An Experimental and Numerical Investigation of Crossflow Effects in Two-Phase Displacements

SPE Journal ◽  
2006 ◽  
Vol 11 (02) ◽  
pp. 216-226 ◽  
Author(s):  
Yildiray Cinar ◽  
Kristian Jessen ◽  
Roman Berenblyum ◽  
Ruben Juanes ◽  
Franklin M. Orr

Summary In this paper, we present flow visualization experiments and numerical simulations that demonstrate the combined effects of viscous and capillary forces and gravity segregation on crossflow that occurs in two-phase displacements in layered porous media. We report results of a series of immiscible flooding experiments in 2D, two-layered glass bead models. Favorable mobility-ratio imbibition and unfavorable mobility-ratio drainage experiments were performed. We used pre-equilibrated immiscible phases from a ternary isooctane/isopropanol/water system, which allowed control of the interfacial tension (IFT) by varying the isopropanol concentration. Experiments were performed for a wide range of capillary and gravity numbers. The experimental results illustrate the transitions from flow dominated by capillary pressure at high IFT to flow dominated by gravity and viscous forces at low IFT. The experiments also illustrate the complex interplay of capillary, gravity, and viscous forces that controls crossflow. The experimental results confirm that the transition ranges of scaling groups suggested by Zhou et al. (1994) are appropriate/valid. We report also results of simulations of the displacement experiments by two different numerical techniques: finite-difference and streamline methods. The numerical simulation results agree well with experimental observations when gravity and viscous forces were most important. For capillary-dominated flows, the simulation results are in reasonable agreement with experimental observations. Introduction Streamline methods are very efficient numerical techniques for field-scale reservoir simulation, but they are not without limitations. They treat flow along each streamline as independent of adjacent streamlines and therefore do not typically represent crossflow in the simulations. If users of streamline methods are to interpret simulation results reliably, they will need to assess whether any of the mechanisms not modeled in the simulations ar. important enough to limit the accuracy of the simulations appreciably. Transfer of fluid in the direction transverse to streamlines can result from diffusion and dispersion, crossflow caused by viscous and capillary forces, and gravity segregation. The scaling of diffusion and dispersion has been investigated in a number of previous studies. If the injected gas is miscible or partially miscible with the oil, diffusion and dispersion mechanisms may play a significant role in the displacement (Mohanty and Johnson 1993; Fayers and Lee 1994; Tchelepi 1994; Jiang and Butler 1994; Burger and Mohanty 1997). In particular, Burger and Mohanty (1997) showed that diffusion through the oil phase can limit mass transfer from oil residing in low-permeability regions. Similar arguments can also apply to other mechanisms of crossflow: viscous and capillary crossflow as well as gravity segregation (Fayers and Lee 1994.Burger and Mohanty 1997; Zapata and Lake 1981; Zhou et al. 1994).

Author(s):  
Yasuo Koizumi ◽  
Ryou Enari ◽  
Hiroyasu Ohtake

Behavior of a falling liquid film of highly viscous fluid in the counter-current flow condition was examined. In experiments, water and silicon oils of 500, 1000 and 3000 cSt were used as the liquid phase and air was adopted as the gas phase. A test section vertically oriented was a circular pipe of 30 mm in inner diameter and 5.4 m in length. Flooding velocities of the air-water system were well correlated with traditional correlations such as the Wallis correlation and the Kamei correlation. However, the flooding velocities of silicon films were greatly lower than the expected. When the effect of the viscosity was incorporated into the Wallis correlation, it predicted the experimental results well. The flooding in the air-silicon system was initiated by sudden growth of a wave on the film as in the air-water system although the film Reynolds number of the falling silicon film was considerably low; 0.02 ∼ 4. A considerable amount of droplets were detected a long time before the initiation of flooding in the air–silicon oil experiments as well as in the air–water experiments. The correlations tested for the onset condition of entrainment gave much higher gas velocities than the measured. Predicted velocities were rather close to the flooding velocities. The falling film thickness was predicted well by applying the universal velocity profile to the film flow over a wide range of a film Reynolds number; ranging from a water film to a 3000 cSt silicon oil film.


1974 ◽  
Vol 14 (06) ◽  
pp. 619-632 ◽  
Author(s):  
Allan Spivak

Spivak, Allan,* Member SPE-AIME, Chevron Oil Field Research Co., La Habra, Calif. Abstract This paper describes a study of gravity segregation (underrun or override of injected fluids) in two-phase, secondary recovery displacement processes. Reservoir simulation was used to investigate the factors that influence gravity segregation and the magnitude of gravity effects for both water floods and gas floods. The degree of segregation for a given set of conditions was determined bycomparing the results of two-dimensional cross-sectional with one-dimensional horizontal calculations, andcomparing the results of three-dimensional vs two-dimensional a real calculations. The degree of segregation is quantitatively described by the dimensionless number E defined as (Rbt)no gravity -(Rbt)gravity E =, (Rbt)no gravity where Rbt is recovery at breakthrough. Gravity segregation effects in two-phase displacement processes were found to increase withincreasing processes were found to increase withincreasing permeability (either horizontal or vertical),permeability (either horizontal or vertical),increasing density difference,increasing mobility ratio,decreasing production rates. anddecreasing level of viscosity for a fixed viscosity ratio. A series of calculations was made in which the parameters that affect gravity segregation were varied. The effect of each parameter on the degree of gravity segregation was observed. The effect of both stratified and random heterogeneity was also studied. A correlation between the degree of gravity segregation and the dimensionless groups G = 0.00633 and M = mobility ratio was established. This correlation is based on the results of the simulator calculations and a detailed analysis of the equations for three-dimensional, two-phase. immiscible, incompressible flow. The correlation can be used to determine qualitatively whether gravity segregation will be a significant factor in a given flooding process. It can also be used to determine whether the assumption of vertical equilibrium is valid in the simulation by a two-dimensional a real simulation model of reservoirs where fluid saturations vary significantly in the vertical direction. Introduction For many years, gravity segregation in reservoir processes was not accounted for because it could processes was not accounted for because it could not be adequately handled in reservoir engineering calculations. The advent of reservoir simulation provided the capability to handle gravity, and it provided the capability to handle gravity, and it became apparent that gravity effects could significantly affect reservoir performance. This paper describes a study in which a three-dimensional paper describes a study in which a three-dimensional (3-D), two-phase, incompressible simulator was used to look at gravity effects in displacement processes. The objectives of this study wereto processes. The objectives of this study wereto determine what factors influence gravity segregation and in what way;to look at the magnitude of gravity segregation effects;to compare reservoir performance calculations with and without gravity performance calculations with and without gravity effects. PREVIOUS WORK ON GRAVITY PREVIOUS WORK ON GRAVITY SEGREGATION IN DISPLACEMENT PROCESSES Craig et al. did experimental work to study the effects of gravity segregation during water, gas, and solvent flooding. As a result of their studies, they concluded that segregation of fluids due to gravity effects could result in oil recoveries at breakthrough as low as 20 percent of those otherwise expected. They also concluded that performance may in some cases be influenced to a greater degree by heterogeneity than by gravity effects. They were not able to directly compare performance under a given set of conditions with and without gravity. SPEJ p. 619


Author(s):  
Shun Zhong ◽  
Jingyuan Tan ◽  
Zhicheng Cui ◽  
Tanghong Xu ◽  
Liqing Li

Purpose. Impacts appear in a wide range of mechanical systems. To study the dynamical behavior introduced by impact in practical way, a single-degree-of-freedom impact oscillator rig is designed. Originality. A simple piece-wise linear system with symmetrical flexible constraints is designed and manufactured to carry out a wide range of experimental dynamic analysis and ultimately to validate piece-wise models. The new design choice is based on the following criteria: accuracy in representing the mathematical model, manufacturing simplicity, flexibility in terms of parameter changes and cost effectiveness as well avoidance of the delay introduced by the structure. Meanwhile, the new design provides the possibility of the applications of the complex control algorithms. Design/methodology/approach. The design process is described in detail. The initial experimental results of the rig as well as numerical simulation results are given. In this rig, the mass driven force is generated by electromagnet, which can be adjusted and control easily. Also, most of the physical parameters can be varied in a certain range to enhance flexibility of the system allowing to observe subtle phenomena. Findings. Compared with the simulation results, the designed rig is proved to be validated. Then, the initial experimental results demonstrate potentials of this rig to study fundamental impact phenomena, which have been observed in various engineering systems. They also indicate that this rig can be a good platform for investigating nonlinear control methods.


2021 ◽  
Vol 16 ◽  
pp. 43-48
Author(s):  
Vladimir V. Chudanov ◽  
Anna E. Aksenova ◽  
Alexey A. Leonov ◽  
Artem A. Makarevich

The article presents the direct simulation results of two-phase mixtures with phase transition shock tube in dodecane, two-phase expansion tube in water and 2D heat and mass transfer in a vertical channel with sodium. For two versions of the code for CPU and GPU calculations possess efficient scaling in the wide range of grid sizes. Scaling for CPU version of the code is close to ideal and does not depend from the grid size and the number of nodes. Efficiency of scaling for GPU version of the code is limited by the size of calculation region per 1 node and could be varied for different models of processor. The value of scaling factor was demonstrated.


Electronics ◽  
2019 ◽  
Vol 8 (12) ◽  
pp. 1460 ◽  
Author(s):  
Emad Samadaei ◽  
Mohammad Kaviani ◽  
Mina Iranian ◽  
Edris Pouresmaeil

There has been an active interest in the evolution of newer multilevel inverter topologies in which the highest operation of DC sources become an important subject. In the paper, a new structure module presented a seventeen levels asymmetrical multilevel inverter by using two unequal DC sources (with the ratio 3:1). The configuration was focused on creating virtual DC links by two chargeable capacitors. The module had a simple inherent charging for capacitors without any additional circuit. The proposed multilevel inverter could produce higher voltage levels by a lower number of components; therefore, it is suitable for a wide range of applications. Also, the cascade connection of the module led to a modular topology with more voltage levels at higher voltages. The capability of the inherent negative voltage was involved. The simulation results obtained in MATLAB/Simulink, as well as the experimental results, verified the proposed topology.


Author(s):  
Aneet Singh ◽  
Shireesh Kumar Rai

This paper presents six different meminductor emulator circuits based on operational amplifiers. Five circuits of meminductor emulators have been proposed using two operational amplifiers, one memristor, three resistors and one capacitor, whereas the sixth circuit uses two operational amplifiers, two memristors, one resistor and two capacitors. All circuits of the proposed meminductor emulators are very simple over most of the realizations of meminductor emulators in the literature. The behaviors of meminductor emulators are satisfactory over a wide range of frequencies. The proposed configurations of meminductor emulators have been simulated by the LTspice tool. The SPICE models of both operational amplifier (AD711) and memristor have been used for simulation. The workability of the proposed meminductor emulators has also been verified using the basic and well-known structure of operational amplifier. In addition, the pinched hysteresis loop obtained by the simulation results of meminductor emulator has been achieved by the experimental results as well. Chaotic oscillator has been designed using the proposed meminductor emulator to prove the worthiness of the design.


Author(s):  
Priya Deepa ◽  
K. Saravanan

Fluidized beds are extensively used in petrochemical, chemical process industries, pharmaceutical, food and biotechnology industries. They are preferred to process materials with wide range of particle size distribution and offer even temperature distribution and excellent heat and mass transfer. To improve the quality of fluidized bed, mechanical stirring can be employed along with aeration. Hence, an attempt was made to study the hydrodynamics of stirred fluidized bed using air-water system. The characteristics of the fluidized bed can be well understood by studying its hydrodynamics. Pressure drop is one of the vital factor which affects the performance of fluidized bed. Hence, the effects of gas velocity and stirrer speed on pressure drop and power were studied for both stirred and unstirred bed conditions. It was observed that pressure drop and power increases with increase in gas velocity and stirrer speed. Also, the pressure drop and power is low for the stirred bed condition than the unstirred bed condition.


TAPPI Journal ◽  
2018 ◽  
Vol 17 (04) ◽  
pp. 231-240
Author(s):  
Douglas Coffin ◽  
Joel Panek

A transverse shear strain was utilized to characterize the severity of creasing for a wide range of tooling configurations. An analytic expression of transverse shear strain, which accounts for tooling geometry, correlated well with relative crease strength and springback as determined from 90° fold tests. The experimental results show a minimum strain (elastic limit) that needs to be exceeded for the relative crease strength to be reduced. The theory predicts a maximum achievable transverse shear strain, which is further limited if the tooling clearance is negative. The elastic limit and maximum strain thus describe the range of interest for effective creasing. In this range, cross direction (CD)-creased samples were more sensitive to creasing than machine direction (MD)-creased samples, but the differences were reduced as the shear strain approached the maximum. The presented development provides the foundation for a quantitative engineering approach to creasing and folding operations.


2021 ◽  
pp. 004051752098812
Author(s):  
Xixi Qian ◽  
Yuanying Shen ◽  
Qiaoli Cao ◽  
Jun Ruan ◽  
Chongwen Yu

A simulation describing the fiber movement during the condensation was conducted, and the effect of the condensation in the carding machine was studied. The simulation results showed that the condensation has the blending and the evening effect on the condensed sliver, which can be explained by the fiber rearrangement. Moreover, the increasing web width and the decreasing condensing length can result in a more uniform sliver. Further, the evening effect of the web width on the web was verified by experiments. The simulation results were in general agreement with the experimental results.


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