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7/31/2019 Solvent Treating Basics
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Solvents
Uses
Types and Selection
Application Handling
Disposal
3/14/2009 1George E. King EngineeringGEKEngineering.com
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Solvent Types
Checks:
Flash point (safety issues for pumping)
Solubility of damage in solvent
Stability of solvent
Seal stability in solvent
Disposal ease
3/14/2009 2George E. King EngineeringGEKEngineering.com
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Solvent Types and Uses
Xylene removes most wax, asphaltene, sludges
Toluene, same uses as xylene, but has lower flashpoint and harder on seals.
Lemonol may be a passable xylene substitute,safer, but test on the deposit at well conditions.
Kerosene removes wax, some sludges
Crude oil removes some wax, but generally poor
response or very slow #2 diesel not recommended unless filtered to 5
microns with beta of 1000.
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First Treatment
BP
Begin pumping
xylene @ 3bpmPumping xylene @ 7 bpm
Slowdown pump & swap to diesel tank.
Begin pumping diesel @ 8 bpm
Note: Pressure increasing on
wellhead @ ~8,000 gals of ???
Completed
pumping diesel @ 8
bpm
SD and begin
flushing ofequipment.
Start breaking over @ 8 bpm
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Second Treatment
BP
A-5
3500
4000
4500
5000
5500
6000
6500
7000
1/15/06 14:30 1/15/06 15:00 1/15/06 15:30 1/15/06 16:00 1/15/06 16:30 1/15/06 17:00 1/15/06 17:30
0.0
1.0
2.0
3.0
4.0
5.0
6.0
7.0
BHP
BPM
start xylenestart diesel
xylene at perfs
3/14/2009 5George E. King EngineeringGEKEngineering.com
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Solvents, Instead of Acids
use for removal of:
Sludges best solvent depends on composition
Emulsions solvent depends on composition
Paraffins - xylene, kerosene, condensates, some oils Asphaltenes xylene, toluene, lemonol dispersants
Poorest solvents? - #2 diesel (loaded with wax) and
dead crude oils (asphaltic growth issues and wax
loadings)
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Solvent Volumes
paraffin removal
10 to 15 gal/ft of affected zone.
asphaltene removal
10 to 25 gal/ft - and this wont dissolve much!
100 grams of xylene dissolves 9 grams of
asphaltenes
3/14/2009 7George E. King EngineeringGEKEngineering.com
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0
1000
2000
3000
4000
5000
6000
7000
8000
0 1000 2000 3000 4000 5000
BottomH
olePressure(ps
ig)
Total Liquid Rate (stbf/d)
1 - Hydraulics B ase
2 - PRSS 770.000
3 - PRSS 1050.000
1 - IPR Base
2 - SKN 2.000
3 - SKN 16.000
Boqueron 0 2
Reservoir Data
Pres sure = 7100
kh = 1092.0
Skin = 16.00
Boqueron 02 (1 3march01)
Density = 4.000
Perf Diam = 0.50
Penetration = 8.00
Rate vs. Press ure
27-Mar-01 11 :42:54
Depth (MD) = 17276
WHPres (psia) = 770
Tubing I.D. = 2.750 (s1)
Before:
Oil: 2200 bopd
WHP: 770 psiBHFP: 3660 psi
Skin: 16
After:Oil: 3100 bopd
WHP: 1050 psi
BHFP: 5000 psiSkin: 2
Oil(bopd) GOR(scf/bbl) WHP(psi) BHFP(psi) WHT(F) H2S(ppm) GAS(mmscfd) APIGrav SepPress(psi)
Before 2200 2080 770 3660 187 10 4.3 31.5 420
After 3200 1830 1050 5100 198 10 5,92 31.3 200
?
Boqueron Field in Maturn - Venezuela Source Jose Soto
Example of
a solvent
job.
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Event Oil(bopd) GOR(scf/bbl) WHP(psi) BHFP(psi) WHT(F) H2S(ppm) GAS(mmscfd) APIGrav SepPress(psi)
Before 2200 1950 770 3660 195 10 4.3 31.4 420
After 3100 1950 1050 5000 195 10 5.92 31.4 420
With correction of Separator pressure, the data becomes:
Treatment Summary
100 gal per foot perforated of 100% Xylene -> Total:21,000 gals Soak time: 6 hours
Injection rate: 1,1 bpm w/ CT annulus pressure:2000 psi.
Calculated Xylene penetration with 10% porosity @6,5 ft.
Estimated Cost Real Cost
$ 255,000 $ 191,5003/14/2009 9George E. King EngineeringGEKEngineering.com
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Problems with Solvents
rubber/elastomer seal deterioration
density problems (hard to get to and hold onbottom)
getting reasonably pure solvents ie., xylene b.p. is 138-144 C
naphta not nearly as good
just what is a xylene bottom? no real definition
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Solvent migration through a standing brine
column
Xylene will come back to surface fast (fast or
faster than gas?)
Migrates at 5 - 10,000 feet per hour in
seawater.
If you're soaking a pill on bottom, it won't stay
there long.
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Disposal
Most solvents are sold with crude.
Some aromatics may affect oil price, but may
not be a factor in large oil volumes.
Care must be taken not to expose personnel
or the environment to returning solvent.
3/14/2009 12George E. King EngineeringGEKEngineering.com