The New Mexico Liquid Sodium
α ω Dynamo
Experiment
SAFETY PRACTICES, PROCEDURES
AND COMPLIANCE
This document is intended as
the application of sodium metal safety information specific to
the New Mexico Liquid Sodium α ω Dynamo Experiment.
The Dynamo Project Group (DPG) wishes to present how we will
institute, administrate and manage sodium metal safety practices,
procedures and compliance specific to our experiment.
The New Mexico Liquid Sodium α ω Dynamo
Experiment will be performed in compliance with Federal, State,
Industry and Institutional safety practices and procedures involving
the receipt, storage, handling, and use of sodium metal.
Following the introduction, the safety requirements
concerning the receipt, storage, handling, fire fighting, and
contingency plan for spill and cleanup are covered first.
Subsequently we present how these standards will be applied to the
requirements specific to the experiment.
The DPG safety-officer/contact-person is Howard F. Beckley,
New Mexico Institute of Mining and Technology (NMIMT), Department of Physics. He can be reached at the Dynamo Lab: (505)
835-5384, Dept. of Physics: (505) 835-5328, email: hbeckley@nmt.edu.
The NMIMT Energetic Materials Research and Testing Center (EMRTC) will assign an engineer to the Liquid Sodium α ω Dynamo Experiment project to oversee that all safety practices
and procedures are adhered to during operations that involve the
sodium metal. The EMRTC engineer/safety-contact-person has yet to be
identified.
The DPG members consisting of Howard F. Beckley, Stirling
A. Colgate and Van D. Romero, plus the EMRTC engineer will all have to
sign off on the safety and operational readiness of the experiment.
The aforementioned individuals will all be responsible for the safe
operation of the New Mexico Liquid Sodium α ω Dynamo
Experiment.
The fear of sodium may have been fueled by youthful indiscretion in
the chemistry lab, yet metallic sodium is a major industrial
chemical. Domestic and foreign industry has used millions of tons of
metallic sodium over the last 100 years. It is shipped in steel
drums, ISO tanks, tank trailers and railroad tank cars of greater than
40 tons each.1 The mass of sodium in each tank car is more than
several hundred times the mass of sodium used in our experiment. When
sodium metal is shipped in steel drums, the container is
non-returnable. The Liquid Sodium α ω Dynamo Experiment
will use ~ 330 lb of sodium metal in the apparatus, shipped to us
in a steel drum.2
Liquid sodium is the lowest density, high conductivity fluid
that is not a biological poison. There is a vast difference between using
sodium at 110 C as in this experiment and at 600 C as a fast reactor
coolant. Much of the high-end technology of liquid sodium use was
developed for the high temperature coolant purpose. Two facilities,
built on a massive scale and now surplus, have been used for recent
successful sodium dynamo experiments in East Germany and
Latvia.3-5 These experiments were performed in immense halls for
full containment of a liquid sodium equipment failure. We believe that
this scale, cost, and the equipment is an unnecessary burden. We
expect to test a different dynamo flow field in more modern and modest
equipment that is developed and constructed in the laboratory, but
tested at an existing local facility designed for this purpose.
The experimental apparatus and related equipment for the
Liquid Sodium Dynamo has been designed to be semi-portable and
remotely operated. Whenever testing is to take place with liquid
sodium, all the equipment will be moved to a proven testing facility
for high-energy materials: The Energetic Materials Research and
Testing Center (EMRTC) facility at the New Mexico Institute of Mining
and Technology (NMIMT). The EMRTC facility has a 60 year history of
tens of thousands of accident-free tests involving high explosives,
rocket motors, ballistic projectiles, rocket sleds, and other
high-energy phenomena. The liquid sodium tests will be performed by
remote operation in a safety test area that is dedicated to the sole
use by the Dynamo Project Group (DPG). Compared to high-explosives
(HE), sodium is very safe because it cannot detonate. One of the DPG
members, S. A. Colgate6 has had extensive hands-on use of liquid
sodium in laboratory experiments for determining MHD stability for
fusion confinement.
The Energetic Materials Research and Testing Center (EMRTC) facility
at the New Mexico Institute of Mining and Technology (NMIMT) will act
as the receiving agent of the solid sodium metal when shipped from
Dupont Specialty Chemicals Co., Niagara Falls, NY. This is so that
the solid sodium material can be received by a controlled facility for
energetic materials. The sodium metal will be shipped in a 55 gallon
steel drum containing 330 lb of fused sodium (UN1A1/X100/S/USA).1
Drums of fused sodium offer convenient supply of intermediate volumes
(max 420 lb).1 Volumetrically, 330 lb of sodium metal displaces
~ 41 gal.2
The shipping containers will be padded with nitrogen gas (an
anti-oxidant), though inert padding with argon and helium is also
available. The United States Department of Transportation (DOT)
classification for sodium is "Dangerous When Wet". The DOT
identification number for sodium metal is UN 1428.
DPG will be available to manage, oversee, or assist with the receipt
of the sodium metal as EMRTC sees necessary and fit.
THE SODIUM METAL MUST BE STORED IN A
WEATHERPROOF BUILDING THAT DOES NOT HAVE A WATER FIRE EXTINGUISHER
SPRINKLER SYSTEM.
"Sodium should be stored in a dry, fireproof building in sealed metal
containers under inert gas blanketing or under mineral oil. A
remotely located, detached building is preferred. The storage space
must be large enough to accommodate both the maximum expected
inventory of sodium and any empty containers. The building should not
contain flammables, combustibles, or water and should not have a
sprinkler system, water pipes, steam pipes, or skylights. Particular
care must be taken to prevent water entry from roof leaks, rain, snow,
or improper drainage. Potential for flooding should be
evaluated."1
Conforming to the above requirements for a sodium storage facility,
EMRTC has provided the DPG with a small steel building that will be
dedicated to sodium storage only. The building is made of 1/2" steel
plate throughout the floor, walls and roof, with 2" channel used to
displace the floor above the ground. Externally, it is 4' × 4'
square, 7' tall at the rear and 7'6" tall at the front. The 7 deg
slanted roof projects 20" out from the front. The door is 3'6" wide
× 7' tall, and can readily be made completely weatherproof and
secure. This building was chosen because it conveniently accommodates
the sodium-filled drum/pallet system, discussed in Sec. 5
(Preparation for Long-term Sodium Storage), for long-term safe,
weatherproof, accessible storage.
For reasons discussed in Sec. 6 (Storage and Transfer System for
Sodium Use), DPG prefers that the sodium is stored under a blanket of
mineral oil which we will supply.
DPG will be available to manage, oversee, or assist with the storage
of the sodium metal as EMRTC sees necessary and fit.
It is not anticipated that at any time
sodium metal, solid or liquid, will be
intentionally physically handled by
any person associated with the project.
Although DPG does not anticipate that any personal physical contact with
the solid sodium metal will take place, safety issues dictate that all
Safety Practices and Procedures Must be Absolutely Followed at
All Times. The development of Safety Practices and Procedures for
the Liquid Sodium Dynamo Experiment will conform to industry standards
and be suited specific to this application. DPG and EMRTC are working
together to develop and refine the Safety Practices and Procedures for
the Liquid Sodium Dynamo Experiment.
Handling solid sodium metal requires special Personal Protective
Equipment (PPE) to avoid personal injuries. A variety of PPE will be
made available by the DPG, and the Proper Equipment for the
particular job or task Must Be Worn. PPE availability,
training, planning, and working carefully are the keys to preventing
serious injuries and/or fires involving sodium metal.
A list of the PPE made available for solid sodium handling is as
follows: chemical splash goggles, loose-fitting dry moleskin mittens,
neoprene or NomexTM apron, approved hard hat, industrial safety
shoes.
Although DPG does not anticipate that any personal physical contact with
the liquid sodium metal will take place, safety issues dictate that
all Safety Practices and Procedures Must be Absolutely Followed
at All Times. The development of Safety Practices and Procedures for
the Liquid Sodium Dynamo Experiment will conform to industry standards
and be suited specific to this application. DPG and EMRTC are working
together to develop and refine the Safety Practices and Procedures for
the Liquid Sodium Dynamo Experiment.
Additional protective equipment including fire retardant clothing is
required when handling liquid sodium metal. It is essential to layer
and drape the clothing to optimize its protection, so a variety of
clothing should be worn. Flame retardant clothing made from 6.0
Oz NomexTM fabric (air permeability of less than 100 ft/min)
will be made available by DPG. The clothing will be designed so that
it is loose fitting, and can be readily torn or cut off quickly in
case the wearer is splashed with liquid sodium. Leather belts should
not be worn. Heavy leather safety shoes with leather or canvas spats
attached, can be worn for additional protection.
A face shield must be worn in addition to goggles when protection of
the entire face is needed. A face shield is not a replacement for
chemical goggles; they must be worn together when a face shield is
required. Special chemical splash goggles are recommended and will be
provided by DPG; American Optical Special Goggle No. SCS247-711, with
cemented-in 0.060" lenses, rubber band, and special forehead and nose
shields. The nose shield is equipped with a short hook on the beak
which permits effective use of a fire- retardant NomexTM aramid
fiber bandanna to cover the face, ears and neck. Use of this
goggle/bandanna offers excellent head protection while maintaining
comfort and good communication capability. Mole skin mittens will be
used for hand protection. Mittens can be slipped off quickly if they
are splashed with liquid sodium.
"Sodium fires are extinguishable with dry sodium carbonate (
light soda ash) or by exclusion of air. The following materials
should not be used on sodium fires, since they react violently with
sodium (see "Chemical Properties"):
- water
- halogenated hydrocarbons, such as carbon tetrachloride
- carbon dioxide
Class A, B, and C fire extinguishers should never be used on
sodium fires and normally should not even be stored in the sodium
area. Class D or dry powder extinguishers containing soda ash,
Na-XTM or Metl-XTM are compatible with sodium, provided
nitrogen and not carbon dioxide is used to expel the powder. Caution
should be used with a pressurized extinguisher because the liquid
sodium may be spattered by the discharge from the extinguisher. Salt
or dry graphite powder may also be used on sodium fires, but they are
less effective than dry soda ash. Signs should be posted at building
entrances and throughout the area warning against the use of water and
standard type fire extinguishers."1
"Plant and local fire departments that might respond to a
fire in a sodium area should be afforded prior and periodic training
specific to sodium use areas and fire fighting techniques. These
personnel should know where sodium is stored and acceptable techniques
to extinguish sodium fires. Fire response personnel should consult
knowledgeable plant personnel in determining proper sodium fire
fighting actions."1
"Sodium fires burn on the surface of a molten sodium
"pool." Fires may be extinguished by smothering, after first
containing the liquid sodium to minimize its surface area.
Firefighters should stay upwind. Dry soda ash can be used to dike a
sodium spill, and liberal quantities should be spread over the burning
surface. If sodium is burning in open equipment such as a drum or
tank, sheet steel can be used to cover and smother the fire."1
The DPG recognizes the need to be prepared for the unlikely, but
possible event that a spill of liquid sodium metal could occur.
During the operation of the experiment the apparatus is
surrounded by a safety shield that is designed to contain the loss of
sodium should a mechanical failure occur: See Sec. 8.4, Safety Shield
for the Apparatus. It is necessary to note that either small
quantities or large, thin distributions of liquid sodium will cool to
the solidification temperature very rapidly. Thus the cleanup of
spilled liquid sodium material would most likely have to deal with a
solid sodium metal distribution. In preparation for any unexpected
equipment failure during transfer of liquid sodium metal
that could result in a large-scale, catastrophic loss of liquid sodium
metal or mineral oil from the apparatus or drum, a number of buckets
of dry, light soda ash (Na2CO3) to dike and cover
the sodium metal will be available in the immediate vicinity of the
experiment. The action of covering the liquid sodium metal with
Na2CO3 will help to exclude the oxidizing atmosphere from the
surface and abate the possibility of a sodium fire. Should a sodium
fire occur, the Na2CO3 would be used to cover or smother it, and
extinguish the sodium fire by the exclusion of air.1 In preparation
for these contingencies, the following materials and equipment will be
available at the test site (in addition to all aforementioned PPE):
- A drum of dry, light soda ash (Na2CO3) to be
distributed into buckets at the test site prior to each sodium metal
transfer and experimental test that involves sodium metal.
- A partially-filled drum of moisture-free mineral oil that any
spilled sodium metal and Na2CO3 can be placed into upon cleaning
up a spill.
- A broom and shovel for cleaning up any spilled sodium metal and
Na2CO3. Used to sweep and scoop spilled material and place it
in the partially-filled drum of moisture-free mineral oil.
- A minimum of 4 Class D or dry powder extinguishers containing
soda ash, Na-XTM or Metl-XTM, placed conspicuously around
the test area.
During the process of transferring liquid sodium metal from storage
drum to apparatus and apparatus to storage drum, local and EMRTC fire
department personnel and their equipment will be on hand to assist in
an emergency resulting from a loss of sodium metal. The operation of
the dynamo when filled with sodium will be done remotely: See Sec. 8,
The Experiment. Should a dynamic loss of sodium from the apparatus
occur, the safety shield is designed to contain it from being sprayed
into the atmosphere and autocatalytically igniting. Should a fire
result during the remote operation of the experiment, it has been
mutually decided by DPG and EMRTC that the fire will be allowed to
burn, and the smoke dissipate into the atmosphere. The building in
which the experiment itself is run is considered to be disposable in
this regard. In the unfortunate circumstance of a consuming fire
starting, the loss of the experimental apparatus is of far greater
impact than the building in which its operated.
When the solid sodium metal is initially received at the specified
EMRTC facility for storage, the drum containing the fused sodium will
be prepared to have the preponderance of the nitrogen gas padding
replaced with a blanket of mineral oil (white oil) for long-term
storage stability and ultimate use. The drum in which the fused
sodium is shipped has a 2" and a 3/4" bung on the top and a 2" bung on
the bottom in line with the 2" top bung. All three of these bungs
have standard NPT threads.
Initially the drum will be opened at the 3/4" bung and have a tee
fitting connected to it such that an external supply of nitrogen gas
can be introduced and maintained inside the drum at the top through
one port of the tee while a pressure control valve is fitted in the
second port. The pressure control valve will be set at a maximum of
one ounce per square inch pressure as a safety measure because the
drums are not built to be pressurized. Prior to filling the drum with
the mineral oil blanket, the drum will be lifted onto its own
custom-made, fitted-pallet that accommodates the gravity-feed drain
ball-valve that is to be permanently installed in the bottom 2" bung.
Under the maintained head-pressure of nitrogen gas at one ounce per
square inch, the bottom 2" bung will be removed and replaced with an
elbow fitting and the ball valve. Subsequently the mineral oil will
be introduced to the drum through the 2" top bung while the nitrogen
gas padding is vented through the pressure control valve. This will
set up the drum/pallet system containing the fused sodium for
long-term storage and use.
To use the sodium metal in the experiment, the drum/pallet will need
to moved from the storage building to the experiment test area. The
use of the sodium metal in the drum will take place by heating the
drum to liquefying temperature, 110 C (230 F), and gravity-feed
transferring the liquid sodium to the preheated experimental apparatus
through heated fluid transfer lines.7 A single recirculating
hot-oil heat source will be used to liquefy the sodium in the drum and
in the apparatus. DPG will be using a standard 20 kW electric hot
water heater filled with mineral oil as the heat source. The
sodium metal storage drum will have approximately 100' of 3/4" soft
copper tubing wrapped around it in a coil consisting of approximately
16 turns. A high-quality insulating blanket will encase the
coil-wrapped drum assembly on its pallet. A 2 L/s (1/2 gal/s) hot-oil
pump set up in a recirculating configuration to heat both the drum and
the apparatus will connect to the drum's coils and the apparatus
through heated valves and low-flow-restriction detachable connections.
Figure 1 shows a plan-view schematic of the equipment configuration
stated above. Figure 2 shows a side-view schematic of the equipment
configuration stated above where the drum/pallet system is raised to
allow the gravity-feed transfer of the liquid sodium metal from the
drum to the apparatus. Given the various thermal characteristics of
heat transfer for the system, calculations show that liquefying the
sodium will take approximately 30 minutes. In addition we will have
two electric heat guns available during transfer operations along with
a thermocouple probe with a remote readout of temperature so that any
unplanned solidification of sodium during transfer can be readily
identified and rectified.
Figure 1:
A plan-view schematic of the Ω-Phase of the Liquid
Sodium α ω Dynamo experiment apparatus and sub-system
equipment. The main platen supports the test cell apparatus on its
bearing pedestals, the electric motor drive system and the lubrication
oil system. The motor drive system as shown consists of a
continuous-duty AC motor, variable speed transmission, and main drive
shaft. The main drive shaft is a pillow-block bearing supported shaft
on which are mounted the low-speed (LS) 1:1 drive sheave, the electro
clutch that engages to drive the high speed (HS) 1:4 drive sheave, and
2 electric actuated disk brakes. The electric disk brakes are
configured such that the primary disk brake is engaged when energized
to slow or stop the rotation as desired. The secondary disk brake is
configured to be engaged when de-energized for emergency shut-down
purposes. The necessity of this is such that if something happens and
the experiment needs to be immediately and completely shut down, the
secondary brake will automatically engage by de-energization (killing
the power) and stop all rotation. The heating equipment consists of a
20 kW electric heater, hot-oil pump and electric motor, return oil
reservoir, control valves and low-flow-restriction detachable fluid
transfer connections. The safety shield that surrounds the rotating
test cell apparatus is removed for the sodium transfer process, and is
therefore not shown.
There are several points to note about the the use of sodium metal and
mineral oil in the storage drum/pallet system and the experimental
apparatus.
- Prior to setting up the apparatus and drum/pallet system for
heating for sodium metal transfer, the apparatus will be partially
filled with the same mineral oil used to blanket the sodium in the
drum. The apparatus will also be preheated to avoid any possible
solidification of the liquid sodium metal during gravity-feed transfer.
- The mineral oil also "wets" the aluminum cylindrical
structure, fluoroelastomer seals8 (not the fluoropolymer PTFE),
bearings, and safety valve that make up the test-cell of the
apparatus. This significantly reduces the physical contact between
the sodium metal and the seals and aluminum.9
- A finite amount, ~ 2 liters, of mineral oil will
intentionally be left in the apparatus when filled with sodium metal.
Due to the different specific gravity of mineral oil vs sodium metal,
~ 0.81 vs ~ 0.93 at 100 C, when the apparatus in spun up to
the very low rotation rate of 60 rpm, the mineral oil will
centrifugally float to the region of the rotational axis relative to
the sodium. Thus the seals and bearings internal to the apparatus
will operate in a hot mineral oil environment, not a liquid sodium
environment. After an experimental run, the apparatus will be cooled
while rotating so that the sodium will solidify with the mineral oil
retained at the axis. Thus the only time that the seals could come in contact with
the sodium is under the static configuration during the filling or
draining process. In these circumstances the pressure will be small
and would only be due to gravity acting on the liquid sodium.
- When filling (draining) the apparatus with (of) liquid
sodium,
the mineral oil internal to the test-cell will remain floating on the
liquid sodium as the sodium flows in either direction. The mineral
oil will follow the last of the sodium into the storage drum as it
exits the apparatus during draining. A measured quantity of mineral
oil must be introduced to the apparatus before filling. Because of
the blanketing effect of this mineral oil, nitrogen gas or air can be
exchanged
through a port in the top of the apparatus as the sodium metal flows
into or out of the storage drum. Thus during the liquid sodium
filling/draining process liquid sodium will be covered with a blanket
of mineral oil.
- The recirculating heated mineral oil system that liquefies the
sodium in the apparatus is physically isolated and separate from the
internal structure of the test-cell itself. The inner cylinder is
heated by the recirculating mineral oil flowing inside it, as depicted
in Figs. 1 and 2. Thermal heat exchange takes place through contact
of the sodium metal with the inner cylinder. Thus during the
operation of the experiment there is no physical exchange of material
internal to apparatus with anything outside the apparatus.
Figure 2:
A side-view schematic of the Ω-Phase of the Liquid
Sodium α - Ω Dynamo experiment apparatus and sub-system
equipment. Note that the drum/pallet system is raised to allow the
gravity-feed transfer of the liquid sodium metal from the drum to the
apparatus. The electric forklift used to raise the drum/pallet system
is not shown for clarity.
Figure 3 shows some of the constructed parts the Ω-Phase of the
Liquid Sodium α - Ω Dynamo experiment. The main plate
upon which the constructed assembly resides is 5 feet wide × 10
feet long. The motor for rotational power and the power transmission
system is to be mounted on this platen axially parallel to the dynamo
apparatus. An independent pressurized oil system for the primary
bearing lubrication will also be mounted on this platen.
The separate heat-source system discussed above will need to be placed
in line with, and at the end of the platen at what is the right-hand
side in Fig. 3. The approximate size of the heat-source system will
be 4' × 4'. In order to transfer the sodium metal from the
insulated storage drum/pallet system to the apparatus it will need to
be placed along side the platen on what is the far side in Fig. 3, and
raised to a height of ~ 5' from the floor. This is to facilitate
the gravity-feed transfer of the liquefied sodium metal from the drum
to the apparatus. The approximate size of the drum/pallet system will
be 3' × 3'. Figure 1 shows a plan-view schematic of this
equipment configuration. Figure 2 shows a side-view schematic of this
equipment configuration where the drum is raised to facilitate the
gravity-feed transfer of sodium to the apparatus. A capable electric
forklift is probably best suited to the task of lifting the
drum/pallet system. There are three facets of reasoning for using an
electric forklift which are due to the approximate 1 hour of time
required for heating and transferring the sodium metal. These facets
are: 1) electric forklifts utilizing a ball-screw jack don't drift
down with time like so many hydraulic forklifts, 2) electric forklifts
don't present the problems associated with carbon monoxide output in
an enclosed area, 3) electric forklifts are typically more
maneuverable than equivalently capable engine-driven forklifts.
Draining of the apparatus by gravity-feed transfer back to the drum
can take place at floor level. Subsequent to transferring the liquid
sodium metal from the drum to the apparatus, the drum will be removed
from the immediate work area.
Figure 3:
Figure 3 shows the constructed parts the
Ω-Phase of the Liquid Sodium α - Ω Dynamo
experiment mounted on the bearings and supporting pedestals. Also
shown is the port plate and two ported reservoir plenum cylinders
and the inlet & outlet recirculating oil rotary unions.
The primary drive shaft, belt pulleys, and electric motor have yet
to be added.
As can be seen in Figs. 2 and 3, the dynamo apparatus is semi-portable
in the sense that it is mounted on large casters and capable of being
towed by a suitable piece of equipment over smooth surfaces. It will
be taken to and removed from the EMRTC test facility by means of a
3-ton flatbed truck. The static weight of the complete experimental
assembly is ~ 2.5 tons. When delivered to the site, a suitable
forklift will be used to lift the apparatus from the truck. A series
of screw-jacks will be fitted to the bottom of the platen to stabilize
the apparatus for rotational tests. The main platen will be
restrained to the floor of the test area by 8 turnbuckles situated as
normal pairs at each corner (Figs. 1 and 2).
The operation of the dynamo when filled with sodium will be done
remotely. The apparatus and its diagnostic systems were intentionally
designed to be remotely operated. The temperature, pressure, rotation
rate and volumetric flow rate at a number of locations on the rotating
equipment will be monitored by computer. In addition, the heating
system and lubrication system will be provided with separate safety
measures. Real-time monitoring within design-limit thresholds will
allow for emergency shutdown of rotation and heating systems, while
leaving the bearing lubrication system active. We will be using a
large 1-ton utility van as the remote operations facility. This van
has been provided by the NMIMT Research and Economic Development
Division (R&ED).
A pressure-relief safety valve is incorporated into the apparatus to
relieve any pressure buildup from heating or from a transient pressure
spike. The safety valve will mechanically exhaust material from the
apparatus test-cell into a containment vessel which is at atmospheric
pressure. It will operate automatically to relieve pressure at a
preset value. It is designed to be capable of operating over thermal
range of 20 - 150 C. The safety valve is physically situated on the
rotation axis of the apparatus. It is incorporated into, but not
integral with the thrust-end shaft of the apparatus (Figs. 1 and 2).
A removable, electrically heated, safety shield will surround the
cylindrical vessel and will be used whenever the apparatus is rotated
and filled with either mineral oil or sodium. The safety shield is
designed to confine any dynamic sodium metal loss and absorb the
kinetic energy and containment of disrupted parts should a mechanical
failure occur. The safety shield also provides a 115 deg C thermal
region immediately external to the vessel so that the thermal load and
gradient in the experiment is reduced.
The experimental apparatus and its related systems will take up a
rectilinear area of ~ 10' wide × 15' long (Fig. 2). There
will be a minimum of a 5' wide clear work/walk space around this area.
Thus an approximate minimum area of 20' in width and 25' in length
will be used for the safe setup and operation of the dynamo.
The electrical power for the rotation of the dynamo will be provided
by a 3-phase, 440 VAC, 50 amp circuit. Rotational power can be
provided by either a continuous-duty AC motor that drives a
variable-speed transmission or an AC-motor/DC-generator set that
drives a DC motor for variable speed. We are flexible in this sense
because we have not yet selected the rotational power source.
The 20 kW electric hot-oil heat system will be run from a 220 VAC
single-phase power source. This is intended be a standard
residential-type "hot water" heater. This system will also include
the use of a 3 kW hot-oil recirculation pump as described above, also
run by single-phase 220 VAC.
The lubrication system will run on standard 110 VAC, 20 amp service.
The remote operation van will need to be serviced with a minimum of
two 110 VAC lines for operations of the remote controls, alarms,
computer, lights, etc. The remote operations van can be displaced up
200 meters away from the experimental operation site as safety
dictates and warrants.
1 Dupont Specialty Chemicals, Technical Information,
E-92775-1 (1994)
2 The volumetric displacement of the Liquid Sodium
α ω Dynamo Experiment in its Phase-I configuration is
155.6 L = 1.556 × 105 cm3. Sodium metal has a solid
density at 20 C of 0.968 g/cm3, therefore the mass of sodium that
the apparatus can contain is 150.6 kg = 332 lb.
3 Gailitis, A., Lielausis, O., Dement'ev, S., Platacis,
E., Cifersons, A., et. al. "Detection of a Flow Induced Magnetic
Field Eigenmode in the Riga Dynamo Facility" Phys. Rev. Let. 84
4365-4368 (2000).
4 Busse, F.H., Müller, U., Stieglitz, R., & Tilgner,
A., "A Two-scale Homogeneous Dynamo: An Extended Analytical Model and
Experimental Demonstration Under Development", Magnitnaya
Girdrodinamika, T.32, 259-271 (1996).
5 Raedler, K.-H., Apstein, E., Rheinhardt, M., and
Schüler, M., "The Karlsruhe Dynamo Experiment; A Mean Field
Approach" Studia geoph. et geod. (Prague) 42 1-9 (1998).
6 Colgate, S.A., "Liquid-sodium Instability
Experiment", UCRL 4560 (1955).
7 No transfer of sodium from the drum to apparatus or
apparatus to drum will take place using pumps. The safety reason for
this is that even when heated, the thermal conductivity of the sodium
is great enough that a localized solidification can develop through
heat-transfer cooling and the pump can dead-head, cavitate or freeze
shut, depending on the location of the solidification, and can ruin
the pump, burn up the motor, or break fluid transfer lines.
8 The dynamic radial seals used in the apparatus have as
the lip material the fluoroelastomer FKM (ASTM D 1418 symbol), being
the same as FPM (ISO 1629 symbol). This material offers the greatest
chemical resistance to mineral oil, sodium metal and its derivatives
(NaOH and Na2O2) of any conventionally used lip seal material.
The fluoroelastomer LongLifeTM seals from Chicago Rawhide are
made of the premium lip-seal material that has the widest temperature
range and chemical resistance. The LongLifeTM seals will handle
temperatures from -40 to 204 C (-40 to 400 F). They resist most
special lubricants and chemicals that can destroy nitrile,
polyacrylates or silicons. Even though the fluoropolymer PTFE offers
wider media resistance in comparison to standard elastomers with a
temperature range of -73 to 260 C (-100 to 500 F), it is not to be
used for the seals in the experiment because sodium metal is one of
the few materials that will adhere to PTFE and mechanically degrade its
sealing ability.
9 Tests in the NMIMT Dynamo Lab with a 3 cm i.d. cylinder
have shown that the "wetting" of the aluminum surface with mineral
oil does completely nullify any chemical interaction between sodium
metal and aluminum. These tests were performed at 115 C in both
static and rotating configurations, where the centripetal acceleration
was ~ 54 g, and the duration of the test was 1 day. Under these
conditions the mineral oil was centrifugally spun to the center of the
cylinder because it represented the low-pressure, or buoyant region of
the test apparatus. This is simply due to the fact that the mineral
oil has a lower specific gravity than that of the liquid sodium:
~ 0.81 vs ~ 0.93 at 100 C. Even though the mineral oil was
centrifugally spun out of the interface region to very thin dimensions
(as measured by electrical resistivity), no reaction took place
between the sodium and aluminum because there was no atmospheric
oxygen or moisture able to enter the interface region. The
conclusions from the DPG tests are that without O2 present to form
Na2O2 or H2O to from NaOH at the interface, no chemical
reaction between the liquid sodium metal and aluminum could take
place.
This document was generated using the
LaTeX2HTML translator Version 97.1 (release) (July 13th, 1997)
Copyright © 1993, 1994, 1995, 1996, 1997,
Nikos Drakos,
Computer Based Learning Unit, University of Leeds.
The translation was initiated by Kate Weatherall on 11/22/2000
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