enhanced hydrogen uptake und reaction kinetics during ......imaging at antares (frm-2) 50 % argon 10...
TRANSCRIPT
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20191/21
KIT / Institut für Angewandte Materialien
www.kit.edu
Enhanced Hydrogen Uptake und Reaction Kinetics During
Oxidation of Zircaloy-4 in Nitrogen Containing Steam
Atmospheres
M. Grosse, S. Pulvermacher, M. Steinbrück (KIT – IAM)
B. Schillinger (TU Munich)
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20192/21
Introduction
Why the reaction of Zircaloy in steam-nitrogen mixed atmospheres is an
issue?
➢ Air ingress during SFP accidents and after vessel failure in severe reactor
accidents.
➢ It is well known that the presence of nitrogen can accelerate the reaction of
zirconium alloys with oxygen or steam.
Basic reactions, strongly simplified :
with oxygen 𝑍𝑟 + 𝑂2 → 𝑍𝑟𝑂2with steam 𝑍𝑟 + 2𝐻2𝑂 → 𝑍𝑟𝑂2 + 2𝐻2with nitrogen 2𝑍𝑟 + 𝑁2 → 2𝑍𝑟𝑁
Re-oxidation of nitrides:
ZrN + O2 → ZrO2 + N
𝑍𝑟𝑂2
0 5000 10000 15000 200000
200
400
600
800 N2 conc., %
0
0.1
0.2
0.5
0.7
1
2
5
10
50
70
80
90
100
m
, g
/m²
time, s
H2O+N2
H2ON2
Mass gain of Zircaloy-4 oxidized at 800°C
in steam-nitrogen mixtures,
(Steinbrück et al., NUMAT 2014)
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20193/21
Introduction
If ZrN precipitate, cracks are formed and
the ZrO2 layer is not longer protective
against further oxidation.
The behavior of the reaction of zirconium
with oxygen, steam and nitrogen was
investigated in a large number of
experiments.
Modeling in severe accident codes is not
yet satisfying.
𝑍𝑟𝑂2
𝒁𝒓
𝒁𝒓𝑵
The results of tests using different experimental setups are contradictory.
One reason for the differences are different gas flow rates applied in the tests.
A model describing the influence of the gas flow rates on the reaction behavior
was developed at KIT.
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20194/21
Flow rate model[M. Grosse et al. ICAPP 2016]
𝐻2O g + (Zr𝑂 + 𝑉𝑂2+)(𝑜𝑥) = 𝑍𝑟𝑂2 ox + 2𝐻𝑎𝑑
+
Basic reactions with steam if an oxide
layer is already formed
𝑂𝑂 𝑜𝑥 + 𝑍𝑟 𝑚 = (𝑍𝑟𝑂 + 𝑉𝑂2+ + 2𝑒−)
Wagner, C., Die Löslichkeit von Wasserdampf in ZrO2-Y2O3-Mischkristallen,
Ber. Bunsen-Ges. Phy. Chem., Vol. 72, 1968, pp. 778-781
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20195/21
Flow rate model[M. Grosse et al. ICAPP 2016]
Basic reactions with nitrogen if no
oxygen or steam is available
𝑁2(𝑔) + 4 𝑍𝑟𝑂 + 𝑉𝑂2+ + 2𝑒− (𝑜𝑥) = 2𝑍𝑟𝑂2(𝑜𝑥) + 2ZrN(ox)
𝑂𝑂 𝑜𝑥 + 𝑍𝑟 𝑚 = (𝑍𝑟𝑂 + 𝑉𝑂2+ + 2𝑒−)
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20196/21
1 2 3 4 5 6 70.0
0.1
0.2
0.3
0.4
0.5
0.6
0.7
0.8
0.9
(, g
m-2
s-1)1
/4
Oxygen concentration, wt%
900°C
1000°C
1100°C
1200°C
1300°C
𝑁2(𝑔) + 4 𝑍𝑟𝑂 + 𝑉𝑂2+ + 2𝑒− (𝑜𝑥) = 2𝑍𝑟𝑂2(𝑜𝑥) + 2ZrN(ox)
Flow rate model[M. Grosse et al. ICAPP 2016]
Experimental evidence: reaction rate K ~ xO4 for the reaction of N2 with Zr(O)
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20197/21
Flow rate model[M. Grosse et al. ICAPP 2016]
ሶ𝑛𝑉𝑂2+ = ሶ𝑛𝑜𝑥𝑦𝑔𝑒𝑛,𝑟𝑒𝑎𝑐𝑡 =
𝐾𝑛𝑜𝑥2 𝑡∗
Do we know the oxygen vacancy flux to the surface?
Yes, we know!
ሶ𝑛𝑁2 =𝐾𝑛𝑜𝑥2 𝑡∗
−ሶ𝑛𝑂22− ሶ𝑛𝐻2𝑂 /4How many nitrogen reacts?
𝑛𝑁 = න
𝑡
𝑘𝑛𝑂2 𝑡∗
−ሶ𝑛𝑂22 + ሶ𝑛𝐻2𝑂
2ሶ𝑛𝑂22 + ሶ𝑛𝐻2𝑂
𝑑𝑡 + 𝑛0𝑁Molar concentration of
nitrogen taken up:
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20198/21
Flow rate model[M. Grosse et al. ICAPP 2016]
❑ Number of cracks can be assumed to be proportional to the number of
ZrN precipitates.
❑ No hints that the size of the ZrN precipitates depend on time or
temperature.
❑ Therefore, the fraction of cracks should be proportional to the nitrogen
concentratiion in the oxide.
𝑓𝑐𝑟𝑎𝑐𝑘𝑠 = 𝐴න
𝑡
𝐾𝑛𝑂2 𝑡∗
−ሶ𝑛𝑂22
+ ሶ𝑛𝐻2𝑂
2ሶ𝑛𝑂22
+ ሶ𝑛𝐻2𝑂
𝑑𝑡 + 𝑛𝑁0
❑ The reaction rate is weighted sum of the reaction rate of positions with
cracked and undisturbed oxide.
ሶ𝑛𝑍𝑟 = 𝑓𝑖𝑛𝑡𝑒𝑟𝑓𝑎𝑐𝑒𝑐𝑟𝑎𝑐𝑘𝑒𝑑𝐾𝑛𝑍𝑟 + 1 − 𝑓𝑖𝑛𝑡𝑒𝑟𝑓𝑎𝑐𝑒𝑐𝑟𝑎𝑐𝑘𝑒𝑑𝐾𝑛𝑂
2 𝑡∗
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 20199/21
Flow rate model[M. Grosse et al. ICAPP 2016]
• total starvation (starvation of all gases reacting): The lower the
oxygen, steam and nitrogen flow rate, the lower is the reaction rate
• partial starvation (starvation only of oxygen and stream): The lower
the oxygen and steam flux, the higher is the reaction rate.
• global starvation: starvation at the whole material
• local starvation: starvation only at locations with increased reaction
rate (e.g. cracks) or if oxygen and steam was already consumed by
the material located before in flow direction.
2 x 2 kinds of starvation
ሶ𝑛𝑁2 =𝐾𝑛𝑜𝑥2 𝑡∗
−ሶ𝑛𝑂22− ሶ𝑛𝐻2𝑂 /4
Determining parameter: quantity
of steam and oxygen starvation
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201910/21
Experimental validation of the model
0 500 1000 1500 2000 2500 30000
50
100
150
Time, s
m
, g
/m2
SF1
SF2
SF4
SF6
SF8
SF10
INFLUENCE OF THE STEAM AND OXYGEN
FLOW RATE ON THE REACTION OF
ZIRCONIUM IN STEAM/NITROGEN AND
OXYGEN/NITROGEN ATMOSPHERES, (M.
Grosse et al., ICAPP 2016)
The lower the oxygen and
steam flow rate the earlier is the
transition in the reaction kinetics
and the higher is the reaction
rate after the transition.
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201911/21
Neutron radiography
Which are the consequences for the hydrogen uptake and why can
we study these processes by in-situ neutron radiography?
Crack formation in the zirconium oxide layer is connected with enhanced
hydrogen uptake by the metallic zirconium. Hydrogen concentration is a
marker for oxide cracks.
0 3600 7200 10800 14400 18000
0
200
400
600
800
1000
1200
1400
1600
cH, w
pp
m
oxidation time, s
M. Grosse et al.,
Nucl. Instr. & Meth. A 651 (2011). 253
Zircaloy-4, 1000°C
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201912/21
Basis Neutron radiography
Intensity measured at the detector pixel x,y:
Total macroscopic neutron cross section:
( )syxIyxIyxTyxI total −== exp),(),(),(),( 00
),,(),,(),,(),(
),,(),,(
4 tyxNtyxNtyxNyx
tyxNtyx
OONNHHZry
total
i
i
i
totaltotal
totaltotaltotal +++=
=
−
0,0 0,1 0,2 0,3 0,4 0,5 0,6
0,0
0,5
1,0
1,5
2,0
2,5
3,0
3,5
900°C
1000°C
1100°C
1200°C
1300°C
to
tal,
cm
-1
H/Zr atomic ratio
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201913/21
Experiments - Antares beam line (FRM-2)
Experiments were performed at the
ANTARES neutron imaging beamline
at the FRM-2 research reactor (TU Munich,
Garching, Germany)
using the KIT-INRRO furnace
Lateral resolution: ~ 0.25 mm (l ~ 225 mm,
L/D ≈ 971)
exposure time: 29 s
readout time: 1.2 s
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201914/21
Test matrix of experiments with different flow
rates
4 temperatures800°C
900°C
1000°C
1100°C
5 flow rates24 l/h
36 l/h
48 l/h
60 l/h
72 l/h
The oxidation times applied
depended on temperature.
Analysis of the reaction gases
by mass spectrometry in the
pre-tests,
Analysis of the hydrogen
absorption by in-situ neutron
imaging at Antares (FRM-2)
50 % argon
10 % steam
40 % nitrogen
Steam-air-tests
Several tests with 40% air and
10% steam with 24 l/h and 60 l/h,
respectively, at 800°C
2 in-situ with 24 l/h tests,
respectively, at 800°C and 1000°C
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201915/21
In-situ Neutron imaging – influence of flow rate
36 l/h 72 l/h24 l/h 48 l/h
ste
am
-nitro
gen
900°C
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201916/21
Results 900°C
absorbed hydrogenreleased hydrogen
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201917/21
In-situ Neutron imaging – different atmospheres800°C
1000°C
steam-nitrogen steam steam-air
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201918/21
In-situ Neutron imaging – different atmospheres
Breakaway at the very beginning
of test
(the first image after starting the
injection of the reactive gases
show breakaway)
Starting time for breakaway < 30 s
1000°C 24 l/h
steam-nitrogen
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201919/21
In-situ Neutron imaging – different atmospheres
absorbed hydrogenreleased hydrogen
Released and absorbed hydrogen during the tests at 1000°C
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201920/21
Summary and conclusion
• Hydrogen concentration is an indicator for cracks in the oxide layer. An enhanced
hydrogen absorption during the reaction of Zircaloy-4 in nitrogen-steam
atmosphere were observed.
• At 800, 900 and 1000°C a change from parabolic-linear to pure linear oxidation was
observed. Partial starvation occurred.
• The lower the flow rates, the higher are the oxidation rates and the later are
the transitions in the kinetics
• Breakaway at 1000°C starts very early (during the first 30s)
• Reactions at 1100°C show the largest mass increase. The kinetics are linear from
beginning, because of total starvation.
• The KIT model of the influence of the gas flow rate shows that the reaction of
zirconium alloys in nitrogen containing atmospheres depends on the quantity of
steam and oxygen starvation:𝐾𝑛𝑜𝑥2 𝑡∗
−ሶ𝑛𝑂22− ሶ𝑛𝐻2𝑂. It was confirmed qualitatively.
• Main conclusion for nuclear reactor safety: Beware having nitrogen in the reactor
during severe accidents!
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201921/21
Acknowledgment
Thanks to
FRM-2 for providing beamtime at the ANTARES neutron imaging beamline,
the ANTARES team in particular D. Bausenwein for their support in the neutron
imaging experiments and
U. Stegmaier and P. von Appledorn from KIT for their support in the re-
commissioning of the INRRO furnace.
Thank you for your attention
19th International Symposium on Zirconium in the Nuclear Industry
Manchester UK, May 19-23 201922/21
KIT / Institut für Angewandte Materialien
www.kit.edu
Enhanced Hydrogen Uptake und Reaction Kinetics During
Oxidation of Zircaloy-4 in Nitrogen Containing Steam
Atmospheres
M. Grosse, S. Pulvermacher, M. Steinbrück (KIT – IAM)
B. Schillinger (TU Munich)