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Multiphysics Modeling of the Graphite
Electrode Joint in Electric Arc Furnaces
for Scrap Steel Recycling
Nathan May
James Glickstein
Maren Waldner
1
Problem Statement
• The Electric Arc Furnace
(EAF) uses graphite rods
as electrodes to strike a
powerful arc to melt
scrap steel
• GrafTech International is
a world leader in
supplying graphite
electrodes for the EAF
process
2
Problem Statement
• The Electric Arc Furnace (EAF) is a massive
industrial process, converting scrap steel into new
raw material (millions of tons per year worldwide)
• Less greenhouse gas emissions versus Basic Oxygen
Furnace steelmaking process (BOF, “Blast Furnace”)
[1]
• BOF: 1.6 tonnes CO2/tonne steel
• EAF: 1.08 tonnes CO2/tonne steel
[1] US EPA, AVAILABLE AND EMERGING TECHNOLOGIES FOR REDUCING GREENHOUSE GAS EMISSIONS
FROM THE IRON AND STEEL INDUSTRY, Sept 2012, https://www.epa.gov/sites/production/files/2015-
12/documents/ironsteel.pdf
3
Problem Statement
• Previous finite element models have been very valuable
to GrafTech’s electrode business
• Previous models were relatively simple and coarse; new
software and hardware enable next-generation of FEM
• Develop a multiphysics model of the electrode joint,
including:
• Structural mechanics and contact physics
• Heat transfer
• Electric currents
• Validate model through comparison with real data
• Better understand process/performance relationships
• Reduce design cycle time
4
Problem Statement
Power Cables
Electrode Clamp
Furnace Lid
Graphite Electrode
Electrode Joint
Steel Pile
5
Problem Statement
Power Cables
Electrode Clamp
Furnace Lid
Graphite Electrode
Electrode Joint
Arc
Steel Melt
6
Failure Mechanism: Stub Loss
7
Internal
Threaded
Pin
High
Thermal
Stresses
Stub Loss
Failure Mechanism: Oxidation
Graphite reacts with
oxygen at high temp
to form CO2 Characteristic
“oxidation
profile” taper
Some materials/furnace
conditions cause faster
oxidation
8
Failure Mechanism: Column Break
Internal
Threaded
Pin
Bending force
from scrap pile
Internal
Threaded
Pin
Bending force
from scrap pile
9
Problem Statement
• Graphite Electrode consumption is a significant cost driver
of EAF, in particular:
• Stub loss: the tip of the electrode can crack and cause chunks of
electrode to fall into the melt
• Oxidation: furnace temperature is well over 1000 degC, and
graphite oxidizes into CO2 rapidly at this temperature
• Column breaks: “scrap cave-ins” or poor electrode addition exert
bending stress on column, leading to breaks high up and major
process disruption
• Successive electrodes are connected at a “joint,” which
becomes a critical point for reducing failure
• Because of the extreme environment, direct measurements
are often difficult or impossible
• Graphite is a non-homogenous, anisotropic material
• Multiscale (>8 meters electrode and <10 microns defects)
and multiphysics situation
10
Approach
• Make a model that considers all three failure
mechanisms!
• Used COMSOL Multiphysics v5.3 (model developed in
v5.0)
• Structural Mechanics module
• Heat Transfer module
• Electric Current module
• Moving Mesh module
• 2D Axisymmetric model:
• Stationary pre-tensioning simulation
• Transient multiphysics simulation of firing cycle
• 3D model:
• Bending stress simulation
• Transient multiphysics simulation of non-axisymmetric modes
11
Model Scheme
12
Flowing water
w/phase change
Radiation from
electric arc
Radiation and powerful
convection from hot
furnace
Contact physics for
solid mechanics, heat
transfer, and electric
currents
Electric terminal
Model Validation
• Results were used on a comparative
basis, in particular comparing the
stress states of known failure
location across different cases
• Used a variety of stress metrics,
focusing on tresca and maximum
principle stress criteria
• Focus on joint area as most
common failure location
• Completed hundreds of simulations
of different cases, grouped into
about ten study areas
13
Stub Loss versus Firing Cycle
• EAF process has a
characteristic firing cycle
• Involves heating and cooling
segments
• Causes significant thermal
stresses from temperature
and material gradients
14
Stub Loss versus Firing Cycle
• EAF process has a
characteristic firing cycle
• Involves heating and cooling
segments
• Causes significant thermal
stresses from temperature
and material gradients
15
Stub Loss versus Firing Cycle
• EAF process has a
characteristic firing cycle
• Involves heating and cooling
segments
• Causes significant thermal
stresses from temperature
and material gradients
16
Stub Loss versus Firing Cycle
17
• EAF process has a
characteristic firing cycle
• Involves heating and cooling
segments
• Causes significant thermal
stresses from temperature
and material gradients
• Our analysis involves
comparing these stresses at
different times and places
Oxidation
• Water flows from
clamps down the
exterior of the electrode
• Reduces temperature
• Provides barrier to
oxygen migration
• Too much water flow
can shift energy balance
unfavorably
18
Oxidation
• Dependent on several factors:
• Furnace type
• Furnace oxygen/inert gas usage
• Furnace power settings
• Water cooling
• Deep multiphysics coupling is
required
• Simulate water as a phase-
change domain (built-in to
COMSOL), but with constant
velocity field
19
Oxidation
20
No Water Flow With Reference
Water Flow
Oxidation
21
With Reference
Water Flow
• Use in-house testing to
develop temp vs oxidation
rate curves
• Integrate vs temperature
and time
• Simulate total oxidation
• Test different materials’
oxidation rates, simulate
consumption rate savings
• Predicted oxidation rates
match reality quite well
Electrode Bending
22
Bending force from
scrap pile
3D Cases
• 3D geometry is required for
bending and other stress
states
• Results make the model
even more powerful,
though require increasingly
demanding hardware
• Model DoF/memory can
exceed 2e7/350 Gb
• Results are very useful in
understanding column
breaks
23
Future Work
24
• Already a useful design and
engineering tool for GrafTech
• More 3D simulations!
• Deeper sensitivity analysis vs
furnace conditions and
materials
• Crack propagation and failure
at high temperature
• Cohesive zone debonding
• Physical testing/comparison
with DIC
Future Work
25
• Already a useful design and
engineering tool for GrafTech
• More 3D simulations!
• Deeper sensitivity analysis vs
furnace conditions and
materials
• Crack propagation and failure
at high temperature
• Cohesive zone debonding
• Physical testing/comparison
with DIC
¿Questions?
Thank you for listening!
26
Thanks to Josh Thomas of
AltaSim for help setting up
early model version!
Model Validation
27
Oxidation
• Oxidation is the baseline driver of
graphite electrode consumption
rates
• Around half of electrode baseline
consumption is wasted as oxidation
• Improved technology has steadily
reduced oxidation rates, but more
can be achieved!
• Water cooling is one key reducer of
oxidation
• Modeling can help us understand
key operating parameters to control
and limit oxidation
28

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may_presentation.pdf

  • 1. Multiphysics Modeling of the Graphite Electrode Joint in Electric Arc Furnaces for Scrap Steel Recycling Nathan May James Glickstein Maren Waldner 1
  • 2. Problem Statement • The Electric Arc Furnace (EAF) uses graphite rods as electrodes to strike a powerful arc to melt scrap steel • GrafTech International is a world leader in supplying graphite electrodes for the EAF process 2
  • 3. Problem Statement • The Electric Arc Furnace (EAF) is a massive industrial process, converting scrap steel into new raw material (millions of tons per year worldwide) • Less greenhouse gas emissions versus Basic Oxygen Furnace steelmaking process (BOF, “Blast Furnace”) [1] • BOF: 1.6 tonnes CO2/tonne steel • EAF: 1.08 tonnes CO2/tonne steel [1] US EPA, AVAILABLE AND EMERGING TECHNOLOGIES FOR REDUCING GREENHOUSE GAS EMISSIONS FROM THE IRON AND STEEL INDUSTRY, Sept 2012, https://www.epa.gov/sites/production/files/2015- 12/documents/ironsteel.pdf 3
  • 4. Problem Statement • Previous finite element models have been very valuable to GrafTech’s electrode business • Previous models were relatively simple and coarse; new software and hardware enable next-generation of FEM • Develop a multiphysics model of the electrode joint, including: • Structural mechanics and contact physics • Heat transfer • Electric currents • Validate model through comparison with real data • Better understand process/performance relationships • Reduce design cycle time 4
  • 5. Problem Statement Power Cables Electrode Clamp Furnace Lid Graphite Electrode Electrode Joint Steel Pile 5
  • 6. Problem Statement Power Cables Electrode Clamp Furnace Lid Graphite Electrode Electrode Joint Arc Steel Melt 6
  • 7. Failure Mechanism: Stub Loss 7 Internal Threaded Pin High Thermal Stresses Stub Loss
  • 8. Failure Mechanism: Oxidation Graphite reacts with oxygen at high temp to form CO2 Characteristic “oxidation profile” taper Some materials/furnace conditions cause faster oxidation 8
  • 9. Failure Mechanism: Column Break Internal Threaded Pin Bending force from scrap pile Internal Threaded Pin Bending force from scrap pile 9
  • 10. Problem Statement • Graphite Electrode consumption is a significant cost driver of EAF, in particular: • Stub loss: the tip of the electrode can crack and cause chunks of electrode to fall into the melt • Oxidation: furnace temperature is well over 1000 degC, and graphite oxidizes into CO2 rapidly at this temperature • Column breaks: “scrap cave-ins” or poor electrode addition exert bending stress on column, leading to breaks high up and major process disruption • Successive electrodes are connected at a “joint,” which becomes a critical point for reducing failure • Because of the extreme environment, direct measurements are often difficult or impossible • Graphite is a non-homogenous, anisotropic material • Multiscale (>8 meters electrode and <10 microns defects) and multiphysics situation 10
  • 11. Approach • Make a model that considers all three failure mechanisms! • Used COMSOL Multiphysics v5.3 (model developed in v5.0) • Structural Mechanics module • Heat Transfer module • Electric Current module • Moving Mesh module • 2D Axisymmetric model: • Stationary pre-tensioning simulation • Transient multiphysics simulation of firing cycle • 3D model: • Bending stress simulation • Transient multiphysics simulation of non-axisymmetric modes 11
  • 12. Model Scheme 12 Flowing water w/phase change Radiation from electric arc Radiation and powerful convection from hot furnace Contact physics for solid mechanics, heat transfer, and electric currents Electric terminal
  • 13. Model Validation • Results were used on a comparative basis, in particular comparing the stress states of known failure location across different cases • Used a variety of stress metrics, focusing on tresca and maximum principle stress criteria • Focus on joint area as most common failure location • Completed hundreds of simulations of different cases, grouped into about ten study areas 13
  • 14. Stub Loss versus Firing Cycle • EAF process has a characteristic firing cycle • Involves heating and cooling segments • Causes significant thermal stresses from temperature and material gradients 14
  • 15. Stub Loss versus Firing Cycle • EAF process has a characteristic firing cycle • Involves heating and cooling segments • Causes significant thermal stresses from temperature and material gradients 15
  • 16. Stub Loss versus Firing Cycle • EAF process has a characteristic firing cycle • Involves heating and cooling segments • Causes significant thermal stresses from temperature and material gradients 16
  • 17. Stub Loss versus Firing Cycle 17 • EAF process has a characteristic firing cycle • Involves heating and cooling segments • Causes significant thermal stresses from temperature and material gradients • Our analysis involves comparing these stresses at different times and places
  • 18. Oxidation • Water flows from clamps down the exterior of the electrode • Reduces temperature • Provides barrier to oxygen migration • Too much water flow can shift energy balance unfavorably 18
  • 19. Oxidation • Dependent on several factors: • Furnace type • Furnace oxygen/inert gas usage • Furnace power settings • Water cooling • Deep multiphysics coupling is required • Simulate water as a phase- change domain (built-in to COMSOL), but with constant velocity field 19
  • 20. Oxidation 20 No Water Flow With Reference Water Flow
  • 21. Oxidation 21 With Reference Water Flow • Use in-house testing to develop temp vs oxidation rate curves • Integrate vs temperature and time • Simulate total oxidation • Test different materials’ oxidation rates, simulate consumption rate savings • Predicted oxidation rates match reality quite well
  • 23. 3D Cases • 3D geometry is required for bending and other stress states • Results make the model even more powerful, though require increasingly demanding hardware • Model DoF/memory can exceed 2e7/350 Gb • Results are very useful in understanding column breaks 23
  • 24. Future Work 24 • Already a useful design and engineering tool for GrafTech • More 3D simulations! • Deeper sensitivity analysis vs furnace conditions and materials • Crack propagation and failure at high temperature • Cohesive zone debonding • Physical testing/comparison with DIC
  • 25. Future Work 25 • Already a useful design and engineering tool for GrafTech • More 3D simulations! • Deeper sensitivity analysis vs furnace conditions and materials • Crack propagation and failure at high temperature • Cohesive zone debonding • Physical testing/comparison with DIC
  • 26. ¿Questions? Thank you for listening! 26 Thanks to Josh Thomas of AltaSim for help setting up early model version!
  • 28. Oxidation • Oxidation is the baseline driver of graphite electrode consumption rates • Around half of electrode baseline consumption is wasted as oxidation • Improved technology has steadily reduced oxidation rates, but more can be achieved! • Water cooling is one key reducer of oxidation • Modeling can help us understand key operating parameters to control and limit oxidation 28