Master of Petroleum Well Engineering Ad A d v an anc c ed Dr Drii l l i n g Pr Prac actt i c es CASING DESIGN
April – 2005 Assoc. Prof. Sampaio
jsampaio@peten
[email protected] g.curtin.edu.au jsampaio@peteng. curtin.edu.au
Casing Design Why Run Casing? Types of Casing Strings Classification of Casing Wellheads Burst, Collapse and Tension
– Ex Exa ampl ple es
Effect of Axial Tension on Collapse Strength – Ex Exa ampl ple es
Casing Design Why Run Casing? Types of Casing Strings Classification of Casing Wellheads Burst, Collapse and Tension
– Ex Exa ampl ple es
Effect of Axial Tension on Collapse Strength – Ex Exa ampl ple es
Casi Ca sing ng De Desi sign gn - In Intr trod oduc ucti tion on What is casing? Why run casing? 1. To prevent the hole from caving in, 2. Onsh shor ore e - to pr pre eve vent nt contamination of fresh water sands, 3. To prevent water migration to producing formation,…
Casing
Cement
Casing Design - Why run casing - cont’d 4. To confine production to the wellbore, 5. To control pressures during drilling, 6. To provide an acceptable environment for subsurface equipment in producing wells, 7. To enhance the probability of drilling to total depth (TD). e.g., you need 14 ppg to control a lower zone, but an upper zone will fracture at 12 lb/gal. What to do?
Functions of Casing Individu Drive pipe
Conductor pip
Provides a means of nippling up diverters Provides a mud return path Prevents erosion of ground below rig
Same as Driv Supports the weight of nex casing strings Isolates very formations
Functions of Casing Individu Surface casing
Provides a means of nippling up BOP Provides a casing seat strong enough to safely close in a well after a kick Provides protection of fresh water sands
Intermediate ca
Usually set in th abnormally pres zone Provides isolatio potentially troublesome zon Provides integrit withstand the h
Functions of Casing Individually – Production casing
Provides zonal isolation (prevents migration of water to producing zones and isolates different production zones) Confines production to wellbore Provides the environment to install
Liners
Drilling liners
– Same as Interm casing
Production liner
– Same as produc casing
Tieback liners
– Tie back drilling production liner surface. Conver
Types of Strings of Casin Diameter 1. Drive Pipe or Structural Pile (Gulf Coast and offshore only) 150’-300’ BML
16”-60”
2. Conductor String 100’ - 1,600’ BML
16”-48”
3. Surface Pipe 2 000’ 4 000’ BML
85 /8”-20”
Exa
1
Types of Strings of Casing – con Diameter 4. Intermediate String 5. Production String 6. Liner(s)
75 /8”-133 /8” 4½”-95 /8”
Exa
9
Example Hole and String Size Hole Size
Pipe Size
36”
Structural casing
30”
26”
Conductor string
20”
17½”
Surface pipe
12¼”
Intermediate String
133 /8” 95 /8”
Classification of CSG.
Outside diameter of pipe (e.g. 95 /8”) Wall thickness (e.g. ½”) Grade of material (e.g. N-80) Type to threads and couplings (e.g. A LCSG) Length of each joint (e.g. Range III) Nominal weight (e.g. 47 lb/ft)
Most Common Grades
Minimum Yield Strength (KPSI)
Ultimate Strength
H-40
40
60
J-55
55
75
K-55
55
95
C-75
75
95
L-80
80
95
N-80
80
100
C-90
90
100
C-95
95
105
P-110
110
125
V-150
150
160
Length of Casing Joints RANGE
LENGTH (ft)
I
16 - 25
II
25 - 34
Casing Threads and Coupli API round threads – short API round thread - long Buttress Extreme line Other …
( CSG ( LCSG ( BCSG ( XCSG
Casing Threads and Couplings –
Wellhead & Christmas Tre •Wellhead •Hang Casing Strings •Provide Seals
•Christmas Tree •Control Production from Well
Wellhead & Christmas Tree – co
Casing Performance - Unia
Loadings Axial Tension (couplings & bo Burst Pressure Collapse Pressure Bending Buckling
Casing Performance - Uniaxia
Tension Strength/Failure
Tension Strength
Tension Strength – Couplings: API Tables for various couplings – Body (perm. deform.)
F ten =
π
4
(d
2 n
− d
2
)
σ
yield
F ten = pipe body yield strength d n = nominal diameter
Tension Strength – Example 1
Compute the body-yield strength fo 7”, N-80, 23 lb/ft casing. Solution: From API Table (1 & 2) d n = 7 in d = 6.366 in σ
yield
= 80,000 psi
Tension Strength Formula
Uses Nominal Diameter API minimum Thickness 87.5% o original (nominal) thickness Yield Strength Rupture much larger May deform plastically
Casing Performance - Uniaxia Burst (Internal Pressure) Yield the body Yield the coupling Leak the coupling
P
Burst (Internal Pressure)
Barlow (API allows 87.5% of thickness)
Thin Wall Assumption
Pbr =
2(0.875 t ) d n
σ
yield
P br = pipe body burst pressure d n = nominal diameter
Burst
(Internal Pressure) – Example Exampl
Compute the body burstpressure fo 7”, N-80, 23 lb/ft casing. Solution: From API Table d n = 7 in d = 6.366 in σ
→ t =
80 000 psi
7 − 6.366 2
= 0.317 in
Collapse (External Pressure
Collapse (External Pressure) – con
The following factors are importan The collapse pressure resistance of a depends on the axial stress (biaxial s There are different regimes of collaps failure (depends on ratio dn /t) Yield Strength Collapse (thick wall) Plastic Collapse Transition Collapse Elastic Collapse
Collapse (External Pressure) – con
Yield Strength Collapse Pressure
⎡ (d n t ) − 1⎤ ( pcr ) yield = 2(σ yield )e ⎢ 2 ⎣ (d n t ) ⎦ P cr = pipe body collapse pressure d n = nominal diameter
Collapse (External Pressure) – con
Plastic Collapse Pressure
( pcr ) plastic
⎡ F 1 ⎤ = (σ yield )e ⎢ − F 2 ⎥ ⎣ (d n t ) ⎦
P cr = pipe body collapse pressure d n = nominal diameter
Collapse (External Pressure) – con
Transition Collapse Pressure
( pcr )trans
⎡ F 4 ⎤ = (σ yield )e ⎢ − F 5 ⎣ (d n t ) ⎦
P cr = pipe body collapse pressure d n = nominal diameter
Collapse (External Pressure) – con
Elastic Collapse Pressure
( pcr )elast =
46.95 × 10
6
(d n t )(d n t − 1)
P cr = pipe body collapse pressure d n = nominal diameter
2
Collapse (External Pressure) – con
F 1, F 2, F 3, F 4, F 5 … These values are for the uniaxial stress Different values for effective yield stress For Biaxial calculate the effective Yield Stress and interpolate the F’ s
Collapse (External Pressure) – con
Upper Limit for Yield Strength Collaps
⎛ F 3 ⎞ ⎟ + (F (F 1 − 2) + 8⎜⎜ F 2 + ⎟ σ ( ) yield e ⎠ d n ⎝ ≤ t ⎛ F 3 ⎞ ⎟ 2⎜ F 2 + ⎜ ⎟ σ ( ) ⎝ ⎠ 2
Collapse (External Pressure) – con
Upper Limit for Plastic Collapse
d n t
≤
(σ yield ) e (F 1 − F 4 ) F 3 + (σ yield ) e (F 2 − F 5 )
Collapse (External Pressure) – con
Upper Limit for Transition Collapse
d n t
≤
2 + F 2 F 1 3 F 2 F 1
Collapse (External Pressure) – con
Boundaries for Axial Stress = 0
Collapse (External Pressure) – Exam
Calculate the Collapse pressure rating for a 7 N-80, 23 lb/ft casing. Solution: 7 in, N-80, 23 lb/ft → t = 0.317 in Grade
F1
F2
F3
F4
N-80
3.071
0.0667
1,955
1.988
d
7
Collapse (External Pressure) – Exam
( pcr ) plastic
( pcr ) plastic
⎡ F 1 ⎤ = (σ yield ) e ⎢ − F2 ⎥ − F 3 ⎣ ( d n t ) ⎦
⎡ 3.071 ⎤ = 80,000 × ⎢ − 0.0667⎥ − 1,955 = 3,83 ⎣ 22.08 ⎦
Triaxial Collapse
Effect of Axial Stress in the Colla Resistance – Effective Yield Stres Von Mises Criteria (Distortion En
(σ
Material fails (ductile – yield failure) w total distortion energy equals uniaxial energy
σ
) + (σ 2
σ
) + (σ 2
σ
) ≤ 2
Triaxial Collapse – cont’d
Triaxial
(
σ
)
yield e
2
=
2 σ yield
⎛ σ z + pi ⎞ ⎛ − 3⎜ ⎟ + 3σ z pi − ⎜ ⎝ 2 ⎠ ⎝
Biaxial
(
σ
(σ
)
yield e
=
2 σ yield
) = effective yield stress
− 0.75σ z
2
⎛ σ z ⎞ −⎜ ⎟ ⎝ 2 ⎠
Triaxial Collapse – cont’d
Linear Interpolation for F’ s F’ s depend on Yield Stress For σA < σe < σB interpolate using (lin
− σ A (F B − F A ) F e = F A + σ − σ B A σ
e
F’s Formulas (API Bull. 5C3 F 1 = 2.8762 + 0.10679 × 10
−5
σ
F 2 = 0.026233 + 0.50609 × 10
Y
−6
+ 0.21301× 10
−10
2 σ Y
σ
Y
F 3 = −465.93 + 0.030867σ Y − 0.10483 × 10 − 3
7
2 Y
σ
+ 0.36989
⎡ 3( F 2 / F 1 ) ⎤ 46.95 × 10 ⎢ ⎥ F F 2 ( / ) + 2 1 ⎦ ⎣ F 4 = 2 ⎡ 3( F 2 / F 1 ) ⎤⎡ 3( F 2 / F 1 ) ⎤ σ − ( F 2 / F 1 )⎥ ⎢1 − Y ⎢ ⎥ F F F F + + 2 ( / ) 2 ( / ) 2 1 2 1 ⎦ ⎣ ⎦⎣ 6
− 0.5313
Triaxial Collapse – Example 4
For the casing of Example 3, calculat corrected critical collapse pressure if section of 2000 ft , 7 in, N-80, 23 lbm casing is suspended below it (assume linear weight of 23 lbf/ft and empty borehole - no buoyancy effect). What the corrected collapse pressure if the internal pressure is 1000 psi?
Triaxial Collapse – Example 4 Solution: Weight of Casing Below Point in Question F = 2000 ft × 23 lbf/ft = 46,000 lbf
Cross Section Area Ac =
Axial Stress
(7
π
2
− 6.366 2 ) 4
= 6.6555 in
2
Triaxial Collapse – Example 4 Effective Yield Stress (biaxial)
(
σ
(
σ
)
yield e
)
yield e
=
2 σ yield
− 0.75σ z
2
⎛ σ z ⎞ −⎜ ⎟ ⎝ 2 ⎠
⎛ 6,912 ⎞ = 80,000 − 0.75 × 6,912 − ⎜ ⎟ = 76,32 ⎝ 2 ⎠ 2
2
Triaxial Collapse – Example 4 Interpolated F’ s Grade
F1
F2
F3
F4
C-75
3.054
0.0642
1,806
1.990
“N-76.32”
3.058
0.0649
1,845
1.992
N-80
3.071
0.0667
1,955
1.998
API F’ s Formulas (MsExcel Spreadsheet) σyield
F
76320 F
F
F
F
Triaxial Collapse – Exampl d n
Collapse Regime
t
=
7 0.317
= 22.08
Yield Regime U-Limit: ⎛ F 3 ⎞ ⎟ + (F 1 − 2 ) (F 1 − 2) + 8⎜⎜ F 2 + ⎟ ( ) σ yield e ⎠ d n ⎝ ≤ t ⎛ F 3 ⎞ ⎟ 2⎜ F 2 + ⎜ ⎟ ( ) σ yield e ⎠ ⎝ 2
(
)
2
⎛ ⎜
1 845 ⎞
⎟ (
)
Triaxial Collapse – Example 4 Plastic Regime U-Limit: d n t
22.08 ≤
≤
(σ yield ) e (F 1 − F 4 ) F 3 + (σ yield ) e (F 2 − F 5 )
76,320 × (3.058 − 1.992 ) 1,845 + 76,320 × (0.0649 − 0.0422 )
= 22.79
Collapse occurs in the Plastic Regime
Triaxial Collapse – Example 4
Plastic Collapse Strength ( pcr ) plastic
( pcr ) plastic
⎡ F 1 ⎤ = (σ yield )e ⎢ − F 2 ⎥ − F 3 ⎣ (d n t ) ⎦
⎡ 3.058 ⎤ = 76,320 × ⎢ − 0.0649⎥ − 1,845 = 3,772 ⎣ 22.08 ⎦
Triaxial Collapse – Example 4 Effect of Internal Pressure
Critical pressure expressions are for pressure differential. However, the effective yield s should account or the internal pressure, s the yield will start at the internal wall. The triaxial expression must be used:
(
)
2
⎛ σ + pi ⎞ ⎜ ⎟
2
⎛ σ + p ⎜
Triaxial Collapse – Example 4 2
(
σ
)
yield e
⎛ 6.912 + 1 ⎞ ⎛ 6.9 = 80 − 3 ⎜ ⎟ + 3 × 6.912 × 1 − ⎜ 2 ⎝ ⎠ ⎝ 2
(
)
σ
yield e
σy ield
= 75.800 ksi = 75,800 psi
75800
F1
F2
F3
F4
F5
3.056
0.0646
1830
1.991
0.0421
⎡ 3.056
⎤
Pressure Collapse Table
Casing Design Criteria
Biaxial Method or Uniaxial Method Burst – Conductor – Surface and Intermediate Casing – Production Casing
Collapse Tension
Casing Design Criteria – cont Burst Conductor:
– External pressure is zero – The maximum internal pressure is the formation fracture pressure at the depth conductor set depth. If the fracture pres unknown, assume ∇ pff =1 psi/ft – F.S.=1.1 – Neglect the gas density inside the condu
Burst of Conductor
Casing Design Criteria – cont Burst of Surface & Intermediate Csg.:
External pressure: hydrostatic pressure of the heav used to drill the hole and set the casing Internal pressure: based on pore pressure at the fin of the next casing. If the pore pressure at the botto next casing is not known, assume the following:
⎧∇ p p = 0.564 psi/ft Depth next casing < 8000 ft ⎨ ⎩∇ p p = 0.650 psi/ft Depth next casing ≥ 8000 ft
Assume that a fraction f (usually not less than 40% length is evacuated by gas and (1-f ) fraction of the remains filled with drilling fluid.
Burst of Surf. & Interm. Csg
Casing Design Criteria – cont Burst of Production Casing:
External pressure: hydrostatic pressure due to formation saltwat = 1.1542) Internal pressure: based on pore pressure at the final depth Dc (production depth). If the pore pressure at the bottom of the cas known assume the following:
⎧∇ p p = 0.564 psi/ft Depth casing < 8000 ft ⎨ ⎩∇ p p = 0.650 psi/ft Depth casing ≥ 8000 ft
Assumed the whole internal casing filled with gas (gas lift prod Pressure inside the casing determined as follows: Mg
−
p
p e
RT
( DC − D )
≅ p e
DC − D
−
40000
Burst of Production Casing
Casing Design Criteria – cont Collapse:
Collapse due to fluid in the annulus betwee casing and the borehole Considered the heaviest drilling fluid used t the hole and set the casing Assume casing empty No buoyancy F.S.=1.0 (neglect the strengthening effect cement; most of the casing will not be emp
Collapse of Casing
Casing Design Criteria – cont
Tension: Corresponds to the weight of the casing weight measured in the a (no buoyancy effect) F.S.: – 1.6 for couplings – 1.8 for casing body
Casing Design Example
Evaluate the burst and collapse pressu loadings and design an appropriate sur casing using the biaxial method. Check axial load. – – – – –
Setting depth of the casing string: 4000 Mud density as setting the string: 10.0 l Setting depth of the next csg. string: 11 Mud density of the next phase: 10.5 lb/ Casing size and coupling: 103 /4” Buttres threads, minimum grade K-55
Casing Design Example con
Burst Loading (this is a surface cs
External Pressure:
po(psi) = 0.052 x 10 lb/gal x D(ft po = 0.52 x D
Casing Design Example con
Internal Pressure: ∇pp=0.650 psi /ft /ft (Dnc>8,000 ft) pp = 11,000 x 0.650 = 7,150 psi (1-0,4)xDnc = 6,600 ft p6600= 7,150-0.052x10.5x6,600=3,546 pi= 3,546 psi
Casing Design Example con Burst Pressure – cont’ d: d: F.S. = 1.1 pab = (pi-po) pab= 3,546 – 0.52D
Casing Design Example con Collapse Loading External Pressure: po = 0.52 x D Internal pressure = 0 psi F.S. = 1.0
Casing Design Example con Design for Burst
Start at bottom (minimum burst pres
pab,4000 = 3,546 – 0.52 x 4000 = 1,466 p
Cheapest casing: (p.320-321) K-55, 40.50 lb/ft, Burst Strength 3,130 p Minimum depth that can go: p 3 546 0 52 x D 3130 psi / 1.1
Casing Design Example con
Continue with next cheapest Cas
K-55, 45.50 lb/ft, Burst Strength 3,580 p
Minimum depth that can go: pab,D = 3, 3,546 – 0.52 x D = 3,580 psi / 1.1 Dmin = 561 ft
Casing Design Example con
Continue with next cheapest Cas
K-55, 51.00 lb/ft, Burst Strength 4,030 p
Minimum depth that can go: pab,D = 3, 3,546 – 0.52 x D = 4,030 psi / 1.1 Dmin = -226 ft (above surface)
Casing Design Example con Burst Diagram 0 ft 103 /4 K-55 51.00 lb/ft 561 ft 103 /4 K-55 45.50 lb/ft 1347 ft
103 /4 K-55 40.50 lb/ft
Casing Design Example con Design for Collapse (uniaxial)
Start at top (minimum collapse press pac = 0.52 x D
Cheapest casing: K-55, 40.50 lb/ft, Collapse Strength 1,580 Maximum depth that can go: p = 0.52 x D = 1,580 psi / 1.0
Casing Design Example con
Continue with next cheapest Cas
K-55, 45.50 lb/ft, Collapse Strength 2,090 Maximum depth that can go: pac,D = 0.52 x D = 2,090 psi / 1.0 Dmax = 4.019 ft
Casing Design Example con Collapse Diagram 0 ft
103 /4 K-55 40.50 lb/ft
Casing Design Example con Combine Two Diagrams 0 ft
103 /4 K-55
561 ft
103 /4 K-55 1347 ft
+
=
burst
103 /4 K-55
collapse
Casing Design Example con Collapse Adjustment (Biaxial) Start at bottom (Iterative Process)
No need to check at bottom of 45.50 lb/f
Bottom of 103 /4 K-55 40.50 lb/ft - 3,038 d n t
=
A =
10.75 0.350
π
4
= 30.71
2 2 2 − = 10.75 10.050 11.44 in ( )
Casing Design Example con
Effective Yield Stress (biaxial)
(
σ
)
yield e
⎛ 3,828 ⎞
= 55, 000 − 0.75 × 3,828 − ⎜ ⎝ 2
σy ield
2
2
⎟ = 52, 986 ⎠
52986
F1
F2
F3
F4
F5
2 985
0 0530
1146
1 994
0 0354
Casing Design Example co
Yield Regime U-Limit 1,146 ⎞ ⎛ + ( 2.985 − 2 ) ( 2.985 − 2 ) + 8 ⎜ 0.0530 + ⎟ 52,987 ⎠ ⎝ = 14. 1,146 ⎞ ⎛ 2 ⎜ 0.0530 + ⎟ 52,987 ⎝ ⎠ 2
Not Yield Regime
Casing Design Example con
Plastic Regime U-Limit
52,987 × (2.985 − 1.994) 1,146 + 52,987 × (0.0530 − 0.0354)
Not Plastic Regime
= 25.26 < 30
Casing Design Example co
Transition Regime U-Limit
2 + 0.0530 2.985 3 × 0.0530 2.985
= 37.84 < 30.71
Collapse occurs in the Transition Regim
Casing Design Example con
Transition Collapse Pressure
( pcr ) trans
⎡1.994 ⎤ = 52, 986 × ⎢ − 0.0354 ⎥ = 1, 562 p ⎣ 30.71 ⎦
Maximum depth that can go: pac,D = 0.52 x D = 1,562 psi / 1.0
Casing Design Example con
2nd Iteration Bottom of 103/4 K-55 40.50 lb/ft - 3,001
W = 45.50 lb/ft × (4000 ft − 3009 ft) = 45,318 lbf σ
z
=
45,318 lbf 11.44 in
2
= 3,963 psi
Casing Design Example con
Effective Yield Stress (biaxial)
(
σ
)
yield e
⎛ 3,963 ⎞
= 55, 000 − 0.75 × 3, 963 − ⎜ ⎝ 2
σy ield
2
2
⎟ = 52, 91 ⎠
52911
F1
F2
F3
F4
F5
2 984
0 0530
1143
1 994
0 0354
Casing Design Example con
Plastic Regime U-Limit 52, 911× ( 2.985 − 1.994 ) 1,144 + 52, 911× ( 0.0530 − 0.0354 )
= 25.26 < 3
Not Plastic Regime
Casing Design Example con
Transition Regime U-Limit
2 + 0.0530 2.985 3 × 0.0530 2.985
= 37.86 > 30.71
Collapse occurs in the Transition Regim
Casing Design Example con
Transition Collapse Pressure
( pcr ) trans
⎡1.994 ⎤ = 52, 911× ⎢ − 0.0354⎥ = 1,561 psi ⎣ 30.71 ⎦
Maximum depth that can go: pac,D = 0.52 x D = 1,561 psi / 1.0 D = 3,002 ft
Casing Design Example cont ’d Final Diagram 0 ft
1
561 ft
2
1347 ft
→ 3006 ft
103 /4 K-55
103 /4 K-55
3
103 /4 K-55
Casing Design Example cont ’d
Check for Tension
Critical section: Top of section 3 – Axial Load W=45.50x(4000-3006)+40.50x(3006-1347)=112,417 lbf
103 /4 K-55 40.50 lb/ft – Body Strength: 629 kips/1.8 = 349 kips – Coupling Strength: 819 kips/1.6 = 512 kips
Csg. Design & Pore Pressure pressure
Abnormal ∇P: >0.4365 psi/ft
h t p e d
Normal ∇P: 0.433-0.4365 psi/ft