Remote Sealing of Canisters for Hot Isostatic Pressing
Transcript of Remote Sealing of Canisters for Hot Isostatic Pressing
1 Copyright © 2014 by ASME
REMOTE SEALING OF CANISTERS FOR HOT ISOSTATIC PRESSING
Dennis Wahlquist
Idaho National Laboratory Idaho Falls, Idaho, USA
Ken Bateman Idaho National Laboratory Idaho Falls, Idaho, USA
Tim Malewitz Portage Inc.
Idaho Falls, Idaho, USA
ABSTRACT Battelle Energy Alliance, LLC, has successfully tested a
remote welding process to seal radioactive waste containers
prior to hot isostatic pressing (HIP). Since the 1990s, a variety
of radioactive and hazardous waste forms have been remotely
treated using HIP during trials within Idaho National
Laboratory (INL) hot cells. For HIP treatment at INL, waste
was loaded into a stainless-steel or aluminum canister, which
was evacuated, seal welded, and placed in a HIP furnace. HIP
simultaneously heats and pressurizes the waste, reducing its
volume and increasing its stability, thus lowering the cost and
risk associated with disposal. Weld integrity must be ensured in
order to prevent the spread of contamination during HIP. This
paper presents a process for sealing HIP canisters remotely
using modified, commercially available equipment. This
process includes evacuation, heating, welding, and weld
inspection. The process and equipment have proven to reliably
seal canisters in continued HIP trials.
INTRODUCTION One of the challenges facing Idaho National Laboratory
(INL) is how to safely and economically store and dispose of
4,400 m3 of granular radioactive calcine that was produced
there from 1953 to 1992. Hot isostatic pressing (HIP) is a
promising method of significantly reducing risks associated
with this calcine, its volume, and, in turn, the cost of storing it.
A study conducted by the Australian Nuclear Science and
Technology Organisation (ANSTO) reported that using the HIP
process for volume reduction of INL granular calcine and
solidified sodium-bearing waste would save an estimated
$2 billion in disposal costs (a 50% reduction) over the U.S.
Department of Energy baseline treatment of immobilization in
a borosilicate glass matrix (Begg et al. 2005). HIP uses pressure
and heat to decrease the volume of materials by reducing their
internal void spaces. However, while it may lower INL’s
calcine risks and storage costs, HIP also presents new
challenges—for example, how to safely load radioactive
calcine into manageable-sized containers (i.e., HIP canisters)
that can be sealed and maintain their integrity after being
subjected to HIP processing. INL researchers determined that
the safest way to accomplish this is to remotely fill HIP
canisters with the calcine and seal them via welding in a
shielded hot cell before they undergo HIP.
INL HIP PROCESS In the 1990s, a Model MIH-9 “mini” hot isostatic press
manufactured by ABB Autoclave Systems, Inc., (Fig. 1) was
installed in the Hot Fuel Examination Facility (HFEF)
decontamination hot cell at INL (Bateman et al. 2002). Due to
the high radioactivity of the waste forms that were to undergo
HIP treatment, trials were conducted in the HFEF hot cell using
remotely operated equipment to prevent the spread of
contamination to workers and the public. Extensive research
and pilot-scale testing has been conducted into the HIP process
as a method for treatment of a variety of waste forms, including
ceramic wastes, iodine, corroded fuel pins, irradiated materials,
and sludge. Trials have also been conducted with an INL
Proceedings of the ASME 2014 International Mechanical Engineering Congress and Exposition IMECE2014
November 14-20, 2014, Montreal, Quebec, Canada
IMECE2014-36919
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calcine surrogate consisting of simulated alumina provided by
ANSTO and spiked with radionuclides by Battelle Energy
Alliance (Fig. 2; Bateman 2011). In all cases, HIP produces a
volume-reduced, monolithic waste form with increased stability
for disposal in a repository.
Materials to be HIP processed during the testing at HFEF
were placed inside of stainless-steel or aluminum canisters,
which were evacuated, heated to remove residual moisture, and
then sealed. The sealed HIP canister was placed inside of a
monolithic pressure vessel with a working diameter of 5.9 in.
(15 cm), a height of 11.81 in. (30 cm), and a maximum pressure
rating of 200 MPa. A molybdenum heating element provided a
maximum temperature of 1,450 C to the pressure vessel
(Bateman et al. 2002).
FIG. 1. INL HOT ISOSTATIC PRESS INSTALLED IN A DECONTAMINATION HOT CELL AT INL (BATEMAN 2002).
FIG. 2. SURROGATE INL CALCINE BEFORE (LEFT) AND AFTER (RIGHT) HIP.
HIP CANISTER SEALING CONSIDERATIONS Prior to HIP, the vessel holding the material that was to
undergo the HIP process had to be filled, evacuated of excess
air, sealed (welded), and weld inspected.
INL HIP canister loading and sealing equipment was
designed to (Wahlquist and Bateman 2002):
Provide remote operation from a window of the HFEF
main hot cell in an argon atmosphere
Contain material during operation and minimize the spread
of contaminants during transfer operations.
Allow for visual inspection of completed welds.
HIP CANISTER DESIGN HIP canisters may vary in size and material of
composition. Common HIP canister materials are stainless steel
and aluminum. HIP demonstrations for material batches up to
375 lb (170 kg) have been reported (Whittaker 2012).
For INL HIP trials, two different types of canisters were
used. The first was a cylindrical bellows canister fabricated of
304 stainless steel (Fig. 3) developed at INL. The canister had a
height of 9 in. (22.86 cm) and a diameter of 4.5 in. (11.4 cm)
prior to HIP (Goff et al. 1996). The wall of the canister was a
Hyspan No. 7541P-7.0-1.0 bellows. Seam-welded plates
formed the top and bottom of the canister. The second canister
was an ANSTO 4-in. (10.16-cm)-diameter × 6-in. (15.24-cm)-
high container with two large bellows (Fig. 2). The HIP process
was designed to accommodate both types of canisters.
Integral to the design of HIP canisters was a 7.5-in. (19.05-
cm)-long, 1-in. (2.54-cm)-diameter, 0.035-in. (0.088-cm)-thick
fill tube that was welded into an opening in the top plate. At a
loading station within the hot cell, material was proportioned
from an intermediate container (Fig. 4) through the fill tube into
the HIP canister. The intermediate container was sized to match
the volume of the HIP canister assembly. Butterfly valves were
used to proportion the correct amount of material to fill a given
type of canister. During loading, the HIP canister was vibrated
to facilitate material transfer and reduce the void volume within
the canister (Wahlquist and Bateman 2002).
HIP CANISTER SEALING PROCESS A critical aspect of using HIP for volume reduction of
radioactive calcine at INL is sealing the HIP canister to contain
contamination. Although other techniques are available,
welding is considered to be the best option for sealing the HIP
canisters. For various reasons, techniques other than welding
are unsuitable for canisters that are subjected to the HIP
process. For example, elastomeric seals, solders, and brazing
would not withstand the temperatures associated with the HIP
process. Mechanical joining techniques, such as threading,
swaging, and crimping alone, could result in the joint opening
as the canister wall is deformed during the HIP process. Unlike
the joint methods mentioned above, welding results in physical
joining of the lid or plug to the canister itself. Thus, the wall of
the canister would have to be ruptured before leakage would
occur (Berry et al. 1993).
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FIG. 3. PHOTOGRAPH OF A BELLOWS CANISTER WITH THE FILL/VACUUM TUBE PROTRUDING FROM THE LID BEFORE UNDERGOING THE HIP PROCESS (LEFT). THE
BELLOWS CANISTER AFTER UNDERGOING HIP AND SEALING WITH A WELD SEAL IS SHOWN ON THE RIGHT.
FIG. 4. BALL VALVES AT EACH OPENING OF THE INTERMEDIATE CONTAINER ARE USED TO LOAD
AND UNLOAD THE CONTAINER.
CANISTER EVACUATION AND FILL TUBE CRIMPING Prior to undergoing HIP, the canister had to be evacuated
and excess moisture removed. To prepare for this process, a
piece of quartz wool was fed into the top of the HIP canister via
the fill/vacuum tube to prevent calcine from being removed
during movement and evacuation. A guide wire was used to put
into place a plug that was press fitted into the container to
protect the weld between the fill tube and the canister. Prior to
evacuation, an initial crimp was made in the fill/vacuum tube.
Tube Crimping: The fill/vacuum tube was crimped using a
modified emergency gas pipe shut-off tool that compressed the
tubing. A Mustang Tool A 1-in. (2.54-cm) crimping blade
crushed the tubing together using a 10,000-psi hydraulic pump
(Power Team P A9H) that was modified for in-cell use. An
automatic control valve shut the pump down when a preset
hydraulic pressure was reached (Fig. 5).
Tube Evacuation: Following initial crimping, the HIP
canister was evacuated using a combination of heating and
pressure reduction. Via an NW25 KF vacuum fitting welded to
the end of the fill tube, a Varian TriScroll pump was connected
to the tube and used to lower the canister pressure. This pump
is oil-less, requires very little maintenance, and is capable of
achieving pressures as low as 10 millitorr. A condensate trap
and a dust filter installed upstream of the pump prevented the
introduction of particles and moisture to the HIP canister.
Canister Heating: Concurrent with vacuum system
operation, the HIP canister was heated in a modified
Thermcraft ceramic heater capable of temperatures up to
1,100 C. The typical bake-out temperature was 500 C.
Heating and vacuum treatment was continued until pressure
was less than or equal to 100 millitorr. After this was achieved,
the canister was allowed to cool and a second crimp was added
above the first crimp to flatten the tube for cutting and welding.
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FIG. 5. CRIMPING OF THE FILL/VACUUM TUBE FOR THE CALCINE SIMULANT HIP PROCESS (BATEMAN 2011).
Tube Cutting: Following crimping, an oil-less pneumatic
cutter was used to cut the crimped fill tube just above the tube
crimper jaws in order to prepare the container for welding and
HIP. The cutter was a Turbine Tools J30XHD pneumatic cutting
tool and used a 3-in. (7.62-cm) cutting wheel turning at
25,000 rpm. Modifications to the hot cell pneumatic flow
system were required to allow for the use of the cutting tool.
The flow required for this cutter was about 40 to 50 cfm. The
carriage was used to move the cutter forward through the
tubing. A splatter guard held on by magnets kept debris from
scattering.
HIP CANISTER WELDING The HIP canister weld station that was designed for hot cell
use was built around a Jetline Engineering tungsten inert gas
(TIG) welder. The TIG welding process uses a tungsten
electrode connected to a power supply. An arc is drawn through
a highly ionized column of inert gas, such as argon. The high
temperature of the arc melts the metal to form a seal. An arc
length controller (ALC), in combination with the drive
assembly, is used to control the length of the arc. Major
components of the welder are described below (Wahlquist and
Bateman 2002).
Carriage Assembly: A Jetline Engineering carriage and
slide were modified with new limit switches and mounting
hardware. A new bracket that held the arc length drive assembly
and cutter assembly was attached to the carriage. The forward
limit switch was used to position the tungsten inert gas torch for
the welding operation.
Arc Length Drive Assembly: The purpose of the arc length
drive is to keep the welding arc at a constant distance from the
work piece. A Jetline ALC was used to control the weld. The
torch was started in front of the flattened vacuum/fill tube and
then automatically rose when it reached the tube. The ALC
maintained a proper arc distance to produce the desired weld. A
touch circuit was used to position the welder horizontally.
When the ALC was in manual mode and the tungsten touched
the flattened tube on the side, an audible signal and light turned
on. An Intellitig 40 welding controller was also used to set the
parameters for the seal weld. Once the correct welding
parameters were found, they were programmed into the system
to allow repeated performance.
Welder: A Miller XMT 200 constant current/constant
voltage welder was used to perform the TIG welding. The unit
was not modified for use in-cell. A Miller high-frequency arc
starter was also integrated into the system. The Intelletig 40
controller was used to adjust the welding parameters. The
Jetline carriage assembly and ALC were used to control the
physical attributes of the weld process.
Control Console: The sealing equipment was controlled
from a single console. The control console contained all of the
major components: welder, ALC, Intellitig 40 controller, high-
frequency arc booster, heater controller, and various other
items. An “A” scale at the worktable was used for weighing and
accountability purposes.
The weld process was repeated up to three times at
increasing amperage levels to ensure a satisfactory seal. Weld
inspection equipment was then used to visually examine the
weld (Fig. 6). Use of binoculars and a magnifying glass proved
to be the best inspection method. The integrity of the weld seal
was tested using helium. Helium leak checks were performed in
the air cell section of the HFEF hot cells . A helium leak check
verified that the seal weld integrity was acceptable for HIP. In
addition, physical measurements of the HIP container were
taken to verify satisfactory HIP and seal welding.
Many parameters affect the quality of a weld, including arc
length, temperature, and atmosphere surrounding the weld.
Initially, it was thought that the inert atmosphere of the hot cell
was sufficient to use as the cover gas for the TIG weld process.
Test welds produced an unsatisfactory result, as shown in
Fig. 6. A sample of the atmosphere showed that the argon
atmosphere contained 1,000 ppm oxygen, so purified argon gas
was used as the cover gas, producing a satisfactory weld, as
shown in Fig. 7.
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FIG. 6. UNSATISFACTORY WELD.
FIG. 7. SATISFACTORY WELDS.
CONCLUSION The remote HIP container sealing process and equipment
have been developed and refined to a proven reliable method of
sealing containers prior to HIP. A variety of waste forms,
including simulated INL calcine, have been sealed and
undergone HIP in the HFEF hot cell without container breach
or incident. Using the methods established for canister sealing,
HIP treatment is feasible for use in treatability studies using
actual INL calcine.
ACKNOWLEDGEMENT This work was supported by the U.S. Department of
Energy, Office of Environmental Management, under DOE
Idaho Operations Office Contract DE-AC07-05ID14517.
NOMENCLATURE ALC arc length controller
ANSTO Australian Nuclear Science and
Technology Organisation
cfm cubic feet per minute
HFEF Hot Fuel Examination Facility
HIP hot isostatic pressing
INL Idaho National Laboratory
MPa megapascal
ppm parts per million
psi per square inch
rpm revolutions per minute
TIG tungsten inert gas
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