Title: The distillation mechanism in steam displacement of oil
1The distillation mechanism in steam displacement
of oil
- Dan Marchesin and Hans Bruining,
ECMOR X Sept 4-7, 2006
2An 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
3Steam injection
Steam injection is commercially applied to
recover viscous oils
Amsterdam ECMOR X Sept. 4-7, 2006 19 slides
4Volatile oil enhanced steam drive
Amsterdam ECMOR X Sept. 4-7, 2006 18 slides
5ES-SAGD (Ian Gates)
Co-inject some volatile oil with steam
Courtesy Claes Palmgren
Amsterdam ECMOR X Sept. 4-7, 2006 17 slides
6Laboratory tests showing the effect of coinjected
volatile oil
7Contents
- 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
8MOC 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
9Simulation 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
10Motivation 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
11Model
- 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
12Four 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
13Formulations 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
14Dodecane coinjected (num. sol.)
15Cyclo-butane coinjected (num. sol.)
16Comparison numerical (left) and analytical
solution Medium boiling (heptane) volatile oil
Saturations 0 ?? S?? ? 1., vov fraction of
volatile oil in the oleic phase.
17Numerical (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
18Medium 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
19Blow 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
20Stability 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
21Conclusions
- 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
22Conclusions
- 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