scholarly journals A New Lumped Parameter Model for Natural Gas Pipelines in State Space

Energies ◽  
2018 ◽  
Vol 11 (8) ◽  
pp. 1971 ◽  
Author(s):  
Kai Wen ◽  
Zijie Xia ◽  
Weichao Yu ◽  
Jing Gong

Many algorithms and numerical methods, such as implicit and explicit finite differences and the method of characteristics, have been applied for transient flow in gas pipelines. From a computational point of view, the state space model is an effective method for solving complex transient problems in pipelines. However, the impulse output of the existing models is not the actual behavior of the pipeline. In this paper, a new lumped parameter model is proposed to describe the inertial nature of pipelines with inlet/outlet pressure and flow rate as outer variables in the state space. Starting from the basic mechanistic partial differential equations of the general one-dimensional compressible gas flow dynamics under isothermal conditions, the transfer functions are first acquired as the fundamental work. With Taylor-expansion and a transformation procedure, the inertia state space models are derived with proper simplification. Finally, three examples are used to illustrate the effectiveness of the proposed model. With the model, a real-time automatic scheduling scheme of the natural gas pipeline could be possible in the future.

Author(s):  
M. Behbahani-Nejad ◽  
A. Ghanbarzadeh ◽  
R. Alamian

A transient flow simulation for gas pipelines and networks is proposed. The proposed transient flow simulation is based on the state space equations. The equivalent transfer functions of the nonlinear governing equations are derived for different boundary conditions types. Next, the state space equations are derived from the transfer functions. To verify the accuracy of the proposed simulation, the results obtained are compared with those of the conventional finite difference schemes (such as total variation diminishing algorithms, method of lines, and other finite difference implicit and explicit schemes). The effect of the flow inertia is incorporated in this simulation. The accuracy and computational efficiency of the proposed method are discussed for a single gas pipeline and a sample gas network.


2019 ◽  
Vol 9 (3) ◽  
pp. 481
Author(s):  
Kai Wen ◽  
Jing Gong ◽  
Yan Wu

With the boost of natural gas consumption, an automatic gas pipeline scheduling method is required to replace the dispatchers in decision making. Since the state space model is the fundamental work of modern control theory, it is possible that the classical controller synthesis method can be used for the complicated gas pipeline controller design. In this paper, a cascade control algorithm is proposed based on the state space model that is used for the transient flow simulation of the natural gas pipelines. A linear quadratic regulator is designed following the classical optimal control theory. Finally, the transient process with different control methods shows the effectiveness of the cascade control using information of the entire pipeline. According to the hardware configuration of natural gas pipelines, automatic scheduling process is ready to deploy as one step to the intelligent natural gas pipelines.


1972 ◽  
Vol 5 (12) ◽  
pp. 487-493 ◽  
Author(s):  
A L Dexter

A sub-optimal control scheme is proposed to regulate pressures throughout the Natural Gas Grid. In the scheme, the pressures at certain optimally chosen grid locations are dynamically controlled to achieve good overall regulation throughout the grid. Acknowledging the random nature of the load disturbances, the design of the regulators is based on stochastic control theory. To assess the performance of the scheme, experiments are performed on a lumped-parameter model of the grid system. Results suggest that introduction of the scheme, could substantially improve on the present method of pressure regulation.


2011 ◽  
Vol 2011 ◽  
pp. 1-18 ◽  
Author(s):  
F. S. Q. Alves ◽  
H. C. Yehia ◽  
L. A. C. Pedrosa ◽  
F. R. B. Cruz ◽  
Laoucine Kerbache

In many real-life queueing systems, the servers are often heterogeneous, namely they work at different rates. This paper provides a simple method to compute tight upper bounds on two important performance measures of single-class heterogeneous multi-server Markovian queueing systems, namely the average number in queue and the average waiting time in queue. This method is based on an expansion of the state space that is followed by an approximate reduction of the state space, only considering the most probable states. In most cases tested, we were able to approximate the actual behavior of the system with smaller errors than those obtained from traditional homogeneous multiserver Markovian queues, as shown by GPSS simulations. In addition, we have correlated the quality of the approximation with the degree of heterogeneity of the system, which was evaluated using its Gini index. Finally, we have shown that the bounds are robust and still useful, even considering quite different allocation strategies. A large number of simulation results show the accuracy of the proposed method that is better than that of classical homogeneous multiserver Markovian formulae in many situations.


1981 ◽  
Vol 21 (05) ◽  
pp. 521-526
Author(s):  
Richard S. Collier ◽  
Ellis A. Monash ◽  
Paul F. Hultquist

Abstract A mathematical model is developed and tested for the production of natural gas with water encroachment and gas entrapment. The model is built on the material and volumetric balance relations, the Schilthuis water drive model, and a gas entrapment mechanism which assumes that the rate of gas entrapment is proportional to the volumetric rate of water influx. This model represents an alternative to the large grid models because of its low computer, maintenance, and manpower costs. Introduction Reservoir simulation can be considered to have started in 1936 when Schilthuis first stated the material balance equation for petroleum reservoirs. This led to various attempts to simulate the reservoir for zero-dimensional through two-dimensional cases, including the use of electrolytic and electrical analogs and the use of simplified equations and simple geometries solved analytically. Numerical methods awaited the development of the digital computer; the landmark paper here, of course, was that of Bruce et al. in 1953. Much research in numerical analysis was stimulated by the attempts to solve the mathematical equations on computers efficiently and accurately. The reservoir model presented here approaches a natural gas reservoir from a different point of view. It is a zero-dimensional model which does not deal with the detailed interior (microscopic) structure of the reservoir. It assumes that the reservoir consists of an isothermal mass of gas at temperature Ti in porous rock surrounded by an infinite aquifer. As gas is withdrawn from the reservoir, the resulting pressure gradient (approximated by the pressure difference) allows water to infiltrate at a rate proportional to the pressure difference (Schilthuis model). As the water infiltrates, it traps gas at a volumetric rate proportional to the volumetric infiltration rate. Although this is a very simple reservoir model, results show that it is quite realistic. It can be useful in modeling pressure/production relationships for policy and planning purposes. Of course, it does not model the detailed internal behavior of the reservoir needed for certain engineering purposes. Lumped Parameter Model of Natural Gas Reservoir By a lumped parameter model we mean one in which the distributed variables, which normally vary with position, are replaced by a single, effective quantity. For example, in electronic circuit theory, it is usually sufficient to consider a point or "lumped" resistance, capacitance, and inductance in place of distributed quantities in a circuit. Likewise in the oil or gas reservoir, for many cases of interest we may replace the pressure and density with average or "lumped" quantities. This gives a zero-dimensional model in that the space dependence of these quantities need not be calculated explicitly. For example, if we consider an ideal gas with uniform pressure, we may relate the pressure p, the volume V, and the total number of moles of gas G by the relation (1) where R is the universal gas constant and Ti is the initial temperature of the reservoir, which is assumed to be isothermal.


2000 ◽  
Vol 123 (1) ◽  
pp. 18-23 ◽  
Author(s):  
Kazuto Seto ◽  
Mingzhang Ren ◽  
Fumio Doi

A lumping method via an inverse modal analysis approach is proposed in this paper for creating a lumped parameter model for a structure with distributed parameters. On the basis of the lumped parameter model, the formulation of an optimal controller in physical state space is presented and, furthermore, the design of a reduced-order controller is described. The method is demonstrated and verified by the vibration and noise control experiments carried out on a clamped plate. Several modes of the plate with high sound radiating efficiencies are well controlled by using three sensors and one actuator, based on a 9 degree-of-freedom (DOF) lumped parameter model of the plate.


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.  


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