mgo-c refractory selection and evaluation for ......the making, shaping and treating of steel, 11th...
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The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 153
MGO-C REFRACTORY SELECTION AND EVALUATION FOR
STEELMAKING VESSELS
J Terblanche
Arcelormittal
Abstract
The challenge for refractory material producers and consumers is to find the optimum
solution between the quality and cost of the product with its value in use.
Magnesia-Carbon (MgO-C) refractories in Steelmaking vessels play an important part to
reach continuous improvement targets. It will remain a focus area to increase campaign
length of vessels and reduce the cost per ton liquid steel produced.
Improvements of 20% can be achieved by using different quality MgO-C refractories.
1. Introduction
The Vanderbijlpark Works of ArcelorMittal, South Africa, consists of the
following:
• Integrated route with 3x 170t Basic Oxygen Furnaces (BOF), 2x Ladle
Furnaces (LF), 1x RH and 2x Twin strand slab casters with capacity of
2.9 mtpa.
• Minimill route with 3x 150t Electric Arc Furnace (EAF), 2x LF’s, 1x
Vacuum Arc Degasser and 1x Twin strand slab caster with capacity of 1.4
mtpa.
The 3 BOF’s are bottleneck units in the Oxygen Steelmaking Route and various
strategies have been implemented to manage the cost, availability and throughput
of this route. These include :
• Extend campaign length with slag splashing
• Maximum utilization of bottom stirring
The selection and properties of the MgO-C refractories used with these different
philosophies and varying operating conditions determine both the length of the
campaign achieved and the cost of the lining.
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 154
2. Background
The following operational conditions affect lining wear1 :
• Slag chemistry - Basicity
- MgO content
- FeO levels
• Size of scrap charged
• End point temperature
• Reblows
• Production Rates (i.e. heats per vessel per day)
• Holding time (blow end to tap start)
• Hot metal quality (limits total mass of fluxes that can be charged)
In order to optimally utilize or consume the refractories, the following maintenance
or repair techniques are utilized with the impact on performance indicated in Fig.1 :
• Gunning of localized high wear areas
• Slag coating : by keeping some slag in the vessel, adding MgO containing
material and tilting the furnace over the tap floor and charge pad areas.
• Slag splashing by blowing high pressure N2 via the top blown lance2 and
coating the complete surface with a slag layer.
The result achieved with such methods is determined by the time available and the
frequency of these activities. In the case of gunning, the durability can be extended
by using improved raw material and binder systems and for slag splashing, low
oxide- and higher MgO levels in the slag.
The drive to improve efficiencies and reduce costs resulted in a change of strategy.
Slag splashing was stopped and the focus changed to ensure bottom stirring
availability and efficiency for the full duration of the campaign. This leads to lower
campaign lengths as indicated in Fig. 1.
The higher refractory cost is countered by savings as a result of lower oxygen
levels in the steel and slag. Higher quality MgO-C bricks are required in order to
improve campaign lengths with little or no refractory maintenance (i.e. gunning and
splashing).
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 155
3. Lining Development
The different areas and wear mechanisms are displayed in Fig. 2 and
Table 11.
Fig 2 : BOF- wear areas
Fig 1 : BOF campaign history for Vanderbijlpark
-
500
1,000
1,500
2,000
2,500
3,000
3,500
4,000
2003 2004 2005 2006 2007 2008 2009
Heats
use of slag splashing
no splashing
Topcone
Knuckle
Charg
e P
ad
Charg
e p
ad
Tap p
ad
Tru
nnio
n W
Tru
nnio
n E
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 156
Table 1 : Furnace Area Wear Conditions
Furnace Area Wear Conditions
Cone Oxidizing atmosphere
Mechanical abuse
High temperature
Trunnions Oxidizing atmosphere
Slag corrosion
Slag and metal erosion
Charge Pad Mechanical impact
Abrasion from scrap and hot metal
Tap Pad Slag erosion
High temperature
Mechanical erosion
The Refractory performance can be improved by3:
• Design changes in : knuckle area
: cone area
: use of steel cladding
• Zoning of the furnace according to the different wear mechanisms and
material qualities.
4. Evaluation Process
The following tests were conducted :
• Rotor slag test : 300g slag per cycle, 10 cycles of 20 minutes each after
melting of slag
• Oxidation resistance : 50 x 50 x 75mm sample heated in air at 900°C or
1400°C for 8 hrs.
• 2 step rotor slag test : do 10 cycles, cool down and repeat.
4.1 Rotor slag test
Typical BOF slag was used to compare resistance to chemical attack
(Fig. 3). The depth of slag penetration (Fig 4) is important as this will increase the
wear rate during operation. The thermal expansion properties are different
compared to the virgin material which will lead to cracking of this layer during
thermal cycling.
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 157
4.2 Oxidation Resistance
Oxidation of fixed carbon and the binder system occurs during preheat and
operation. The white decarburized layer can be seen on the bricks during the
demolition process.
Both the depth of the oxidized layer and the condition of the oxidized layer are
compared (Fig 5)
Fig 3 : Rotor Slag Wear Ratio
1
1.61
1.071.00
1.59
1.09
0
0.2
0.4
0.6
0.8
1
1.2
1.4
1.6
1.8
B R C
Ra
tio
Ratio 10
Ave 20
Fig 4 : Slag Penetration Ratio 20 Cycles
1.00
1.22
0.81
0.00
0.20
0.40
0.60
0.80
1.00
1.20
1.40
B R C
Pe
ne
tra
tio
n R
atio
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 158
Fig 6 : Condition of oxidized layer
4.3 Two step rotor slag test
Both the global economic slump and normal throughput requirement affect plant
stability. This implies that the golden rule for good refractory performance - “keep
it hot” is not always adhered to. Depending on whether 2 or 3 furnaces are in
operation and with throughput variations from 20 to 54 heats per day, a furnace can
be used for 6 to 27 heats per day. To reduce this effect 1 or 2 furnaces can be
stopped from 8 hrs to a few days at a time. Depending on the production schedule
or maintenance requirement the spare furnace can be on hot or cold standby.
Fig 5 : Oxidation Depth after 4 Cycles @ 1400°C
11.51 12.5
8.61
0
2
4
6
8
10
12
14
B R C
De
pth
(m
m)
B : 2 cycles @ 1400°C R : 2 cycles @ 1400°C
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 159
Table 2 : BOF Operating parameters
2 Furnace Operation 3 Furnace operation
BOF 1 BOF 2 BOF 1 BOF 2 BOF 3
Number Of Casts 18 17 14 7 17
End Point C avg 0.03 0.04 0.04 0.04 0.04
End Point O2 avg 536 532 856 713 906
Slag TFe avg 15.4 15.5 21.9 17.2 20.9
Slag MgO avg 8.2 8.7 6.6 8.0 7.0
End Point Temperature avg 1672 1669 1669 1670 1669
Blow End To Tap Duration
avg 9 11 9 8 16
Tap To Tap avg 57 85 70 220 85
Basicity avg 3.2 3.0 2.9 2.9 3.1
Co-Product avg 19 21 31 26 32
Percentage reblow 5.6 29.4 7.1 14.3 11.8
To simulate this impact the 2 step rotor test was conducted. The result in wear and
condition of the samples after the 2nd
test is displayed in Fig 3.
5. Plant trial
Furnace layout
To evaluate the supplier - material combinations in a reliable trial, it was decided to
do panel tests in 1 furnace rather than to install complete linings in different
furnaces.
Fig 7. BOF Trial Zoning
R
B C
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 160
The life of the furnace will be determined by the highest wear area (material with
the lowest performance) and the campaign may end prematurely as a result of this.
The advantage however is that variations in operational parameters between
furnaces are excluded.
With this layout 2 qualities can be compared to a reference (and each other) on the
trunnion and tap floor area (the highest wear areas during the planning stage of the
trial).
6. Results
Wear profiles can be measured with the laser scanner during operation and results
are displayed in Fig 8 to 11 for the different areas. Extensive gunning maintenance
was started on the high wear areas after 1,000 heats and this is reflected in the data.
Fig 8 : Laser scan profile at heat 1,081
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 161
Fig 9 : Wear rate Tapfloor (mm/heat)
0
0.05 0.1
0.15 0.2
0.25 0.3
0.35 0.4
0.45
753 901 1081 1304
Scanned heats
Tapfloor W : R
Tapfloor W : C
Tapfloor E: R Tapfloor E : B
Fig 10 : Wear rate Trunnion East (mm/heat)
0
0.05 0.1
0.15 0.2
0.25 0.3
0.35 0.4
0.45 0.5
753 901 1081 1304
Scanned heats
Trun E : R
Trun E : B
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 162
Table 3 indicates the expected life of the furnace based on the remaining thickness
and the wear rate since the previous scan. It can be seen that trial quality B
performs better than both the reference and quality C, while quality C compares
well with the reference.
Table 3 : Campaign Forecast
Min Remaining Thickness (mm) = 50
Tap breast East Trunnion West Trunnion
heats
Tapfloo
r W : R
Tapfloo
r W : C
Tapfloo
r E : R
Tapfloo
r E : B
Trunnion
E : R
Trunnio
n
E : B
Trunnion
W : R
Trunnion
W : C
753 1,914 2,076 2,061 3,086 1,628 2,039 1,361 1,448
901 2,356 2,398 2,559 3,375 1,747 2,099 1,504 1,365
1,081 2,045 2,144 2,331 2,950 2,616 3,066 1,547 1,486
Improvement vs
R per area at
901 heats before
gunning started
101.8%
131.9%
120.2%
90.8%
7. Conclusion
Both the Pilot Plant tests and Plant trials indicated a difference in performance of
supplier - quality combinations.
Fig 11 : Wear rate Trunnion West (mm/heat)
0.3
0.4
0.5
0.6
0.7
753 901 1081 1304
Scanned heats
Trun W : R
Trun W : C
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 163
It is possible to achieve up to 20% improvement in the life of the BOF at
Vanderbijlpark by using different qualities MgO-C material.
With changing market conditions the impact of availability and opportunity costs
will have an effect on the selection of Refractory materials in the Steelmaking
Vessels.
Acknowledgement
1. J. Victor for conducting the various tests and reporting of the data.
2. R. Nyamane and the reline crews for the installation of the lining.
3. The crew from MTSA for calibration of the scanner, regular scanning and gunning
maintenance.
4. Me I. de Villiers for the typing and layout of the report.
5. ArcelorMittal for the opportunity to grow as an individual by enabling us to do
development work.
Reference
1. The Making, Shaping and Treating of Steel, 11th
Edition, Steelmaking and Refining
volume P227 - 243
2. Everlasting BOF linings at LTV steel, R.O. Russel a.o. LTV steel company,
Independence, Ohio – USA P220-225
3. Refractories performance improvements – meeting the competitive challenge, Ian
N Mackay, Institute of Refractories Engineers Annual conference, 23 Sept 1994.
The Author
Johan Andries Terblanche, Project Manager, Refractories, Operational Excellence,
ArcelorMittal, South Africa
1986 : B Eng in Metallurgy from PU for CHE, Vaal Triangle Campus
1990-1991 : Production Engineer BOF, Iscor, Vanderbijlpark
The Southern African Institute of Mining and Metallurgy
Refractories 2010 Conference
J Terblanche
________________________________________________________________________
Page 164
1992-1997 : Manager Development, Refractory Services, Iscor, Vanderbijlpark
1998 : Production Manager,v1v2 Continuous Caster, Iscor, Vanderbijlpark
1999-2006 : Plant Manager, Refractory Services, ArcelorMittal, Vanderbijlpark
2007 Project Manager, Refractories,CTO, ArcelorMittal, South Africa