scholarly journals PENURUNAN PERSAMAAN DARCY DARI PERSAMAAN NAVIER-STOKES UNTUK RESERVOIR ALIRAN LINIER DAN RADIAL

PETRO ◽  
2019 ◽  
Vol 8 (2) ◽  
pp. 65
Author(s):  
Listiana Satiawati ◽  
Prayang Sunni Yulia

<p><em>Calculation of hydrocarbon flow in the form of oil or gas in Petroleum Engineering is used the Darcy equation. Deriving the Navier Stokes equation produces a general equation that cannot be used for special conditions, for example linear or radial flow because the formulation is different. In this paper, the Darcy equation obtained through experimental evidence is derived from the Navier Stokes equation with several assumptions and simplifications . The calculation in this paper uses a numerical solution, which uses Fortran language, as one approach. Then by using field data, the Darcy equation is used in calculating the flow rate and the velocity of linear fluid in the reservoir. And also the calculation of the pressure from the well to the outermost point of the reservoir with radial fluid flow, so that the pressure gradient data can be obtained from the well to the outermost point of the reservoir.</em><em></em></p>

1973 ◽  
Vol 13 (02) ◽  
pp. 69-74 ◽  
Author(s):  
Graham H. Neale ◽  
Walter K. Nader

Abstract Using the creeping Navier Stokes equation within a spherical cavity and the Darcy equation in the surrounding homogeneous and isotropic porous medium, the flow field in the entire system is evaluated. Applying this result to a representative generalizing model of a uniformly vuggy, homogeneous and isotropic porous medium, an engineering estimation of the interdependence of the matrix permeability km, the vug porosity permeability km, the vug porositytotal volume of vug space 0v = ----------------------------total volume of sample and the system permeability ks of the vuggy porous medium is derived. This interdependence can be expressed by the formula: Introduction The objective of this study is the derivation of an engineering formula that shows the interdependence of matrix permeability, km, vug porosity, 0 v, and system permeability, ks, of a uniformly vuggy porous medium. In the first section, with the above porous medium. In the first section, with the above goal in mind and to satisfy more general interests, we shall study and predict the flow field within a single cavity bounded by a sphere, of radius R, and in the surrounding homogeneous and isotropic porous medium. In the second section, we shall porous medium. In the second section, we shall suggest as a generalizing model of a uniformly vuggy, homogeneous and isotropic porous medium a regular cubic array of monosized spherical cavities. Applying the formula for the pressure field near a single spherical cavity, we shall then develop the sought engineering formula. To describe the creeping flow of the incompressible liquid of viscosity, in the spherical cavity, we shall employ the creeping Navier Stokes equation, .............................(1) The Darcy equation, ,...........................(2) will be used to describe the flow of this liquid in the porous medium of permeability k that fills the space outside the cavity. p designates the liquid pressure referred to datum, denotes the flow pressure referred to datum, denotes the flow vector, and * is used to indicate macroscopically averaged quantities pertaining specifically to a porous medium. porous medium. In hydrodynamics, one generally requests continuity of the pressure, of the flow vector, and of the shear tensor throughout the fundamental domain of the problem - in particular, along the boundary surfaces, which separate subdomains. When applying these principles to this problem, one would impose at the spherical boundary that separates the cavity from the porous medium:continuity of the pressure,continuity of the component of u that is orthogonal to the surface,continuity of the other component of u that is tangential to the surface,continuity of the shear component tangential to the surface. Arguments of this nature have lead to the suggestion of a generalization of the Darcy equation, namely, the Brinkman equation, ...............(3) However, both the necessity and the validity of this generalization have been challenged; indeed, it has been shown that a mathematically consistent solution of our problem may be obtained, using Eqs. 1 and 2 within the respective subdomains, provided one abandons the request for continuity of the shear at the wall of the cavity (compare Boundary Condition d above).** SPEJ P. 69


Author(s):  
Fuzhi Tian ◽  
Junfeng Zhang ◽  
Daniel Y. Kwok

Electrokinetic phenomena play an important role in microfluidic transport behavior. Review of literature suggests that surface energetic can also be an important factor, but rarely explored. Typically, surface energetic is taken into account by consideration as an arbitrarily selected slip boundary condition in the modified Navier-Stokes equation. In this paper, instead of selecting this arbitrary slip condition, we examine how solid-liquid energy parameters influence the transport of microfluidics in terms of streaming potential. The simultaneous effects of surface energetics and electrokinetics will be conducted by means of a mean-field free energy lattice boltzmann approach recently proposed. Rather than using the conventional Navier-Stokes equation with a slip condition, the description solid-liquid energetic is manifested by the more physical energy parameters in the mean-field description of the method. As a result, the magnitude of liquid slip can be related directly to the solid-liquid interfacial slip. These results will be employed in conjunction with the description of electrokinetic transport phenomena for streaming potential. The variation of streaming potential as a function of the energy parameters (solid-liquid interaction) is clearly demonstrated. In pressure-driven liquid microfluidics, the flow rate may be decreased due to the counter-effect between the electrokinetic and slip.


Author(s):  
Rami Ahmad El-Nabulsi

AbstractA new fractional Navier–Stokes equation is constructed based on the notion of fractional velocity recently introduced in the literature. Its implications in fluid mechanics were discussed. In particular, the Couette and the Poiseuille flows and some insights of fluid flow in microfilaments were addressed accordingly.


Author(s):  
А.В. ГУКАСЯН ◽  
Д.А. ШИЛЬКО ◽  
В.С. КОСАЧЕВ

Решением уравнения Навье–Стокса в задачах Куэтта–Пуазейля были определены границы, в рамках которых описан процесс отжима прессового масла с помощью геометрических и скоростных параметров витков шнека. Вычисления производились для материала с высокой вязкостью, имеющего характеристики эффективной вязкости неньютоновской реологии. С использованием балансовых соотношений потоков удалось спрогнозировать работу маслоотжимных агрегатов в режиме форпрессования и экспеллера. В результате выведена модель отжима растительных масел на основе гидродинамики слоистого течения масличного материала в маслоотжимных агрегатах с учетом распределения потока и гидростатического давления в каналах витков шнека. Использование модели двумерного слоистого течения на основе решения задачи Куэтта–Пуазейля базируется на уравнении Навье–Стокса для установившегося режима. Результаты моделирования основаны на технологических параметрах мезги, поступающей на прессование, начальной масличности подсолнечной мезги и начальном расходе, равном 380 кг/ч, который определяется согласно пропускной способности как аналитическое решение этой задачи. Верхняя граница применимости модели слоистого течения масличного материала определяется соотношением геометрии витка шнека с минимальной пропускной способностью 154 кг/ч и содержанием масла в этом материале в диапазоне от 0 до 0,5 кг на 1 кг масличного материала. Нижняя граница применимости этой модели определяется идеализированным случаем экструдирования мезги по каналам шнека при отсутствии отжима. Зависимости изменения давления от расхода мезги, получаемые на основе слоистой модели, позволяют надежно интерполировать распределение давления по виткам шнека в процессе отжима масличного материала. На практике достигнута остаточная масличность жмыха 10% при производительности 200 кг/ч, что дает хорошее совпадение с полученными расчетными значениями. By solving the Navier–Stokes equation in the Couette–Poiseuille problems, the boundaries were determined, within which the process of pressing oil is described using the geometric and speed parameters of the auger turns. The calculations were performed for a high viscosity material having non-Newtonian rheology effective viscosity characteristics. Using the balance flow ratios, it was possible to predict the operation of the oil-pumping units in the pre-pressing and expeller mode. As a result, a model of vegetable oil extraction is derived based on the hydrodynamics of the layered flow of oilseed material in oil-pressing units, taking into account the flow distribution and hydrostatic pressure in the channels of the auger turns. The use of a two-dimensional layered flow model based on the solution of the Couette–Poiseuille problem is based on the Navier–Stokes equation for the steady-state regime. The simulation results are based on the technological parameters of the pulp entering the pressing – the initial oil content of the sunflower pulp and the initial flow rate of 380 kg/h, which is determined according to the throughput as an analytical solution to this problem. The upper limit of the applicability of the model of layered flow of oil-bearing material is determined by the ratio of the geometry of the auger turn with a minimum throughput of 154 kg/h and the oil content in this material in the range from 0 to 0,5 kgper 1 kgof oil-bearing material. The lower limit of the applicability of this model is determined by the idealized case of extrusion of pulp through the auger channels in the absence of pressing. The dependences of the pressure change on the pulp flow rate, obtained on the basis of the layered model, allow us to reliably interpolate the pressure distribution along the auger turns during the pressing of oilseed material. The residual oil content of the oilcake is about 10% at a capacity of 200 kg/h, which gives a good match with the calculated values.


Author(s):  
S. H. Hong ◽  
S. I. Son ◽  
K. W. Kim

In order to maintain the accurate and precise movement of the actuator of the hydraulic systems, it is necessary to guarantee smooth function of the fluid flow control valves. Concerning hydraulic valves, the spool type directional control valve has particular lock problem. The hydraulic lock occurs when uneven pressure distribution surrounding the spool in the clearance between spool and sleeve causes the spool to move sideways out of its centered position. And the contact between spool and sleeve causes to increase friction and eventually, the spool is blocked inside the sleeve. To reduce the possibility of hydraulic lock, peripheral grooves balancing uneven pressure distribution in the radial clearance is commonly applied to spool. Reynolds equation is commonly used to investigate the lubrication characteristics of the spool valve. However, some of assumptions used in Reynolds equation are not valid when cavitation occurs or fluid inertia is significant in spool valve. So, the study on the applicability and precision of Reynolds equation for spool valve analysis is needed. In this study, the differences between the results from Navier-Stokes equation and Reynolds equation are compared when the cavitation is considered. Frictional forces, lateral forces and leakage flow rate with various aspect ratio of groove are calculated. Besides, when the number of groove is increased, the forces and leakage flow rate are compared. Based on the comparison the applicability of Reynolds equation in calculating the spool valve is also discussed.


2017 ◽  
Vol 143 (6) ◽  
pp. 04017026 ◽  
Author(s):  
Junke Guo ◽  
Haoyin Shan ◽  
Zhaoding Xie ◽  
Chen Li ◽  
Haijue Xu ◽  
...  

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