rm26 electromechanical corrosion of molybdenum electrodes in … · 2014. 12. 16. · etallic sb i...
TRANSCRIPT
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
Electrochemical Corrosion of Molybdenum Electrodes in Soda-Lime
Glass Containing Antimony
M.-Ch. Bölitz*, R. Völkl*, H. Traxler**, R. Holzknecht**, U. Glatzel*
* Metals and Alloys, University Bayreuth, 95440 Bayreuth, Germany
** PLANSEE SE, 6600 Reutte, Austria
Abstract
The electrochemical corrosion of Mo electrodes was investigated at 1435°C in an Sb-containing soda-
lime glass with the chemical components SiO2-Al2O3-Na2O-K2O-MgO-CaO-BaO-B2O3. For comparison
experiments were also carried out with Sb-free glass. Corrosion was only significantly observed in Sb-
containing soda-lime glass, suggesting that the polyvalent element Sb is the cause for the corrosion.
Analytical scanning and transmission electron microscopy reveal indeed the presence of pure Sb on the
surfaces and along grain boundaries of electrodes. This indicates a reduction of Sb cations to metallic
Sb which is accompanied by an oxidation of metallic Mo to Mon+ cations.
The frequency dependence and rate of corrosion has been determined for two electrode materials, pure
Mo and Mo-ZrO2, that were reacted with the antimony-containing soda-lime glass at frequencies of
50 Hz, 500 Hz, and 1000 Hz. Corrosion can already be observed in experiments without electrical
current, and is only electrolytically augmented in 50 Hz experiments. An additional electrolytic corrosion
could not be detected in the 500 Hz and 1000 Hz experiments. Glasses reacted with pure Mo electrodes
contain more Mo than glasses reacted with Mo-ZrO2 electrodes, which can be attributed to the
stabilization of grain boundaries due to ZrO2. The Mo concentration in glasses increases linearly with
time, indicating that the corrosion process is surface controlled.
Keywords
Soda-lime glass, corrosion, transmission electron microscopy; microstructure, electrodes, molybdenum
Introduction
High quality glasses are industrially melted in huge tank furnaces. The electric heating and melting of
glass is standard practice in the glass industry. The heating of electrodes provides an easy process
control and allows us to reach higher temperatures than in conventional gas-fired furnaces. The melt is
more homogeneous, improving the quality and transparency of the glass. Due to the strong
environmental consciousness that has emerged in recent years, and the tightening of environmental
laws, this method also has become an increasingly important option for environmental issues. A large
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
number of glasses, in particular optical glasses, are melted with electrical resistance heating. Different
electrode materials are used, e.g. refractory metals, such as molybdenum, tungsten and their alloys, or
platinum, particularly PtRh- or PtIr-alloys.
Materials made of molybdenum are known for their excellent corrosion resistance in glass melts. Due to
the low price of molybdenum the high melting point of 2623 ° C and a mechanical stability up to
temperatures of over 1600 ° C it is often used as electrode material. Despite these excellent properties,
molybdenum is known to be strongly corroded, resulting in a contamination of the glass. Even if it does
not lead to total loss of electrodes, small amounts of molybdenum produce an undesired coloring of the
glass melt. For the industry the coloration of the melt and the loss of the metallic contact materials mean
a considerable economic damage.
Previous studies concentrated mostly on the electrochemical analysis by anodic and cathodic
polarization and the corrosion protection by means of molybdenum passivation [2-6]. This non-metallic
protective layer prevents corrosion of the base material. Very little work has been carried out with regard
to the microstructural characterization of electrode materials and corrosion products. A lack of
knowledge also exists regarding the kinetics of corrosion. There are few data on corrosion rates [7-8]
and the frequency dependence of rates is hardly investigated [1].
A great influence on the corrosion of molybdenum electrodes has the chemical composition of the melt.
Since molybdenum is not a noble metal, it easily oxidizes in the presence of almost all polyvalent
elements and complexes in the melt, e.g. Sb, Zn, As, Ni, Mn, Co, or Pb, which have a higher standard
potential than molybdenum [7, 9-11]. Studies have shown the high influence of antimony on the
corrosion of molybdenum electrodes. Yamamoto et al. [1] performed experiments in a slicate glass with
an antimony content of 0.0 to 0.34 wt%. The experiments were carried out at 50 Hz, 1435 ° C, and a
fixed current density. The investigations showed that the corrosion rate increases with increasing current
density and increasing antimony concentration. The corrosion rate increases linearly with the antimony
concentration, regardless of whether the experiments were performed with or without current flow.
Experiments with an antimony-free glass show no corrosion of molybdenum electrodes. Yamamoto et al.
[1] have suggested that the primary corrosion process consists in an oxidation of metallic molybdenum
and a simultaneous reduction of antimony cations. Thereby the applied alternating current enhances the
corrosion of the Mo electrodes due to reduction of antimony cations, and the formation of Mo cations.
This study aims at assessing the corrosion behavior and at identifying the corrosion products of
molybdenum and an molybdenum base alloy in soda-lime glass by means of microstructural
investigations using with scanning (SEM) and transmission electron microscopy (TEM).
Experimental
Figure 1 shows a schematic sketch of the corrosion furnace. The furnace is heated via two Super-
Kanthal heating elements. The crucible, filled up with about 650 g glass, is placed on top of a disc which
is continuously rotated during experiments. The furnace can be topped by two different caps. If the glass
is melted and the temperature is reached, the standard cap is replaced by a cap with water-cooled
electrode holders. This cap including the electrodes and a thermocouple is moved downward until the
working electrodes immerse completely into the melt. In our experiments, the heating and cooling rate
were set to 60 ° C per hour. The experiments were performed in a two-electrode arrangement in soda-
Bö
lim
0.6
(E
ex
at
To
po
of
Fo
ins
tra
co
tra
ele
Fig
Re
Ex
Mo
24
sh
ele
ob
litz, Völkl, Tra
me glass me
62 wt.% of S
KTechnolog
xperiments w
1435°C at d
o investigate
olished. Sec
the sample
or further stu
strument op
ansmission
nventional
ansmission
ectron diffra
gure 1: Labora
esults
xperiments
olybdenum
4-hour test in
ow strong c
ectrode surf
bserved.
lid with electrodes athermocoup
xler et al.
elt of the ba
Sb2O3. The
gies, AMEL
were 24 and
different fre
e the corros
condary-elec
es were acq
udy with TE
perating with
electron mi
bright field
electron mi
action patter
atory corrosion
s in Sb-Con
reacts easi
n an antimo
corrosion. T
face and alo
furnac
and ples
sic compos
current den
L 7060) that
d 72 hours.
equencies o
sion of Mo a
ctron (SE),
uired with a
EM, nanome
h gallium io
croscope, o
imaging, th
croscopy (S
rn (SAED).
n furnace set u
ntaining Gla
ly with elem
ony contain
The glass is
ong grain b
ce with super-
camer
18
sition SiO2-A
nsity of all e
fixed it to a
Two differe
of 50 Hz, 50
and the Mo
back-scatte
a Zeiss SEM
eter-thin sam
ns at 30 kV
operating at
e elementa
STEM) and
up at the Unive
ass
ments in a g
ing glass w
colored da
oundaries.
-kanthal eleme
ra + inspection
8th Plansee S
Al2O3-Na2O-
experiments
a constant v
ent Mo mate
0 Hz and 1
alloy in exp
ered (BSE)
M 1540EsB
mples were
V. TEM sam
t 200 kV. Th
al distributio
secondary
ersity Bayreut
glass melt, e
without elect
ark grey and
At the marg
ents, 7 kW
n window
Seminar 2013
-K2O-MgO-
s was contro
value of 1A/
erials, pure
000 Hz.
periments, s
images and
Cross Bea
e cut out wit
ples were s
he microstru
n with EDX
phases we
th and schema
even if no e
rical curren
d metallic Sb
gins of the e
power supply
control unit
CaO-BaO-B
olled by a p
/cm2. The du
Mo and Mo
small slices
d energy-dis
m scanning
h a focused
studied with
ucture was
in combina
re characte
atic cross sect
lectrical cur
t the surfac
b can be ob
electrodes g
de
y
B2O3 with (a
potentiostat
urations of
o-ZrO2, wer
were cut an
spersive X-
g electron m
d ion beam
h a Zeiss Lib
characteriz
ation with sc
erized with s
tion.
rrent is app
ces of the M
bserved by
grain coarse
esign drawing
RM
a) no and (b
the
re investigat
nd then
-ray analyse
microscope.
(FIB)
bra 200FEG
zed by
canning
selected are
lied. After a
Mo electrode
SEM on the
ening is
g:
M 26
b)
ted
es
G
ea
a
es
e
Bö
Ex
dif
alo
Figbou
Th
co
pro
tem
pro
Aft
the
co
co
SE
we
int
15
Tab
Dif
str
we
dia
litz, Völkl, Tra
xperiments w
fferent corro
ong the grai
gure 2: Backscundaries (b).
he Sb depos
ncave shap
ocedure. Th
mperature u
onounced a
ter 24 hours
e grain boun
ntinuous we
re regions o
EM observa
ere removed
to the electr
50 µm and 1
ble I: Maximum
fferent pene
rength of the
ere measure
ameter, ther
a)
xler et al.
with Mo- an
osive attack
in boundari
cattered electr
sits extent u
pe in contac
his is expec
used (1435°
at Mo-ZrO2 e
s Mo-ZrO2–
ndaries in t
etting of the
of the electr
ations on po
d from the e
rode materia
1500 µm, re
m penetration
Ele
etration dep
e electrical
ed before a
refore the e
nd Mo-ZrO2-
k. For both m
es, see Fig
ron image of M
up to 200 µm
ct with the g
cted becaus
°C). The int
electrode s
–electrodes
he margin r
e grain boun
rodes.
olished glass
electrode su
al is observ
espectively (
depths of me
ectrode mate
Mo
Mo-ZrO2
Mo
Mo-ZrO2
pths of Sb w
field on diff
and after the
extent of cor
18
-electrodes
materials, m
. 2.
Mo electrodes
m along the
glass, which
se the meltin
tergranular f
urfaces and
do not show
regions of e
ndaries with
s sections r
urface and a
ved. The pe
(Table I).
etallic antimony
rial Test
2
2
7
7
were found o
ferent sides
e experimen
rrosion can
8th Plansee S
after 24- a
metallic Sb i
shows metall
e surfaces a
h suggests t
ng tempera
film of elem
d the Sb pe
w grain coa
electrodes is
h Sb in thin
reveal Mo p
absorbed in
netration de
y for Mo and M
period
24 h
24 h
72 h
72 h
on the front
s of the elec
nts. The cor
not be eval
b)
Seminar 2013
nd 72-hours
s deposited
ic Sb on the e
and can be
that Sb was
ture of Sb (
mental Sb al
netrates de
arsening, bu
s recognize
margins. S
particles in a
n the melt. A
epth of Sb i
Mo-ZrO2 elect
Max. pene
20
40
15
150
t and back s
ctrodes. Also
rrosion did n
uated with s
)
s at a frequ
d on the sur
electrode surfa
up to 40 µm
s melted dur
630°C) is w
ong the gra
eeper into th
ut a weaken
d. Detailed
b did howev
all experime
After 72 h fu
nto Mo- and
trodes.
etration depth
0 µm
00 µm
50 µm
00 µm
side, which
o the diame
not significa
sufficient ac
ency of 50
rface of the
ace (a) or alon
m thick. The
ring the exp
well below th
ain boundar
he electrode
ning of the g
SEM studie
ver not diffu
ents. The M
urther pene
d Mo-ZrO2-
h
is due to th
eter of the e
antly alter th
ccuracy with
RM
Hz show a
electrode a
ng grain
ey have a
perimental
he
ries is more
e material.
grains along
es show a
use into the
Mo particles
tration of Sb
electrodes
he different
electrodes
he total
h this metho
M 26
and
g
b
is
od.
Bö
To
co
(IC
de
de
ele
ph
Figsha
SE
the
wa
res
pre
are
Figuprcut
a
litz, Völkl, Tra
o make a mo
ntents were
CP-OES). In
etected in th
etected seve
ectrodes. S
hase, see Fi
gure 3: Secondaped inclusion
EM-EDX an
e inclusions
as not possi
solution of c
epared by f
e necessary
gure 4: Preparright in the lamtting out of the
a)
a)
xler et al.
ore precise
e determine
n addition to
he glass, wh
eral 100 µm
EM studies
ig.3 b).
dary electron in.
alyses show
s contains b
ible to dete
chemical an
focused ion
y. Figure 5
ration of a TEMmella. (a) Depoe foil.
statement
ed in glasse
o the random
hich are loca
m away from
show that
images show
w that the g
besides Sb a
rmine the e
nalysis and
beam (FIB
a shows a p
M lamella of thosition of the t
18
about the c
s using indu
mly shaped
ated close t
m the electro
many of the
spherical inclu
globular incl
also Mo. Du
xact chemic
thus to ana
B) technique
polished TE
he globular, mtungsten prote
b)
8th Plansee S
corrosion ra
uctively cou
d molybdenu
to the electr
ode surface
e globular in
usions in the g
lusions con
ue to the sm
cal compos
alyze the pla
e in the SEM
EM foil.
etallic inclusioective layer, (b
Seminar 2013
te of the dif
upled plasm
um particles
rode surfac
and could
nclusions co
glass (a), whic
sist of pure
mall thicknes
sition with S
atelet-shape
M. Figure 4
on in the glassb) preparation
b)
fferent mate
ma optical em
s, small glob
e (Fig. 3 a).
only be obs
ontain a sec
ch often conta
Sb. The pla
ss of this M
EM-EDX. T
ed phase a
shows the
s, so that the pof the ramps,
c)
erials the m
mission spe
bular inclus
. These inc
served with
cond, platel
ain a platelet o
atelet-shap
Mo-Sb phase
To increase
TEM lamel
preparation
plate-shaped p, and (c) fine p
RM
olybdenum
ectroscopy
sions were
lusions are
Mo-ZrO2
et-shaped
r lamella
ed phase in
e (<1 µm), i
the spatial
lla was
n steps, whi
phase stands polishing and
M 26
n
t
ich
b)
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
Figure 5: (a) Scanning transmission electron microscopy (STEM) image and (b) electron diffraction pattern of an Sb-inclusion in the glass and (c) Mo- and (d) Sb elemental mapping. The lamella is enriched with Mo.
To identify the lamellar phase EDX element distribution maps and spectra were acquired with TEM-EDX.
see Fig. 5 c) and d). The globular inclusions consist of pure Sb and the electron diffraction pattern
matches the structure of crystalline Sb (Fig. 5 b, and Table II).
Table II: The table shows the observed and calculated lattice spacings of pure antimony. The corresponding selected area electron diffraction pattern is shown in Figure 5 b). For the calculation of the interplanar spacings, lattice constants a = 430.5 pm and b = 112.5 pm were used for hexagonal Sb.
hkl Interplanar spacing (observed) [pm]
Interplanar spacing (calculated) [pm]
003 390 375
011 369 354
012 321 311
The lamella is composed of Mo and Sb. Quantification of the EDX spectra reveal the intermetallic phase
Mo3Sb7 which is known as the only intermediate phase in the Mo-Sb system [12]. According to the phase
diagram Mo3Sb7 is formed at a temperature below 800°C, thus it is generated by segregation during
quench at the end of the experiments.
a) b)
c) d)
[100]
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
Glass analyses taken by ICP-OES show clear differences in the molybdenum concentrations for the pure
Mo-electrodes and the Mo-ZrO2-electrodes. Microstructural observations suggest that pure molybdenum
is more resistant to corrosion than Mo-ZrO2-electrodes, because less antimony penetrated into the
molybdenum electrode, while antimony migrated well along grain boundaries into the Mo-ZrO2
electrodes.
However, ICP-OES analyses show that after 24 h in contact with Mo-ZrO2 only 600 ppm of molybdenum
were dissolved in the glass. The molybdenum content in experiments with pure Mo-electrodes is
1100 ppm and thus almost twice. This result is confirmed by experiments run for 72 h. The glass melted
with Mo-ZrO2–electrodes contains 2000 ppm molybdenum after 72 h, while glass in contact with pure
Mo-electrodes contains 3100 ppm molybdenum (Fig. 6). Thus the Mo concentration is reduced by
approximately 35% using Mo-ZrO2-electrodes. The increase of Mo contents in the glass at both
electrode materials generally shows that the corrosion proceeds at constant rates. Presumably, the
lower concentration of molybdenum in the glass melted with Mo-ZrO2-electrodes is due to the fact that
molybdenum is dissolved in metallic antimony that in turn is largely associated with grain boundaries in
the electrode surface.
Fig. 6: Mo concentration in soda-lime-reference glass without electrical current (160 ppm) and after experimental periods of 24 h and 72 h.
The linear increase of the Mo-content in the glass with time for both electrode materials shows that the
corrosion is a surface-controlled process, which takes place at a constant rate R [13]. Probably less
molybdenum is dissolved in experiments with ZrO2 stabilized Mo electrodes because a large fraction of
elemental Sb with the dissolved molybdenum remains on grain boundaries. The lower contamination of
glass when using Mo-ZrO2-electrodes agrees with experiments of Martinz et al. [8].
Bö
Fr
Fo
10
de
A d
(Fi
7 b
alo
Figgra
Th
50
me
fre
gla
litz, Völkl, Tra
requency D
or pure Mo e
000 Hz. To p
epth of imme
distinct grai
ig. 7a). Part
b). Furtherm
ong grain bo
gure 7: Back-sain size reduct
he microstru
00 and 1000
etallic Sb on
equency dep
asses howe
xler et al.
Dependence
electrodes a
perform the
ersion of the
in growth is
ticle size re
more, eleme
oundaries (
scattered electtion in Mo-ZrO
uctural obse
0 Hz) and fo
n the surfac
pendent an
ever show s
DM
e of Corros
additional e
e experimen
e electrode
s observed i
eduction can
ental antimo
see also Fig
tron images shO2 electrodes.
ervations on
or the curren
ce and along
d remains t
significant d
Dissolved Mo-particles
Grain size
18
sion
xperiments
nts at higher
s was reduc
n the surfac
n be observ
ony was det
gure 2).
how (a) grain c
n experimen
nt-free expe
g grain bou
the same in
ifferences in
s
e reduction
8th Plansee S
s were carrie
r frequencie
ced from of
ce area in a
ved in conta
tected at all
coarsening in
nts with pur
eriment sho
undaries. Th
n all experim
n the Mo co
n
Seminar 2013
ed out at dif
es with a co
f 3 cm to 1 c
all experime
act with the
l frequencie
Mo-electrode
e Mo electr
ow identical
he mechanis
ments. The I
oncentration
G
fferent frequ
nstant curre
cm. Exposu
ents with pu
Mo-ZrO2-ele
es on the ele
es close to the
odes at diff
phenomen
sm of corro
CP-OES an
n of glasses
Grain coars
uencies of 5
ent density
ure times we
ure Mo elect
ectrode at 5
ectrode sur
e electrode sur
ferent frequ
a, i.e., the f
osion is ther
nalyses of r
s in depend
sening
RM
50, 500 and
of 1A/cm2 t
ere 24 h.
trodes
50 Hz (Fig.
rface and
rface and (b)
encies (50,
formation of
efore not
reacted
ence of the
M 26
d
the
f
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
frequency. The corrosion rates are a clear function of frequency. The Mo concentration is the highest at
50 Hz with 360 ppm (Fig. 8).
Figure 8: The red data points show the Mo contents in Sb-containing soda-lime glass for experiments without current, at 50 Hz, 500 Hz and 1000 Hz. The black points correspond to the Mo contents in antimony-free glass for experiments without current and at 50 Hz. The black horizontal line corresponds to the Mo concentration in the original glass. The figure shows that the frequency and the Sb content greatly affect the corrosion.
In the experiment without electrical current, corrosion can already be observed due to the strong base
character of molybdenum (Mo concentration is about 160 ppm). An additional electrolytic corrosion is
detected at 50 Hz, increasing the Mo concentration to about 360 ppm. At higher frequencies of 500 Hz
and 1000 Hz the Mo concentrations in glasses are however indistinguishable within error limits from the
concentration in an experiment without current. To avoid an undesired electrolytic corrosion it should be
sufficient to perform melting experiments at a frequency of 500 Hz and higher.
Pure Mo Electrodes in Antimony-Free Soda-Lime Glass
The results of experiments with antimony containing soda-lime glass have shown that antimony is the
polyvalent ion responsible for the strong corrosion of molybdenum. The redox reaction between
antimony and molybdenum causes a deposition of elemental antimony and dissolution of Mo cations in
the melt. To study the corrosion in the absence of antimony, two further experiments were performed
with an antimony-free soda-lime glass. Both experiments were carried out for 24 h in contact with pure
Mo electrodes. The experiments were run without current and at a frequency of 50 Hz.
The corrosion without electrical current is very low, such that the electrode surface remains smooth
(Fig. 9). The Mo content in the glass corresponds to the concentration of the original glass. There are
Bö
ha
Th
Figcur
At
(Fi
co
rea
fro
Figpar
a
litz, Völkl, Tra
ardly any Mo
he glass afte
gure 9: Backscrrent. There is
a frequenc
ig. 10 a). Af
ntent is only
action of mo
om the elect
gure 10: (a) Serticles from the
a)
xler et al.
o particles d
er 24 h is on
catter electrons no separation
cy of 50 Hz f
fter 24 h the
y slightly in
olybdenum
trode surfac
econdary elece Mo-surface,
detectable t
nly slightly g
n image of a pun of Mo partic
few very sm
e glass is si
creased in
with anothe
ce show no
tron image an which are ab
18
that are rem
greyish colo
ure Mo electroles visible.
mall Mo part
gnificantly l
comparison
er element i
alloying wit
nd (b) Mo elemsorbed into th
8th Plansee S
moved from
ored.
ode after 24 h
ticles are tra
less colored
n to the orig
in the melt t
th other gla
ment distributiohe melt consist
b
M
Seminar 2013
the surface
ours in contac
ansformed
d than antim
ginal glass (
taking place
ass compon
on map of the t of pure moly
b)
Mo L
e and incorp
ct with an antim
from the su
mony-contai
Fig. 8). App
e. The Mo-p
ents (Fig. 1
molybdenum-bdenum.
porated into
mony-free gla
urface into t
ining glass.
parently, the
particles wh
0 b).
-glass interfac
RM
o the glass.
ss without
he glass
The Mo
ere is a redo
hich detach
ce at 50 Hz. Th
M 26
ox
he
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
Discussion
The results of this study demonstrate that the underlying mechanism of the corrosion of pure Mo and Mo
base alloys is a redox reaction between metallic Mo and polyvalent cations (in this case Sb cations) in
the silicate melt. Metallic Mo is oxidized and dissolved in the silicate melt, while Sb cations are reduced
to Sb metal, which in turn can dissolve additional metallic Mo.
Our investigations concentrated on a frequency of 50 Hz, since electrode corrosion was strongest at this
frequency. Experiments with Mo und Mo-ZrO2 electrodes in soda-lime glass reveal the deposition of
elemental antimony on the electrode surface. In principle Mon+ ions are generated on the anode side,
while at the cathodic side Sb3+ or Mon+ cations can be reduced to metal. The latter depends on the
frequency. At 50 Hz there is sufficient time for the diffusion of Sb3+ ions, such that Sb3+ cations
accelerate to the electrode surface where they can be reduced. At 500 Hz the duration of a half-cycle is
too short, in order to diffuse Sb3+ to the electrode surface or to remove Mon+ cations far enough from it,
such that they deposit again.
Another important observation is that metallic antimony penetrates deeper into Mo-ZrO2 electrodes than
into pure Mo electrodes. We attribute this phenomenon to the observed reduction in grain size and
thereby an increase in internal grain boundaries in Mo-ZrO2 electrodes. In contrast, pure Mo electrodes
show a grain coarsening and thus a reduction in internal grain boundaries, which inhibit the penetration
of metallic Sb deeper into the electrodes. Despite this observation Mo-ZrO2 shows significantly better
corrosion resistance and lower molybdenum contents in the glass than pure Mo electrodes. The reason
is that the finely dispersed ZrO2 stabilizes the grain boundaries such that complete Mo grains can not
detach from the electrode surface as observed for pure Mo electrodes.
Time-resolved ICP-OES analyses (Fig. 6) have demonstrated that the Mo concentrations in soda-lime
glasses in contact with Mo and Mo-ZrO2 electrodes increases linear in time. The slope of the regression
line in Figure 6 allows to determine the dissolution rate R according to following equation [13]:
C(Mo) = C0(Mo) + R t (1)
with C and C0 the Mo concentrations in reacted soda-lime glasses and in the original glass and t the
time. A normalization to the surface area A finally yields the rate constant k:
k = R A-1 (2)
Table III summarizes the calculated corrosion rates and rate constants for Mo and Mo-ZrO2 electrodes.
The data shows that Mo-ZrO2 electrodes dissolve 35% slower than Mo electrodes.
Table III: Corrosion rates and rate constants of Mo and Mo-ZrO2 electrode (r = 0.9 cm) in antimony containing soda-lime glass for a current density of 1 A/cm2, frequency of 50 Hz and a temperature of 1430 ° C. The values are based on 1 kg glass.
Electrode material Corrosion rate R [mg h-1]
Rate constant [g m-2 h-1]
Mo 40,0 43,9
Mo-ZrO2 25,9 28,5
Bölitz, Völkl, Traxler et al. 18th Plansee Seminar 2013 RM 26
References
1. M. Yamamoto, K. Sakai, R. Akagi, M. Sakai, H. Yamashita, T. Maekawa, Electrochemical Corrosion
of Molybdenum Electrodes in an Aluminosilicate Glass Melt Containing Antimony (2004), Journal of
the Ceramic Society of Japan 112 (3) 179-183
1. J. Matěj, E. Krupková, V. Hulínský, The Mechanism of Dissolution of Molybdenum in Glass Melt and
the Effect of Alternating Current (2002), Ceramics – Silikáty 46 (4), 133-139
2. V. Čierna, J. Matěj, M. Maryška, V. Hulínský, A. Langrová, Cathodic Behaviour of Molybdenum
Electrode in Various Glass Melts (2006), Ceramics – Silikáty 50 (1), 32-38
3. J. Matěj, R. Kocourová, A. Langrová, V. Čierna, The Behaviour of Molybdenum Electrode in
Sulphate-Refined Glass Melt (2003), Ceramics – Silikáty 47 (4), 162-168
4. S. Kamakshi, S. und R. Speyer, Electrochemical Corrosion and Protection of Molybdenum and
Molybdenum Disilicide in a Molten Soda-Lime Silicate Glass Enviroment (1996), J. Am. Ceram.
Soc., 79 (7), 1851-56
5. I. Vanmoortel, J. De Strycker, E. Temmerman, A. Adriaens, Insights into the Oxidation Mechanism
of Molybdenum in Molten Glass (2008), Ceramics – Silikáty 52 (1), 1-7
6. D. Gohlke, P. Hoyer, J. Disam, K. Lubbers, G. Leichtfried, H.-P. Martini, Neue Elektrodenwerkstoffe
für das elektrische Schmelzen von Gläsern (1997) Proceedings of the 14th International Plansee
Seminar, Plansee AG, Reutte Vol. I
7. H.-P. Martinz, J. Matěj, G. Leichtfried, The Corrosion of coated and uncoated Mo and of uncoated
Mo-ZrO2 in Glass Melts Under a.c. Loading (2001), 15th International Plansee Seminar, Plansee
Holding AG, Reutte, Vol. 1, 217-228
8. Matej, J., Freivolt, S. and Hulínsky, V., Ceramics-Silikáty, 40, 1 (1996).
9. Holzwarth, S., Rüssel, C. and Tomandl, G., Glastech. Ber., 64, 195 (1991).
10. Fanderlik, I. and Kirsch, R., “Metals in Glassmaking” Ed.by Kirsch, R., Elsevier (1993) Chapter 6
(ISBN 0-444-98706-1).
11. H. Boller, H. Nowotny, Monatsch. Chem., 95, 1272-1282, (1964)
12. W. Stumm, Chemistry of the Solid-Water Interface: Processes at the Mineral-Water and Particle-
Water Interface in Natural Systems, Wiley, 419, (1992)