Dynamic Simulation of Gas-Liquid Homogeneous Flow in Natural Gas Pipeline Using Two-Fluid Conservation Equations

Author(s):  
Mohammad Abbaspour ◽  
Kirby S. Chapman ◽  
Larry A. Glasgow ◽  
Zhongquan C. Zheng

Homogeneous two-phase flows are frequently encountered in a variety processes in the petroleum and gas industries. In natural gas pipelines, liquid condensation occurs due to the thermodynamic and hydrodynamic imperatives. During horizontal, concurrent gas-liquid flow in pipes, a variety of flow patterns can exist. Each pattern results from the particular manner by which the liquid and gas distribute in the pipe. The objective of this study is to simulate the non-isothermal, one-dimensional, transient homogenous two-phase flow gas pipeline system using two-fluid conservation equations. The modified Peng-Robinson equation of state is used to calculate the vapor-liquid equilibrium in multi-component natural gas to find the vapor and liquid compressibility factors. Mass transfer between the gas and the liquid phases is treated rigorously through flash calculation, making the algorithm capable of handling retrograde condensation. The liquid droplets are assumed to be spheres of uniform size, evenly dispersed throughout the gas phase. The method of solution is the fully implicit finite difference method. This method is stable for gas pipeline simulations when using a large time step and therefore minimizes the computation time. The algorithm used to solve the nonlinear finite-difference thermo-fluid equations for two phase flow through a pipe is based on the Newton-Raphson method. The results show that the liquid condensate holdup is a strong function of temperature, pressure, mass flow rate, and mixture composition. Also, the fully implicit method has advantages, such as the guaranteed stability for large time step, which is very useful for simulating long-term transients in natural gas pipeline systems.

2013 ◽  
Vol 2013 ◽  
pp. 1-7 ◽  
Author(s):  
Wenwen Zhong ◽  
Changpin Li ◽  
Jisheng Kou

Numerical simulation of two-phase flow in fractured porous media is an important topic in the subsurface flow, environmental problems, and petroleum reservoir engineering. The conventional model does not work well in many cases since it lacks the memory property of fracture media. In this paper, we develop a new numerical formulation with fractional time derivative for two-phase flow in fractured porous media. In the proposed formulation, the different fractional time derivatives are applied to fracture and matrix regions since they have different memory properties. We further develop a two-level time discrete method, which uses a large time step for the pressure and a small time step size for the saturation. The pressure equation is solved implicitly in each large time step, while the saturation is updated by an explicit fractional time scheme in each time substep. Finally, the numerical tests are carried out to demonstrate the effectiveness of the proposed numerical model.


2011 ◽  
Vol 356-360 ◽  
pp. 875-880
Author(s):  
Rong Ge Xiao ◽  
Bing Qian Wei ◽  
Gang Chen

Flow characteristics of horizontal two-phase gas-liquid stratified flows in condensate natural gas pipeline are studied through both air-water and air- natural gas condensate experiments on the large-scale multiphase experimental loop. Based on measurement and observation of flow pattern, “apparent rough surface” (ARS) model is selected to calculate frictional pressure gradient with gas-liquid momentum balance equations. The predictions of the models are compared with the data measured in the experiment. Some results of pressure gradient are obtained, so ARS interfacial shape is recommended in horizontal two-phase gas-liquid flows with low liquid loading.


2017 ◽  
Vol 44 ◽  
pp. 124-142 ◽  
Author(s):  
Marin Prebeg ◽  
Tore Flåtten ◽  
Bernhard Müller

2014 ◽  
Vol 884-885 ◽  
pp. 242-246
Author(s):  
Wei Qiang Wang ◽  
Kai Feng Fan ◽  
Yu Fei Wan ◽  
Ming Wu ◽  
Le Yang

Intensive study on flowing properties of two-phase fluid of gas and liquid during pipeline pigging helps to improve the safety operation of rich gas pipeline. Therefore, based on the multiphase fluid transient simulation software, a two-fluid model is employed to study the flowing regulation of gas and liquid in practical operation of natural gas pipeline pigging,especially the change rule of velocity,flow pattern, pressure, liquid holdup ratio, and liquid slug in the passing ball process. The results reveal that three flow patterns appeared in pipeline pigging. They are stratified flow, slug flow and bubble flow. The place where the particular flow pattern appears is related to the terrain. The biggest pressure is found at the entrance, then pressure comes down along the pipeline, and fluctuate according to the fluid amount and terrain; the transient velocity of pig is coherent with the terrain and liquid holdup ratio; small slug flows are easy to gather and form into a longer one. The research can somehow guide to the safety operation of natural gas pipeline pigging.


Author(s):  
Mohammad Abbaspour ◽  
Kirby S. Chapman ◽  
Ali Keshavarz

Natural gas systems are becoming more and more complex as the usage of this energy source increase. Mathematical models are used to design, optimize, and operate increasingly complex natural gas pipeline systems. Researchers continue to develop unsteady mathematical models that focus on the unsteady nature of these systems. Many related design problems, however, could be solved using steady-state modeling. Several investigators have studied the problem of compressible fluid flow through pipelines and have developed various numerical schemes, which include the method of characteristics, finite element methods, and explicit and implicit finite difference methods. The choice partly depends on the individual requirements of the system under investigation. In this work, the fully implicit finite difference method was used to solve the continuity, momentum, energy, and equations of state for flow within a gas pipeline system. The particular solution method described in this paper does not neglect the inertia term in the conservation of momentum equation. It also considered the compressibility factor as a function of temperature and pressure, and the friction factor as a function of the Reynolds number. the fully implicit method representation of the equations offer the advantage of guaranteed stability for a large time step, which is very useful for the gas industry. The results show that the effect of treating the gas in a non-isothermal manner is extremely necessary for pipeline flow calculation accuracies, especially for rapid transient processes. The results indicate that the inertia term plays an important role in the gas flow analysis and cannot be neglected from the calculation.


Author(s):  
Haruo Terasaka ◽  
Sensuke Shimizu ◽  
Minoru Kawahara

An advanced numerical method based on the two-fluid model has been developed. The solution method presented here is an extension of the SIMPLEST scheme, a fully implicit scheme for single-phase flow analysis. It is robust and unconditionally stable, and therefore it enables us to use a very large time step size. This feature is suitable for steady and/or slow transient flow analyses. Furthermore, it enhances numerical stability during rapid transient calculations. By using this method, swirling gas-liquid flow in a steam-water separator of Boiling Water Reactors (BWRs) was calculated and the hydrodynamics characteristics were investigated for optimization.


2020 ◽  
Vol 7 (2) ◽  
pp. 17-26
Author(s):  
Pedro Quintela ◽  
Jean Carlos Pérez Parra ◽  
Lelly Useche Castro ◽  
Miguel Lapo Palacios

The transient flow analysis is fundamental to the simulation of natural gas process, in order to adjust the system to real operative conditions and to obtain the highest level of efficiency, compliance and reliability. The simulation of natural gas pipelines and networks requires mathematical models that describe flow properties. Some models that have been developed year after year based on the laws of fluid mechanics that govern this process, interpreted as a system of equations difficult to solve. This investigation describes the fully implicit finite volume method for natural gas pipeline flow calculation under isothermal conditions and transient regime. The simplification, discretization scheme and implementation equations are approached throughout this paper. The model was subjected to two evaluations: sinusoidal variation of the mass flow and opening-closing valve at the outlet of the pipeline, it is compared with two models: fully implicit finite difference method and method of characteristics. This method proved to be efficient in the simulations of slow and fast transients, coinciding the flow oscillations with the natural frequency of natural gas pipeline.  


1974 ◽  
Vol 14 (04) ◽  
pp. 361-370 ◽  
Author(s):  
F. Sonier ◽  
P. Chaumet

Abstract Because of saturation instabilities, conventional multiphase three-dimensional simulators cannot use large time-step sizes if grid blocks are small. Therefore, to be economical, such models do not use a fine grid near wells, and they are inadequate for accurately describing reservoir phenomena around producing wells. Only radial circular models can be used inexpensively to describe coning behavior. However, they are not always reliable because there usually is no axial symmetry around producing wells. producing wells. We propose a three-dimensional reservoir model capable of simultaneously describing flows at a distance from and around wells in a part of an oil reservoir subject to lateral drive from an aquifer or a gas cap. The model uses an asymmetrical curvilinear grid whose mesh sizes increase with distance from the wells. It is a fully implicit model that can use large time-step sizes. A convergence acceleration device is used for equation solving. The results of this model have been checked against those obtained with a large laboratory model. Wells were in a line pattern and in a staggered one. pattern and in a staggered one Introduction In an oil reservoir subject to lateral drive from an aquifer or a gas cap, no axial symmetry exists around the producing wells. As a result of such production and of lateral drive, the transition zone becomes deformed and, in particular, the gas moves along the top of the layer toward the wells. Pressures (especially if the problem is with imposed Pressures (especially if the problem is with imposed bottom-hole pressures) and coning phenomena near the wells in such transition zones is very difficult to describe with existing numerical reservoir models. The grids and numerical methods usually used for this are not properly adapted to solve the problem. FROM THE STANDPOINT OF PATTERN A circular radial coning model is not representative. Also, a conventional three-dimensional model with parallelepipedic grids has the disadvantage of using large blocks corresponding to producing wells (this will be called well blocks in the remainder of the paper). The average pressure and saturation values are quite different from the actual well values since it is in the vicinity of these wells that pressures and saturation vary the most in space. One way of solving this would be to adopt a highly irregular grid with small cells in the vicinity of the wells. The cost of simulation with such a system would be very high because of the excessive number of grids, including some perfectly useless ones in distant zones with low gradients. FROM THE NUMERICAL STANDPOINT From the numerical standpoint a conventional model of the type described above using the finite-difference technique and "implicit-pressure explicit-saturation" concept requires time steps that become smaller as mesh size decreases. This is an additional reason for trying to avoid any tightening up of the grid. As a result, while maintaining a relatively loose grid, some authors have tried to find special processing methods for the individual points made up by the wells:arbitrarily reducing permeability in the well blocks to adjust bottom-hole pressures,approximating pressures by polynomial functions of a high order pressures by polynomial functions of a high order in the vicinity of wells and of a lower order elsewhere,estimating bottom-hole pressure by extrapolation (based on Darcy's law written in radial form and integrated for steady-state conditions) from grid blocks adjacent to the well block, andinserting a radial-circular coning model in well blocks. (This last solution is not a good one because of the unsatisfied symmetry conditions and assumptions on the linking of both models.) We propose here a three-dimensional reservoir model capable of simultaneously describing flows at a distance and in the vicinity of wells. This model is discretized according to a curvilinear grid in the plane of the layer, enabling small meshes to be formed around the well and large meshes in zones farther away without creating any difficulties of linking between meshes. SPEJ P. 361


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