2. Pipeline Design-Hydrotest
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SUBSEA PIPELINE DESIGN CRITERIAHYDROTEST CONDITION
CHAPTER IPREFACE
This file provides detail calculation for designing subsea pipeline that includes:
Wall thickness selection;•On-bottom stability analysis; and•Free-span analysis•
Detail calculation here only provides for hydrotest condition, while calculation on other condition has been provided in other file.
CHAPTER IIDESIGN BASIS
2.1 Pipeline Design Parameter.
Corrosion coating thickness tcorr 4mm:=
Outer diameter Ds 24in 609.6 mm⋅=:=
2.2 Material Properties
Steel density ρs 490pcf 7.849 103
× kg m3−
⋅⋅=:=
Corrosion coating density ρcorr 80pcf:=
Concrete coat density ρcc 190pcf 3.044 103
× kg m3−
⋅⋅=:=
Modulus elasticity E 207000MPa 3.002 107
× psi⋅=:=
Coefficient of thermal expansion α 11.7 106−
⋅ K1−
:=
Structural damping δ 0.126:=
Poisson ratio ν 0.3:=
Pipeline material API5L_Gr_X 52:=
SMYS 290MPa API5L_Gr_X 42=if
317MPa API5L_Gr_X 46=if
359MPa API5L_Gr_X 52=if
386MPa API5L_Gr_X 56=if
414MPa API5L_Gr_X 60=if
448MPa API5L_Gr_X 65=if
483MPa API5L_Gr_X 70=if
:= SMYS 3.59 108
× Pa=
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SMTS 414MPa API5L_Gr_X 42=if
434MPa API5L_Gr_X 46=if
455MPa API5L_Gr_X 52=if
490MPa API5L_Gr_X 56=if
517MPa API5L_Gr_X 60=if
531MPa API5L_Gr_X 65=if
565MPa API5L_Gr_X 70=if
:= SMTS 4.55 108
× Pa=
Manufacturing process Seamless = 1
UO; TRB; ERW = 2
UOE = 0.85
PF 1:=
2.4 Environmental Parameter
Pipeline condition Installation = 1
Hydrotest = 2
Operation = 3
PC 2:=
Highest astronomical tide HAT 0.53m:=
Lowest astronomical tide LAT 0.61m:=
Water depth dmax 22.708m HAT+:= dmax 23.238m=
dmin 14.935m HAT+:= dmin 15.465m=
Kinematic viscosity of seawater v 1.076 105−
⋅ ft2sec
1−⋅:=
Seawater density ρsw 64pcf 1.025 103
× kg m3−
⋅⋅=:=
Gravity( ) g 9.807 m s2−
⋅⋅=
Current at 90% water depth Ur 0.45m s1−
⋅ PC 1= PC 2=∨if
0.48m s1−
⋅ PC 3=if
:= Ur 0.45m
s=
Significant wave height Hs 1.8m PC 1= PC 2=∨if
3.6m PC 3=if
:= Hs 1.8m=
Significant Wave period Ts 6.3s PC 1= PC 2=∨if
8.3s PC 3=if
:= Ts 6.3 s=
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2.5 Pipeline Operational Data
Content density ρcont 0kg m3−
⋅ PC 1=if
1025kg m3−
⋅ PC 2=if
57.522pcf PC 3=if
:=
Design pressure Po 0psi PC 1=if
1350psi PC 3=if
1.5 1350⋅ psi PC 2=if
:=
Design temperature Td 140F:=
Seabed temperature Tsw 23 °C:=
Corrosion allowance Ca 2.54mm:=
External pressure Pe.max ρsw g⋅ dmax⋅:= Pe.max 2.336 105
× Pa=
Pe.min ρsw g⋅ dmin⋅:= Pe.min 1.555 105
× Pa=
Axial pressure Fa 0N:=
Bending stress M 72% SMYS⋅:= M 258.48 MPa⋅=
2.6 Soil Parameter
Soil type 1 = sand
2 = clay
soil 2:=
Medium density of sand ρsand 1860kg m3−
⋅:=
Medium density of clay ρclay 326.309kg m3−
⋅:=
Medium density of soil ρsoil ρsand soil 1=if
ρclay soil 2=if
:= ρsoil 326.309kg
m3
=
Undrained shear stress Su 2kPa:=
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2.8 Design Factor
Internal pressure factor design
ASME B31.4 F1 0.72:=
API RP 1111 fd 0.72:=
Weld joint factor
ASME B31.8 Ee 1:=
API RP 1111 fe 1:=
Temperature derating factor
ASME B31.8 T 1:=
API RP 1111 ft 1:=
Collapse factor
ASME B31.8
f0 0.7:=API RP 1111
Ovalitas
DNV OS F101 fo 0.005:=
Propagation buckling design factor
ASME B31.8
fp 0.8:=API RP 1111
Local buckling factor
DNV 1981
ηxp 0.72:=Longitudinal stress usage factor
Hoop stress usage factor ηyp 0.92:=
Material resistance factor γm 1.15:=
Incidental factor γinc 1.05:=
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CHAPTER IIIWALL THICKNESS SELECTION
3.1 Internal Pressure Collapse Criteria
3.1.1 Internal Pressure Contaiment ASME B31.8 Design Criteria
Initial wall thickness tint.ipc.ASME 17mm:=
Hoop stress σy
Po Pe.max−( )2 tint.ipc.ASME⋅
Ds⋅:= σy 2.461 108
× Pa=
Internal pressure contaiment criteria IPC_ASME_Criteria "accepted" σy F1 SMYS⋅≤if
"not accepted" otherwise
:=
IPC_ASME_Criteria "accepted"=
Safety factor SFipc.ASME
F1 SMYS⋅
σy
:= SFipc.ASME 1.05=
3.1.2 Internal Pressure Contaiment API RP 1111 Design Criteria
Initial steel wall thickness tint.ipc.API 16mm:=
Minimum pressure burst Pb.API 0.9 SMYS SMTS+( )⋅tint.ipc.API
Ds tint.ipc.API−⋅:=
Internal pressure contaiment criteria IPC_API_Criteria "accepted" Po fd fe⋅ ft⋅ Pb.API⋅≤if
"not accepted" otherwise
:=
IPC_API_Criteria "accepted"=
Safety factor SFipc.API
fd fe⋅ ft⋅ Pb.API⋅
Po
:= SFipc.API 1.018=
3.2 External Pressure Collapse
External pressure (Pe) on hydrotest condition is smaller than internal pressure (Pi), hence wall thickness selection
calculation on external pressure collapse criteria isn't done in this condition.
3.3 Local Buckling Criteria
External pressure (Pe) on hydrotest condition is smaller than internal pressure (Pi), hence wall thickness selection
calculation on local buckling criteria isn't done in this condition.
3.4 Propagation Buckling Criteria
External pressure (Pe) on hydrotest condition is smaller than internal pressure (Pi), hence wall thickness selection
calculation on API RP 1111 propagation buckling criteria isn't done in this condition.
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3.5 Selected Wall Thickness
This following t.int.ins is selected wall thickness from hydrotest condition.
The final selected wall thickness is obtain from comparing this initial wall thickness eith other initial wall thicness
from installation and operation condition.
tint.hyd max tint.ipc.ASME tint.ipc.API, ( ):=
tint.ins 9mm:=(Obtained from installation condition calculation)
tint.hyd 17 mm⋅=
tint.op 18.54mm:= (Obtained from operation condition calculation)
tcalc max tint.ins tint.hyd, tint.op, ( ):= tcalc 0.73 in⋅=Selected wall thickness from calculation
Selected wall thickness Pipe OD 6.625" WT 0.75" ts 0.75in:=
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CHAPTER IVON BOTTOM STABILITY ANALYSIS
4.1 Vertical Stability
4.1.1 Pipe Weight Calculation
Initial concrete coating thickness tint.cc 0mm:=
Internal diameter ID Ds 2 ts Ca−( )⋅− := ID 576.58 mm⋅=
Corrosion coating diameter Dcorr Ds 2 tcorr⋅+:= Dcorr 617.6 mm⋅=
Total outer diameter Dtot Ds 2 tcorr⋅+ 2 tint.cc⋅+:= Dtot 617.6 mm⋅=
Steel pipe mass / length mst
π
4Ds2
ID2
−
⋅ ρs⋅:= mst 241.454
kg
m=
Corrosion coating mass / length mcorr
π
4Dcorr
2Ds2
−
⋅ ρcorr⋅:= mcorr 9.881
kg
m=
Concrete coat mass / length mcc
π
4Dtot
2Dcorr
2−
⋅ ρcc⋅:= mcc 0
kg
m=
Content mass / length mcont
π
4ID2
⋅ ρcont⋅:= mcont 267.629kg
m=
Added mass;
Dicplaced water; Buoyancy / length
Bπ
4Dtot
2ρsw⋅:= B 307.118
kg
m=
Total pipe mass / length mtot mst mcorr+ mcc+ mcont+ B−:=
mtot 211.846kg
m=
Total pipe weight / length Wtot mtot g⋅:= Wtot 2.077 103
×N
m⋅=
4.1.2 Vertical Stability Calculation
Vertical stability VS
mtot B+( )B
:= VS 1.69=
Vertical_Stability "accepted" VS 1.1>if
"not accepted; enlarge concrete coating thickness" VS 1.1≤if
:=
Vertical_Stability "accepted"=
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4.2 Lateral Stability
4.2.1 Hydrodynamics Parameter Calculation
4.2.1.1 Wave-Induced Particle Velocity
Spectral peak period Tp 1.05 Ts⋅:= Tp 6.615 s=
Periode
referensi
Tn
dmin
g:= Tn 1.256 s=
Peakedness
parameterϕ
Tp
Hs
:= ϕ 4.931s
m0.5
=
γ 5 ϕ 3.6sec
m
≤if
1 ϕ 5sec
m
≥if
3.3 otherwise
:= γ 3.3=
Figure 4.1 Significant water velocity, Us* (DNV RP E305)
Water particle velocity
(Wave induced)
Tn
Tp
0.19=
Us
0.22 Hs⋅
Tn
:= Us 0.315m
s=
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4.2.1.2 Zero-Up Crossing Period
Figure 4.2 Zero-up crossing period, Tu (DNV RP E305)
Zero-up crossing period Tu 1 Tp⋅:= Tu 6.615 s=
4.2.1.3 Average Velocity on Pipeline
Velocity on 90% depth Ur 0.45m
s=
The amount of current passing through the pipe is affected by the type of seabed soil in which the pipe is laid.
In terms of the soil is clay soil, the soil roughness is negligible, so in this case UD = Ur
UD Ur:= UD 0.45m
s=
4.2.1.4 Hydrodynamics coefficient
Reynold's number Re
UD Us+( )v
Dtot⋅:= Re 4.728 105
×=
Wave - current velocity ratio M
UD
Us
:= M 1.427=
Drag coefficient CD 1.2 Re 5 104
⋅<if
1.3 5 104
⋅ Re< 1 105
⋅<if
1.53Re
3105
⋅
− 1 105
⋅ Re< 2.5 105
⋅<if
0.7 otherwise
:= CD 0.7=
Lift coefficient CL 1.5 Re 5 104
⋅<if
1 5 104
⋅ Re< 1 105
⋅<if
1.2Re
5105
⋅
− 1 105
⋅ Re< 2.5 105
⋅<if
0.7 otherwise
:= CL 0.7=
Inertia coefficient CM 2 Re 2.5 105
⋅<if
2.5Re
5105
⋅
− 2.5 105
⋅ Re< 4.9 105
⋅<if
1.5 otherwise
:= CM 9.457− 109
×=
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4.2.2 Seabed Soil Factor
Figure 4.4 Recommended friction factors for clay (DNV RP E305)
ratio
Dtot Su⋅
mtot g⋅:= ratio 0.595=
Soil friction
factor
μ 2.3:=
4.2.3 Hydrodynamics Force
Wave particle acceleration As 2 π⋅Us
Tu
⋅:= As 0.3m
s2
=
fL. θ( )1
2
ρsw
g⋅ Dtot⋅ CL⋅ Us cos θ( )⋅ UD+( )2⋅:=
Lift force
Drag force fD. θ( )1
2
ρsw
g⋅ Dtot⋅ CD⋅ Us cos θ( )⋅ UD+( )2⋅:=
Inertia force fI. θ( ) πDtot
2
4⋅
ρsw
g⋅ CM⋅ As⋅ sin θ( )⋅:=
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4.2.4 Lateral Stability Calculation
4.2.4.1 Calibration Factor
Figure 4.3 Calibration factor, Fw, as function of K and M (DNV RP E305)
K
Us Tu⋅
Dtot
:= K 3.378=Keulegan-Carpenter number
Calibration factor Fw 1:=
4.2.4.2 Lateral Stability Check
i 0 180..:=phase angle range
θi i deg⋅:=
Required submerged weight ms. θ( )fD. θ( ) fI. θ( )+( ) μ fL. θ( )⋅+
μ
Fw⋅:=
mreq. θ( ) max ms. θ( )( ):=
mreq. θ( ) 18.991kg
m=
SFw
mtot
mreq. θ( ):= SFw 11.155=
LS "accepted" SFw 1≥if
"not accepted, enlarge concrete coating thickness" SFw 1<if
:=LATERAL STABILITY
LS "accepted"=
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CHAPTER VFREE-SPAN ANALYSIS
5.1 Static Analysis
Static span length Lfr.st 50m:=
Total pipe weight / length Wtot 2.077 103
×N
m⋅=
Drag force FD max fD. θ( )( ) g⋅:= FD 129.803N
m⋅=
Inertia force FI max fI. θ( )( ) g⋅:= FI 0N
m⋅=
Support type 1 = pinned - pinned
2 = fixed - pinned
3 = fixed - fixed
support 1:=
End condition constant( ) Cfr.st 8 support 1=if
10 support 2=if
12 support 3=if
:= Cfr.st 8=
Distributed pipe weight Wd Wtot2
FD2
FI2
+
2
+:= Wd 2.082 103
×N
m⋅=
Area moment of inertia Iπ
64Ds4
ID4
−
:= I 1.354 10
3−× m
4⋅=
Section modulus ZI
Ds
2
:= Z 4.441 103−
× m3
⋅=
Longitudinal stress σl
Wd Lfr.st2
⋅
Cfr.st Z⋅:= σl 1.465 10
8× Pa=
Hoop stress σy 2.461 108
× Pa=
Equivalent stress σe σl2
σy2
+:= σe 2.864 108
× Pa=
Allowable stress σallow 0.72 SMYS⋅( ) PC 1=if
0.9 SMYS⋅( ) PC 2= PC 3=∨if
:=
σallow 3.231 108
× Pa=
Static span criteria static_span_criteria "Static span length accepted" σe σallow<if
"Minimize static span length" otherwise
:=
static_span_criteria "Static span length accepted"=
Safety factor SFfr.st
σallow
σe
:= SFfr.st 1.128=
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5.2 Dynamic Analysis
5.2.1 Critical Span Length
5.2.1.1 Stability Parameter
Effective mass meff mst mcorr+ mcc+ mcont+ B+:=
meff 826.082kg
m=
Stability parameter Ks
2 meff⋅ δ⋅
ρsw Dtot2
⋅:= Ks 0.532=
5.2.1.2 Reduced Velocity
Figure 5.1 Reduced velocity for cross-flow oscillations based on the reynolds number.
Figure 5.2 Reduced velocity for inline oscillations based on the stability parameter
Reynold's number Re 4.728 105
×=
Reduced velocity for cross-flow
oscillation
Vr.cf 5.9:=
Reduced velocity for inline oscillation Vr.in 1.4:=
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5.2.1.3 Critical Span Length
End condition constant Cfr.dy π2
support 1=if
15.5 support 2=if
22 support 3=if
:= Cfr.dy 9.87=
Critical span length for cross-flow
motion
Lfr.dy.cf
Cfr.dy Vr.cf⋅ Dtot⋅
2 π⋅ Us Ur+( )E I⋅
meff
⋅:= Lfr.dy.cf 65.997m=
Critical span length for inline motion Lfr.dy.in
Cfr.dy Vr.in⋅ Dtot⋅
2 π⋅ Us Ur+( )E I⋅
meff
⋅:= Lfr.dy.in 32.149m=
Critical span selected for dynamic
analysis criteria
Lfr.dy min Lfr.dy.cf Lfr.dy.in, ( ):= Lfr.dy 32.149m=
5.2.2 Dynamic Stress
5.2.2.1 Vortex Shedding Frequency
Figure 5.3 Strouhal's number for circular cylinder as function of Reynold's number
Reynold's number Re 4.728 105
×=
Strouhal's number St 0.2:=
Vortex shedding frequency fv
St Us Ur+( )⋅
Dtot
:= fv 0.2481
s=
5.2.2.2 Pipeline Natural Frequency
Pipeline natural frequency fn
Cfr.dy
2 π⋅
E I⋅
meff Lfr.dy4
⋅
0.5
⋅:= fn 0.8851
s=
Pipe frequency criteria pipe_frequency_check "pipeline critical span accepted" fv 0.7fn≤if
"redesign pipe" otherwise
:=
pipe_frequency_check "pipeline critical span accepted"=
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DEFINITION
pcflb
ft3
:=
year 31536000sec:=C K:=
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Ν
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