◽  
P. Bitsikas ◽  
G. Dogkas

In the present work, a three dimensional (3D) Computational Fluid Dynamics (CFD) analysis is applied to a designed small compact regenerator with specific porosity and wire diameter. The regenerator was studied as a part of a Stirling Engine designed in a simple way. The gas temperature along the regenerator followed an approximately linear profile, while the metal temperature showed a small deviation during the engine cycle. The heat transfer coefficient between the gas and the matrix of the regenerator, along with the associate heat transferred were also derived. The heat exchanged in the regenerator is significantly higher to the respective heat in the engine’s heater and cooler. Additionally, the pressure drop and the related energy dissipation are studied. Their variation is largely dependent on both mass flow-rate and working gas velocity. The friction factor coefficient for the designed regenerator is correlated with Reynolds number and an equation of two variables is derived. Finally, the results of the CFD simulation are compared to those produced by a one-dimensional numerical model. These results include gas mass, mass flow-rate and Reynolds number, as well as the heat transferred between the gas and the regenerator matrix. Except for the case of the exchanged heat, the deviation between the two approaches is very small.


2005 ◽  
Vol 128 (1) ◽  
pp. 131-141 ◽  
Author(s):  
Mahmoud A. Ahmed

A theoretical analysis has been developed to predict the critical height and the location of the onset of gas entrainment during discharge from a stratified two-phase region through two oriented-side branches mounted on a vertical wall. In this analysis, a point sink model was first developed, followed by a more accurate three-dimensional finite branch model. The models are based on a new modified criterion for the onset of gas entrainment. The theoretically predicted critical height and the location of the onset of gas entrainment are found to be a function of the mass rate of each branch (Fr1 and Fr2), the distance between the centerlines of the two branches (L∕d), and the inclination angle (θ). The effects of these variables on the predicted critical height and the onset location were investigated. Furthermore, comparison between the theoretically predicted results and the available experimental data was carried out to verify the developed models. The comparison shows that the predicted results are very close to the measured data within a deviation percentage of 12% at Fr1>10. This small deviation percentage reflects a good agreement between the measured and predicted results.


1992 ◽  
Vol 114 (1) ◽  
pp. 80-84 ◽  
Author(s):  
A. Salhi ◽  
C. Rey ◽  
J. M. Rosant

This paper is concerned with axial pressure gradient in single-phase and two-phase flow at low void fraction in a narrow annular space between two concentric cylinders, the inner one rotating. From experimental results, the coupling function (inertial forces/centrifugal forces) is parameterized by Taylor or Rossby numbers for two values of the intercylindrical width (clearance). The results are discussed with regard to different flow regimes and it is shown in particular that transition from the turbulent vorticed regime to the turbulent regime occurs at Ro ≃ 1. The proposed correlation agrees in a satisfactory manner to all the regimes studied in our experiments and in those given in the bibliography. In addition, original tests with a two-phase liquid/gas flow at 5 percent G.O.R. (gas oil ratio), for a finely dispersed gas phase are also reported. These results indicate a similar behavior to single-phase flows, justifying the transposition of the same correlation in the framework of the homogeneous model.


2017 ◽  
Vol 139 (5) ◽  
Author(s):  
Saurabh Bhardwaj ◽  
Amaresh Dalal

In the present study, the interfacial dynamics of displacement of three-dimensional spherical droplet on a rectangular microchannel wall considering wetting effects are studied. The two-phase lattice Boltzmann Shan−Chen model is used to explore the physics. The main focus of this study is to analyze the effect of wettability, low viscosity ratio, and capillary number on the displacement of spherical droplet subjected to gravitational force on flat as well as grooved surface of the channel wall. The hydrophobic and hydrophilic natures of wettabilities on wall surface are considered to study for viscosity ratio, M≤1. The results are presented in the form of temporal evolution of wetted length and wetted area for combined viscosity ratios and wettability scenario. In the present study, it is observed that in dynamic droplet displacement, the viscosity ratio and the capillary number play a significant role. It is found that as the viscosity ratio increases, both the wetted area and the wetted length increase and decrease in the case of hydrophilic and hydrophobic wettable walls, respectively. The groove area on the vertical wall tries to entrap fraction of droplet fluid in case of hydrophilic surface of the vertical wall, whereas in hydrophobic case, droplet moves past the groove without entrapment.


Author(s):  
Saurabh Bhardwaj ◽  
Amaresh Dalal

In the present study, the interfacial dynamics of displacement of three dimensional spherical droplet on a rectangular microchannel wall considering wetting effects are studied. The two-phase lattice Boltzmann Shan-Chen model is used to explore the physics. The main focus of this study is to analyse the effect of wettability, low viscosity ratio and capillary number on the displacement of spherical droplet subjected to gravitational force. The hydrophobic and hydrophilic nature of wettabilities on wall surface are considered to study with capillary number, Ca=0.1, 0.35 and 0.66 and viscosity ratio, M ≤ 1. The results are presented in the form of temporal evolution of wetted length and wetted area for combined viscosity ratios and wettability scenario. In the present study, it is observed that in dynamic droplet displacement, the viscosity ratio and capillary number play a significant role. It is found that as viscosity ratio increases, both the wetted area and the wetted length increase and decrease in the case of hydrophilic and hydrophobic wettable wall respectively.


Author(s):  
Miguel A. Reyes-Gutie´rrez ◽  
Luis R. Rojas-Solo´rzano ◽  
Jose´ Colmenares ◽  
Juan C. Mari´n-Moreno ◽  
Antonio J. Mele´ndez-Rami´rez

This work presents a three-dimensional CFD study of a two-phase flow field in a Gas-Liquid Cylindrical Cyclone (GLCC) using CFX4.3™, a commercial code based on the finite volume method. The numerical analysis was made for air-water mixtures at near atmospheric conditions, while both liquid and gas flow rates were changed. The two-phase flow behavior is modeled using an Eulerian-Eulerian approach, considering both phases as an interpenetrating continuum. This method computed the inter-phase phenomena by including a source term in the momentum equation to consider the drag between the liquid and gas phases. The gas phase is modeled as a bimodal bubble size distribution to allow for the presence of free- and entrapment gas, simultaneously. The results (free surface shape and liquid angular velocity) show a reasonable match with experimental data. The CFD technique here proposed, demonstrates to satisfactorily reproduce angular velocities of the phases and their spatial distribution inside the GLCC. Computed results also proved to be useful in forecasting bubble and droplet trajectories, from which gas carry under (GCU) and liquid carry over (LCO) might be estimated. Nevertheless, moderate differences found between the computed GCU and experimental measurements, suggests that new adjustments may be done to the numerical model to improve its accuracy.


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