presentación de powerpoint - sim&tec · invap. 2.14 2.16 2.18 2.20 2.22 2.24 2.26 2.28 2.30...
TRANSCRIPT
![Page 1: Presentación de PowerPoint - Sim&Tec · INVAP. 2.14 2.16 2.18 2.20 2.22 2.24 2.26 2.28 2.30 2.32 0 100 200 300 400 500 600 700 Distance from the stand center [mm]] Measurements Hot](https://reader033.vdocument.in/reader033/viewer/2022060823/609d2c7ee43e6f5e7e211472/html5/thumbnails/1.jpg)
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Modeling for:
❑ Aero and Astro industry
❑ Construction industry
❑ Oil and gas industry
❑ Steel industry
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BW Offshore | https://bwoffshore.com/
EPRI | http://www.epri.com
ExxonMobil Upstream Research Co. | http://www.exxonmobil.com
FAdeA S.A. | http://www.fadeasa.com.ar
Instituto Nacional de Tecnología Industrial (INTI) | http://www.inti.gov.ar
INVAP S.E. | http://www.invap.com.ar
Nucleoeléctrica Argentina S.A. (NA-SA) | http://www.na-sa.com.ar
Patagonia Shales Services | http://www.patss.com.ar
PTC-Alliance | http://www.ptcalliance.com/
QUIP | http://www.quip.com.br
REPSOL-Bolivia | http://www.repsol.com
ROCH S.A. | http://www.roch.com.ar/
Socotherm Americas | http://www.socotherm.com.ar
TECHINT E&C | http://www.techint-ingenieria.com/
TENARIS | http://www.tenaris.com
TERNIUM | http://www.ternium.com
Tubo Trans Electric S.A. | http://www.ttesa.com.ar
Veng S.A. | http://www.conae.gob.ar
YPF | http://www.ypf.com
YTEC S.A | http://www.ypf.com/ypfylaindustria/YPFTecnologia/Paginas/YPF-Tecnologia-S-A.aspx
3
OUR CUSTOMERS
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Applications
1. Collapse of tubular products
2. Flexible risers: meso-scale model
3. SAGD pipes
4. OCTG threaded connections
5. Sucker rod connections
6. Modeling of hydraulic fracturing
7. Fracture of mechanical components
8. Composite pressure vessels (COPVs)
9. Sloshing
10.Vibrations in FPSO Starboard Crane
11.Satellite structures
12.Metal forming - METFOR
13.CFD
14.FSI: LNG pipeline at Dunkerque
15.FSI: Heat exchanger
5
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Collapse of tubular products
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Comparison: numerical vs. experimental results
Buckle arrestors: flattening mode
TENARIS7
Collapse of tubular products
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Comparison: numerical vs. experimental results
Buckle arrestors: flipping mode
8
Collapse of tubular products
TENARIS
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Flexible risers: meso-scale model
9Exxon Upstream Research Co.
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Torsion Test #1
0
2000
4000
6000
8000
10000
12000
14000
16000
18000
20000
22000
24000
26000
28000
30000
32000
0 5 10 15 20 25 30 35 40 45 50 55 60 65 70 75 80 85 90 95 100 105 110
Twisted Angle over the slotted section (degrees)To
rque
(ft-l
bs)
Experimental
FEM
Comparison: numerical vs. experimental results
10
SAGD pipes
TENARIS
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OCTG Premium Connections: tensile test
disp = 10.60 mm
disp = 16.60 mm
disp = 20.06 mm
disp = 31.91 mm
disp = 46.72 mm
disp = 5.77 mm
disp = 4.10 mm
Make Up
disp = 52.65 mm
11
OCTG threaded connections
TENARIS
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OCTG threaded connections
TENARIS
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Relative principal stresses
Tpi/Ty
(Ty = 59,77 kg/mm2)
Detail of the
threaded
area
Detail of the
threaded
area
API Design
Principal stress I
New Design
Principal Stress I
Premium connections design
13
Sucker rod connections
TENARIS
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Sucker rod connections
TENARIS
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Modeling of hydraulic fracturing
Brazilian test with a slot
Mohr Coulomb
Drucker
Prager
(inner)
Drucker Prager (outter)
Maximum
tension
Model validation: numerical simulation with different material models
YTEC
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Modeling of hydraulic fracturing
YTEC
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0
10
20
30
40
50
60
70
80
90
0 1 2 3 4 5 6
Frac
ture
len
gth
[m]
Time [sec]
Arbitrary mesh
Structured mesh
17
Modeling of hydraulic fracturing
YTEC
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KGD
18
Modeling of hydraulic fracturing
YTEC
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y
x
z
Penny Shape
19
Modeling of hydraulic fracturing
YTEC
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Penny Shape
20
Modeling of hydraulic fracturing
YTEC
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Modeling of hydraulic fracturing
Sequential fractures
YTEC
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Simultaneous fractures
22
Modeling of hydraulic fracturing
YTEC
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Modeling of hydraulic fracturing
Simultaneous fractures
YTEC
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Modeling of hydraulic fracturing
Simultaneous fractures
YTEC
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Fracture of mechanical components
ALUAR
Clam bucket
Maximum Damage 19%
Interface damage (%)
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Stresses in different layers
#1𝝋 = 𝟒. 𝟖°
#1𝜑 = 26°
#1𝜑 = 48°
#1𝜑 = 72°
Composite pressure vessels (COPVs)
VENG
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50 lt vessel burst test
Test burst pressure :
Pe = 54 MPa
FEM burst pressure :
PMEF =52 MPa
PMEF / Pe = 0.963
27
Composite pressure vessels (COPVs)
VENG
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Sloshing
VENG
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Damper locations
29
Vibrations in FPSO Starboard Crane
BW Offshore
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-1,50E+05
-1,00E+05
-5,00E+04
0,00E+00
5,00E+04
1,00E+05
1,50E+05
23,00 23,50 24,00 24,50 25,00 25,50 26,00 26,50 27,00
Forc
e [N
]
Time [s]
Force - Damper 1
Damper #1 FEM Model Response Damper #1 load pin damper adquisition
-1,50E+05
-1,00E+05
-5,00E+04
0,00E+00
5,00E+04
1,00E+05
1,50E+05
23,00 23,50 24,00 24,50 25,00 25,50 26,00 26,50 27,00
Forc
e [N
]
Time [s]
Force - Damper 2 Damper #2 FEM Model Response
Damper #2 load pin damper adquisition
30
Vibrations in FPSO Starboard Crane
BW Offshore
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Arsat
31
Satellite structures
INVAP
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Thermoelastic analysis Dynamic Analysis
32
Satellite structures
INVAP
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Shaker adapter
33
Satellite structures
INVAP
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2.14
2.16
2.18
2.20
2.22
2.24
2.26
2.28
2.30
2.32
0 100 200 300 400 500 600 700
Distance from the stand center [mm]
Thic
knes
s [m
m]
Measurements
METFOR
Hot rolling of flat products
34
Metal forming - METFOR
TENARIS
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The Mannesmann piercing process
35
Metal forming - METFOR
TENARIS
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Metal forming - METFOR
TENARIS
The Mannesmann piercing process
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Airplane wing
37
CFD
FAdeA
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CFD
FAdeA
Airplane wing
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• fixed at inletP1-inletP2-outletP7.
• fixedNormalDisplacement at Supports.
Supports length – 0.20m
Fluid mesh and BC Solid mesh and BC
Mass Flow Inlet P1Mass Flow Inlet P2
Pressure Outlet P7
Mass Flow = 0 kg/s
FSI: LNG pipeline at Dunkerque
TECHINT E&C
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Inlet P1
Inlet P2
FSI: LNG pipeline at Dunkerque
TECHINT E&C
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FSI: LNG pipeline at Dunkerque
TECHINT E&C
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Fluid Mesh Solid Mesh
FSI: Heat exchanger
TECHINT E&C
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Fluid Velocities
TECHINT E&C
FSI: Heat exchanger
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Solid Stresses
Central Section Near first baffle Section
TECHINT E&C
FSI: Heat exchanger
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