1.553
Journal of Nuclear Materials 122& 123(1984)1553-1557 North-Holland. Amsterdam
DIFFUSION
OF HYDROGEN
AND DEUTERIUN
IN ZrVFe
Knize, J.L. Stanton, and J.L. Cecchi
R.J.
Plasma Physics Laboratory,
Princeton
University,
Princeton,
08544, USA
New Jersey
we have examined the desorption and pumping behavior of a ZrVFe alloy bulk getter. Fr20m lthese for cm Swas calculated to be DN = exp [13.6(0.9) - 18,700(600)/T] data, the diffusivity cm2s-' for deuterium. Using this value of hydrogen and DD = exp [8.7(2.1) - 14,600(1400)/T] DH' the regime where the hydrogen pumping speed becomes pressure dependent was calculated.
and
1. INTRODUCTION evaporable
Non
relatively per
high For
these
in
tokamak and
hydrogenic
recycling
ST101g3 activated which into
for
have
(84% for
temperature
Al)
pumping
PumP
to to
an
to
700°C
operation
is maintained
by
to pump isotopes
depending
exponentially problem
radiative
heating
especially inside
a
alternative
in
of
a
One
it
Optimization necessitates
a
getter operation parameters,
operates
and
of
promising
detailed
regenerates
at
lower.
getter
including pressure,
in
performance of
the
of experimental getter mass,
0022-3115/84/$03.00 @ ElsevierSciencePublishersH.V. (North-Holland Physics Publishing Division)
first of
ZrVFe
II we summarize
interpret
discussed
in
presented
and
summery follows
analyze
we
of
the
deuterium
from
a
detailed
high
pressure
the theory
measurements.
our apparatus
and
Section
III.
discussed
in
The
procedures
are
Results Sec.
used
IV,
are and
a
in Section V.
2. Theory of Pumping We
and
and
been
paper
measurements
determined
an
kinetic have
this
(DR)
at
play
surface
In
hydrogen
as
may
ZrVFe
for
desorption
of
In Section
performance
understanding
for a variety
(DD)
experimental
to ZrAl
of _ 100-200°C
the
diffusivities
be
kinetics.
surface
The K
and
at low
or during pumping diffusion
5
present
the
as
bulk
elsewhere.8'g
is
such
on
reported
to
Zr, 24.6% V, 5.4% Fe) which is similar that
alloy
ki
on
cB4 (70%
temperatures
ZrVFe
role.
the
ST707
except
is the
important
known.
will
operation
desorption6,
parameters
with
structures,
geometries
limiter.
pump
getter
surrounding
constricted
pressures'
pumping.
potential as
higher
the
One
dependent
rapid
are
D
or for pumping
getter
During
analysis
with
desorption,
for
equilibrium
ki,
diffusivity
the
primarily
the
rate
ZrAl
slow
elevating
550-7oooc,
and
K
operation
once the material
speed
pumping
pressures
of
temperature.
of
During
This
temperature.
can be predicted5
constant
(desorption
regeneration
utilization
is
diffuse
and hydrogen
accomplished
alloy
ZrAl
heating (C,N,O)
Subsequently,
temperature
for
the ZrAl
Regeneration is
have been
getter.
by
irreversibly
hydrogen) getter
and
impurities
reversibly.
parameters:
control of 2 impurities. These
of 200-400°C
impurities
they
devices
incorporated
bulk.
any regime
speeds
in-torus
Zr-16%
allows the
reasons,
getter
possess
and pumping
fusion
limiters'
applications
getters
capacities
area.
used
bulk
and Desorption
our
using
data a
and
theory
operation
described
in detail
summarize
here
relevant
the
predict of
bulk
getter getter
in Ref. 5. features
of
We the
theory. The surface reaction of a hydrogen
isotope
1554
R.J. Knize et al. /Diffusion
(such as H) and ZrVFe is
and the boundary
condition
is
TD = ro - r.*
(7)
1
ki
i
H2 + 2CZrVFe)
ofhydrogen and deuterium in ZrVFe
(1)
2(H-ZrVFe),
The
final
equation
necessary
to
specify
the
0 problem where
ki
and
ko
adsorption
and
desorption
area.
?he adsorbed
ri =
are,
respectively, rates
per
determines
the chamber pressure
the unit
flux (ri) is
V g
= IF - A jI'i-I'o)- PSI,
with V the chamber P
is
the
pressure,
and
the
desorption
(r,) is
flux
chamber, back-up
and ko jc(L,t)j2,
(3)
volume,
A the
getter
pumping
speed.
experiments,
r0 =
(8)
(2)
ki P,
where
P,
area
To analyze
we require
(8) for the
F the flux into the
surface
cases
solutions
and desorption
pumping
speed.
the present to
of pumping
pressure
and S the
Qs.
at constant
at a constant
These
(5)
back-up
solutions
are
as
follows. where
c(L,t)
is the hydrogen
the surface.
concentration
at
In equilibrium,
P = Kco2,
The
and
K
=
that
ko/ki
the
of thickness there
is
the
equilibrium
equilibrium getter
L mounted
of hydrogen
by the diffusion
concentration.
on a substrate face,
in the bulk
We
geometry
Po is given by the usual
particle
conservation,
constant
equation
= F/Pa.
for
behavior
by the dimensionless
x=0.
The
is described
of SG is governed
parameter
H,5
s P /A H=-"" D co/L
(10)
equation,
So is the
ratio
diffusion is diffusivity.
The
flux
at
the
surface r, is
initial
getter
and co is the equilibrium the
the
(9)
The characteristic
where
D
at
so that
(5)
with
SG
constant
is of planar
is no flux at the back
behavior
speed
(4)
co is the
assume
pumping
pressure
SG
where
getter
of the limited
surface
In
speed is independent
limited
this
diffusion
ac(x*,t) rD = -D ax-
Ix' =L
(6)
decay
case,
of pressure
as the getter fills toward exponential
rate
case,
after with
an
initial
pressure
H
1s
to the
the
pumping
and decreases
equilibrium
SoPo/co.
is the rate limiting
varies
flux
speed
For H << 1, diffusion
flux.
unimportant.
pumping
concentration.
with an
For H >> step.
1,
In this
time (- .lL2/D). SG -l/2 and exhibits a as P
R.J. Knize et al. /Diffusion
behavior
temporal exponential
decreases
which
with
of hydrogen and deuterium in Zr VFe
an
3. EXPERIMENTAL
apparatus
The
experiment A
Hydrogen
regeneration
increasing
equilibrium
ZrVFe
pressure.
by the backup
behavior for
the
of
increase
concomitant
pumped
ZrVFe
in
the
The
desorbed
gas
is
to that
For
hydrogenic
is described
a
hydrogenic
is similar
solid.
the
concentration
with
The initial time
system.
semi-infinite
condition,
is effected
temperature
of the degorption
an
this
surface
by
is
C(L,Jc) = C(L,O)
chamber
of
166
pumped
by
a
during
diffusion
and the desorption
gradient
becomes primarily
stabilizes dependent
on surface kinetics,
c(L,t) = (SKt +
cc
)
,
(13)
with
three
type
temperature c'
depends
[sa c(L,O)]
on the initial
diffusion-limited
is
a
constant
which
Prior
to
flow
gas admitted
the
into the
"as
thermocouples
flow
D21
allowed
measured
which
showed
over the getter surface
a
the
run,
getter
in order
to activate
thermally
desorbed
concentration
as
The
it.
then
gas
flow "as measured
9,
introduced
speed
limited
[Eq. so
(4, = co/p,
ZrVFe)
"as
hydrogen
into
H2
the
(or Da)
chamber
The
(9)1. the
where
10
and
by the turbomolecular
flow
concentration
Torr-e/q The
gas the
the getter
time
final
and
p is the density
than
embrittlement.
desorbed
the pressure
to determine
that
less
hydrogenic
the
from
(and K) "as -. 0.1 Torr-Q/g.
pumping
heated
getter "as also
that
so
determined
"as
were
"as
to _ 700°C for at least 45 minutes
resistively
TestChamber
K
conductance
(or
area of less than i- 10°C.
loading and the initial
desorption.
a heated valve and
this
H2
temperature
variations
an
Differential
of this
getter
off The
with
through
the
of the total The
a
(or D2) gas "as
across
infer
Integration
chamber.
with
and two Bayard-
H2
chamber
measurements
rates.
monitored
conductance.
to
be
valved
by a piezoelectric
calibrated
also
This pump
was
manometer
the
followed
PumP
speed.
gauges.
into
used
steel
can
speed measurements.
capacitance ionization
pressure
getter
and
WSS
1.
stainless
which
desorption
pressure
calculation
_, -1
B volume,
getter pumping
absolute
were
a
present
in Fig.
wafer
turbomolecular
for
chamber
Pd leak
(12) the
in
300 a/s H2 pumping
used
was
the
alloy
ZrVFe
contained
measured
in
schematically
is
Alpert
11
SAES
standard
a
where
AND PROCEDURES
utilized
shown
module
introduced
Eventually,
APPARATUS
decay rate y, where
(11)
by
1555
of the
to
avoid
getter
"as
pump
while
then the
FP
time FIGURE
Schematic
diagram
of
for getter measurements.
1
the
dependence
recorded. apparatus
util.ized
during
of
Measurements
desorption
temperature
the
in
were
the
of
was
the
diffusivity
for
the
getter
228O-776OC.
The
made
range
pressure
1556
R.J. Knize et al. /Diffusion
range
of temperature
could
be
measured
was
severely
>
1
(P
reasons high
for which the diffusivity from
limited
and
(jSGPdt
the
the
pumping
the
behavior of H
avoidance
limited).
diffusivity
pressure
pumping
by the requirements
large)
embrittlement
of hydrogen and deuterium in Zr VFe
For
determined
of these
from
speed was measured
the
\
IO-S-
only lo+
for hydrogen
at one temperature. _- lo‘5“? NE lo+” 2
lo-710-a-
I/T(10-3K-') FIGURE 4 Deuterium
diffusivity
alloy temperature
DD as a function
of the
T.
4. RESULTS AND DISCUSSION Figure Desorption time. was
of
The
the
getter
initially P1/2
h2' concentration
getter
temperature
loaded
is
as
a
function
was
with
3.1
proportional
to
of
531°C
and
Torr-R/g
of
the
surface
c(L,t).
2
hydrogen
pressure
c(L,t)l
during
initial dependence
(S,
predicted
calculated.
verify
of
these
pumping
speed
.i_lyo 1.0
1.2
FIGURE 3 Hydrogen
diffusivity
alloy temperature
T.
DH as a function
of the
results,
exponential
decay
This
diffusivity 3
and
to Arrenhius
functions
=
to
measured
rate
at 288°C H -
can be found measurement
is shown as an open circle
The
[13.6(0.9)
order
the
independent
agrees
measurements.
e~p
was
For these parameters
using
Fig.
the
the hydrogen
from
the diffusivity
in
I/TL10-3K-‘l
In
5.9 and therefore
of the
1.4
From
variables
(DD) diffusivities
calculated
(111.
t1/2
diffusivity
temperature.
and 2.6 x 10m4 Torr.
Eq.
to
3 and 4 show the measured
desorption was
the
The
the
F.q. (12).
the
sG)
Figures
diffusivity
proportional
exhibits
by
of
desorption.
CDS) and deuterium
functions
as
root
slope and the measured
co,
hydrogen
is
typical
behavior
t112
K,
square
[which a
time
measured
the
shows
with
with
desorption
the
diffusivities
were
fitted
the results;
- 18,700(600)/T]
exp [8.7(2.1) - 14,600(1400)/T]
cm2s-’ cm2s-‘.
and
DH = DD
R.J. Knize et al. /Diffusion
pumping verified T("Cl
1557
of hydrogen and deuterium in Zr VFe
from where
measurement
speed
the diffusivity
the desorption the pumping
dependent
independently
measurements
results. speed
begins
is is calculated
obtained
The pressure
PD
to be pressure
for ZrVFe.
ACKNOWLEDGMENTS We
would
technical U.S.
like
to
Department
thank
This
support. of
E.
Pinelli
for
work is supported
Energy
Contract
No.
by DE-
ACOZ-76-CH03073.
REFERENCES 5
FIGURE Pressure temperature the
where
PD T.
pumping
H=l
as
a
For pressures
speed
is
function
greater
of
Using
these
characteristics predicted
of
for
parameters. pressure
One
the
K,81g
the
2. J. L. Cecchi, R. J. Knize, H. F. Dylla, R. J. Fonck, D. K. Dwens, and J.J. Sredniawski, J. Nucl. Mater. 111&112 (19821 305.
diffusivity
and
3. The St 101 alloy is manufactured Getters, S.p.A., Milan, Italy.
by
SAES
4. The St 707 alloy is manufactured Getters, S.p.A., Milan, Italy.
by
SAES
the
ZrVFe
important the
operational
alloy
can
of
be
external
prediction speed
pumping
dependent.
is the becomes
This will occur when H -
pD where
lorP-
5. R. J. Knize and J. Phys. 54 (1983) 3183.
L.
Cecchi,
J.
APP~.
6. R. J. Knize and J. L. Cecchi, Mater. 111&112 (1982) 645.
J.
Nucl.
7. J. L. Cecchi and R. J. Knize, Technol. Al (1983) 1276. D2A2 P D =2'
(14)
KSO
5 shows that PD is strongly
temperature
dependent.
5. SUMMARY We have measured diffusivities dependence
measured pumping
in ZrVFe
of
diffusivity
the hydrogen
the at
using speed
the initial
desorption. one
the at
using
and deuterium
The
temperature exponential
a
high
time
deuterium was
decay
pressure.
also of
the This
J. Vac.Sci.
8. C. Boffito, B. Ferrario, and D. Martelli, J. Vat. Sci. Technol. Al (1983) 1279. 9.
Figure
111&112
Mater.
and
range
any
where
pressure
of
and
ki
Nucl.
limited
diffusion
values
of
J.
than PD,
falls as P-1'2.
measurements
1. P. Mioduszewski, (1982) 253.
R. J. Knize, J. Cecchi, in print.
L.
Stanton,
and
J.
L.