wif categorization exercise · 2018-01-17 · acceptance criteria. 16 example 5 wif well integrity...
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WIF Categorization Exercise
Svein Inge Rafoss, Leading advisor well integrity completion and intervention, Statoil
WIF Well Integrity Workshop, May 26, 2011
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Category Principles & Colours
WIF Well Integrity Workshop, May 26, 2011
Category Principle
RedOne barrier failure and the other is degraded/not verified, or leak to surface.
Orange One barrier failure and the other is intact, or a single failure may lead to leak to surface.
Yellow One barrier degraded, the other is intact.
Green Healthy well - no or minor issue.
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Group 1
Group 2
Group 3
Group 4
Group 5
Group 6
Group 7
Group 8
Group 9
Group 10
Group 11
RNNPreported
Ex 1 o o o o o o o
Ex 2 o
Ex 3 o o o
Ex 4
Ex 5 o o o o o o o o o o
Ex 6
Ex 7 o
Ex 8 o o o o o o o o o
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Group 1
Group 2
Group 3
Group 4
Group 5
Group 6
Group 7
Group 8
Group 9
RNNPreported
Ex 1
Ex 2
Ex 3
Ex 4
Ex 5
Ex 6
Ex 7
Ex 8
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X-mastree
PWV
HMV
MMV
KVPT
PT
PI
A B C
PI
9 5/8" - window @ 2500m MD/2058m TVD
Prod Packer @ 2407m MD/ 1994m TVD
FIT @ 9 5/8" shoe N/A sg
FIT @ 13 3/8" shoe 1.71 sg
7" liner hanger packer @ 2440m MD
DHSV nipple @ 280m MD
TOC 9 5/8” @ 2195m MD/1848m TVD
FG @ Prod packer 1.xx sg
SV
13 3/8" @ 2181m MD/1838m TVD
TOC 13 3/8" @ N/A m MD
20" @ 732m MD
SV
Seal stem @ 2438m MD
Example 1
• 9 year old platform Oil Producer• DHSV: Testing within leak criteria• Christmas Tree: Testing within leak
criteria• A-Annulus valve: Testing within leak
criteria• Completion string & Production
packer: Testing within leak criteria• Formation at intermediate casing:
Formation Strength can not withstand max pressure from reservoir (with oil column)
• Production casing: Buttress threads• Wellhead & Tubing hanger: Leak
tight. • Casing cement: Poor sealing cement
outside the 9 5/8” casing• B-Annulus: Hydrocarbons build up in
B annulus. Pressure buildup less than API criteria.
• C-Annulus: No pressure
WIF Well Integrity 2009 Workshop, May 28, 2009
Primary Barriers
Fm strength at 9 5/8” shoe
9-5/8” casing (below prod pkr)
9-5/8” casing cement (up to prod pkr)
Production packer
Prod tubing
DHSV
Secondary Barriers
Formation at prod packer
9-5/8” casing (above prod pkr)
9-5/8” casing cement (above prod packer)
Tubing hanger
Wellhead
XMT
: failed/suspected failed barrier element
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X-mastree
PWV
HMV
MMV
KVPT
PT
PI
A B C
PI
9 5/8" - window @ 2500m MD/2058m TVD
Prod Packer @ 2407m MD/ 1994m TVD
FIT @ 9 5/8" shoe N/A sg
FIT @ 13 3/8" shoe 1.71 sg
7" liner hanger packer @ 2440m MD
DHSV nipple @ 280m MD
TOC 9 5/8” @ 2195m MD/1848m TVD
FG @ Prod packer 1.xx sg
SV
13 3/8" @ 2181m MD/1838m TVD
TOC 13 3/8" @ N/A m MD
20" @ 732m MD
SV
Seal stem @ 2438m MD
Example 1
• 9 year old platform Oil Producer• DHSV: Testing within leak criteria• Christmas Tree: Testing within
leak criteria• A-Annulus valve: Testing within
leak criteria• Completion string & Production
packer: Testing within leak criteria• Formation at intermediate casing:
Formation Strength can not withstand max pressure from reservoir (with oil column)
• Production casing: Buttress threads
• Wellhead & Tubing hanger: Leak tight.
• Casing cement: Poor sealing cement outside the 9 5/8” casing
• B-Annulus: Hydrocarbons build up in B annulus. Pressure buildup less than API criteria.
• C-Annulus: No pressure
WIF Well Integrity 2009 Workshop, May 28, 2009
Primary Barriers
Fm strength at 9 5/8” shoe
9-5/8” casing (below prod pkr)
9-5/8” casing cement (up to prod pkr)
Production packer
Prod tubing
DHSV
Secondary Barriers
Formation at prod packer
9-5/8” casing (above prod pkr)
9-5/8” casing cement (above prod packer)
Tubing hanger
Wellhead
XMT
: failed/suspected failed barrier element
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X-mastree
PWV
HMV
MMV
KVPT
PT
PI
A B C
PI
9 5/8" - window @ 2500m MD/2058m TVD
Prod Packer @ 2407m MD/ 1994m TVD
FIT @ 9 5/8" shoe N/A sg
FIT @ 13 3/8" shoe 1.71 sg
7" liner hanger packer @ 2440m MD
DHSV nipple @ 280m MD
TOC 9 5/8” @ 2195m MD/1848m TVD
FG @ Prod packer 1.xx sg
SV
13 3/8" @ 2181m MD/1838m TVD
TOC 13 3/8" @ N/A m MD
20" @ 732m MD
SV
Seal stem @ 2438m MD
Example 1
WIF Well Integrity 2009 Workshop, May 28, 2009
: failed/suspected failed barrier element
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Example 2
• 3 year old subsea Oil Producer
• DHSV: Testing within leak criteria
• PMV: Leak rate exceeds API criteria
• PWV, XOV, CIV,AMV: Testing within leak criteria. Tested monthly.
• Completion string & Production packer: Testing within leak criteria
• Production casing, Wellhead & Tubing hanger: Leak tight
• Casing cement: In compliance with Norsok D-010
WIF Well Integrity Workshop, May 26, 2011
A B C
13 3/8" csg @ 2320m MD/2103m TVD
TOC 13 3/8” @ 1912m MD/ 1769m TVD. See note 3.
10 3/4"-9 5/8" XOV @ 444m MD
9 5/8" csg @ 5465m MD/4318m TVD
TOC 9 5/8” @ 4500m MD/3643m TVD. See note 2.
7" liner hanger @ 5271m MD/4181m TVD
Prod. packer @ 5211m MD/4134m TVD
TOC 7” @ 5478m MD/4325m TVD. See note 1.
DHSV @ 353m MD
FIT @13 3/8” shoe 1.87 sg
FIT @ 9 5/8” shoe 1.84 sg
PBR @ 5195m MD
Perforations@ 5520 6159 MD
20" csg @ 909,6m MD/ 905,4m TVD
TOC 20” @ 294m MD/294m TVD. See note 4.
LOT @ 20” shoe 1.46 sg
AWV
PMVAMV
Horizontal x-mas tree
XOV
WOV
Tbghng plug
Debris Cap
ITC with plug
PT
PT
TCI
THI MIV
HXTextension
CIV1
min @ 5465m MD/ 4318m TVD 1.97 sg.
min @ 5211m MD/ 4134m TVD 1.97 sg.
PWV
PMV leak above accept criteria. See Disp below. PWV holds test criteria. PWV, XOV, CIV and MIV tests once per month.
min 1.71 sg.
Primary Barriers
Cap Rock
Liner Cement
Liner Hanger
Fm strength at 9 5/8” shoe
9-5/8” casing (below prod pkr)
9-5/8” casing cement (up to prod pkr)
Production packer
Prod tubing. Includes PBR (not qualified)
DHSV
Secondary Barriers
Formation at prod packer
9-5/8” casing (above prod pkr)
9-5/8” casing cement (above prod packer)
Tubing hanger/seals/plug
Wellhead
XMT/valves
: failed/suspected failed barrier element
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Example 2
• 3 year old subsea Oil Producer
• DHSV: Testing within leak criteria
• PMV: Leak rate exceeds API criteria
• PWV, XOV, CIV,AMV: Testing within leak criteria. Tested monthly.
• Completion string & Production packer: Testing within leak criteria
• Production casing, Wellhead & Tubing hanger: Leak tight
• Casing cement: In compliance with Norsok D-010
WIF Well Integrity Workshop, May 26, 2011
A B C
13 3/8" csg @ 2320m MD/2103m TVD
TOC 13 3/8” @ 1912m MD/ 1769m TVD. See note 3.
10 3/4"-9 5/8" XOV @ 444m MD
9 5/8" csg @ 5465m MD/4318m TVD
TOC 9 5/8” @ 4500m MD/3643m TVD. See note 2.
7" liner hanger @ 5271m MD/4181m TVD
Prod. packer @ 5211m MD/4134m TVD
TOC 7” @ 5478m MD/4325m TVD. See note 1.
DHSV @ 353m MD
FIT @13 3/8” shoe 1.87 sg
FIT @ 9 5/8” shoe 1.84 sg
PBR @ 5195m MD
Perforations@ 5520 6159 MD
20" csg @ 909,6m MD/ 905,4m TVD
TOC 20” @ 294m MD/294m TVD. See note 4.
LOT @ 20” shoe 1.46 sg
AWV
PMVAMV
Horizontal x-mas tree
XOV
WOV
Tbghng plug
Debris Cap
ITC with plug
PT
PT
TCI
THI MIV
HXTextension
CIV1
min @ 5465m MD/ 4318m TVD 1.97 sg.
min @ 5211m MD/ 4134m TVD 1.97 sg.
PWV
PMV leak above accept criteria. See Disp below. PWV holds test criteria. PWV, XOV, CIV and MIV tests once per month.
min 1.71 sg.
Primary Barriers
Cap Rock
Liner Cement
Liner Hanger
Fm strength at 9 5/8” shoe
9-5/8” casing (below prod pkr)
9-5/8” casing cement (up to prod pkr)
Production packer
Prod tubing. Includes PBR (not qualified)
DHSV
Secondary Barriers
Formation at prod packer
9-5/8” casing (above prod pkr)
9-5/8” casing cement (above prod packer)
Tubing hanger/seals/plug
Wellhead
XMT/valves
: failed/suspected failed barrier element
10
Example 3• Original well from 1979• Old casings incl 9-5/8 with
buttress treads.• Class B cement (Old cement
without silica, known to crack up over time)
• Re-completed in 2011, due to leak from Vidar formation into Annulus B with pressure potential above 3500 psi at surface
• New 7 casing with premium threads
• No ASV (deviation), on gaslift• Vidar formation taken into
production below packer (overshot without seals)
• No pressure build-up in Annulus B after re-completed.
WIF Well Integrity 2011 Workshop, May 26
11
Example 3• Original well from 1979• Old casings incl 9-5/8 with buttress
treads.• Class B cement (Old cement without
silica, known to crack up over time)• Re-completed in 2011, due to leak
from Vidar formation into Annulus B with pressure potential above 3500 psi at surface
• New 7 casing with premium threads• No ASV (deviation), on gaslift• Vidar formation taken into production
below packer (overshot without seals)• No pressure build-up in Annulus B
after re-completed.
• Categorized by COPNO as Yellow due to common barrier and one failure can lead to gas leak to other annuli (no gas tight threads from 9-5/8 and out)
WIF Well Integrity 2011 Workshop, May 26
12
Example 4• Drilled and completed in 2008.
• Deviated well bore – max DLS 4 deg / 100 ft.
• CT fishing operation in 2009 pushed plug (TTRBP) to bottom of liner section – below perfs. (Total 3 CT Runs).
• CT Straddle Stimulation performed in 2010. (Total 13 Runs)
• 40 Finger Multi-fingered calliper run across full tubing length after CT Straddle Stim.
• Multi-fingered calliper results identified a maximum grooved wall penetration of 47% at 1,626’ with cross-sectional area loss of 5%.
WIF Well Integrity 2011 Workshop, May 26
13
• New values of Burst, Tension and Collapse calculated and re-modelled within WellCat to verify safety factors.
• 7500 psi tubing re-stimulation burst safety factor identified to be lower than company safety factor of 1.200.
• 6000 psi tubing re-stimulation case modelled and found to give an acceptable burst safety factor.
• Permanent non-conformance created on well and findings communicated to Drilling / Completion / Intervention and Production Groups.
Example 4
WIF Well Integrity 2011 Workshop, May 26
14
• New values of Burst, Tension and Collapse calculated and re-modelled within WellCat to verify safety factors.
• 7500 psi tubing re-stimulation burst safety factor identified to be lower than company safety factor of 1.200.
• 6000 psi tubing re-stimulation case modelled and found to give an acceptable burst safety factor.
• Permanent non-conformance created on well and findings communicated to Drilling / Completion / Intervention and Production Groups.
• WIF Categorization…
Example 4
WIF Well Integrity 2011 Workshop, May 26
15
Example 5
WIF Well Integrity Workshop, May 26, 2011
Tubing to annulus leak above API acceptance criteria
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Example 5
WIF Well Integrity Workshop, May 26, 2011
Tubing to annulus leak above API acceptance criteria
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Example 6
WIF Well Integrity Workshop, May 26, 2011
Producer on Gas lift.
Inflow test of A-annulus failed.
Leak detection tool found communication @ lower GLV 2628 m md.
Unable to pull GLV
Plug installed below lowest GLV @ 2772 m MD. Inflow tested OK.
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Example 6
• Green WellPrimary Barrier:
PackerTubing below plugInflow tested Plug
Secondary Barrier:Prod casingWellheadX-mas tree
WIF Well Integrity Workshop, May 26, 2011
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Example 7
WIF Well Integrity Workshop, May 26, 2011
• Subsea/tieback well, failed on initial production. Well was completed in September/October 1998 and attempted put on production 24.12.98. During production the surface wellhead lifted approx. 32 cm. Caused by the thermal expansion and the fact that the 9 5/8” lock ring in subsea wellhead is not locked in the wellhead. In addition, the 13 3/8” x 9 5/8” annulus is a closed volume as pressure is not bled off into the formation below the 13 3/8” casing shoe.
• P/A Operation in 1999. The well was killed and the production tubing down to the packer was pulled. The perforated intervals were isolated with cement and casing isolated with cement plugs.
• 2007 Small fluid leak observed from annulus B (from WH inspection port)
• October 2010 Small gas leak observed from annulus (HC gas)
20 WIF Well Integrity Workshop, May 26, 2011
• Subsea/tieback well, failed on initial production. Well 15/12-A-02 (exploration well 15/12-6S) was completed in September/October 1998 and attempted put on production 24.12.98. During production the surface wellhead lifted approx. 32 cm. Caused by the thermal expansion and the fact that the 9 5/8” lock ring in subsea wellhead is not locked in the wellhead. In addition, the 13 3/8” x 9 5/8”annulus is a closed volume as pressure is not bled off into the formation below the 13 3/8”casing shoe.
• P/A Operation in 1999. The well was killed and the production tubing down to the packer was pulled. The perforated intervals were isolated with cement and casing isolated with cement plugs.
• 2007 Small fluid leak observed from annulus B (from WH inspection port)
• October 2010 Small gas leak observed from annulus (HC gas)
Example 7
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Example 8
WIF Well Integrity Workshop, May 26, 2011
SV
13 3/8” csg
KWV PWV
UMV
LMVX-mas
tree
DHSV
9 5/8” csg
FG = 2,15 SG
FIT = 1,88 SG
7” liner
4 1/2” liner
FIT = 1,80 SG
Prod. packer
SV
13 3/8” csg
KWV PWV
UMV
LMVX-mas
tree
DHSV
9 5/8” csg
FG = 2,15 SG
FIT = 1,88 SG
7” liner
4 1/2” liner
FIT = 1,80 SG
Prod. packer
SV
13 3/8” csg
KWV PWV
UMV
LMVX-mas
tree
DHSV
9 5/8” csg
FG = 2,15 SG
FIT = 1,88 SG
7” liner
4 1/2” liner
FIT = 1,80 SG
Prod. packer
Primary Barrier
Cemented Liner, casing
Liner Top Packer
Tubing above the DHSV
DHSV
Production packer
Casing
Secondary Barrier
Cemented Casing, liner
Wellhead
Tubing Hanger
Annulus Valve
Xmas tree
•22th of October 2009, water injection was started up after a shut in. After 90 minutes the annulus pressure raised immediately to injection pressure. A tubing to annulus communication was determined.
•Obtained a good inflow test on the DHSV
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Example 8
WIF Well Integrity Workshop, May 26, 2011WIF Well Integrity Workshop, May 26, 2011
SV
13 3/8” csg
KWV PWV
UMV
LMVX-mas
tree
DHSV
9 5/8” csg
FG = 2,15 SG
FIT = 1,88 SG
7” liner
4 1/2” liner
FIT = 1,80 SG
Prod. packer
SV
13 3/8” csg
KWV PWV
UMV
LMVX-mas
tree
DHSV
9 5/8” csg
FG = 2,15 SG
FIT = 1,88 SG
7” liner
4 1/2” liner
FIT = 1,80 SG
Prod. packer
SV
13 3/8” csg
KWV PWV
UMV
LMVX-mas
tree
DHSV
9 5/8” csg
FG = 2,15 SG
FIT = 1,88 SG
7” liner
4 1/2” liner
FIT = 1,80 SG
Prod. packer
Primary Barrier
Cemented Liner, casing
Liner Top Packer
Tubing above the DHSV
DHSV
Production packer
Casing
Secondary Barrier
Cemented Casing, liner
Wellhead
Tubing Hanger
Annulus Valve
Xmas tree
•22th of October 2009, water injection was started up after a shut in. After 90 minutes the annulus pressure raised immediately to injection pressure. A tubing to annulus communication was determined.
•Obtained a good inflow test on the DHSV