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ORNL-TM-5503.txt
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ORNL/TM-5503
Temperature Gradient Compatibility
Tests of Some Refractory Metals and
Alloys in Bismuth and Bismuth-Lithium
Solutions |
R. DiStefano
B
J.
0. B. Cavin
Printed in the United States of America. Available from
National Technical Information Service
U.S. Department of Commerce
5285 Port Royal Road, Springfield, Virginia 22161
Price: Printed Copy $4.00; Microfiche $2.26
This report was prepared as an account of work sponsored by the United States
Government. Neither the United States nor the Energy Research and Development
Administration/United States Nuclear Regulatory Commission, nor any of their
employees, nor any of their contractors, subcontractors, or their employees, makes
any warranty, express or implied, or assumes any legal liability or responsibility for
the accuracy, completeness or usefulness of any information, apparatus, product or
process disclosed, or represents that its use would not infringe privately owned rights.
Wy ‘
ORNL/TM-5503
Distribution
Category UC-76
Contract No. W-7405-eng-26
METALS AND CERAMICS DIVISION
TEMPERATURE GRADIENT COMPATIBILITY TESTS OF SOME REFRACTORY
METALS AND ALLOYS IN BISMUTH AND BISMUTH-LITHIUM SOLUTIONS
J. R. DiStefano and 0. B. Cavin
Date Published: November' 1976
Sl NOTICE — E
: eport was prepared as an account of work |
1 mmd by the Unitod States Government. Neither | '
i lthe United States mor the United States Energy
i | mesearch and Development Administration, nor any of}
i Jtheir employees, mor any of their contractors,
| subcontractors, or their employees, makes any
; L'wasranty, sxpress or implied, or assuines sny legal
* | dability or responsibitity for the sccuracy, completeness
.| or uscfuiness of any informati tus, product or
. | process disciosed, or represents that its wse would not
i | infringe privately owned rights.
OAK RIDGE NATIONAL LABORATORY MASM
P
)
Oak Ridge, Tennessee 37830
- operated by
UNION CARBIDE CORPORATION
for the
ENERGY RESEARCH AND DEVELOPMENT ADMINISTRATION
DISTRIBUTION OF THIS DOCUMENT IS UNLIMITED Qfi_
&
Abstract .« « ¢ o« ¢ o o ¢ o o
Introduction . « « ¢« ¢« ¢ « &
Results o+ o o o ¢ ¢ o o ¢ o &
Quartz Tests - Group 1 .
Quartz Tests - Group 2 .
Metal Loop Tests in Bi—2,5%
Summary and Conclusions . . .
Acknowledgments . . . . . . &
REfETrenCeS « o o o o o o o o o o o o o o o o s
CONTENTS
-
iii
11
11
15
30
32
33
33
TEMPERATURE GRADIENT COMPATIBILITY TESTS OF SOME REFRACTORY
METALS AND ALLOYS IN BISMUTH AND BISMUTH-LITHIUM SOLUTIONS
J. R. DiStefano and 0. B. Cavin
ABSTRACT
Quartz, T-111 and Mo thermal—convection 1oop tests were
conducted at temperatures up to 700°C (100°C AT) to determine
the compatibility of several refractory metals/alloys with
bismuth and bismuth-lithium solutions for molten salt breeder
reactor applications. Methods of evaluation included weight
change measurements, metallographic examination, chemical and
electron microprobe analysis, and mechanical properties tests.
Molybdenum, T-111, and Ta—10% W appear to be the most promising
containment materials, while niobium and iron-based alloys
are unacceptable.
INTRODUCTION
A key feature in the conceptual design of the single-fluid molten
salt breeder reactor (MSBR) is the connecting chemical processing plant
to continuously remove protactinium and fission products from the fuel
salt (Fig. 1). Protactinium, the intermediate element in the breeding
chain between thorium and 233U, has a significant neutron capture cross
section and must be kept out of the core to obtain a good breeding ratio.
Rare-earth-element fission products are also neutron poisons and so must
be stripped from the fuel. A promising approach for MSBR fuel processing
uses liquid bismuth containing dissolved lithium and thorium as reductants
to extract protactinium and rare earth elements from fuel salt containing
both uranium and thorium (Fig. 2). 1In 1968 the chemical feasibility of
this process was demonstrated. .
' One of the requirements for the development of the reductive extraction
process is identifying materials that are compatible with both molten
flouride salts and bismuth-containing reductants. Hastelloy N (Ni—?% Cr-167%
'Mo—5% Fe) has excellent compatibility with molten salts at 500~700°C;?
however, it does not have good compatibility with bismuth. Of ten elements
tested, graphite, tungsten, and molybdenum appear most promising (Table 1)
and they are also compatible with molten flouride mixtures, Extensive
investigations of bismuth as a reactor coolant have shown that inhibitors
- such as magnesium, titanium, and zirconium are often required to reduce
the high corrosion rates of conventional materials in bismuth.?!
However, these types of inhibitors would not be readily acceptable for use
in the molten salt system because they would be eliminated from the bismuth
stream by several of the proposed steps in processing.
- ORNL-DWG 68-1185ER
PRIMARY
SALT PUMP
SECONDARY
NoBFy-NaF SALT PUMP
COOLANT SALT
PURIFIED
SALT
+— GRAPHITE -
MODERATOR
REACTOR
HEAT
EXCHANGER
566°C .
-
| -CHEMICAL
PROCESSING
PLANT
TLiF ~BeF, - Thiy - UF,
FUEL SALT e STEAM GENERATOR
TURBO-
GENERATOR
STEAM
Fig. 1. 8ingle-Fluid, Two-Region Molten-Salt Breeder Reactor.
N
ORNL-DWG 71-9004R
FUEL SALT
RECONSTITUTION
URANIUM PROTACTINIUM RARE EARTH
ELEMENTS
REMOVAL
REACTOR
REMOVAL REMOVAL
FISSION PRODUCTS
TO WASTE
Fig;'Z. - Simplified Flowsheet for Processing the Fuel in a Molten-
- Salt Breeder Reactor. . - ' , . o :
v}
Table 1. Solubilities of Some Elements in Bismuth at 600°C
Element Solubility, ppm -~ Reference
W -~ Not detectable 3
C | - <1 > , 4
Mo | <1 S 536
Be 6 - 6
v 45;110 . 11
Fei o =10 | - 5
Cr : 145 5
Nb o 100200 8
Co ' 590 9
Ni | 65,750 | 10
The low solubility of graphite, tungsten, and molybdenum in bismuth
has been confirmed in compatibility tests by other investigators, and, in
addition, rhenium, tantalum, tantalum alloys, and certain ceramic oxides
and carbides also appeared to be promising for bismuth containment.12_17
In a high temperature isothermal system thermodynamic equilibrium
among components is generally reached relatively quickly; the compatibility
of the system can often be predicted if phase diagrams of the components
are known. When there are thermal fluctuations ‘and/or gradients within
a system and the equilibrium constant for a corrosion reaction is
temperature dependent, continuing corrosion can occur. For example, 1if
iron dissolves in bismuth, and the solubility increases with temperature,
simultaneous dissolution and deposition of iron will occur in the system.
Under steady state conditions the solution or deposition rate equation for
a given location can be expressed.
J K( Cear = )
where J is the flux of material entering or leaving the liquid metal, X is
a rate constant, C,,. 15 the equilibrium solubility of the solute, and C
is the actual concentration of the solute. The driving force for either
dissolution or deposition is directly proportional to the concentration
differential that exists in the system at a particular location and the
appropriate rate constant for the rocess. Our data (Table 1) agree with
previous compatibility experiments'? that suggest that C is very low
for graphite and the refractory metals tungsten, rhenium, moiybdenum, and
tantalum. Niobium and iron are somewhat less promising, but still show
relatively low solubility in bismuth.
The reductive extraction process for protactinium removal uses
bismuth containing small concentrations of lithium, and the metal transfer
process for removing rare earth element fission products from the fuel
‘salt uses bismuth containing 2-3 wt %Z Li. Since the solubility of
materials in bismuth-lithium solutions could be appreciably different from
their solubility in pure bismuth (Table 1), tests had to be conducted in
the appropriate chemical processing solutions.
| Thermal convection loops used in these tests were fabricated from
quartz, T-111 (Ta—87% W-2%Z Hf), and molybdenum. The quartz loops were
satisfactory for testing in pure bismuth and in bismuth containing up to
0.01 wt Z lithium. No quartz loops with higher lithium concentrations
were operated because of the reaction between Si02 and lithium. Loops
fabricated from quartz were relatively inexpensive and could be operated
in an alr environment. Samples of the materials being tested were
suspended in the vertical hot- and cold-leg sections (Fig. 3). To prevent
the samples from floating, they were attached to a quartz rod that was
held at the top of each leg. Several types of sample geometries were
used, including flat tabs, cylindrical tubes, and cylindrical and sheet
tensile specimens.
- External heaters were placed on each leg to preheat the loop above
the melting point of bismuth or the Bi-Li solution. A pot containing the
- melt to be circulated was attached by a mechanical connector to the bottom
of the cold leg (Fig. 3.). Before filling, the loop was evacuated so a
pressure differential would force the liquid into the loop. During
operation, the metal line below the quartz was unheated to allow formation
of a solid plug to serve as a freeze valve. When the test was completed,
this section of the line was heated to allow the fluid to drain back into
the attached pot.
The design of the metal thermal convection loops was similar to that
of the quartz loops (Fig. 4). Two sections of 7/8-imn. OD X 0.050 in.
tubing were bent to form one vertical-horizontal segment (Fig, 4). The
segments were joined by making gas-tungsten-arc saddle welds at the top
and bottom of the vertical legs. Tubular sheet and tensile specimens
were suspended in each of the vertical legs. Wires linked the specimens
together to ridigly attach the specimen chain to the vertical legs at the
top and bottom.
The metal loops were used to test a bismuth-lithium alloy containing
2,5 wt Z Li. This alloy was prepared and purified in a molybdenum-lined
stainless steel container (labeled "transfer pot" in Fig. 4)., The lines
extending from the top of the loop surge tank were made of tantalum for
ease of fabrication and corrosion resistance. A commercially-produced
Nb—-1% Zr-type 316 stainless steel dissimilar metal joint connected the
transfer pot to the loop. The Nb—1% Zr end was welded to the tantalum
tube; a mechanical fitting connected the stainless steel end to the ,
transfer pot lines. Two types of heaters were used: The main hot-leg
heater contained a radiating tantalum element while standard Calrod
heaters were strapped to other portions of the loop (Fig. 4). The
molybdenum loop is shown (Fig. 5) prior to being installed in a vacuum
chamber where the test was runm. _
vl
*
Fig. 3.
and Cold Legs.
Y-93581
Quértz Thermal Convection LooP'w:Lth.Metal Samples 1in Hot
" ORNL-DWG 74-12762
TO VACUUM/ '
Ly THERMOCOUPLE WELL
THERMOCOUPLE WELL = TO vACUUM
CLOSED FILL LINE — SURGE TANK
MOUNTING FRAME ~
VERTICAL LEGS —___ ||
P
L
N } Lt HOT LEG HEATER
b
Ly
i
i
|
TEST SPECIMENS - L
TYPICAL 2 L
b
t
CALROD HEATERS
{3 LEGS)
A
,s
POST TEST h_,
DRAIN LINE -
OUMP TANK
@m
Fig. 4. Design of Metal Thermal Convection Loop Apparatus.
(i
TR
L5k
kA
¥
ER T
Blish LR
Vo
Molybdenum Thermal Convection Loop Prior to Test in
Fig. 5.
Vacuum Chamber.
After evacuation and baking out of the vacuum chamber, the entire
loop was heated to 500°C, since the melting point of Bi—2.5 wt % Li is
slightly less than 500°C (Fig. 6). As the transfer pot was heated to
600°C (900°C in the case of the molybdenum loop), the loop was evacuated,
and differential pressure was used to transfer the bismuth-lithium
solution into the loop. During operation the tantalum heater heated the
hot leg, but the required temperature differential was maintained with
little or no heat to the rest of the loop from the Calrod heaters.
To stop the test, the heaters were turned off and the bismuth-
lithjum solution was allowed to solidify. When the system had cooled,
the vacuum chamber was opened and the bottom of the cold leg cut off. A
drain tank was placed immediately under this portion of the cold leg, the
chamber re-evacuated, and the loop heated to approximately 600°C to
allow it to drain.
Samples generally_required cleaning before meaningful weight and |
dimensional measurements could be obtained. Several different techniques
removed the bismuth or Bi-Li that adhered to the samples. If the amount
were small, mechanically cleaning the samples was sufficient. A more
satisfactory technique was to amalgamate the bismuth by dipping the
sample into hot mercury (approximately 100—-150°C) and then removing the
amalgam mechanically.
Bismuth used in these studies was Grade 69 obtained from Cominco
American Corporation. Except for Quartz loops 1 and 2, the as~-received
material was first purified by bubbling hydrogen through the molten metal
for two hours at 350°C, in a molybdenum-lined container. Initially the
exit gas burned intermittently and had a reddish hue. Subsequently the
gas burned continuously and was almost colorless indicating that reaction
with hydrogen had ceased. If an alloy were required, solid lithium was
added to solid, purified bismuth, and the mixture was heated above the
melting temperature of the alloy. The phase diagram shows that the melting
temperature of the alloy varies with lithium concentration (Fig. 6).
Additionally, in the Group 1 series (see results section) the bismuth or
bismuth-1ithium solution was filtered prior to introduction into the loop
through a type 316 stainless steel filter having openings of 10 um.
Determinations of various impurities before and after the various treat-
ments (Table 2) showed no significant improvement in the purity of the
bismuth; however, visual observations of the exit gas flame and the
appearance of the bismuth indicated that some purification had occurred
during hydrogen firing.
The addition of more lithium to bismuth as required for the two metal
thermal convection loop tests was much more difficult because (1) the
melting temperature of the alloy is much higher, (2) the bismuth-lithium
reaction is strongly exothermic, and (3) during alloying there is a
‘tendency to form LizBi (Bi—9% Li), which melts at 1150°C. A special
apparatus was used to prepare Bi—2.5% Li for these tests (Fig. 7).
Lithium was first purified by hot gettering with zirconium foil at 800°C,
and the required amount transferred into a type 304 stainless steel
container. Sequential steps were then as follows:
1. Solid bismuth was loaded into a molybdenum-lined stainless steel
container and the container was sealed under argon.
ORNL-DWG 75-9963
WEIGHT PERCENT BISMUTH
60 80 9092 94 9% 97 28 99
1200 g MEFT T 7 |
1100 /M
R
W1/
/1N
8
\\
LiyBi
/
/ LiBi
TEMPERATURE (°C)
3
Q
8
'l 415°
by,
400 ' 300° _ \
| LiBi(H)
!
300 | 27
! 195.5)
200 1R 15) ]
T 475
(180% > _j,
5
100 T
o .
0O © 20 30 4 S € 70 8 %0 100
) ATOMIC PERCENT ISMUTH Bi
‘Fig. 6. Lithium-Bismuth Phase Diagram.
Table 2. Concentration of Impurities in Bismuth
Used in Quartz Loop Tests, ppnm
c:::‘;:fl‘n o er Fe Mn M Mo c Hy 0z
As-received <5 <5 <5 <5 <1 <20 <1 <6
| After hydrogefi ireatment 2 8 1l 3 | 0.1 - NDa. 5 9
Filtered through stainless 20 30 3 0.2 w* s 7
steel screen
aND = Not determined.
TO OIL BUBBLER-VENT
T
ORNL-DWG 74-12579
304SS LITHIUM FILL LINE
Tovi Ay TO JRGON AND BLOW BACK LINE
Vi
304SS THERMOCOUPLE WELL
30455~ 3 Va4 TO VACUUM
<1 N\ —
304584V, 1o ]
~"ARGON
T ’ '
: ml A ot
: / { o } } -
E ; HYDROGEN § / TO ARGON
1~ MOLYBDENUM TUBES |
YN et 4—304SS
2. : | THERMOCOUPLE
; MOLYBDENUM LINER | WELL |
? i=-304LSS
: PISMUTH / 4| | LITHIUM 4
iy i< 304s5S
e 4 in,———— 25 in—»
Fig. 7. System Used to Prepare and Purify Bi-Li Alloy.
ot
11
2. The bismuth container was evacuated and heated at 650°C.
3. Hydrogen was bubbled through the molten bismuth for approximately
24 hr.
4, The temperature of the bismuth was raised to 700°C; the lithium
was heated to 250°C in a separate container.
5. Lithium was transferred into the bismuth container by pressure
differential. Molten lithium was injected below the liquid
bismuth surface (Fig. 7).
After alloying a sample was taken and a typical analysis was
lithium-2.4%, hydrogen-l4 ppm, and oxygen-90 ppm.
Nominal operating conditions for all of the loop tests was 700°C
maximum hot leg temperature and a minimum cold leg temperature of 590—
625°C. For the quartz loop tests Cr-Al thermocouples were used; they
were located in wells protruding through the quartz into the liquid
stream. Thermocouples made of Pt, Pt—10%Z Rh were similarly inserted into
wells through the T-111 tubing wall to measure temperature in test CPML-1.