Slugging in multiphase flow as a mixed initial-boundary value problem for a
quasilinear hyperbolic system
Florent Di Meglio, Glenn-Ole Kaasa, Nicolas Petit, Vidar Alstad
Abstract— This paper studies the multiphasis slugging flow
phenomenon occurring in oil wells and flow lines. The main con-
tribution is a low-dimensional distributed parameters model,
comprising the gas mass fraction, the pressure, and gas velocity
as states. Along with appropriate boundary conditions, on the
one-dimensional space domain, it constitutes a well-posed mixed
initial-boundary value problem for a quasilinear hyperbolic
system. Numerical simulation results obtained with a presented
characteristics method solver stress the validity of the approach
and the fair representativeness of the model. In particular,
the period of simulated oscillations and their overall shape
is in accordance with reference results from the literature.
Controllability and observability open problems are formulated
for future works.
I. Introduction
In this article, we propose a model of the slugging phe-
nomenon taking the form of a low-dimensional hyperbolic
system of conservation laws. Slugging is a two-phase flow
regime occurring during the process of oil production. In cer-
tain circumstances, the inhomogeneous repartition of gas and
liquid into the long transport pipes leads to this oscillating
flow pattern, which is detrimental to the overall production
and is at the source of severe issues concerning safety of
operations. The physical description of this phenomenon is
as follows. Elongated bubbles of gas, separated by “slugs”
travel from one end of a pipe to the other. This results in
large pressure oscillations and an intermittent flow. A main
negative effect is that the average (over time) production of
oil is decreased compared to steady flow regimes.
Modeling this phenomenon is a difficult task, because its
origins are not completely understood yet. Early models have
focused on the transitions between flow patterns [31] or the
prediction of the flow characteristics (e.g. average liquid
hold-up, pressure drop...) [1]. More recently, distributed
parameters models have been developed in commercial sim-
ulation softwares, such as OLGA
TM
or TACITE
TM
. They are
based on nonlinear Partial Differential Equations (PDEs),
and reproduce with a good accuracy the dynamical behavior
of slugging wells. However, even if they rely on well-
documented physics and modeling assumptions, their “black-
box” nature (for the end-user) and the high dimensionality
F. Di Meglio (corresponding author) is a PhD candidate in Mathematics
and Control at MINES ParisTech, 60, Bd St-Michel, 75272 Paris, Cedex
06, France
G.O. Kaasa is Research Engineer at StatoilHydro ASA, Research Center
Porsgrunn, Heroya Forksningspark 3908 Porsgrunn, Norway
N. Petit is Professor at MINES ParisTech, 60, Bd St-Michel, 75272 Paris,
Cedex 06, France
V. Alstad is Research Engineer at Statoil ASA, Research Center Pors-
grunn, Heroya Forksningspark 3908 Porsgrunn, Norway
of the state equations make these softwares hardly usable for
mathematical analysis, let alone control design.
Conversely, reduced models have been developed [8], [24],
[30]. They are based on nonlinear Ordinary Differential
Equations (ODEs) and capture the main features of the
slugging oscillations. Their relative simplicity makes them
suitable for control (and observer) design, at the expense of
sometimes tedious tuning procedures aimed at reproducing
field data (see, e.g., [10]). These models rely on restrictive
modeling assumptions which, in turn, might seem inappropri-
ate from a physical modeling view-point. The Jansen model
[24] is designed specifically for gas-lifted wells, whereas
the Storkaas model [30] corresponds to risers with a low-
point. The model proposed in [8] assumes the existence of
an irregularity in the pipe geometry at the birth of instability.
In this article, we propose a low-dimensional model which
is minimal, in the sense that no assumptions are made on
the geometry or setup of the system, and that it reproduces
with a fair accuracy observed behaviors. Following many
other modeling works (e.g. [1], [3], [12], [16]), the drift-flux
approach is used. This implies that the momentum equations
for the gas and the liquid are combined into a single one, and
that an affine slip relation with constant parameters relates
the velocities of the two phases. Importantly, this is the only
empirical relation used in the model. The approach is very
similar to the density wave model of Sin` egre [28], which
was first described and illustrated by OLGA simulations in
[22]. In [28], a distributed parameters model was provided,
along with a thorough stability analysis, describing the
phenomenon. Yet, the analysis relies on simplifications which
preserve the stability properties, but may hurt the physical
interpretation
1
.
The main contribution of this article is a low-dimensional
model of slugging phenomenon taking the form of a hy-
perbolic system of conservation laws, with a one-sided
boundary actuation. The advantages of such a formulation
are two-fold. First, it is consistent with recent mathematical
tools of analysis of PDE control systems, e.g. results that
guarantee well-posedness of the problem. Similarly, theoret-
ical controllability and observability results might be used.
Such problems of well-posedness and boundary control of
hyperbolic systems have been widely studied [6], [25], [26].
Second, the method of characteristics (see [2], [5], [27] for
application to hyperbolic control systems) can be used to
numerically solve the equations, which reduces the compu-
1
In particular, the gas velocity is assumed constant in time and space,
which is not realistic in practice. No such assumption is made here.
2011 American Control Conference
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