Evaluation system for corrosion defects in pipelines
-
Upload
brynne-vang -
Category
Documents
-
view
54 -
download
0
description
Transcript of Evaluation system for corrosion defects in pipelines
![Page 1: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/1.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Evaluation system for corrosion defects in
pipelines
Dr. Gyöngyvér B. Lenkey, Dr. László Tóth, Zsolt Balogh
![Page 2: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/2.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Objectives of the work
Evaluation of the applicability of FEM for predicting the failure pressure and the safe operation pressure for corroded pipelines
Development of safety diagrams Development of evaluation system for
corrosion defects
![Page 3: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/3.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Previous projects
Development of FEM model with real defect geometry
Development of simplified defect geometries and comparative assessment
Comparison of FEM results with pressure tests and with engineering methods
Development of failure criteria for failure pressure
![Page 4: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/4.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Mapping the real 3D defect geometryMapping the real 3D defect geometry
Sample (negative)
Laser distance
measurment
![Page 5: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/5.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Boundary conditions for FEM modelBoundary conditions for FEM model
Modelling the pressure test: Quarter modell Increasing internal pressure Increasing axial tension (proportional with
the pressure)
![Page 6: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/6.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
0
200
400
600
800
1000
1200
1400
0 0.5 1 1.5
-
M
Pa
Parameters of FEM calculationsParameters of FEM calculations Elastic-plastic material law (determined from tensile
tests, ReH=350 MPa, Rm=480 MPa)
Von-Mises yield criteria, isotropic hardening Large deformation option
![Page 7: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/7.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Transfer the real defect geometry Transfer the real defect geometry into the FEM modellinto the FEM modell
![Page 8: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/8.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Development of simplified defect Development of simplified defect geometriesgeometries
1 4 7
10 13 16 19 22
S1
S9
S17
0
0,5
1
1,5
2
2,5
3
3,5
4
1 3 5 7 9
11 13
15
17
19
21
S1
S6
S11
S16
S21
0
0,5
1
1,5
2
2,5
3
3,5
4
1 3 5 7 9
11 13
15
17
19
21
S1
S6
S11
S16
S21
0
0,5
1
1,5
2
2,5
3
3,5
4
Parabolic modell Rectangular modell 6th order surface modell
![Page 9: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/9.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Predicting the failure pressurePredicting the failure pressure
0
200
400
600
800
1000
1200
0 5 10 15 20 25
Pressure, MPa
Str
ess,
MP
a
Eq. stress Main stress SMYS SMYS+69 Rm'
ReH
Rm'
pF
![Page 10: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/10.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Criterion: eq = Rm '
0
5
10
15
20
25
0 1 2 3 4 5 6 7
Defect depth, mm
Pre
ssu
re, M
Pa
Real defect
Rectengular modell
Parabolic modell
Measured failure pres.
6th order modell
Validation of failure criterion and Validation of failure criterion and applicability of simplified geometriesapplicability of simplified geometries
![Page 11: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/11.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
0
5
10
15
20
25
0 1 2 3 4 5 6 7
Hibamélység,mm
Nyo
más
,MP
a
ASME B31.G RSTRENG DNV RP-F 101 Battelle Shell-92 Mért tönkr. nyomás
Comparison of measured and Comparison of measured and predicted failure pressure values – predicted failure pressure values –
with engineering methodswith engineering methodsP
ress
ure
, MP
a
Defect depth, mm
Meas. fail. pres.
![Page 12: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/12.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Objectives of the present project
Performing large number of FEM calculations with simplified defect geometry (parabolic)
Development of safety diagrams and defect evaluation system
![Page 13: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/13.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Material Diameter (D), mm Thickness (t), mm
1 A52K 323,9 5
2 X52 323,9 6,3
3 X52 406,4 5,6
4 DX60 406,4 7,1
5 X52 609,6 10
6 DX60 609,6 8
7 DX52 406,4 7,1
8 DX52 406,4 8
Basic data for the FEM calculations
Different pipe geometry (diameter, wall thickness)
Different materials Different defect sizes (d, L, b)
Defect length, mm Defect width (circumferential), mm
Relative defect depth, d/t
12 6 0,25
24 18 0,5
48 42 0,62
150 60 0,72
282 0,85
402
498
![Page 14: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/14.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Definition of critical pressure values (pys, pyf, pF)
0
200
400
600
800
1000
1200
0 5 10 15 20 25
Pressure, MPa
Str
ess,
MP
a
Eq. stress Main stress SMYS SMYS+69 Rm'
ReH
Rm'
pys pyf pF
![Page 15: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/15.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Development of safety diagrams
Different representation possibilities (as a function of L/D, d/t, L or d)
E.g. normalisation of critical pressure values:
for pF-flawless=2.Rm'.t/(D-t) ,
1. norm - pys= pys/ pF- flawless,
2. norm - pyf= pyf/ pF- flawless,
3. norm - pF= pF/ pF- flawless,
4. norm - pü= pü/ pF- flawless.
![Page 16: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/16.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Normalised pressure values vs. L/D –comparison with the operation pressure
b=42; d/t=0.25
0.0
0.2
0.4
0.6
0.8
1.0
0 0.5 1 1.5
L/D
no
rm-p
, M
Pa
norm-pF; t=8
norm-pYs; t=8
norm-pYf; t=8
norm-pF; t=7,1
norm-pYs; t=7,1
norm-pYf; t=7,1
norm-pü (t=8)
norm-pü (t=7.1)
b=42; d/t=0.85
0.0
0.2
0.4
0.6
0.8
1.0
0 0.5 1 1.5
L/D
no
rm-p
, M
Pa
norm-pF; t=8
norm-pYs; t=8
norm-pYf; t=8
norm-pF; t=7,1
norm-pYs; t=7,1
norm-pYf; t=7,1
norm-pü (t=8)
norm-pü (t=7.1)
![Page 17: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/17.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Final safety diagramsA52K; D=323,9mm; t=5mm; B=6mm
0
1
2
3
4
5
6
7
8
9
10
0 0.2 0.4 0.6 0.8 1
d/t
p, M
Pa
L=12mm, Pys
L=24mm, Pys
L=48mm, Pys
L=150mm,Pys
L=282mm,Pys
L=402mm,PysL=498mm,Pys
Pü
For Pys
![Page 18: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/18.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
A52K; D=323,9mm; t=5mm; B=6mm
0
2
4
6
8
10
12
14
0 0.2 0.4 0.6 0.8 1
d/t
p, M
Pa
L=12mm, Pyf
L=24mm, Pyf
L=48mm, Pyf
L=150mm, Pyf
L=282mm, Pyf
L=402mm, Pyf
L=498mm, Pyf
Pü
For Pyf
![Page 19: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/19.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
For PF
A52K; D=323,9mm; t=5mm; B=6mm
6
8
10
12
14
16
18
0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9 1
d/t
p, M
Pa
L=12mm, PF
L=24mm, PF
L=48mm, PF
L=150mm, PF
L=282mm, PF
L=402mm, PF
L=498mm, PF
Pü
PF-1-1
PF-1-2
PF-1L1
L2
![Page 20: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/20.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Definition of safety factors
For the critical pressure values:
– n1=Pys/Pü for the beginning of plastic deformation
– n2=Pyf/Pü for the localisation of the plastic deformation
(contraction)
– n3=PF/Pü for the failure (plastic instability)
Operational safety? – combination of n1, n2, n3 –
application possibility of risk based approaches –
owner’s responsibility!
![Page 21: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/21.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Summary and conclusionSummary and conclusion FEM calculations gave more accurate prediction for the
failure pressure than engineering methods. The predicted failure pressure (based on FEM calculations)
were in good agreement with the pressure test results. Simplified defect geometries could be applied for predicting
the failure pressure, so it gives opportunity to perform large number of FEM calculations and development of safety diagrams.
With the application of the safety diagrams a proper safety evaluation system can be developed together with the owner.
Possibility for more complex safety assessment system and application of risk based principles.
![Page 22: Evaluation system for corrosion defects in pipelines](https://reader035.fdocuments.us/reader035/viewer/2022081503/568135d7550346895d9d46bc/html5/thumbnails/22.jpg)
Bay Zoltán Foundation for Applied ResearchInstitute for Logistics and Productgion Systems
BAY-LOGI
Köszönöm a figyelmüket!Köszönöm a figyelmüket!