erosion damage
DESCRIPTION
N/ATRANSCRIPT
Erosion Damage
• Erosion creates both wear of a surface due in part to impinging a slurry of particles, droplets, or bubbles in a fluid stream.
• The damage variables are related to: – The mass of the particles, – The velocity of the flowing fluid, – The distance to the target, –
• The most severe effects are from high speed gas flow carrying hard, angular materials such as formation sand, proppant, or similar debris, that strike the surface of equipment at an oblique angle.
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Sand production damage
in a surface connection –
the problem started with
a small leak, probably
interior erosion to the
point where a seal was
lost, then the expanding
gas made the problem
much more severe.
Erosion - Sand production damage
BP Canada 8/25/2015 2 George E. King Engineering
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Max Velocities for Particle Sizes
0
50
100
150
0 100 200 300
Particle size, u
ma
x v
el. f
/se
c
0.1 ft3/day
1 ft3/day
Maximum flowing fluid
velocity for increasing
particle diameters.
Although smaller
particles do less damage
than larger particles (less
mass), the sheer number
of small particles can
still do a significant
amount of damage.
Maximum velocity when solids are the the flow stream? Not much!
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Max Producing Velocity
0
0.5
1
1.5
2
2.5
3
3.5
4
0 1000 2000 3000
particle size, u
Ma
x V
elo
cit
y, fp
s
1 ft3/day
4” pipe
Direct
impingement
This data shows that
direct impingement is
much worse than flow
inside a pipe (flow
parallel to the pipe
wall).
Tubing flow with frac
fluid –high velocity and
high concentration of
sand – produces only
slight problems.
Problems start when the
angle of impingement is
changed.
The Impingement Angle
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Threshold
velocity for
screen like
clearances - 5
mpy limit in 316
Stainless. Gas
Flow.
0.00001 ft3/day
0
0.5
1
1.5
2
2.5
3
0 0.005 0.01 0.015
Flow Path Diameter, in
Th
res
ho
ld v
el. fp
s
"Tee"
Direct
0.00001 ft3/day
Potential for damage
from particles to
sand screen sized
openings.
Damage at the screen – sharp angle
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Wirewrap Screen Erosion w/ Air
SLIM-PAK™ 8 Gauge BAKERWELD®
Baker Tests
Note – the difference in the “life” or resistance of any screen to direct impingement of a sand slurry is measured in minutes – none are long lived.
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Multi-Layered Sintered Screen Erosion
Baker Tests
Surface damage of a steel shell may be minor or major, but the real damage is in the wire mesh – this is very rapid.
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Test Screen Erosion – but be careful of conclusions……
Vector Shroud Vector Weave
Baker Tests
Note – although it looks better – the test time of a few minutes is not meaningful in the life of a well – this screen will fail a few minutes after the others – not a significant improvement. 8/25/2015 8
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Screen Damage from Trinidad
Trinidad
The damage to the exterior screen shows the type of damage that a high velocity gas flow containing sand.
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Erosion Screen Damage from Trinidad
Weave
Seam
Upper
shroud
removed
showing
Dutch
Twill
Weave
(DTW)
Screen.
Notice that
the major
damage is
on the
seam.
Trinidad 8/25/2015 10
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Erosion Screen Damage from Trinidad
Upper shroud and
support screen removed
showing base pipe.
Notice that the major
damage is at the center
hole.
Considerable erosion
from outside to inside is
seen here.
Due to handling, the
material blocking some
of the
holes has fallen out.
Plugged hole
Erosion
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Erosion Screen Damage from Trinidad
Plugged hole showing gravel/formation fines.
Eroded center hole.
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Screen Plugging – usually the start of the failure
The plugging, which may
be from dope, scale, rust,
mud, cement, or sand can
quickly reduce the flow
area of the screen. Since
total flow area is usually
around 10%, any loss can
be severe, focusing flow
through a few remaining
open holes and increasing
erosion.
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Plugged screen – and resulting erosion
The hole in screen was probably produced by a high velocity flow
through one of the few remaining unplugged ports. 8/25/2015 14 George E. King Engineering
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Erosion holes in wash
pipe (and screen) – result
of using a large CaCO3
pill to control losses and
then circulating the OHGP
into place. Hot spots
amplified the flux
velocity.
Lawrence Ramnath,
Trinidad, 2002
Erosion – not just from produced solids….
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Erosion angle – any angle other than parallel (zero angle of impingement)
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Erosion – more severe at the surface
Choke body erosion at the surface from rapidly expanding gas and extremely high velocities.
Erosion most severe at angles – not in parallel flow.
Hard, angular particles are the most severe.
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Old equipment showing the effects of erosion following leak development.
The bone yard…..
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Erosion Damage – exit of the choke
Erosion damage in the exit end – high velocity gas.
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Erosion – sand slurries continue to cut…..
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Erosion in a partly open plug valve.
Never use a valve to throttle any flow operation or venting of gas – use a choke.
Valves in the flow line should be fully shut or fully open.
A small leak through a valve will become worse (wash out) very quickly in most cases, particularly when solids are in the flow stream.
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Erosion in a fixed choke bean – Trinidad.
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Time to failure? A few minutes.
Notice the shape of the eroded opening?
Most probably from a perforating producing formation sand.
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Erosion – after breakthrough. The high velocity that develops after erosion breaks through creates much more serious erosion and much more damage. Repair leaks immediately and shut the well in until they can be repaired.
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OK – now both damage and a lot of cleanup……
Very fine sand carried through a small leak in a surface pipe by rapidly expanding gas.
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What remains of a rotary table on a drilling rig after release of solids laden mud at extremely high velocity.
The erosion will enlarge the opening until the velocity through the opening drops below the threshold for metal loss to the solids stream.
Erosion from Solids in the Mud
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