Title of Invention

HEAT-RESISTANT STEEL

Abstract A high temperature corrosion resistant stainless steel having a composition (by weight) of: C ≤ 0.2%, but more than zero, N ≤ 0.1% but more than zero, O ≤ 0.1% but more than zero, Si ≤ 0.4% but more than zero, Al ≤ 0.5% but more than zero, Mn ≤ 0.5% but more than zero, Cr 20 to 25%, Ni ≤ 2.0% but more than zero, Zr + Hf 0,01 to 0.1%, Ti ≤ 0.5% but more than zero, Mo + W ≤ 2.5% but more than zero, Nb + Ta ≤ 1.25% but more than zero, V ≤ 0.5% but more than zero, and balance of Fe and naturally occurring impurities and not more than 0.010% of S impurity. This steel is particularly suitable for the manufacturing of interconnects in solid oxide fuel cells.
Full Text FIELD OF THE DISCLOSURE
The present disclosure relates generally to a steel product, which at
high temperatures forms an oxide scale with good surface conductivity and
an excellent adhesion to the underlying steel. In particular, it relates to a
ferritic chromium steel suitable for the use as interconnects or bipolar plates
in solid oxide fuel cells or other high temperature applications such as
catalytic converters in cars and trucks.
BACKGROUND
Ferritic chromium steels are used for applications with high
requirements on heat resistance, such as for example interconnect materials
in Solid Oxide Fuel Cells (SOFC) or if alloyed with Al, as a material for
catalytic converters. They are very suitable materials for use in SOFC
applications since the Thermal Expansion Coefficients (TEC) of ferritic steels
are close to the TECs of the electro-active ceramic materials used in the
SOFC stack, such as yttrium-stabilized zirconia (YSZ) which is the common
material used as electrolyte in the fuel cell. This has/for instance, been
studied by Linderoth et al. in "Investigation of Fe-Cr ferritic steels as SOFC
interconnect material", Mat. Res. Soc. Symp. Proa, Vol. 575, (1999), pp.
325-330.
It is desired that the oxide scale formed on the steel interconnect
material does not spall off or crack due to thermal cycling, i.e., the oxide
scale should have good adhesion. The formed oxide scale should also have
good electrical conductivity and not grow too thick during the life time of the
fuel cell, since thicker oxide scales will lead to an increased electrical
resistance. The formed oxide should also be chemically resistant to the
gases used as fuels in an SOFC, i.e., no volatile metal-containing species
such as chromium oxyhydroxides should be formed. Volatile species such
as chromium oxyhydroxide will contaminate the electro-active ceramic
materials in a SOFC stack, which will lead to a decrease in the efficiency of
the fuel cell.
One disadvantage with the use of commercial ferritic chromium steel
is that they are usually alloyed with aluminum and/or silicon, which form
AI2O3 and/or SiO2 at the working temperature of the SOFC. Both these
oxides are good electrical insulating oxides, which will increase the electrical
resistance of the cell and lower the fuel cell efficiency.
This has led to the development of ferritic steels with low Al and Si
contents, to ensure good conductivity of the formed oxide scales. These
newly developed steels are usually also alloyed with manganese. The
addition of Mn in the steel will induce the formation of chromium oxide based
spinell structures in the formed oxide scale. However, Mn in general has a
poor effect on the corrosion resistance of the steel; it is therefore desired that
the Mn content in the steel be monitored carefully at low levels. Too high a
concentration of Mn in the steel will lead to the growth of thick oxide scales
due to severe high temperature corrosion.
In addition to Mn, several of these new developed steels are alloyed
with group III elements, i.e., Sc, La and Y and/or other rare earth elements
(REM). The addition of La, Y or REM is made to increase the lifetime of the
material at high temperatures. Strong oxide formers such as La, Y and REM
are said to decreases the oxygen ion mobility in the formed Cr2O3 scale,
which will lead to a decrease in the growth rate of the oxide scale. The
amount of added REM to the'steel has to be carefully monitored, since too
high a concentration of REM will lead to production process difficulties, as
well as undesired corrosion properties of the steel.
In patent application US 2003/0059335, the steel is alloyed with a
small amount of La (0.01 - 0.4% by weight) and optionally also with small
amounts of Y and Ce (0.1 to 0.4% by weight).
In patent application EP 1 298 228 A2, the steel is also alloyed with
either Y (= 0.5% by weight) or REM (= 0.2% by weight) or La (0.005 - 0.1%
by weight).
In US 6,294,131 B1, the steel is also alloyed with REM (0.005 to 0.5
% by weight) and in patent application US 2002/0192468 A1 the final steel is
alloyed with 0.01 - 1.5% yttrium, rare earth metals, and oxides thereof.
In addition to these above-mentioned patents, there are some
commercially available ferritic steel for interconnects in SOFC. Two of these
are the steel sorts A and B (see further details of A and B in Example 3
below), A being alloyed with 0.04% La, and B with a La content of max 0.2%
by weight. All the above mentioned patents and commercially available
steels are alloyed with small amounts of rare earth metals such as Y, La and
Ce. The addition of reactive rare earth metals will lead to a decrease in
corrosion resistance compared with the steel alloy of this invention.
SUMMARY
It is an object of the present invention to provide a steel alloy with
excellent high temperature corrosion resistance. Another object of the
present invention is that the oxide scale on said steel alloy has a good
adherence and a low surface resistivity. A further object of the present
invention is that the above mentioned properties are so good that said alloy
does not need alloying with any REM or group'III metals, which in turn will
lead to a simpler and more cost-effective steel production process. Yet
another object of the present invention is to provide a steel alloy for the
manufacturing of interconnects and/or bi-polar plates to Solid Oxide Fuel
Cells. A further object of the present invention is to provide a steel alloy for
the manufacturing of catalytic converters in automobile applications.
The above objects and further advantages are achieved by carefully
monitoring the contents of different alloying elements of the steel alloy, in
accordance with claim 1. This is done by alloying the steel with 20 to 25%
by weight of chromium and monitoring the content of oxide formers such as
silicon, aluminum and manganese at low levels. In addition to this,
elements, such as Ni, Mo and group IV (titanium group) and group V
elements (vanadium group) of the periodic table of elements, are added to
the alloy. Said alloy is produced in a conventional steel production process.
The final product of said alloy can have the form of a strip, foil, wire, tube,
bar or even as a powder, preferably as strip or a foil.
One factor is that said alloy is heat resistant at temperatures up to
900°C and that the oxide scale formed does not grow too thick. Therefore,
the mass gain per unit area of said alloy is less than 1.5 mg/cm2, when the
steel alloy has been oxidized in air or in air +1% H2O mixture for 1000 hours
at 850°C or any environment similar to the gases used in a Solid Oxide Fuel
Cell. A further aspect is that the grown oxide scale does not spall off, i.e.,
has a good adhesion to the underlying alloy.
To be able to use the steel alloy as interconnect or bipolar plate in
SOFC, the thermal expansion of said alloy should not deviate considerably
from the thermal expansions of the anode material or the electrolyte material
used in the fuel cell. Therefore, said alloy has a thermal expansion
coefficient of 10 to 15-10-6oC -1 in the temperature range 0 to 900°C, or even
more preferably 11 to 14 10-6oC -1 and most preferably 11.5 to 13-10-6 °C-1.
As a consequence thereof, the thermal expansion mismatch (TEM) between
the electro-active ceramic materials in the fuel cell and the thermal
expansion of said alloy is not greater than ± 25%, or preferably less than ±
20%, or most preferred lower than ± 15%. Here the thermal expansion
mismatch (TEM) is defined as (TECSS - TECce)/TECSs, where the TECSS is the
thermal expansion of the steel alloy and TECce is the thermal expansion of
the electro-active ceramic materials used in anode-supported fuel cells.
Yet another important object is that said alloy has a good conductivity.
The bipolar plate works as a current collector in a fuel cell. To avoid
degradation of the fuel cell efficiency, the contact resistance of the steel alloy
is kept as low as possible throughout the lifetime of the fuel cell. The area
specific resistance (ASR) of said alloy in a SOFC setup should be kept low
but also the increment of ASR with time is kept as low as possible. If the
increment of the ASR is large, this can lead to a decrease of the fuel cell
efficiency.
BRIEF DESCRIPTION OF THE FIGURES
Figure 1 shows the weight gain per unit area plotted vs. time of an
exemplary embodiment of a disclosed steel alloy, together with the four steel
alloys (Sandvik ID numbers 433, 434, 436 and 437) produced for
comparison, oxidized in air for 336, 672 and 1008 hours, respectively.
Figure 2 shows a SEM cross-section micrograph of the oxide scale
formed on an exemplary embodiment of a disclosed steel alloy oxidized in
air for 336 hours at 850°C.
Figure 3 shows a Glow Discharge Optical Emission Spectroscopy
(GDOES) depth profile of the oxide scale formed on an exemplary
embodiment of a disclosed steel alloy oxidized in air for 336 hours at 850°C.
Figure 4 shows the weight gain per unit area for eight different steel
grades including an exemplary embodiment of a disclosed steel alloy and
the four steel alloys (Sandvik ID numbers 433, 434, 436 and 437) produced
for comparison after oxidization in air +1% H2O at 850°C after 500 hours.
DETAILED DESCRIPTION
Chemical Composition: The chemical composition of the steel alloy consists
essentially of (by weight-%):
C = 0.2% but more than zero, preferably 0.001 = C = 0.2%
N = 0.1% but more than zero, preferably 0.001 = N = 0.1%
O = 0.1% but more than zero, preferably 0.001 = O = 0.1%
Si = 0.4% but more than zero, preferably 0.01 = Si = 0.4%
Al = 0.5% but more than zero, preferably 0.001 = Al = 0.5%
Mn = 0.5% but more than zero, preferably 0.01 = Mn = 0.5%
Cr 20 to 25%
Ni = 2.0% but more than zero, preferably 0.01 = Ni = 2.0%
Zr + Hf = 0.1% but more than zero, preferably 0.001 = Zr + Hf =
0.1%
Ti = 0.5% but more than zero, preferably 0.01 = Ti = 0.5%
Mo + W =, 2.5% but more than zero, preferably 0.01 = Mo +W = 2.5%
or even more preferably 0.1 =, Mo+W= 2.0%
Nb + Ta = 1.25% but more than zero, preferably 0.01 = Nb + Ta =
1.25%
V = 0.5% but more than zero, preferably 0.01 = V = 0.5%
and balance of Fe and naturally occurring impurities, but not more
than 0.010% of S impurity. Said alloy is produced in an ordinary steel
production process.
In one exemplary embodiment of the disclosed steel alloy, the
chemical composition comprises the following elements (by weight-%):
C = 0.1% but more than zero, preferably 0.001 = C = 0.1%
N = 0.1% but more than zero, preferably 0.001 = N = 0.1%
O = 0.1% but more than zero, preferably 0.001 = O = 0.1%
Si = 0.4% but more than zero, preferably 0.01 = Si s 0.4%
Al = 0.4% but more than zero, preferably 0.001 = Al = 0.4%
Mn = 0.4% but more than zero, preferably 0.01 = Mn = 0.4%
Cr 20 to 25%
Ni = 1.0 % but more than zero, preferably 0.01 = Ni = 1.0%
Zr = 0.1% but more than zero, preferably 0.001 = Zr = 0.1%
Ti = 0.5% but more than zero, preferably 0.01 = Ti = 0.4%
Mo = 2.5% but more than zero, preferably 0.01 = Mo = 2.5% or even
more preferably 0.1 = Mo = 2.0%
Nb = 1.25% but more than zero, preferably 0.01 = Nb = 1.25%
V = 0.1 % but more than zero, preferably 0.01 = V = 0.1%
and balance of Fe and naturally occurring impurities, but not more
than 0.010 % of S impurity. Said alloy is produced in an ordinary steel
production process.
High Temperature Corrosion Resistance: The disclosed alloy is heat
resistant at temperatures up to 900°C and the oxide scale formed upon
oxidization does not grow too thick. In Table 1, the theoretical mass gain per
area unit for a chromium oxide scale with different thicknesses is calculated.
The calculations assume that a dense and pure Cr2O3 scale.is formed on the
surface of the steel. The Cr2O3 has a density of 5300 mg/cm3 and the mass
percent of oxygen in the Cr2O3 is 31.6%. This will gjve a mass gain per unit
area of 0.16 mg/cm2 for a 1 µm thick pure and dense chromium oxide scale,
and 0.82 mg/cm2 for 5 µm thick oxide scale.
Noted here should be that these values of mass gain of the formation
of pure Cr2O3 are theoretical. When a ferritic chromium steel alloy is
oxidized, usually mixed oxides are formed and the weight gain depends on
the added alloying elements. However, a low weight gain is important since
higher weight gains will lead to thicker oxide scale formations, which in turn
will increase the resistance of the steel. The disclosed steel alloy therefore
has a weight gain of less than 1.5 mg/cm2 after 1000 hours of exposure to
air and/or air + 1% H2O at 850°C.
A further feature is that the grown oxide scale does not spall off, i.e.,
has a good adhesion to the underlying alloy.
Thermal Expansion: To be able to use steel as interconnects or bipolar
plates in SOFC, the thermal expansion of the alloy should not deviate greatly
from the thermal expansion of the anode material or the electrolyte material
used in the fuel cell. Therefore, the steel alloy has a thermal expansion
coefficient of 10 to 15-10-6 °C-1 in the temperature range 0 to 900°C, or even
more preferably 11 to 1410-6 °C-1, and most preferably 11.5 to 13-10-6 °C-1.
Further, the thermal expansion mismatch (TEM) between the electro-active
ceramic materials in the fuel cell and the thermal expansion of said alloy is
not greater than ± 25%, preferably less than ± 20%, and most preferably
lower than ±15%.
Here the thermal expansion mismatch (TEM) is defined as (TECSS-
TECce)/TECSs, where the TECSS is the thermal expansion of the alloy and
TECce is the thermal expansion of the electro-active ceramic materials. The
thermal expansion of said steel alloy can be tuned to match the thermal
expansion of the electro-active ceramic materials in the fuel cell by carefully
monitoring the amount of alloying elements, such as nickel, in the steel alloy.
Conductivity: The disclosed steel alloy has a good conductivity and, in a
SOFC setup, have an ASR of less than 50 m? cm2 after 1000 hours,
preferably an ASR even lower that 25 m? cm2 after 1000 hours, on both
anode and cathode side of the interconnect. Moreover, the increment of the
ASR is not greater than 10 m? cm2 per 1000 hours, preferably even lower
than 5 m? cm2 per 1000 hours on both the anode and the cathode side of
the interconnect. This factor promotes a good efficiency of the fuel cell
throughout the life time of the fuel cell, which might be as long as 40 000
hours.
A preferred embodiment of the disclosed steel alloy will now be
described in more detail. First, the steel alloy is produced by ordinary
metallurgical steel making routines to the chemical composition as
described, for example, in the following Examples. Then said steel alloy is
hot-rolled down to an intermediate size, and thereafter cold-rolled in several
steps with a number of recrystallization steps, until a final specific thickness
of normally less than 3 mm, and a width of maximally 400 mm. The linear
thermal expansion of said steel alloy was determined by dilatometer
measurement and was found to be 12.3-10-6 °C-1 for the temperature range
30 to 900°C.
Example 1: A 0.2 mm thick steel alloy strip with a nominal composition (by
weight) of max 0.2 % C, max 0.1 % N, max 0.1 % O, max 0.4 % Si, max 0.5
% Al, max 0.5 % Mn, 20 to 25 % Cr, max 2.0 % Ni, 0,001 to 0.1 % Zr + Hf,
max 0.5 % Ti, max 2.5 % Mo +W, max 0.5 % V, max 1.25 % Nb +Ta and
balance of Fe (with naturally occurring impurities) was produced by an
ordinary steel making process, followed by hot-rolling down to a thickness of
less than 4 mm. Thereafter, it was cold-rolled in several steps with a number
of recrystallization steps down to a final thickness of 0.2 mm. Strips of four
other steel alloys were produced in the same way for comparison with the
steel alloy of Example 1. The compositions of these additional steel alloys
and their Sandvik identity numbers are given in Table 2.
Coupons of the five steel alloy strips with the size 70 x 30 x 0.2 mm
were oxidized in air at 850°C for 336, 672 and 1008 hours, respectively. In
Figure 1, the mass gain per unit area is plotted as a function of time for the
five steel alloys. According to Figure 1, a mass gain of less than 1.1 mg/cm2
per 1000 hours is obtained for the steel alloy of Example 1, insuring a good
high temperature corrosion resistance and a lower growth rate of the formed
oxide scale. However, for the steel alloys made for comparison (Sandvik ID
numbers 433, 436 and 437) with a Mn content of 0.5% (by weight) and the
addition of rare earth metals in the form of Ce, all showed a mass gain of
more than 1.8 mg/cm2 per 1000 hours, and the steel alloy with a Mn content
of 5% (by weight) had a mass gain of almost 5 mg/cm2 per 1000 hours. The
extreme large weight gain for steel alloy with 5% Mn (Sandvik ID number
434) shows the importance of good monitoring of the Mn content in the alloy
to avoid high temperature corrosion. A conclusion to be drawn from this is
that the Mn content in the steel alloy should be carefully monitored and low
amounts of Mn as alloying element is preferred if good high temperature
corrosion resistance is to be obtained.
In Figure 2, a cross sectional Scanning Electron Microscopy (SEM)
micrograph of the formed oxide scale after 336 hours at 850°C in air on the
steel alloy of Example 1 is shown. In Figure 2, it can be seen that the
formed oxide scale is also well adherent to the underlying steel alloy and that
the oxide scale thickness is less than 3 urn.
The chemical composition of the formed oxide scale after oxidization
in air for 336 hours at 850°C was determined by Glow Discharge Optical
Emission Spectroscopy (GDOES). In Figure 3, the GDOES depth profile for
the formed oxide scale is shown. The different scales for different elements
should be noted. In Figure 3, it can be seen that the manganese content in
the formed oxide scale increases at the surface to about 12% by weight.
The thickness of this manganese-rich oxide scale is about 0.5 µm, followed
by a more chromium-rich oxide scale of approximately less than 2.4 µm.
The formation of a manganese-rich oxide scale at an outermost layer at the
surface is of importance since ternary chromium oxides such as MnCr2O3
are believed to lower the formation of volatile chromium species such as
chromium oxyhyroxides. It can also be seen that the titanium content is
approximately 0.4% by weight in the oxide scale. Finally, it can be noted
that at the interface of the steel alloy and the oxide scale, a region of silicon
oxide is obtained. The formation of silicon oxide should be kept as low as
possible but is unavoidable if the steel is alloyed or has small residuals of
silicon in the matrix. However, as long as the formation of insulating silicon
oxide at the steel interface is only as small islands of particles, and not as a
continuous layer, it is acceptable for the performance of the fuel cell. X-ray
diffraction of the oxidized coupon showed that the oxides formed in the scale
had both spinell (MCr2O3) and corundum (M2O3) types of structures.
Example 2: As an additional example of an exemplary embodiment of the
disclosed steel alloy, coupons of the final steel alloy strip with the sizes of
approximately 30 x 40 x 0.057 mm were oxidized in air at both 750°C and
850°C for 500 and 1000 hours, respectively. In Table 3, a summary of
oxidization results of the four samples together with the exact coupon sizes
of the initial samples is given. The result at 750°C showed a very low mass
gain per unit area, lower than 0.2 mg/cm2 after 500 hours of oxidization and
the mass gain did not increase greatly after 1000 hours. Instead, it was still
lower than 0.3 mg/cm2 after 1000 hours. For the two sample oxidized at
850°C, the mass gain per unit area was larger but still low, less than 1.1
mg/cm2, which was also the result for the thicker strip (0.2 mm) samples,
oxidized in Example 1.
The low mass gains observed in both Examples 1 and 2 above were
compared with published values of mass gain attained on other
commercially available steels, and other test melts. In Table 4, values as
obtained from the literature on other steel grades together with the values
obtained in the present study have been summarized for comparison with an
embodiment of the present invention. In Table 4, it can be seen that the
weight gain of exemplary embodiments of the disclosed steel alloy is low
compared to other commercially available steel grades. For instance, it has
been reported that the commercialty.available steel ZMG232 has a weight
gain of approximately 0.5 mg/cm2, already after 100 hours exposure of air at
850°C. The same alloy when exposed to air +1% H2O mixture for only 670
hours at 850°C has an even larger weight gain of 1.54 mg/cm2.
Example 3: As a third example, coupons of exemplary embodiments of the
disclosed steel alloy and the four test melts (Sandvik ID numbers 433, 434,
436 and 437) described in Example 1 and the Sandvik 0C44 alloy, were
oxidized together with coupons of two commercially available steel grades
designed for the use as interconnects in SOFC, alloy A and alloy B at 850°C
in air + 1% H2O for 500 hours. In Figure 4, the weight gain for the different
steel grades after oxidation at 850°C in air + 1% H2O is shown. In Figure 4,
it can be seen that the exemplary embodiments of the disclosed steel alloy
have a much lower weight gain compared with the four Sandvik test melts,
and also have a much lower weight gain than the two commercially available
steel grades. In this context, a low weight gain is equal to a good high
temperature corrosion resistance. The second lowest weight gain is
obtained by the Sandvik 0C44 alloy with the nominal composition (by weight)
of max 0.018% C, max 0.025% N, max 0.5% Si, max 0.35% Mn, 21.1 to
21.8% Cr, max 0.3% Ni, max 0.02% P, max 0.007% S, max 0.15% Mo, max
0.010% Ti, max 0.01% Nb, max 0.03 % Ce, max 0.015% Mg and balance of
Fe (with naturally occurring impurities). As seen in Example 1, the steel
alloy Sandvik ID number 434 with a high Mn content has the largest weight
gain almost 3 mg/cm2 after 500 hours of exposure. The commercial
available alloy B with a composition of (by weight) C = 0.02%, Si = 0.40%,
Mn = 0.50%, Ni = 0.26%, Cr = 21.97% Al = 0.21%, Zr = 0.22%, La = 0.04%
and balance of Fe according to reference "Development of Ferritic Fe-Cr
Alloy for SOFC separator", T. Uehara, T. Ohno & A. Toji, Proceedings Fifth
European Solid Oxide Fuel Cell Forum, Lucerne, Switzerland, edited by J.
Huijsmans (2002) p. 281, has the second largest weight gain of almost 2.5
mg/cm2 after 500 hours of exposure. The three other Sandvik steel alloys
ID#433,436 and 437 with only 0.5% by weight Mn and the commercial
available alloy A with a nominal composition of (by weight) Cr 21.0 to 24.0%,
C max 0.03%, Mn max 0.8%, Si max 0.5%, Cu max 0.5%, Ti max 0.25, P
max 0.05, La max 0.2% and balance of Fe, have weight gains of less than 1
mg/cm2, but still much higher than exemplary embodiments of the disclosed
steel alloy and the Sandvik 0C44 alloy.
Example 4: All the three previous examples have described the excellent
high temperature corrosion resistance of exemplary embodiments of
disclosed steel alloy. In this fourth example, the low electrical resistivity of
the exemplary steel alloys will be exemplified. The contact resistance was
measured in dry air for 2900 hours at 750°C with a temperature peak of
850°C for 10 hours in the beginning. The load of the contact was 1 kg/cm2
at the start and the contact area was 0.5 cm2. The measured area specific
resistance (ASR) was initially, i.e., after the 850°C temperature peak lower
than 15 m? cm2 and had after 2900 hours, including 6 thermal cycles,
increased to below 25 m? cm2. The increment of the ASR with time was
lower than 5 m? cm2 per 1000 hours. If extrapolated linearly, the ASR of the
contact would be less than 200 m? cm2 after 40,000 hours of exposure. It is
important for the fuel cell efficiency that the ASR is low throughout the
lifetime of the fuel cell. Furthermore, when the contact resistance was tested
under anode gas environment, i.e., Ar + 9% H2 at 750°C, the ASR was even
lower, well under 10 m? cm2 after 600 hours of exposure. The increment of
the ASR was very low, under 2 m? cm2 per 1000 hours. If extrapolated
linearly the ASR of the contact on the anode side would be much lower than
200 m? cm2 after 40,000 hours of exposure, even lower than 100 m? cm2
after 40,000 hours of exposure. These values can be compared with the
contact resistance of approximately 26 m? cm2 after exposure of air at
750°C for 1000 hours for the commercially available steel ZMG 232 which

Although the present invention has been described in connection with
preferred embodiments thereof, it will be appreciated by those skilled in the
art that additions, deletions, modifications, and substitutions not specifically
described may be made without department from the spirit and scope of the
invention as defined in the appended claims.
WE CLAIM:
1. A high temperature corrosion resistant stainless steel, consisting essentially of
(by weight):
0.001 0.001 = Ti = 0.5%;0.1 = Mo +W = 2.0%;0.01 = Nb + Ta = 1.25%;0.01 = V = 0.5%;
and balance of Fe and naturally occurring impurities and not more than 0.010% of S
impurity.
2. A high temperature corrosion resistant stainless steel, consisting essentially of
(by weight):
0.001 Ti = 0.4%;0.01 = Mo = 2.5%; 0.01 = Nb = 1 25%;0.01 = V = 0.1 %; and balance of Fe
and naturally occurring impurities and not more than 0.010% of S impurity.
3. The stainless steel according to claim 1 or 2, wherein the stainless steel has a
weight gain of less than 1.5 mg/cm2 when oxidized in air or air + 1% H2O at 850°C
after 1000 hours, without any spallation of the oxide scale.
4. The stainless steel according to any of the previous claims, wherein the
stainless steel has a linear thermal expansion coefficient of more than 11.5-10-6 (°C-
1) but less than 13.010-6 (°C-1) in the temperature range of 30 to 900°C.
5. The stainless steel according to any of the previous claims, wherein the
stainless steel has a thermal expansion mismatch (TEM) with an electro-active
ceramic material in a solid oxide fuel cell of less than + 15 %.
6. The stainless steel according to any of the previous claims, wherein the
stainless steel for use as an interconnect or a bipolar plate material in Solid Oxide
Fuel Cells.
7. The stainless steel according to claim 1 or 2, wherein the stainless steel for
use as a catalytic converter in automobile applications.


A high temperature corrosion resistant stainless steel having a
composition (by weight) of: C ≤ 0.2%, but more than zero, N ≤ 0.1% but
more than zero, O ≤ 0.1% but more than zero, Si ≤ 0.4% but more than zero,
Al ≤ 0.5% but more than zero, Mn ≤ 0.5% but more than zero, Cr 20 to 25%,
Ni ≤ 2.0% but more than zero, Zr + Hf 0,01 to 0.1%, Ti ≤ 0.5% but more than
zero, Mo + W ≤ 2.5% but more than zero, Nb + Ta ≤ 1.25% but more than
zero, V ≤ 0.5% but more than zero, and balance of Fe and naturally
occurring impurities and not more than 0.010% of S impurity. This steel is
particularly suitable for the manufacturing of interconnects in solid oxide fuel
cells.

Documents:

03771-kolnp-2006 abstract.pdf

03771-kolnp-2006 claims.pdf

03771-kolnp-2006 correspondence others.pdf

03771-kolnp-2006 description (complete).pdf

03771-kolnp-2006 drawings.pdf

03771-kolnp-2006 form-1.pdf

03771-kolnp-2006 form-2.pdf

03771-kolnp-2006 form-3.pdf

03771-kolnp-2006 form-5.pdf

03771-kolnp-2006 international publication.pdf

03771-kolnp-2006 international search report.pdf

03771-kolnp-2006 priority document.pdf

3771-KOLNP-2006-(19-09-2011)-CORRESPONDENCE.pdf

3771-KOLNP-2006-(25-05-2012)-CORRESPONDENCE.pdf

3771-KOLNP-2006-(25-05-2012)-FORM-27.pdf

3771-KOLNP-2006-(26-08-2011)-AMANDED CLAIMS.pdf

3771-KOLNP-2006-(26-08-2011)-CORRESPONDENCE.pdf

3771-KOLNP-2006-(26-08-2011)-OTHERS.pdf

3771-KOLNP-2006-AMANDED CLAIMS 1.1.pdf

3771-KOLNP-2006-AMANDED CLAIMS.pdf

3771-KOLNP-2006-CORRESPONDENCE 1.1.pdf

3771-KOLNP-2006-CORRESPONDENCE 1.3.pdf

3771-KOLNP-2006-CORRESPONDENCE 1.4.pdf

3771-KOLNP-2006-CORRESPONDENCE 1.5.pdf

3771-kolnp-2006-CORRESPONDENCE-1.1.pdf

3771-KOLNP-2006-CORRESPONDENCE-1.2.pdf

3771-KOLNP-2006-CORRESPONDENCE.pdf

3771-KOLNP-2006-DESCRIPTION (COMPLETE) 1.1.pdf

3771-KOLNP-2006-DESCRIPTION (COMPLETE) 1.2.pdf

3771-KOLNP-2006-DRAWINGS 1.1.pdf

3771-KOLNP-2006-DRAWINGS 1.2.pdf

3771-KOLNP-2006-EXAMINATION REPORT REPLY RECIEVED.pdf

3771-KOLNP-2006-EXAMINATION REPORT.pdf

3771-KOLNP-2006-FORM 1 1.1.pdf

3771-KOLNP-2006-FORM 1-1.2.pdf

3771-KOLNP-2006-FORM 18 1.1.pdf

3771-kolnp-2006-form 18.pdf

3771-KOLNP-2006-FORM 2 1.1.pdf

3771-KOLNP-2006-FORM 2-1.2.pdf

3771-KOLNP-2006-FORM 3 1.1.pdf

3771-KOLNP-2006-FORM 3.pdf

3771-KOLNP-2006-FORM 5.pdf

3771-KOLNP-2006-GRANTED-ABSTRACT.pdf

3771-KOLNP-2006-GRANTED-CLAIMS.pdf

3771-KOLNP-2006-GRANTED-DESCRIPTION (COMPLETE).pdf

3771-KOLNP-2006-GRANTED-DRAWINGS.pdf

3771-KOLNP-2006-GRANTED-FORM 1.pdf

3771-KOLNP-2006-GRANTED-FORM 2.pdf

3771-KOLNP-2006-GRANTED-SPECIFICATION.pdf

3771-KOLNP-2006-OTHERS 1.1.pdf

3771-KOLNP-2006-OTHERS 1.2.pdf

3771-KOLNP-2006-OTHERS.pdf

3771-KOLNP-2006-PA.pdf

3771-KOLNP-2006-PCT IPER.pdf

3771-KOLNP-2006-REPLY TO EXAMINATION REPORT 1.1.pdf

abstract-03771-kolnp-2006.jpg


Patent Number 250190
Indian Patent Application Number 3771/KOLNP/2006
PG Journal Number 50/2011
Publication Date 16-Dec-2011
Grant Date 14-Dec-2011
Date of Filing 15-Dec-2006
Name of Patentee SANDVIK INTELLECTUAL PROPERTY AB
Applicant Address S-811 81 SANDVIKEN
Inventors:
# Inventor's Name Inventor's Address
1 SCHUISKY, MIKAEL MOSSVÄGEN 25 C, S-811 34 SANDVIKEN
2 GORANSSON, KENNETH S. KANSLIGATAN 28, S-802 52 GAVLE
3 ROSBERG, ANDREAS VIKINGAVÄGEN 32, S-811 60 SANDVIKEN
PCT International Classification Number C22C 38/50
PCT International Application Number PCT/SE2005/00707
PCT International Filing date 2005-05-17
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 0401292-8 2004-05-19 Sweden