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The distillation mechanism in steam displacement of oil

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Title: The distillation mechanism in steam displacement of oil


1
The distillation mechanism in steam displacement
of oil
  • Dan Marchesin and Hans Bruining,

ECMOR X Sept 4-7, 2006
2
An example of all the pathological problems with
conservation laws
  • Elliptic regions (Not discussed here)
  • Non-Lax shocks () and uniqueness
  • Small diffusion is dominating efficiency of
    process

E. Isaacson. D. Marchesin, and B. Plohr ,
Transitional waves for conservation laws, SIAM J.
Math. Anal. 21, 831-866 (1990)
Amsterdam ECMOR X Sept. 4-7, 2006 20 slides
3
Steam injection
Steam injection is commercially applied to
recover viscous oils
Amsterdam ECMOR X Sept. 4-7, 2006 19 slides
4
Volatile oil enhanced steam drive
  • Proposed by Dietz (1979)

Amsterdam ECMOR X Sept. 4-7, 2006 18 slides
5
ES-SAGD (Ian Gates)
Co-inject some volatile oil with steam
Courtesy Claes Palmgren
Amsterdam ECMOR X Sept. 4-7, 2006 17 slides
6
Laboratory tests showing the effect of coinjected
volatile oil
7
Contents
  • Reasons why modeling of this process is complex
  • Formulation including capillary and diffusion
    effects
  • Dodecane, cyclo butane and heptane Bifurcations
    depending on boiling points
  • Importance of diffusion processes
  • Peak wave and effect on recovery

Amsterdam ECMOR X Sept. 4-7, 2006 15 slides
8
MOC models complicated due to saddle to saddle
connection in shocks (not a Lax shock)
Sw,Sg,So0,vov 0
initial
Sw,So,vov 0
Steam
  • Shock velocity
  • Sw(-)
  • Sg(-)
  • Sw()
  • Darcy velocity ()
  • Water balance
  • Oil balance
  • Energy balance
  • Welge shock condition
  • Missing equation?

Bruining, J., Duijn, C.J. van, "Uniqueness
Conditions in a Hyperbolic Model for Oil Recovery
by Steamdrive, Computational Geosciences" No 4,
pp 65-98 (2000), Traveling waves in a finite
condensation rate model for steam injection,
ibid. 2006
9
Simulation gives unrealistic results due to
numerical dispersion
Sw,Sg,So0,vov 0
initial
Sw,So,vov gt0
Steam
Volatile oil bank
Initial composition
Amsterdam ECMOR X Sept. 4-7, 2006 13 slides
10
Motivation of combined analytical and numerical
approach
  • Simulators overemphasize diffusion/ capillary
    diffusion are the solutions realistic?
  • Are we allowed to disregard diffusion all
    together?
  • Does the form of the diffusion e.g. saturation
    dependence affect the global solution even if it
    is small?
  • Existence and uniqueness? We are using empirical
    relations to describe the convection flow
  • Possible bifurcations analysis i.e. solutions
    change behavior if parameters cross critical
    values ().
  • Discovery of new recovery mechanisms

Bruining, J. and Marchesin, D. , Nitrogen and
steam injection in a porous medium with water,
TIPM (March 2006), 62 (3), 251-281
Amsterdam ECMOR X Sept. 4-7, 2006 12 slides
11
Model
  • Injection steam and volatile oil vapor in core
    SwSwc, So1-Swc
  • No dissolution of water in the oleic phase.
  • Volatile oil vapor mixes in all proportions with
    steam. Liquid volatile oil mixes with dead oil.
    Dead oil only occurs in the oleic phase.
  • Viscosities depend on T and the composition vov .
  • No volume effects on mixing
  • Capillary forces and diffusional effects
    incorporated
  • Local thermodynamic equilibrium -gt f c p 2

12
Four conservation laws water, dead oil, volatile
oil, energy
  • ?ov(T) volatile oil concentration in oleic phase
  • ?gv(T) volatile oil concentration in gaseous
    phase
  • uov(T) Darcy velocity volatile oil in oleic phase
  • ugv(T) Darcy velocity volatile oil in gaseous
    phase

13
Formulations of interest
  • Analytical solution without capillary and
    diffusion -gt hyperbolic problem (solution
    discussed here) details in paper submitted to
    Phys. Rev. E
  • Numerical solution with capillary and diffusion
    (see Figs. 1, 2, 3.) details in paper submitted
    to Phys. Rev. E
  • Traveling wave solution in steam
    condensation zone (formulation presented in
    paper)

Bruining, J. and Marchesin, D. , Maximal Oil
Recovery by simultaneous condensation of alkane
and steam, Submitted to Phys Rev E
Amsterdam ECMOR X Sept. 4-7, 2006 9 slides
14
Dodecane coinjected (num. sol.)
15
Cyclo-butane coinjected (num. sol.)
16
Comparison numerical (left) and analytical
solution Medium boiling (heptane) volatile oil
Saturations 0 ?? S?? ? 1., vov fraction of
volatile oil in the oleic phase.
17
Numerical (left) and analytical solution, Medium
boiling volatile oil initially present
Saturations 0 ?? S?? ? 1., vov fraction of
volatile oil in the oleic phase.
Amsterdam ECMOR X Sept. 4-7, 2006 5 slides
18
Medium volatile oil slug injection problem.
Rescaled temperature 0 ?? T ? 1., vov is
fraction of volatile oil in the oleic phase.
Amsterdam ECMOR X Sept. 4-7, 2006 4 slides
19
Blow up of previous plot
Structure of the transition zone consisting of a
3- and a 2-phase part. Rescaled temperature 0
?? T ? 1. Volatile oil peak indicated by vov
between hot steam zone and cold liquid zone .
Amsterdam ECMOR X Sept. 4-7, 2006 3 slides
20
Stability of diffusion bank
First 7 time intervals volatile oil is
coinjected with the steam. Second 7 time
intervals pure steam injection. volatile oil
peak is essentially preserved ensuring high
recovery of oil
Amsterdam ECMOR X Sept. 4-7, 2006 2 slides
21
Conclusions
  • During steam injection with co-injection of
    volatile oil a volatile oil peak is formed
    between the steam zone and the liquid zone
  • The volatile oil peak is a component of a
    traveling wave solution this is a new type of
    wave
  • After turning to pure steam injection the
    volatile oil peak remains more or less unchanged
  • A steady volatile oil peak is capable of reducing
    the residual oil during steam drive and hence
    enhances the oil recovery
  • These conclusions must still be rigorously
    validated by solving the traveling wave problem

Amsterdam ECMOR X Sept. 4-7, 2006 last slide
22
Conclusions
  • Finite volume methods can give erroneous results
    when describing non-Lax shocks
  • Only medium range boiling volatile oils added to
    the steam help to improve the oil recovery low
    range boiling oils form a 3-ph zone beyond the
    SCF. High range boiling oils stay behind.
  • Molecular diffusion plays an important role in
    determining the efficiency of volatile oil
    enhanced steam drive recovery.
  • (un) stable nodal points
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